theoretical and experimental investigation into high current hollow cathode arc attachment

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THEORETICAL AND EXPERIMENTAL INVESTIGTION INTO HIGH CURRENT HOLLOW CATHODE ARC ATTACHMENT by Ryan T. Downey A Dissertation Presented to the FACULTY OF THE GRADUATE SCHOOL UNIVERSITY OF SOUTHERN CALIFORNIA In Partial Fulfillment of the Requirements for the Degree DOCTOR OF PHILOSOPHY (ASTRONAUTICAL ENGINEERING) December 2008 Copyright 2008 Ryan T. Downey

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Page 1: Theoretical and Experimental Investigation into High Current Hollow Cathode Arc Attachment

THEORETICAL AND EXPERIMENTAL INVESTIGTION INTO HIGH CURRENT

HOLLOW CATHODE ARC ATTACHMENT

by

Ryan T. Downey

A Dissertation Presented to the FACULTY OF THE GRADUATE SCHOOL

UNIVERSITY OF SOUTHERN CALIFORNIA In Partial Fulfillment of the

Requirements for the Degree DOCTOR OF PHILOSOPHY

(ASTRONAUTICAL ENGINEERING)

December 2008 Copyright 2008 Ryan T. Downey

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Acknowledgements

The defense of this thesis marks the completion of the most intellectually,

emotionally, finically, and physically trying period of my life. Due to the unusual

circumstances surrounding my time and support in graduate school, much was sacrificed

in the pursuit of this degree and its associated education, from time spent with friends and

family, financial resources, peace of mind and personal health. Through it all, I consider

my most significant accomplishment to be the education gained along the journey, not in

an academic sense, but the knowledge acquired about myself, and my perspectives on the

world around me. I consider this gained wisdom to be invaluable.

Many people contributed to the eventual completion of this thesis, and when my

legs were week, the finish line still distant, they gave me the support and encouragement

without which I may not have finished the race. The fist person to thank is my advisor,

Professor Dan Erwin, who provided me with the safe harbor during the storm. Thank you

for our many discussions, your ongoing support and ability to provide perspective, and

your commitment to seeing me complete this work. To my former colleagues at NASA’s

Jet Propulsion Lab where my work started, Jay, Al, Ray and Yiangos; It was my privilege

to work with some of the most talented people in the field, and I consider you all among

them.

My sincere thanks to my lab mates at USC, Nate and Taylor, who provided me

with much discussion and support through the years, over many, many, many cups of

coffee. To Anthony, who was my company on far too many late nights at the lab,

providing me with insight and assistance both personal and professional; the difficulty of

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times can be tempered by the measure of those who accompany you on the journey. My

thanks for showing this to be true. My experiments could not have been completed

without the tireless and loyal dedication of my lab assistant Paul, who brought an

excitement and curiosity which served as a daily reminder of why I got into this whole

mess in the first place. To Andrew Ketsdever, who stepped up to the plate when no one

else would; My most sincere thanks and gratitude for all your support.

To my friend and mentor Keith Goodfellow, who provided me with my first ideas

of what a real rocket scientist is: I thank you for seeing something in me that I wasn’t

quite sure I saw myself. In every sense of the word, both professional and personal, you

are one of the finest teachers I have ever known…(not a bad rock climber either!) I hope

someday to be able to do for my students what you have done for me.

To Jon, who has known me longer than just about anyone: We’ve both seen many

changes in each other throughout our lives, though unchanged is our love of science

fiction, which fueled many of my early dreams of space. Thanks for sharing with me the

experience of “the human condition”, our many Trek nights, and always having time to

lend me your thoughts.

Mom and Dad; For as long as I can remember you have always encouraged my

crazy ideas of one day becoming a rocket scientist. When I was a child, you put up with

my trying habit of taking things apart to figure out how they worked, even though I didn’t

always figure out how to put them back together again. Your patience has finally come to

fruition. Thanks for everything.

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Finally, to Kristy; None of this would have been possibly without you. Nothing I

can write here can begin to approach how I feel about your tireless love and support, and

so I will simply say thank you for being my greatest teacher, and, I love you.

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Table of Contents Acknowledgements............................................................................................................. ii

List of Tables ................................................................................................................... viii

List of Figures .................................................................................................................... ix

Abbreviations.................................................................................................................... xv

Abstract:.......................................................................................................................... xvii

Chapter 1: Introduction ....................................................................................................... 1

1.1 The Importance of Electric Propulsion ..................................................................... 2

Chapter 2: MPD Thruster and Cathode Operation ............................................................. 6

2.1 The MPD/LFA Thruster ........................................................................................... 6

2.2 Hollow Cathode Operation ..................................................................................... 10 Conventional Hollow Cathode:................................................................................. 10 Single Channel Hollow Cathode:.............................................................................. 12 Multi-Channel Hollow Cathode:............................................................................... 14

2.3 The Importance of Temperature ............................................................................. 18

2.4 Internal Plasma Column- IPC ................................................................................ 22 Effects of Mass Flow Rate on Plasma Conditions.................................................... 30 IPC Control Parameters and Experimental Observations......................................... 36

Chapter 3: History and State of the Art ............................................................................ 39

3.1 Historical Related Research.................................................................................... 39

3.2 State of the Art – MCHC’s and LFA thrusters ....................................................... 45

Chapter 4: Role of This Doctoral Work............................................................................ 50

Chapter 5: Methods........................................................................................................... 52

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5.1 Theoretical Methods ............................................................................................... 52

5.2 Experimental Methods ............................................................................................ 56 Langmuir Plasma Probe............................................................................................ 60 Cathode Stage ........................................................................................................... 66 Optical Pyrometery ................................................................................................... 68 Cathodes.................................................................................................................... 71 Signal Processing and Data Acquisition (DAQ)....................................................... 73

Chapter 6: Single Channel Hollow Cathode model.......................................................... 75

6.1 Assumptions............................................................................................................ 75

6.2 Governing Equations .............................................................................................. 77 Conservation of Mass – Species Continuity Equation.............................................. 78 Conservation of Momentum – Species Equation of Motion .................................... 80 Conservation of Energy – General Species Energy Equation .................................. 87 Electron Energy Transport Equation ........................................................................ 89 Heavy Species Energy Transport Equation .............................................................. 92 Neutral Species Energy Equation ............................................................................. 92 Combined Heavy Species Energy Equation ............................................................. 93 Remaining Equations:............................................................................................... 94

6.3 Summary of Equations:........................................................................................... 96

6.4 Numerical Methodology ......................................................................................... 98 Finite Volume Method............................................................................................ 100

6.5 Boundary Conditions by Boundary Location ...................................................... 102 Boundary 1: Gas entrance....................................................................................... 102 Boundary 2: Cathode Walls .................................................................................... 104 Boundary 3: Cathode Exit Plane............................................................................. 106 Boundary 4: Cathode Centerline:............................................................................ 106

6.6 Solution Procedure................................................................................................ 107

6.7 Connecting Theoretical Model and Experimental Work ...................................... 108

Chapter 7: Experimental Results and Conclusions......................................................... 110

7.1 Cathodes................................................................................................................ 110

7.2 Observed Trends ................................................................................................... 118 High-Voltage / Low-Current Discharges................................................................ 118 High-Current / Low-Voltage Discharges................................................................ 120 Plasma Data ............................................................................................................ 140

7.3 Active Zone........................................................................................................... 148 Computational Predictions:..................................................................................... 155

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7.4 Connection to Multi Channel Hollow Cathodes................................................... 167

7.5 Summary of Results.............................................................................................. 171 Magnitude of Peak Temperature:............................................................................ 172 “Hot Spot” or “Active Zone”:................................................................................. 172 Location of Peak Temperature:............................................................................... 174 Temperature Gradient: ............................................................................................ 174 Discharge Voltage:.................................................................................................. 174 Power: ..................................................................................................................... 175 Electron Temperature: ............................................................................................ 176 Plasma Potential:..................................................................................................... 176 Plasma Density: ...................................................................................................... 176 Plasma Generation .................................................................................................. 176

7.5 Suggestions for Future Work ................................................................................ 178

References:...................................................................................................................... 180

Appendix A:.................................................................................................................... 186

Evaluation of Governing Equations............................................................................ 186 Plasma Density, ni=ne ............................................................................................. 187 Plasma Temperature, Te .......................................................................................... 189 Plasma Potential, φ ................................................................................................. 191 Electric Field Vector, E........................................................................................... 193 Ion Current Density Vector, ji................................................................................. 194 Electron Current Density Vector, je ........................................................................ 196 Heavy Species Temperature, Th.............................................................................. 196 Neutral Gas Velocity Vector, un ............................................................................. 199 Neutral Gas Density, nn........................................................................................... 201

Boundary Conditions – Summary............................................................................... 203

Appendix B: .................................................................................................................... 206

Collision Frequencies.................................................................................................. 206

Appendix C: .................................................................................................................... 208

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List of Tables

Table 1. Ionization energy for common electric propulsion propellants .......................... 26

Table 2 . MPD thruster research groups ........................................................................... 40

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List of Figures

Figure 1: MPD thruster and force vectors [26].................................................................. 7

Figure 2. Force vectors in ALFA^2 Li-LFA...................................................................... 8

Figure 3. Orificed Hollow Cathode [42].......................................................................... 11

Figure 4. Axial temperature trends of a typical SCHC [18] ............................................ 14

Figure 5: Two different designs for Multi-channel Hollow Cathodes............................. 16

Figure 6. Inter-rod spacing in "macaroni packet" design MCHC. Each hollow region acts as an individual SCHC. Figure from reference [65]...................................... 16

Figure 7. Multi-Channel Hollow Cathode – “macaroni packet” design – side view....... 17

Figure 8. MCHC during operation, as seen head on. Photo from reference [65] ............ 17

Figure 9. Tungsten MCHC before operation in MPD thruster. Photo from reference [65] ................................................................................................................... 19

Figure 10. Tungsten MCHC after operation in MPD thruster. Photo from reference [65] ................................................................................................................... 20

Figure 11. Sensitivity of emitted current to temperature and work function [26] ........... 22

Figure 12 Equipotential Lines for flow rates, low (a), moderate (b), high (c) [18] ......... 33

Figure 13. Computed electron temperature in an orificed hollow cathode [42].............. 33

Figure 14. Active MCHC with Lithium -Barium mixture, photo from reference [65]................................................................................................................................... 44

Figure 15. Active MCHC with Lithium only, photo from reference[65] ........................ 44

Figure 16. Schematic view of 250 kW Li-LFA, ALFA^2, [13] ...................................... 47

Figure 17. Improvements over SOA, reference [13] ....................................................... 47

Figure 18. The six MCHC designs tested by MAI .......................................................... 49

Figure 19. Vacuum chamber w/ door open – early iteration of cathode setup ................ 58

Figure 20. Vacuum chamber, side view........................................................................... 59

Figure 21: Construction of Langmuir probe end tip. ....................................................... 62

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Figure 22: Layout of vacuum side experimental components, Langmuir probe in retracted position.............................................................................................................. 63

Figure 23: Layout of vacuum side experimental components, Langmuir probe in fully extended position..................................................................................................... 64

Figure 24: Electrical schematic of the Langmuir probe circuit. ...................................... 65

Figure 25: Langmuir probe data trace, 2 mm Tantalum cathode, 100 sccm, 35 Amp discharge. “Double Trace” effects of the voltage pulse are clearly visible ............ 66

Figure 26. Two-axis Stage to which the cathode is mounted .......................................... 68

Figure 27. Chamber and optical pyrometer ..................................................................... 69

Figure 28: 10 mm diameter Tungsten cathodes and 2 mm diameter Tantalum cathodes............................................................................................................................ 72

Figure 29: Layout of the power supply and diagnostic electronic systems. .................... 73

Figure 30. Computational zone........................................................................................ 75

Figure 31. Discretization scheme showing stepwise function for scalar values............ 100

Figure 32. Sample flow chart for theory and experimental work ..................................109

Figure 33. Damaged cathode and flange........................................................................ 112

Figure 34. Close-up of damaged cathode ...................................................................... 112

Figure 35: Up close view of 6 mm Tungsten cathode, post test. ................................... 113

Figure 36. 2 mm Tantalum and 10 mm Tungsten cathodes. Images are pre-discharge. ....................................................................................................................... 114

Figure 37. Comparison of exit planes of 2 mm Tantalum, and 10 mm Tungsten cathodes. Images are pre-discharge. .............................................................................. 115

Figure 38. Close-up view of 2 mm Tantalum cathodes. Images are pre-discharge....... 116

Figure 39: Images of the 10 mm diameter Tungsten cathode after operation at 2 kW.................................................................................................................................. 117

Figure 40. Dependence of peak temperature location on flow rate, for high-voltage, low-current discharge through 6 mm Tungsten cathode.................................. 119

Figure 41. Discharge voltage vs. flow rate, 2 mm Tantalum cathode ........................... 121

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Figure 42. Discharge voltage vs. flow rate, current as parameter, lower current range. 2 mm Tantalum cathode...................................................................................... 121

Figure 43. Discharge voltage vs. flow rate, current as parameter, higher current range. 2 mm Tantalum cathode...................................................................................... 122

Figure 44: Discharge voltage vs. discharge current for a 2 mm Tantalum cathode ...... 122

Figure 45. Discharge voltage vs. discharge current, flow rate as parameter, low flow rate range. 2 mm Tantalum cathode ...................................................................... 123

Figure 46. Total Discharge Power vs. Flow rate, 2 mm diameter Tantalum cathode, with discharge current as a parameter, lower current range............................ 123

Figure 47: Total Discharge Power vs. Flow rate, 2 mm diameter Tantalum cathode, with discharge current as a parameter, higher current range........................... 124

Figure 48: Discharge power vs. Discharge current, with mass flow rate as a parameter, lower mass flow rate range. 2 mm Tantalum cathode. ................................ 124

Figure 49: Discharge power vs. Discharge current, with mass flow rate as a parameter, lower mass flow rate range. 2 mm Tantalum cathode. ................................ 125

Figure 50. Energy input per mass throughput, 2 mm Tantalum cathode....................... 125

Figure 51. Resistance of Argon plasma discharge vs. mass flow rate, discharge current as a parameter .................................................................................................... 127

Figure 52: Value of minimum resistance of the Argon plasma discharge, and flow rate at which minimum resistance occurs, vs. discharge current................................... 127

Figure 53: Plasma resistance vs discharge current, Argon flow rate as a parameter, 2 mm Tantalum cathode................................................................................................. 128

Figure 54: Axial temperature profile along 2 mm Tantalum cathode at 60 sccm flow rate ......................................................................................................................... 130

Figure 55. Axial temperature profile along 2 mm Tantalum cathode at 70 sccm flow rate ......................................................................................................................... 130

Figure 56 Axial temperature profile along 2 mm Tantalum cathode at 100 sccm flow rate ......................................................................................................................... 131

Figure 57. Axial temperature profile along 2 mm Tantalum cathode at 120 sccm flow rate ......................................................................................................................... 131

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Figure 58. Location and magnitude of the peak temperature of 2 mm Tantalum cathode, vs. flow rate ..................................................................................................... 132

Figure 59: Peak temperature vs. mass flow rate, 2 mm Tantalum cathode ................... 132

Figure 60: Location of the maximum temperature of 2 mm Tantalum cathode vs. mass flow rate ................................................................................................................ 134

Figure 61: Location of Peak Temperature dependence upon current, flow rate as a parameter, 2 mm Tantalum cathode............................................................................... 134

Figure 62. Magnitude of peak temperature vs. discharge current, 2 mm Tantalum cathode ........................................................................................................................... 135

Figure 63: Wall temperature profile of 2 mm diameter Tantalum cathode at 20 Amp discharge. .............................................................................................................. 136

Figure 64: Wall temperature profile of 2 mm diameter Tantalum cathode at 25 amp discharge, Argon mass flow rate as a parameter.................................................... 137

Figure 65: Wall temperature profile of 2 mm diameter Tantalum cathode at 90 sccm Argon mass flow rate, discharge current as a parameter. ..................................... 138

Figure 66: Wall temperature profile of 2 mm diameter Tantalum cathode at 90 sccm Argon mass flow rate, discharge current as a parameter. ..................................... 138

Figure 67. Pressure 40mm upstream inside 10 and 6 mm diameter cathode vs. flow rate. ........................................................................................................................ 139

Figure 68: Sample of raw data from Langmuir probe trace, 2 mm Tantalum cathode, 150 sccm, 30 Amp discharge........................................................................... 140

Figure 69: Electron Temperature vs. Discharge current, Mass flow rate as parameter. 2 mm Tantalum cathode............................................................................... 141

Figure 70: Plasma Density vs. Discharge current, discharge current as parameter. 2 mm Tantalum cathode................................................................................................. 142

Figure 71: Plasma ionization fraction vs. discharge current at location 10 cm downstream of 2 mm Tantalum cathode........................................................................ 143

Figure 72: Plasma Potential (phi) and Discharge Voltage (DV) vs. Discharge Current, Mass Flow rate as parameter. 2 mm Tantalum cathode .................................. 144

Figure 73: Electron temperature vs. Mass flow rate, discharge current as parameter. 2 mm Tantalum cathode............................................................................... 145

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Figure 74 : Plasma Potential vs. Mass Flow rate, discharge current as parameter. 2 mm Tantalum cathode.................................................................................................... 146

Figure 75: Plasma Density vs. Mass Flow rate, discharge current as parameter. 2 mm Tantalum cathode.................................................................................................... 146

Figure 76: Plasma ionization fraction as a function of mass flow rate at location 10 cm downstream of 2 mm Tantalum cathode, discharge current as parameter.......... 147

Figure 77: Sample of analysis of thermionic emission profile data for active zone calculations. ................................................................................................................... 149

Figure 78: Width of the active zone inside the cathode vs. mass flow rate................... 150

Figure 79: Width of the active zone vs. the discharge current, parametric with mass flow rate ................................................................................................................ 151

Figure 80: Computed plasma density profile in 6 mm Tungsten cathode 3.3 Amp 121 Volt discharge, 215 sccm flow rate......................................................................... 157

Figure 81; Damage of the rear mating flange after high power testing of the 10 mm Tungsten cathode. ................................................................................................... 158

Figure 82: Computed neutral particle density profile in 6 mm Tungsten cathode 3.3 Amp 121 Volt discharge, 215 sccm flow rate..........................................................159

Figure 83: Computed plasma potential profile in 6 mm Tungsten cathode 3.3 Amp 121 Volt discharge, 215 sccm flow rate......................................................................... 160

Figure 84: Computed electron temperature (eV) potential profile in 6 mm Tungsten cathode 3.3 Amp 121 Volt discharge, 215 sccm flow rate. ........................... 160

Figure 85: Computed heavy species temperature (K) profile in 6 mm Tungsten cathode 3.3 Amp 121 Volt discharge, 215 sccm flow rate. ........................................... 162

Figure 86: Computed plasma density profile in a 6 mm Tungsten cathode, 3.6 Amp discharge, 185 sccm Argon flow rate. .................................................................. 162

Figure 87: Computed neutral particle density profile in a 6 mm Tungsten cathode, 3.6 Amp discharge, 185 sccm Argon flow rate. ............................................................ 163

Figure 88: Computed plasma potential profile in a 6 mm Tungsten cathode, 3.6 Amp discharge, 185 sccm Argon flow rate. .................................................................. 163

Figure 89: Computed electron temperature (eV) profile in a 6 mm Tungsten cathode, 3.6 Amp discharge, 185 sccm Argon flow rate. .............................................. 164

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Figure 90: Computed heavy species temperature (K) profile in a 6 mm Tungsten cathode, 3.6 Amp discharge, 185 sccm Argon flow rate. .............................................. 164

Figure 91: Normalized plasma parameters vs. normalized pressure. Baselined to 185 sccm case. ............................................................................................................... 166

Figure 92: Normalized plasma parameters vs. normalized pressure. Baselined to 215 sccm case. ............................................................................................................... 166

Figure 93: Gas flow in MCHC upstream of channels.................................................... 168

Figure 94: Exit plane of MCHC before, and after operation. Note the increased erosion in the central channels....................................................................................... 170

Figure 95: Example of a generic computational zone grid ............................................ 186

Figure 96: Computed plasma density profile in 6mm Tungsten cathode 3.3 amp 121 volt discharge, 215 sccm flow rate. ........................................................................208

Figure 97: Computed neutral particle density profile in 6mm Tungsten cathode 3.3 amp 121 volt discharge, 215 sccm flow rate............................................................ 209

Figure 98: Computed electron temperature (eV) potential profile in 6mm Tungsten cathode 3.3 amp 121 volt discharge, 215 sccm flow rate. ............................. 209

Figure 99: Computed plasma potential profiles in 6 mm Tungsten cathode, 3.3 Amp, 121 Volt discharge, 215 sccm flow rate...............................................................210

Figure 100: Computed heavy species temperature in 6 mm Tungsten cathode, 3.3 Amp, 121 Volt discharge, 215 sccm flow rate...............................................................210

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Abbreviations Symbols used: D characteristic dimension/length (m) e elementary charge (C) q species specific elementary charge (C) n species number density (#/m3) λ mean free path (m), wavelength (m) εo permittivity of free space εi ionization energy ε emisivity φ work function (eV), plasma potential (V) Φs potential drop (V) η plasma specific resistivity σ collisional cross-section (m2) ν collision frequency (s-1) kb Boltzmann’s constant ki ionization rate coefficient h Plank’s constant j current density (A/m2) A material constant, area (m2) T temperature (eV or Kelvin) E electric field (V/m) Kn Knudsen Number m electron mass (kg) M heavy species mass (kg) n ionization rate density (#/sm3) P,P pressure (Pa) q conductive heat flux (W/m2) r radius (m) t time (s) u velocity (m/s) κ thermal conductivity(W/mK) Γ flux density (#/sm2) S inelastic collision energy loss (kg/ms3) Z atomic number Subscripts and Superscripts: a generic species type a b generic species type b n neutral

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grey graybody black blackbody i ion, ionization e electron h heavy species (ion or neutral) pe plasma electron b Boltzmann, beam s sheath th thermionic wall cathode wall eff effective c cathode o reference value en electron-neutral ei electron-ion eV indicates value in electron Volts K indicates value in Kelvin th thermionic wf work function Constants: kb Boltzmann’s Constant, kb = 1.3806*10-23J/K, 8.6174*10-5 eV/K e basic electronic charge, e = 1.6*10-19 C ε0 Permittivity of free space ε0 = 8.85*10-12C2/Nm2 me mass of single electron, me = 9.11*10-31kg α Richardson Constant, α = 1.2017*106A/ K2m2

R Gas constant, R = 8.3144 J/moleK c speed of light c = 3*108m/s

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Abstract:

This research addresses several concerns of the mechanisms controlling

performance and lifetime of high-current single-channel-hollow-cathodes, the central

electrode and primary life-limiting component in Magnetoplasmadynamic thrusters.

Specifically covered are the trends, and the theorized governing mechanisms, seen in the

discharge efficiency and power, the size of the plasma attachment to the cathode (the

active zone), cathode exit plume plasma density and energy, along with plasma property

distributions of the internal plasma column (the IPC) of a single-channel-hollow-cathode.

Both experiment and computational modeling were employed in the analysis of the

cathodes. Employing Tantalum and Tungsten cathodes (of 2, 6 and 10 mm inner

diameter), experiments were conducted to measure the temperature profile of operating

cathodes, the width of the active zone, the discharge voltage, power, plasma arc

resistance and efficiency, with mass flow rates of 50 to 300 sccm of Argon, and discharge

currents of 15 to 50 Amps.

Langmuir probing was used to obtain measurements for the electron temperature,

plasma density and plasma potential at the cathode exit plane (down stream tip). A

computational model was developed to predict the distribution of plasma inside the

cathode, based upon experimentally determined boundary conditions. It was determined

that the peak cathode temperature is a function of both interior cathode density and

discharge current, though the location of the peak temperature is controlled gas density

but not discharge current. The active zone width was found to be an increasing function

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of the discharge current, but a decreasing function of the mass flow rate. The width of the

active zone was found to not be controlled by the magnitude of the peak cathode wall

temperature. The discharge power consumed per unit of mass throughput is seen as a

decreasing function of the mass flow rate, showing the increasing efficiency of the

cathode. Finally, this new understanding of the mechanisms of the plasma attachment

phenomena of a single-channel-hollow-cathode were extrapolated to the multi-channel-

hollow-cathode environment, to explain performance characteristics of

these devices seen in previous research.

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Chapter 1: Introduction

In January of 2004, US president George Bush announced the new Vision for

Space Exploration (VSE) [49], in which he directed NASA to return humans to the lunar

surface, establish a permanent human presence on the moon by 2020, and to eventually

send human explorers to the Martian surface. In achieving these difficult and expansive

goals with a high rate of efficiency and financial affordability, it is understood that high

specific impulse propulsion technology is desirable, specifically electric propulsion (EP),

solar and/or nuclear. Owing to their perforce in both thrust and specific impulse (Isp),

Magnetoplasmadynamic (MPD) thrusters (also called Lorentz Force Accelerators,

LFA’s) have been identified as a prime candidate for such missions as heavy lunar cargo

(supporting a lunar base/outpost), piloted missions to Mars, and heavy cargo missions to

Mars [62, 23, 17, 34].

Magnetoplasmadynamic thrusters have a desirable combination of high Isp

(~3,000 to 10,000s) and relatively high thrust (~10 to 100N), while providing a large

power processing density attractive to spacecraft designers. Although MPD/LFA

thrusters provide large thrust for an EP device, they provide relatively low thrust

compared to chemical systems, and so like all EP systems, they are required to have a

long lifetime: thousands of hours of reliable performance.

The cathodes of MPD thrusters have been identified as the primary lifetime-

limiting component, thus much MPD thruster research focuses on cathode related issues.

Due to the high operating temperatures of MPD thrusters, cathodes are made of refractory

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metal (such as Tungsten or Tantalum), and have historically been solid rods, however in

recent years investigations into hollow cathodes, specifically Multi-Channel Hollow

Cathodes (MCHC), have yielded promising results.

Little literature exists discussing high-current hollow cathodes, with much of the

available work coming from a program of study conducted by the Moscow Aviation

Institute of former Soviet Union during the mid 1990’s. A complete understanding of the

physics, lifetime and performance of MCHC devices is necessary in order to advance

MPD thruster technology to the level of a reliable flight propulsion system. This research

focuses on the internal plasma properties in a single channel of the multi-channel

cathode, with the goals of a predictive capable model yielding internal plasma properties,

which can be input into existing “cathode life models”.

1.1 The Importance of Electric Propulsion

In order to make the great expanses of the solar system accessible to both robotic

scientific investigation and manned exploration, it is necessary to transport resources

across inter-planetary distances by means of high efficiency. All space missions are

measured by a change in velocity (noted as ΔV, and read as “delta-V”), which is the total

change in velocity necessary to accomplish the mission, or in-short, it is a measure of the

energy necessary to achieve the mission’s propulsion goals. The choice of propulsion

systems used for a particular mission is largely mission specific, with a wide array of

options available to mission designers. The field of available options can be roughly

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broken down into two categories, 1: high-thrust low-efficiency, and 2: low-thrust high-

efficiency. Typically category 1 propulsion systems are chemical engines (such as those

carrying the space shuttle into orbit), while a significant portion of category 2 systems are

Electric Propulsion (EP, such as the ion engine which propelled the Deep Space 1

mission).

By far the most common form of spacecraft propulsion is the traditional chemical

system, where by (usually) two propellants, the fuel (such as hydrogen) and the oxidizer

(such as oxygen) are mixed together, combusted at high temperature and pressure, and

then expanded via a contoured nozzle which produces thrust by gas-dynamic means.

Chemical rocket engines produce large amounts of thrust, which is why all launch

vehicles employ these types of systems, but they have a low Isp and so are relatively fuel

inefficient. In chemical engines, energy stored in the chemical bonds of the propellants is

released through the combustion process and then converted to kinetic energy, producing

thrust. Thus the amount of available energy is determined by the combustion chemistry of

the fuel and oxidizer.

In Electric Propulsions system, the energy is produced by an external power

source (batteries, solar array’s, nuclear reactor, etc.) and is transferred to the propellant

producing thrust, thus (to first approximation) the amount of energy available to be

converted to directed kinetic is only limited by the capability of the power supplies (and

material limits). An EP system is categorized by the means by which energy is

transferred to the propellant: Electrothermal, Electrostatic, or Electromagnetic.

It is always desirable to achieve mission goals with the best possible use of

resources and the most efficient systems available, however for lifting off of a planetary

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body (Earth, Moon or an asteroid), when the spacecraft is subject to a large gravitational

force, high thrust chemical engines are exclusively required. However, once in orbit,

where low thrust systems can achieve the required goals, mission designers have more

options available from which to choose. It is here that the Electric Propulsion systems

have their greatest impact to space exploration, for higher efficiency systems require less

propellant to achieve the same ΔV. If a spacecraft now needs to carry less propellant, it

can carry more cargo in the form of scientific instruments, people, power systems, etc.

The propellant-efficiency of a propulsion system is measured in Specific Impulse,

Isp (measured in seconds), which is a measure of how fast the engine exhaust is expelled

from the thruster. Consider an individual particle in the exhaust plume; the higher the

exhaust velocity of that particle, the more momentum it will add to the spacecraft.

exhaust

o

uIspg

≡ (0.7.1)

From the rocket equation, we can see that the value of the thrusters’ specific

impulse becomes exponentially important in determining the amount of propellant

necessary to achieve a certain Δv:

Minitial = M final eΔv

Ispgo⎛⎝⎜

⎞⎠⎟

(0.7.2)

where Minitial and Mfinal are the vehicle mass prior to and after the engine burn.

The current cost of launching payload into Earth orbit has been (roughly)

estimated at $10,000 per kg – thus, in-space propulsion systems requiring large amounts

of propellant will need pay a high price to place this propellant in orbit. From this it is

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easy to see how high Isp electric propulsion systems are desirable from both the resource

utilization, and financial, points of view. Any future, large scale, sustained exploration

effort will be required to make the best possible use of available resources to achieve

long term viability. Electric Propulsion systems are currently the most efficient means of

in-space propulsion available, thus their continued development is a key requirement for

an affordable, and achievable, expanded program of space flight as described by NASA’s

Vision for Space Exploration. To attempt a large scale, long term program of space

exploration without means of high efficiency propulsion systems is to ensure its financial

infeasibility, and ultimate failure.

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Chapter 2: MPD Thruster and Cathode Operation

2.1 The MPD/LFA Thruster

An MPD thruster is a type of Electric Propulsion system, which makes use of the

nature of charged particles to produce useable thrust with high efficiency.

Magnetoplasmadynamic thrusters are classified as electromagnetic devices (though

gasdynamic forces also play a role in the production of thrust). Electromagnetic thrusters

produce a plasma and generate thrust by use of electromagnetic fields to accelerate the

charged particles in a direction opposite of the spacecrafts desired vector of travel. A

basic schematic drawing of an MPD thruster can be seen in Figure 1. (For further

discussion of electrothermal and electrostatic systems, see [33]).

A typical Self-Field MPD thruster consists of a central rod shaped cathode inside

a cylindrical anode. An electrically neutral gas flows from behind the cathode and is

introduced into the discharge region between the two electrodes. Initially, a high voltage

is placed between the two electrodes, forming plasma by the initial breakdown of the gas,

after which point a high current supply is engaged and the high voltage supply is

disengaged. During initial breakdown under the high voltage, a small current flows

through the plasma across the large voltage drop via enhanced field emission from a

relatively cold cathode. After initial breakdown of the gas is achieved, a high current is

then driven through the plasma, however since the bulk cathode is still too cold to support

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Figure 1: MPD thruster and force vectors [26]

the required current through thermionic emission, the current is initially generated by

small “cathode spots” on the cathode surface. These spots are characterized as small,

non-stationary, highly mobile regions of intense heat (near the material boiling point)

supplying electrons via a combination of field emission and thermionic emission [54].

This initial ignition of the discharge is the most destructive phase of cathode

operation, as (for each cathode spot) the large heat loads on such a small amount of

surface area cause the explosive release of vaporized cathode material and electrons, a

process which occurs very rapidly before each emission site is terminated and another

one is born at a different location. This non-stationary mode continues until the total heat

provided by the many cathode spots raises the surface temperature to levels sufficient to

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support steady-state thermionic emission over a relatively large surface area. Thus the

initial startup phase is characterized by large material erosion rates, three or four orders

of magnitude higher than rates experienced under steady-state operation [54].

During steady state operation, current flows between the two electrodes causing

the neutral gas to be ionized by collisions with electrons emitted thermioniclly from the

cathode surface. This current creates an azimuthal magnetic field, which interacts with

the motion of the charged particles, and a force tangent to both is created, governed by

the Lorentz Force equation: Fmag = q v × B( ) in the absence of any electric field. It is for

this reason that MPD thrusters are also referred to as Lorentz Force Accelerators, or

LFA’s. (Historically, thrusters using gaseous propellant are called MPD’s, and those

using vaporized metal propellant at called LFA’s, further discussion on this topic is found

later in this paper.)

Figure 2. Force vectors in ALFA^2 Li-LFA

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An electric field is created with both radial and axial components, driving current

flow between the two electrodes. For qualitative description, a quick application of the

right hand rule helps one see that the resultant force acts to accelerate the plasma both

axially outward (termed the “blowing” force) and radially inward (termed the “pumping”

force) with the total thrust created proportional to J2. The ionization of the propellant gas

creates a quasi-neutral plasma, and the Lorentz force accelerates both ions and electrons

along the same force vector, thus space-charge limiting and beam neutralization are not

factors in MPD thrusters as they are on other electric propulsion systems (ion, hall, etc.).

Additionally, if the anode-cathode pairing is placed inside an external solenoid

(co-axial with the cathode) producing a strong applied solenoidal magnetic field coaxial

with the cathode, there is further plasma acceleration due to the interaction between the

plasma and the applied magnetic field - this system is called an Applied Field MPD

Thruster. Typically the applied field is used in “low power” systems (P < 500 kW), and

is strong in magnitude in comparison to the magnetic field produced by the main

discharge (BApplied>>BSelf).

Several different thrust producing mechanisms have been identified in MPD

thrusters [35]:

1. Self Field Acceleration (Lorentz force acceleration),

2. Gas Dynamic Acceleration

3. Swirl acceleration

4. Hall acceleration

Swirl and Hall acceleration are caused by the interaction between the discharge

current flowing through the plasma and the external applied magnetic field, and thus are

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pertinent to applied field thrusters only. The relative dominance of each thrust

mechanism is still a mater of debate among researchers. Since the plasma acceleration

mechanisms (with the possible exception of gas dynamics) play no significant

discernable role in the internal physics of hollow cathodes, which is the focus of this

work, there will be no further discussion of this topic. For additional related material see

[33, 63, 14]

2.2 Hollow Cathode Operation

Conventional Hollow Cathode:

A conventional orificed hollow cathode consists of a hollow cylindrical tube with

a plate on the down stream end, as seen in Figure 3. The plate has a small orifice in it,

through which the plasma exits. Inside the tube is a porous Tungsten insert, impregnated

with a Barium Calcium aluminate source material, for work function reduction. Before

the discharge is ignited, the tube is heated to working temperature (~1,000 K) by an

external source, typically a resistive heating element in physical contact with the exterior

of the tube. The Barium in the insert material migrates its way up to the surface of the

cathode where a layer of adsorbed oxygen and Barium atoms is formed, reducing the

work function of the material. The working gas is ionized by collisions with the electrons

emitted from the insert, and a quasi-neutral plasma exits through the orifice.

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Figure 3. Orificed Hollow Cathode [42]

Ions created in the collisions will make their way to the walls of the cathode where they

will be accelerated through the sheath potential drop and strike the surface of the insert

depositing heat, recombining and then drifting off as a neutral. This process continues the

heating of the cathode, and a balance between heating through ion bombardment and

cooling through (mostly) thermionic emissions is attained, at which point the external

heater is turned off. Adsorbates lost to evaporation are then replenished by a continuously

renewing supply of Barium and Barium-Oxide, until the insert’s supply is depleted, at

which point cathode temperatures rise and it has (largely) reached the end of its useful

lifetime.

The orifice plate serves as a physical barrier acting to retain the neutral gas inside

the cathode, increasing the resonance time of any one particle and increasing the

likelihood of ionization. The total pressure is nearly constant inside the cathode, and

typically the ionization fraction is very low. Insert temperature levels peak at the

Insert material

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downstream end in contact with the orifice plate, and decreases at a rate inversely

proportional to distance upstream.

Some examples of this type of cathode are the NSTAR (NASA Solar Electric

Propulsion Technology Application Readiness) cathode used on the NASA Deep Space 1

ion engine, the plasma contactor used on the International Space Station, and the NEXIS

(Nuclear Electric Xenon Ion System) cathode used on the NEXIS ion engine developed

under Project Prometheus. Such low current cathodes have demonstrated relatively long

operational lifetime in both ground and in-space testing. In one particularly significant

experiment, an NSTAR type cathode, similar in configuration to the design used for the

International Space Station plasma contactor, was run for 27,800 hours at an emission

current of 12 Amps with a Xenon flow rate in the range of 4.2 to 4.7 sccm. Optical

pyrometery measurements recorded average cathode peak temperature of 1533K during

the first 23,776 hours of operation while discharging 12 Amps [53]. In comparison, MPD

cathodes are required to discharge current levels up to several kilo-Amps. Hollow

cathodes see space application use in many devices including Hall thruster, ion engines,

and plasma contactors.

Single Channel Hollow Cathode:

A single channel hollow cathode (SCHC) is a simple device consisting of a single,

cylindrical hollow tube, with no orifice plate or low work-function insert material, with

some means of mating to the propellant feed system. In MPD thrusters, no external

heating device is used to pre-heat the cathodes due to the limited usefulness of such a

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device once exposed to a cathode operating at temperatures > 2,500K during the MPD

discharge. All electron emission is directly from the walls of the tube, and the plasma is

generated (largely) inside the hollow region. In MPD thrusters, if the flow rate of

propellant is high enough to be considered a viscous continuum, upon exiting out of a

SCHC the flow is choked due to the large pressure difference between the inter-electrode

space, and the cathode hollow region. Due to the open ended geometry there exists a

large axial pressure gradient along the cathode, with propellant gas density dropping

considerably as it approaches the cathode exit. A density distribution is established,

leading to changing mean-free-paths throughout the cathode.

Basic electron emission and ionization processes in a SCHC are similar to those

in a traditional orificed hollow cathode, although due to the absence of a porous insert,

there are no issues of Barium depletion, and useful lifetime is determined by the

evaporation rate of the cathode wall itself. Experimental work on SCHC devices has

shown that from the cathode exit plane, the surface temperature rises to a peak

temperature at a location some distance L upstream, the temperature then falls as you

proceed further upstream. This distance L is a function of the cathode size, discharge

current, propellant flow rate, and choice of propellant gas, though the exact form of this

function is still a matter of debate among researchers. Figure 4 shows the axial

temperature profile of a typical SCHC discharge.

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Figure 4. Axial temperature trends of a typical SCHC [18]

Multi-Channel Hollow Cathode:

A multi-channel hollow cathode (MCHC) consists of several parallel channels of

ionization, the exact geometry of which can vary depending upon design. The two most

common designs are:

1. A single rod with several holes drilled parallel to the central axis,

2. A single hollow tube of diameter D, with many smaller solid rods of diameter d

(where D>>d) placed inside the tube, where the channels are created by the

spaces in between the rods. This is knows as a “macaroni packet” and is by far the

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more common design. Several different hollow emission regions are formed by

the inter-rod spacing, see Figure 6.

In all cases, the entire cathode component is commonly constructed of the same material,

and is usually Tungsten (or Tungsten impregnated with a work function reducing

material, such as Thorium). The two common designs are shown in Figure 5.

Figure 6 shows the regions formed in construction of the macaroni packet design,

where inter rod spacing creates many channels through which the gas flows. There are

generally three types of channel cross sections formed, and each channel acts as an

individual single channel hollow cathode as shown schematically in Figure 7. Each

channel will have its own unique interaction with the plasma which is determined by the

channels geometry and distance from the cathode centerline.

The MCHC design is particularly well suited in an MPD thruster due to the high

operating temperatures. Even though the porous Tungsten insert in the traditional hollow

cathode has a lower work function, it would not survive long in the environment of an

MPD, and so is not used. Instead, all the electron emission in a MCHC comes directly

from the cathode wall itself. In practice, a MCHC can be thought of as several SCHC’s

operating in parallel.

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Figure 5: Two different designs for Multi-channel Hollow Cathodes

Figure 6. Inter-rod spacing in "macaroni packet" design MCHC. Each hollow

region acts as an individual SCHC. Figure from reference [65]

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Figure 7. Multi-Channel Hollow Cathode – “macaroni packet” design – side view

Upstream of the channels the neutral gas is introduced to the cathode, and at some

point in the flow it develops the familiar parabolic velocity profile where the particles in

the center of the flow move faster than those at the periphery. Thus, each channel will

have a different mass flow rate, and therefore a different IPC (Internal Plasma Column,

discussed in section 2.4). An operating MCHC is seen head-on in Figure 8.

Figure 8. MCHC during operation, as seen head on. Photo from reference [65]

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2.3 The Importance of Temperature

MPD thrusters are driven by constant current power sources, in experimental

practice these are often arc-welding power supplies. The electron current flowing in the

discharge comes largely from thermionic emission off the cathode surface, which is

directly controlled by the temperature of the surface material (and work function) – thus a

certain surface current density will be produced by a certain surface temperature. For

current levels necessary in MPD thruster cathodes, the operating temperature of a

Tungsten cathode approaches the melting temperature of the material (3680K), and thus a

non-trivial amount of the material will evaporate during normal operation. Previous

research has shown that at high temperatures the evaporation of cathode surface material

is exponentially proportional to the surface temperature (~ eT) [54]. For a given arc

attachment area, exerting a larger force on the plasma requires a larger discharge current,

which requires a higher temperature, which in turn leads to a higher evaporation rate and

thus a shorter cathode lifetime. Thus (at this time) the reliable lifetime of an MPD

thruster system is largely a function of the cathode temperature, indeed surface

temperature is the key determinant of all thermionic cathodes. Figure 9 and Figure 10

show a MCHC before and after operation, where the result of extended operation at high

temperature is very apparent.

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Figure 9. Tungsten MCHC before operation in MPD thruster. Photo from reference [65]

It is for this reason that the ability to predict the temperature distribution of the

cathode for given operating conditions is of prime importance, for these distributions can

then be input to evaporation models and thus the useful lifetime of the cathode can be

predicted. Much work in cathode research focuses on predicting and reducing the

operating temperature of the cathode, following this course, two main paths have been

pursued, cathode geometry and reduction in work function.

For a given cathode material, it is desirable to achieve longer cathode life times

by reducing the operating temperature through a reduction of the surface current density,

while still maintaining total current levels and thruster performance. This is accomplished

by changing the geometry such that the same discharge current is emitted by a larger

surface area of the cathode. With a solid rod cathode, it is only the exterior surface area

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Figure 10. Tungsten MCHC after operation in MPD thruster. Photo from reference

[65]

of the cathode which emits – for a single hollow tube cathode, the interior and exterior

surfaces emit, and hence the required current density is effectively reduced by a factor of

two. In a MCHC, each channel acts as an individual hollow tube cathode, and thus the

emission area increases significantly, enabling a reduction in the current density surface

temperature, though a detailed understanding of the interaction between the plasma and

the interior of a MCHC is not present in the literature.

In addition to the erosion processes in the cathode, the other significant cathode

mechanism strongly controlled by temperature is the thermionic emission of electrons

from the material surface. All conductors will emit electron current in proportion to the

temperature of the material, and material properties. This emission is governed by the

well known Richardson equation for thermionic emission:

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eff

b wall2 swall eff wf

o

,4

k T qEj AT eφ

φ φπε

= = − (2.2.1)

Where “j” is the emitted surface current density in A/m2, A is known as the

Richardson coefficient, and is = 6x105 A/m2/K for Tungsten [25]. Φwf is the work

function (in eV) of the material (= 4.5 for pure Tungsten [25]), and Φeff is the effective

work function, which is an effective reduction of the work function by an applied electric

field over the surface of the material, the cathode sheath. It is clear to see that the

electron current emitted from the surface of a hot cathode is very sensitive to both

temperature and work function, with the latter the dominant parameter. A reduction in the

work function by 0.5 eV yields greater than an order of magnitude difference in emitted

current. In addition, a drop in surface temperature of 10% yields a corresponding

reduction in emitted current density of 95.5 %.This sensitivity can been seen in Figure 11

(note the units in the figure). From this, it is easy see that nearly all of the emitted current

of a hollow cathode comes from a relatively small region of the material wall, the region

termed the “active zone” or “hot spot”. The precise definition of what constitutes the

active zone varies among studies, but is generally taken as the region of cathode wall

responsible some high percentage of the thermionically emitted current, typically ~70-

100%.

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Figure 11. Sensitivity of emitted current to temperature and work function [26]

The choice of cathode material, as well as choice of propellant, has an influence

on cathode temperature by reducing the work function of the material. Choosing a

cathode material with a reduced work function, such as using Thoriated Tungsten rather

than pure Tungsten, will reduce the temperature (for constant emission) - approximately

1~2% thorium is typical of such cathodes. With Tungsten cathodes, it has also been

shown that by mixing a small amount of Barium with the propellant, the Barium will

deposit itself as a monolayer on the Tungsten surface, and reduce the work function.

2.4 Internal Plasma Column- IPC

The bulk volume of the plasma in MPD thrusters exists in the annular zone

between the cathode and anode - the extension of the plasma to the interior region of the

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hollow cathode, is termed the Internal Positive Column, or IPC (sometimes called the

Internal Plasma Column). The IPC is also termed the “plasma attachment area” in some

literature due to its close interface in both proximity and phenomenon with the surface of

the cathode.

Though the IPC is of prime importance, its limits and area of coverage have been

ill defined (both qualitatively and quantitatively) in MCHC literature. It is largely

regarded as part of the hot spot, or active zone [18], of a thermionically emitting hollow

cathode, and includes the regions of the cathode immediately upstream and downstream

of the location of peak cathode temperature. This is largely due to a lack of theoretical

research into such devices, as there currently is no reliable/validated model capable of

qualitative and quantitative predictions of how far the plasma will penetrate upstream

inside a MCHC device.

The importance of the IPC can be understood through its relation to the plasma

generation processes at work in the hollow region. Plasma is generated inside the cathode

by the ionizing collisions between neutral atoms in the propellant stream and the

thermionic (beam) electrons which are emitted from the cathode walls and then

accelerated through the sheath potential into the main plasma volume. The ionization

potential of the neutral gas sets a minimum energy requirement for a single ionization

event to occur - thus single event ionization will only occur when electrons of high

enough energy strike the neutrals, these high energy electrons coming from two sources:

when thermionically emitted electrons accelerated through the sheath gaining sufficient

energy, or from electrons in the high energy tail end of the distribution. In a multi-step

ionization process, many separate collisions can each deliver finite amounts of energy to

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a neutral atom, with each collision raising the atoms internal electronic energy level and

bringing it that much closer to ionization. Up to this point the relative contributions of

single and multiple collisions to the ionization process of the hollow cathode IPC have

not been well defined, largely due to lack of experimentally verified data of plasma

properties in the IPC, and little information about this exists in the literature. Recent work

in this area conducted at Princeton University [8], have modeled the plasma generation

process in the IPC as a multi-step ionization process.

Many collisions between electrons and neutral atoms result in excited atoms

which do not become ions. When these atoms return to lower energy levels they emit

radiation (seen as the bright glow of the plasma arc), some of which deposit energy back

in the cathode walls, some of which is adsorbed by other particles of the plasma. Some

radiation not adsorbed by other particles does not impact on the cathode wall, but a

certain fraction of the total radiated power directed upstream out of the thruster and lost

to the system – these events appear as energy losses to the system as no useful action

(thrust, heat, etc) can be gained from them (with the possible exception of finding your

cathode in the dark). If the plasma is optically thick, then this radiation from de-excitation

will be absorbed back into the plasma. An excited atom then has a probability (as a

function of time) of decaying to a lower energy level, however if the amount of time that

an atom remains in an excited state is of the same order as the electron neutral collision

frequency, the excited atom has a high probability of further excitation, a process which

will eventually yield an ionization event. This further contributes to multi step ionization.

Examining the relative contributions to the total rate of plasma generation made

by both single collision and multi-collision processes can yield valuable insight. Consider

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when the electron temperature is much less than the ionization energy of the neutral

atom, and the neutral species speed is much less than the electron speed. The equation for

the direct ionization (single collision) rate coefficient as a function of electron

temperature is then [22]:

{ }( )

ie

4heavye

e o o 22e i o

8 ,4

Ti

Z qqTk T em

ε πσ σ

π ε πε

= = (2.3.1)

Where Zheavy is the number of valence electrons in the heavy species particle, and σo is

approximately the geometrical atomic cross section, of the neutral heavy species atom

(the electron temperature is in units of electron Volts).

Now, in the same plasma, consider ionization via a multi-step (stepwise) process.

The equation for the stepwise ionization rate is expressed as:

{ }( )

ie

e

10s eii e 5 3 3

o o

14

Tm qgk T eg h T

ε

πε

−⎛ ⎞≈ ⎜ ⎟⎜ ⎟

⎝ ⎠ (2.3.2)

Where g and h are the statistical weight and Planks constant, respectively.

A comparison of the direct ionization rate coefficient to the stepwise rate

coefficient yields:

{ }{ } ( ) ( )

7 7 / 22s 2 4 4i e i o e e

2 22i e o o ee o o

,4 4

k T g a m q m qI Ik T g ThT hσ πε πε

⎛ ⎞ ⎛ ⎞≈ ≈ ≈⎜ ⎟ ⎜ ⎟⎜ ⎟ ⎝ ⎠⎝ ⎠

(2.3.3)

This relation shows that in plasmas with electron temperatures low in comparison

to the first ionization energy of the neutral atom, the step-wise ionization process will

dominate. When Te ≈ εi both processes are significant contributors to plasma generation,

and when Te >> εi the direct ionization process will dominate. Thus for the type of

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26

plasma considered in hollow cathodes, where electron temperatures in the range of 1 to 5

have been reported, the coefficient ratio can range from 50 to 104, The step-wise

ionization rate is thus several orders of magnitude more significant than the direct

ionization rate. The stepwise ionization rate coefficient can then be calculated from:

{ }{ }

ie

7 / 2si e

i e e

7 / 2 7 / 2s ei i o

e e e

8 T

k T Ik T T

qTI Ik k eT m T

ε

σπ

⎛ ⎞≈ ⎜ ⎟

⎝ ⎠

⎛ ⎞ ⎛ ⎞≈ ≈⎜ ⎟ ⎜ ⎟

⎝ ⎠ ⎝ ⎠

(2.3.4)

The total rate of ionization is:

ie

7 / 2 7 / 2Total s ei i i i o

e e e

81 1 TqTI Ik k k k eT T m

ε

σπ

−⎡ ⎤ ⎡ ⎤⎛ ⎞ ⎛ ⎞⎢ ⎥ ⎢ ⎥= + ≈ + ≈ +⎜ ⎟ ⎜ ⎟⎢ ⎥ ⎢ ⎥⎝ ⎠ ⎝ ⎠⎣ ⎦ ⎣ ⎦

(2.3.5)

Where for Argon, we have σo = 1.9x10-21m2.

The final ionization rate, or the number of positive ions created per second per unit

volume, is given by:

i

Totaln e e,n u u kν σ σ= = (2.3.6)

Gas 1st Ionization energy (eV) 2nd Ionization energy (eV)

Argon 15.76 27.64 Lithium 5.39 75.67

Hydrogen 13.59 - Xenon 12.13 21.22

Table 1. Ionization energy for common electric propulsion propellants

The energy of the electrons is determined by the acceleration through the sheath

field plus initial thermal energy determined by the cathode wall temperature, thus the

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region of cathode wall supplying single event ionizing-capable electrons is tied to the

axial profile of the radial potential drop of the sheath. Table 1 lists the first and second

ionization energy for several types of propellants commonly used in electric propulsion.

Defining the IPC as the region of interior cathode volume containing the plasma

and the plasma’s attachment to the cathode walls, and considering only single collision

ionization, we can say that the IPC is therefore set by the region of the cathode wall(s)

where the sheath voltage profile is above this minimum determined by the gas properties.

Contributions to the ionization process made by the high energy electrons contained in

the tail end of the electron energy distribution function will set this minimum sheath

voltage somewhat lower than the ionization energy of the propellant gas. Where the

sheath voltage drops below this minimum should be the end (or very near the end

considering both high energy thermionic electrons in the tail end of the distribution, and

some upstream diffusion) of the active zone or region of plasma generation - thus with

the limits of ambipolar diffusion in a high speed neutral flow [8], this provides an upper

limit to the length of the IPC. If a model can accurately predict the profile of the sheath

drop, this will provide a prediction of how far the plasma will penetrate into the hollow

region.

Now, if one also considers setp-wise (multi-collision) ionization, the IPC can be

extended a significant amount further upstream into the cathode, as individual electrons

no longer need energy equal to the ionization energy of the neutral gas. It is important to

note that this thesis work does include contributions made by both direct ionization, and

multi-step ionization events. In experiment we observe the IPC to penetrate much further

into the cathode than the point at which the sheath drop equals the ionization energy of

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the working gas, thus the role of the multi-step excitation and ionization process is

significant and must be included.

The nature of the IPC is both a cause and consequence of the cathode

temperature, which depends upon many factors but in summary is determined by an

energy balance between all processes (plasma related and otherwise) heating and cooling

the cathode. From the plasma, energy is brought to the cathode by ions (mostly single

ions, and a small number of double ions) and (reverse) electrons. The ions are naturally

attracted to the cathode, and it is assumed that all ions which enter the sheath region will

strike the cathode wall after falling through the attractive sheath drop. Each ion strike

deposits a certain amount of heat in the cathode wall, proportional to the sheath drop

(with the assumption of positive singly charged atoms only).

{A note on nomenclature, particles in the central region of the cathode which

covers all volume except the sheath region, are termed bulk plasma particles. Particles in

the sheath region are termed sheath particles, and electrons thermioniclly emitted from

the hot cathode wall are termed beam electrons.}

For electrons, the sheath drop is repulsive, and thus in order to reach the cathode

surface, plasma electrons are required to have an energy higher than the sheath drop. If

we assume a Maxwellian distribution of thermal (bulk plasma) electrons, we can note the

following: Once the bulk plasma electrons undergo many collisions they will have

transferred most of their energy to ions and neutrals, and thus on average do not posses

the required energy to reach the surface. After a certain number of collisions the electrons

are said to be thermalized, and will attain some local average electron temperature below

the 1st ionization potential of the working gas.

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Assuming the electrons in the IPC have a Maxwellian distribution, it is only the

high-energy tail end of the distribution which can overcome the sheath drop and strike the

cathode wall. It is only the high energy electrons which are within a single mean free path

of the boundary between the sheath and the main plasma which are of importance here,

since any electrons further away will undergo a collision leading to reduced energy and a

speed in a different direction. Sheath models are usually assumed to be collisionless

regions.

As the sheath drop increases, electrons entering the bulk plasma have more pre-

collision energy, thus once they become thermalized they are hotter (as compared to a

lower sheath voltage). The average thermal electron temperature is therefore higher as

one approaches the cathode exit.

The main source of cathode cooling has been shown to be thermionic electron

emission to the plasma [26]. A less significant amount of cooling is provided by neutral

recombination on the surface, whereby an electron from the wall will combing with an

ion adsorbed on the surface, releasing energy equal to the material work function plus the

temperature of the wall. Once a cathode has reached steady state operation, a balance will

have been achieved between the heating and cooling processes, therefore models which

fail to accurately capture the nature of these processes will result in inaccurate

temperature predictions.

Experimental work [18] has shown that the magnitude of the sheath potential drop

inside a SHCH can vary greatly with axial distance from the cathode exit. This range of

potential drop across the sheath (for a given geometry and gas type) is related to the mass

flow rate and the discharge current. The total cathode drop begins near the cathode exit,

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and ends at the potential of the cathode wall itself. Between these two boundaries the

sheath and pre sheath drop is across the IPC, and can be approximated as purely axial

along the cathode centerline, and purely radial near the wall (see Figure 12).

Effects of Mass Flow Rate on Plasma Conditions

Experiments have shown that reducing the gas flow rate has the effect of

increasing both the IPC length and (within certain ranges of flow rate) the cathode

voltage drop [18, 9]. It is believed that this effect occurs due to the reduction of neutral

density which increases the beam electron mean free path and reduces the electron-

neutral collision frequency, thus fewer ionizing collisions will occur for a given volume

and given electron emission current off the surface. The mean free path, and electron

neutral collision frequency are given by:

λ =

1nnσ en

=1

nnπdn2 2

(2.3.7)

νen =

nne2

mη (2.3.8)

In order for the discharge to maintain the same current it must compensate for this

loss of available charge carriers and increased electron mfp. Consider two possible results

which can occur next:

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A. Increased current density from the same emission region (to increase the

likelihood of electron-neutral collisions)

B. Increased attachment area (emission region).

If the discharge current is below the level required for the plasma to be fully ionized, and

the discharge voltage is such that each beam electron has at most (on average) one

ionizing collision, we can observe the following:

Upon closer examination of option A, note that increased current density from

constant emission surface area will require an increase in the sheath voltage. The larger

sheath drop will reduce the work function through enhanced Schottky effect, and give

added energy to ions impacting the surface, which will drive the temperature up. Both of

these effects will tend to drive the thermionic emission current density to higher levels. If

the sheath voltage is made high enough, beam electrons will exit with enough energy to

ionize two neutrals. As the energy of the electrons exiting the sheath increases, so does

the energy of the thermal electrons in the plasma, and thus a larger percentage of these

will have the energy necessary to overcome the sheath potential, strike the wall and

deposit even more heat. If the discharge current remains the same with a reduced flow

rate, the ionization fraction will increase.

Now let us examine possibility B, increased attachment area. Figure 12 shows the

effects of flow rate on the IPC length, and equipotential surfaces in the volume for

possibility B. It is reasonable to see that when the density decreases, the plasma faces less

opposition to diffusion further upstream - if the electric field penetrates further upstream,

the region of wall over which the minimum sheath drop required for ionization exists,

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increases. A larger surface area of cathode wall will now be emitting elections, with

energy levels above the minimum necessary for ionizing collisions, into a larger volume

of gas (with lower density due to reduced flow rate). These ions will deliver heat during

wall strikes, increasing the wall temperature, and the balance will be maintained. When

the electric field penetrates further upstream, the total cathode drop increases, and so does

the total discharge voltage, thus additional power is again required for the cathode to emit

the same current at the reduced flow rate.

Further, and more importantly, one must consider the contributions made by multi-

electron impact events on the ionization process. As shown by Mikellides et. al. [42], in

the internal plasma of an orificed hollow cathode flowing Xenon, the average electron

energy levels are well below the ionization potential for Xenon (as shown in Figure 13),

and thus the contribution of ionization through multi-step excitation can be significant.

This is particularly important in the cathodes of MPD thrusters, where the sheath voltage

drop can be as low as a few volts [26]. This is reasonable when one considerers that such

cathodes function within the range of continuum flow where the plasma is highly

collisional, and each neutral atom can expect to undergo many collisions during its time

in the cathode.

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Figure 12 Equipotential Lines for flow rates, low (a), moderate (b), high (c) [18]

Figure 13. Computed electron temperature in an orificed hollow cathode [42]

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As the density in a cathode decreases, the frequency of electron impacts on an

individual atom decreases. From this we can extrapolate that ionization via a multi-step

excitation process due to collisions with many low energy electrons is less likely, and

thus to maintain ionization, higher energy electrons are necessary (each electron must

bring more energy to the collision). The smaller the collision frequency, the larger the

necessary average electron energy. Since it is acceleration through the sheath voltage

which provides energy to the electrons, the average electron energy increases with sheath

voltage, which itself increases with the total voltage drop for the discharge and hence the

power consumed by the discharge. From this view of the multi-step excitation process, it

is easy to understand the relation between plasma density and cathode voltage. This

process plays a key role to understanding the relationship between the power consumed

by the discharge and the plasma density inside the cathode.

As nature would have it, the increase in discharge voltage necessary for an

increased plasma penetration depth is lower than that for constant plasma penetration

depth and so scenario B is the one observed in experiment. Again, this is linked to the

contribution made by the multi-step excitation and ionization process for lower energy

electrons. Modeling of this phenomenon is clearly a complex and detailed problem, with

other processes not described in this simple thought model. Mathematically, these

phenomenon are detailed in the model contained in chapter 6.

The plasma will maintain the discharge by whatever means consumes the least

amount of power - since the means by which this occurs has been experimentally

determined, what remains is to capture these trends in a predictive model. Previous

experiments [18, 9] with gas and Lithium fed SCHC’s have shown that an increasing

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discharge voltage and IPC length correspond with decreasing flow rate. This correlation

was first reported by Delcroix and Trindade [18] with gas cathodes, and again later by

Cassady [9] while working with Lithium, though none of the researchers offered detailed

explanation to the relation. A decrease in discharge voltage with increasing flow rates is

also seen in orificed hollow cathodes, along with the transition from “spot mode” to

“plume mode” (though it should be noted that comparison between orificed hollow

cathodes and SCHC’s have inherent inaccuracies due to the complexities which arise

from the presence of the orifice plate). Adding further complications the understanding,

Cassady’s experiments also had to contend with the deposition of Lithium on the cathode

surface, reducing the work-function.

If the flow rate is reduced to the point at which it becomes free molecular, then

one must consider the probability of an excited neutral atom leaving the cathode before

being further excited to ionization. In this case the ion neutral collision frequency will be

reduced, and thus the probability decay rate of an excited atom may not be comparable

with its resonance time within the cathode, or the excitation-collision frequency. Thus the

presence of electrons capable of ionizing in a single collision event become necessary,

which required a larger cathode voltage drop. Further, any excited neutral atoms which

leave the cathode are effectively “lost energy”, causing an increase in the demand for

energy in the IPC which translated to a higher electron temperature through larger sheath

voltages (and lower discharge efficiency).

To date there are no SCHC models available which accurately describe the

relation between discharge voltage, flow rate and IPC penetration depth. This work

intends to provide substance towards a more comprehensive model of the IPC, both

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qualitatively and quantitatively, and to determine the IPC properties for given operating

conditions (current, mass flow rate, cathode geometry, gas and material properties). If the

plasma attachment area can be increased, the cathode temperature can be reduced by

reduced surface current density. The focus of this work is on determining the total

penetration depth of the IPC, the distribution of the internal plasma and its properties

(plasma density, temperature, and potential, as well as properties of the neutral gas) with

the intention of optimization for long cathode lifetime.

IPC Control Parameters and Experimental Observations

Experimental observations recorded by previous hollow cathode research has

yielded several universally accepted conclusions [9, 18], the most significant among

these are:

1. Increasing mass flow rate decreases IPC penetration depth.

2. Increasing cathode diameter increases the IPC penetration depth.

3. Peak cathode temperature is weakly dependent upon mass flow rate.

4. An MCHC has a lower discharge voltage than a SCHC while operating at

identical discharge current and mass flow rates.

5. Discharge voltage decreases with increasing mass flow rate.

6. Discharge voltage decreases with decreasing cathode diameter.

7. Discharge voltage decreases when the plasma is confined (such as with a

magnetic field)

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It is important to note here that previous works have noted these observations, but have

not produced qualitative theory to explain the governing mechanisms at work. To such

end, it is helpful to identify overarching trends in the data, from which larger insights can

be drawn.

For bullets 5 and 6, notice that if the mass flow rate is increased the flow becomes

more collisional, additionally if the cathode diameter is decreased (reducing the cross

sectional area through which the gas can flow) the flow density will increase also leading

to more collisions. Additionally, increasing the cathode diameter and thus the cathode

exit area, increases the loss of de-excitation caused radiation from the IPC to the exterior

region. This loss of radiation that would have been otherwise recaptured by either the

plasma or the cathode walls, is an additional energy loss from the system. Plasma

confinement (bullet 7), such as that caused by the magnetic field of an applied-field

thruster will also cause a more collisions by retarding diffusion. Noticing these

previously reported trends one can extrapolate that operating conditions which cause the

flow to be less-rarefied / more-collisional will decrease the discharge voltage (for a given

current thus increasing the discharge efficiency). More is presented on this notion in the

final chapter of this work. This is an important relation, because the discharge efficiency

is directly proportional to the discharge voltage.

Flowing the same amount of gas through a MCHC requires gas movement

through many channels much smaller than a corresponding SCHC, thus the flux of flow

will increase (equal mass flow over reduced total cross sectional area, comparing cathode

of equal inner diameter). This means that the channel will, on average, have a higher

density (more collisional) flow than the corresponding single channel. Thus, for the same

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discharge current and mass flow rate the MCHC would be expected to operate at a lower

discharge voltage - a relation that has been experimentally observed [9].

An understanding of the ionization process inside the hollow cathode is key to

predicting the efficiency of the system. This is because the ionization frequency of the

neutral atoms is very sensitive to the electron energy (temperature), which is determined

(largely) by the sheath voltage drop. The larger the voltages required for the ionization

process, the less efficient the discharge because the power consumed by the discharge is

of course directly proportional to the total voltage.

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Chapter 3: History and State of the Art

3.1 Historical Related Research

MPD thrusters evolved from arcjet thrusters, and thus historically have used

gaseous propellants, indeed early literature labels the devices as “MPD-Arcjets”. Initial

research yielded promising performance in the way of produced thrust and Isp, though

these thrusters were plagued by low efficiencies. Since the 1950’s many different groups

have conducted research into MPD/LFA thrusters using a variety of different propellants,

including Argon, Helium, Nitrogen, Lithium, Hydrogen and Ammonia among others. A

brief list of MPD research groups is presented in table 2.

It was eventually realized that cathodes are the major life limiting component of

MPD thrusters, and so a large percentage of the available literature is naturally devoted to

the study of cathodes. A brief review of notable past research into MPD and cathode

research is presented, covering work by Delcroix, Polk, Goodfellow, MIA/ Tikhonov,

Mikellides, and Cassidy.

1) Delcroix – University of Paris [18]

Pioneering work on hollow cathodes was conducted at the University of Paris by

Delcroix and Trindade [18] in the 1970’s. This is the first extensive study involving

MCHC’s and was largely experimental in nature, reporting mostly qualitative

observations. Delcroix et al. experimentally demonstrated that when compared to a single

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NASA-Jet Propulsion lab NASA-Glenn/Lewis research Center

AVCO-Everett Los Alamos National labs Moscow Aviation Institute

McDonnell Douglass Corporation Osaka University

University of Stuttgart Tokyo University

Princeton University University of Illinois Ohio State University

Massachusetts Institute of Technology USAF

United States of America United States of America United States of America United States of America

Soviet Union United States of America

Japan Germany

Japan United States of America United States of America United States of America United States of America United States of America

Table 2 . MPD thruster research groups

channel cathode operating at the equivalent discharge voltage and flow rate, separation of

the gas flow through a multichannel cathode would divide the current load over the

channels, reduce the overall discharge voltage and the operating temperature of the

cathode. This research also experimentally showed the reduction in discharge voltage

accompanying an increase in the working gas density.

This research was the first to introduce the notion of an active zone of the cathode,

in which most of the ionization was predicted to take place. This corresponds with the hot

spot, the location of peak surface temperature where thermionic electron emission is

greatest. Peak surface temperatures were measured and noted to occur at locations

upstream from the cathode exit plane – distance upstream was shown to be controlled by

the mass flow rate. Several regimes of operation were noted, including Normal (N), Low

Gas-Flow (LQ), Low-Current (LI) and High-Pressure (HP) regimes.

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2) Polk – NASA-JPL/Princeton University [54]

Jay Polk conducted high current cathode research at JPL/Princeton University in

the early 90’s, focusing his efforts on development of an understanding of the methods

controlling cathode material reduction. Polk developed code modeling the migration and

erosion of cathode material with temperature dependency. This work examined in detail

the temperature driven process of cathode surface material evaporation, identifying the

initial phase of the discharge ignition as the most destructive.

This work built on previous research predicting that starting a “cold”, non-

electron emitting, would cause the formation of many micro spots on the surface, which

supplied electrons to the discharge via a combination of enhanced field emissions and the

evaporation of small amounts of surface material. This process continues, depositing heat

to small surface area regions of the cathode until a suitable surface temperature is

reached, and the electrons necessary to sustain the discharge can be provided by

thermionic emission. This provides a basis of predicting reliable cathode lifetime if one

can accurately predict the operating temperature profile.

3) Goodfellow – NASA-JPL/University of Southern California [26]

Also in the late 80’s/early 90’s, Keith Goodfellow conducted experimental and

theoretical research into high current solid rod cathodes in gaseous propellants at Purdue

University, and later at JPL/University of Southern California. This work provided

reasonable temperature prediction ability for MPD thruster solid rod cathodes, including

plasma/sheath modeling and cathode temperature distribution.

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Although this work focused exclusively on solid rod cathodes, a detailed 1-

D/phenomenological model of the plasma sheath was developed to study interaction

between the cathode surface and the plasma. Much insight can be drawn from these

understandings and translated to the study of plasma interaction with hollow cathodes on

the basis of similarity in both geometry and fundamental processes. This work provides a

basis of the IPC phenomena description and qualitative sheath model contained in the

current research.

Goodfellow identified the major sources of heat deposition and rejection for hot

cathodes, along with their relative significance as a function of surface temperatures.

Experiments showed that the peak surface temperature was not strongly dependant upon

gas flow rate, but was strongly dependant upon discharge current. Further work

demonstrated the total surface area of plasma attachment to the cathode would increase

with decreasing mass flow rate, along with a peak temperature located at some distance

upstream from the cathode tip.

4) Moscow Aviation Institute [65]

In 1994-1998 the Moscow Aviation Institute (MAI) conducted the first extensive

testing of a Li-LFA (Lithium propellant Lorentz Force Accelerator) with a MCHC,

testing several cathode designs, under the direction of scientific supervisor Victor

Tikhonov. This work was performed with the support of Princeton University and

NASA-JPL, and was limited largely to experimental research. The MIA experiments

yielded a qualitative feel for more optimal MCHC design - testing of 6 different cathode

geometries were reported along with performance and arc attachment dependency upon

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design. The experiments included development and testing of 3 different thrusters, a 30

kw, 150 kw, and 200 kw – all three were applied field thrusters.

MIA testing also included introducing additives to the flow of Lithium propellant

- significant reduction in material erosion was reported during experiments in which an

amount of Barium was introduced into the discharge. It was predicted that the Barium

atoms would deposit themselves on the cathode Tungsten, and this layer would reduce

the work function. These predictions were verified when it was shown that the cathode

operating temperature showed noticeable reduction during the Lithium + Barium runs

while operating at equal discharge current, compared to the Lithium only runs. Because

the Barium was heated and vaporized at an uncontrolled rate, it was not possible to obtain

a detailed model of the effects of Barium addition from the data generated by the MAI

experiments.

5) Mikellides – NASA-JPL [42]

In the early 2000’s, the Advanced Propulsion Concepts group at NASA’s JPL

began developing a detailed computational theory regarding the plasma and erosion

processes of an NSTAR traditional hollow cathode. As part of this program, and based

upon previous efforts conducted at Ohio State University, Ioannis Mikellides developed

the IROrCa2D (Insert Region of an Orificed hollow Cathode) code modeling the plasma

properties inside an NSTAR cathode, and later the IROrCa2D evolved OrCa2D code

modeling the NEXIS cathode. IROrCa2D is a 2D-axisymmetric time independent code

that models plasma and neutral gas interaction in the emitter region of a low current

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Figure 14. Active MCHC with Lithium -Barium mixture, photo from reference [65]

Figure 15. Active MCHC with Lithium only, photo from reference[65]

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orificed hollow cathode with Xenon propellant. Large portions of work described in this

thesis have origins in the model in the IROrCa2D code.

6) Cassady – Princeton University [8]

Leonard Cassady working in the early-mid 2000’s at Princeton University’s Electric

Propulsion and Plasma Dynamics Lab, conducted a study of single and multi-channel

hollow cathodes using Lithium Propellant, influenced heavily by the MIA work of the

previous decade. Although this work relies upon the somewhat imprecise approximation

of the IPC modeled as block of uniform plasma with constant properties, created by the

electron emission of the surrounding cathode wall assumed to be at uniform temperature,

it never-the-less correctly predicts trends in the cathode voltage, temperature profile and

ionization fraction as a function of current, Lithium flow rate and cathode channel

diameter.

Note that as of this writing, the research at MIA and Princeton University are the

only relevant studies of a MCHC operating in an high power Li-LFA system

environment, and are considered the current state-of-the-art in the field.

3.2 State of the Art – MCHC’s and LFA thrusters

The current state of the art in MPD-type thrusters is the Lithium propellant (with

Barium addition) self-field LFA with a multi-channel hollow cathode, such as those

designed in the MIA study of the mid 1990’s, termed the Li-LFA [35, 1, 56]. The best

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data point thus far (for an applied field thruster) is for a Lithium fed LFA operating at 69

percent (thrust) efficiency, 5500s Isp, thruster power of 21 kW, Lithium flow rate of 10

mg/s, and an applied field of 0.24 T – this thruster used a conical rod shaped cathode

[35]. Although this represents the best performance (from an efficiency and Isp point of

view), this lacks the most advanced system components, specifically the cathode design,

and thus is not considered SOA.For comparison, the best performance date for a Li-LFA

with a multi-channel hollow cathode is the 200 kw MIA thruster, which ran at ~ 50

percent efficiency and 4200s Isp, with 192.7 kW discharge power [13].

In 2003 the Advanced Propulsion Technology Group at NASA-JPL was

continuing efforts on a 0.5 MW class self-field Li-LFA [56] and associated testing

facilities, designed as follow on studies to the MIA/Princeton work of the 1990’s. This

work at JPL was funded under the Advanced Propulsion Concepts (APC) program and

had been the slowly continuing efforts of Goodfellow and Polk for several years.

Unfortunately the APC program was cut from the NASA budget later that year.

In 2004-5 two proposals were made by the group for Li-LFA’s, a 250 kW applied

field and the 0.5 MW self-field (shown in Figure 16), both of which were awarded under

Project Prometheus, NASA’s plan to begin using Nuclear Electric Propulsion systems for

deep space robotic exploration. This work was intended to advance the technology

readiness level (TRL) of the Li-LFA from TRL-4 to TRL-5. A large part of this research

was to focus on MCHC issues, however shortly after the award was made for the 0.5 MW

thruster, it was retracted. The 250 kW thruster (termed the Advanced Lithium-fed

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Figure 16. Schematic view of 250 kW Li-LFA, ALFA^2, [13]

Figure 17. Improvements over SOA, reference [13]

Applied-field LFA, or simply ALFA2, or “Alpha Squared”) funding was continued with

Princeton University as the lead investigating organization, but was reduced to half of the

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originally awarded level. Target performance for ALFA2 was 60 to 63 percent efficiency,

6200s Isp, and >3 years of reliable lifetime - respectively the efficiency and Isp

performance goals represented 30 and 46 percent gain over SOA (the MIA 200 kW

thruster) [13]. The Phase 1 study was completed in mid 2005, although by that time many

NASA programs found themselves competing for funding with the more visible

components of the new VSE (namely design and construction of the Crew Exploration

Vehicle, CEV). The EP components of project Prometheus were canceled in late 2005, all

related research was shelved and Prometheus itself was effectively ended.

By late in the fall of 2005, NASA HQ had received many complaints regarding the

cancellation of project Prometheus, in particular many university research groups voiced

concerns noting the numerous graduate students who’s doctoral research was funded by

the program. In December, NASA decided to continue funding for the ALFA2 project at a

greatly reduced level and with the stipulation that the funds be used solely to support the

projects associated graduate students. Funding support would continue to the period of

one calendar year, and was termed “ALFA2 Student Soft Landing”. Consequently, the

ALFA2 cathode research was re-tooled and relocated from JPL to the University of

Southern California, and continues as the study in this paper. Other research funded by

ALFA2 Student Soft Landing continues at Caltech, Princeton, Michigan University and

WPI.

The phase 1 study and JPL’s proposed development of the 250 kW and 500 kW

Li-LFA with MCHC are considered the next development in SOA of MPD thrusters at

the system level, with the work done at MIA being the highest achieved level of MPD

thruster development.

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Figure 18. The six MCHC designs tested by MAI

The SOA of multi-channel hollow cathodes is somewhat harder to quantify, as

there has been little detailed research into these devices operating in the relevant

environments. Most of the relevant experimental data are results from the MIA studies of

the mid 90’s, during which Lithium fed MCHC’s were used at power levels up to 192.7

kW. Six different cathode geometries were tried, with the “optimized” design found

empirically, as shown in Figure 18. Though no comprehensive detailed theory governing

the operation of the MCHC exists yet, some experimental studies have been conducted,

yielding a phenomenological understanding of the devices [8, 9].

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Chapter 4: Role of This Doctoral Work

Objectives of the doctoral work (both theory and experiment) are as follows:

Experimental Goals

1. Construction of test facility for the conduction of hollow cathode experiments,

with Argon as the working medium, at discharge power levels up to 2kw.

2. Generation of experimental data correlating IPC properties with cathode design

and discharge operating conditions. IPC properties of specific interest are:

Electron and ion temperature, plasma potential, plasma density all at the cathode

exit plane.

3. Generation of experimental data correlating cathode temperature profile with

cathode design and discharge operating conditions – specifically an axial

temperature profile of the exterior cathode surface

4. Provide input boundary conditions for computational model.

Theory/Modeling Goals

1. Generation a 2-d axisymmetric computational model, predicting the distribution

profile of specific plasma properties in the interior region of a single channel

open-ended hollow cathode, which can be used in future extrapolation to model

multi-channel hollow cathodes, provide a quantitative understanding of the high

current SCHC arc-attachment phenomena, and provide input to models predicting

useful cathode lifetime. Plasma properties of specific interest are: Electron and

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ion temperature and density, plasma potential and density, neutral gas temperature

and density, current streamlines.

2. Verification of gained quantitative description of the arc attachment phenomenon

of a single channel of a MCHC, with the qualitative descriptions already existing

in the literature

3. Generation of a better understanding of the IPC distribution and its relation to

cathode lifetime, including effects on the efficiency of the operating cathode.

Overall, this work is intended to provide advancement to the understanding of the

cathode plasma arc attachment phenomenon. Specifically, the experimental data

generated in this study provides material for trend analysis of the performance of high

current hollow cathode arc in an MPD relevant environment. The theory effort of the

study is designed to be a starting point for the eventual development of a computational

model describing the workings of a multi-channel-hollow-cathode, for conduction very

high levels of discharge current through a plasma.

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Chapter 5: Methods

5.1 Theoretical Methods

Due to the similarities in both geometry and governing physics, a model of a

single channel open ended hollow cathodes is being developed by an evolution of the

IROrCa2D code developed by Mikellides at JPL. The IROrCa2D code was designed to

model the physics inside a low current orificed hollow cathode, with Xenon as the

working gas. These cathodes were used during NASA’s NSTAR program, and have been

flown on the Deep Space 1 mission (as both the main ion-engine plasma source cathode

and the neutralizer cathode) and as the ISS plasma contactor.

Though both the governing physics and geometry are similar, there are several

significant differences between the NSTAR cathodes and those in this study, which

require a reexamination of the assumptions made in deriving the equations used in

IROrCa2D.

The major differences between the two models are summarized:

1. Pressure. In the NSTAR hollow cathode, the orifice plate acts to impede the flow

of plasma and neutral gas from the emission zone, thus the total pressure gradient

inside the cathode is small enough to be considered essentially zero. This is a

close approximation to all space within the computation zone, with the exception

of the near orifice region. The IROrCa2D model uses the total pressure inside the

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cathode, experimentally determined user input number, when computing

densities. In the open-ended cathode, this is not the case, as there are no physical

barriers to the flow field (except the tube walls), thus the pressure gradient

becomes considerable. This mass flow rate pressure profile becomes a necessary

component of the new model.

2. Neutral gas dynamics. In the NSTAR cathode, the velocity of the neutral gas

particles is very low in comparison to the ion and electron velocities, and thus is

considered to be zero: ui,e >> un . This assumption is again tied into the concept of

a non-divergent total pressure and the neutrals can be considered relatively

stagnant.

In the open-ended cathode, we encounter a situation more similar to

ordinary tube flow, where the neutral gas has been shown to exit the cathode at

sonic speeds. In this case the velocity of the neutrals is no longer negligible, and

cannot be ignored in comparison to the ion and electron velocities.

The assumption of a neutral gas velocity equal to 0 led to many

simplifications in the derivation of the final form of the MHD equations, thus

causing a necessary revision of the governing equations when considering the

cathode under study.

3. Ionization fraction. The IROrCa2D model makes the assumption of a weakly

ionized plasma [42] in the emitter region – the NSTAR cathodes typically run in

the range of 6 to 12 Amps, and on the order of 10 sccm Xenon flow rate. These

numbers are typical for cathodes providing plasma to the discharge region of ion

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engines (low-current, high-voltage), however MPD thrusters are high current low

voltage devices, and ionization fractions approaching 100 percent are more

typical. The assumption that is made in IROrCa2D is nn + ne ≈ nn, and thus the

neutral gas density remains approximately constant throughout the computation

region.

Again, this assumption leads to simplifications in the derivation of the

final form of the MHD equations, thus causing a necessary revision of the

governing equations when considering the cathode under study. In the conditions

of this study, discharge currents up to 60 Amps were used to produce a

moderately ionized plasma. Further assumptions are made by assuming that the

ionization-collision frequency is small compared to other collision frequencies. In

the case of MPD plasma, ionization collision frequencies are much higher, which

must be accounted for.

4. Geometry. The geometry of the cathode under study closely resembles that of a

traditional (NSTAR) type hollow cathode, with the exception of the orifice plate

and the emitter. The geometry of a SCHC is that of a simple hollow tube, while

the geometry of the orificed hollow cathode is shown in Figure 3.

a. Orifice plate. NSTAR cathodes consist of a hollow tube with a plate

covering the down stream end, and in the center of this plate is a small

orifice on the central axis (dorifice << dcathode). This plate serves to restrict

the exit of the neutral gas from the emitter region to ensure that ionization

is more likely for any one neutral, thus obtaining higher propellant

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utilization efficiency. The orifice plate is absent in the open-ended hollow

cathode, and this must be incorporated into the computational model. To

this end, boundary conditions at the downstream end of the computation

region must be reexamined.

b. Emitter. NSTAR cathodes employ an impregnated porous Tungsten insert

within the emission zone, which stands between the cathode walls and the

plasma, and is the main source of thermionic emissions. Inside the pores

of the insert is a Barium Calcium aluminate source material, which during

cathode heating releases Barium and Barium-oxide particles into the

Tungsten pores. Once these particles migrate to the insert surface they are

adsorbed forming a thin layer of Barium and oxygen atoms which reduced

the surface work function allowing cathode operation at lower

temperatures. During NSTAR cathode operation, typical temperatures

experienced by the emitter can reach ~1,600K [53]. The common failure

mode for cathodes of this design is characterized by the inserts inability to

deposit further Ba and O atoms to replace those lost to evaporation. Time

to failure is largely a function of operating temperature. In IROrCa2D,

electron emission comes only from the insert, any emission from the

orifice plate or non-insert cathode walls is ignored.

Since MPD cathodes run much hotter than ion/hall cathodes, use of

an insert of the type described above is not practical due to significantly

reduced lifetime when heated to such extreme temperatures. Thus all

thermionic emission in MPD cathodes comes directly from the cathode

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material itself, in this case the walls of the hollow tube. Computationally

speaking, all surfaces emit. Further, it was decided to use pure Tungsten

cathodes rather than thoriated Tungsten to avoid issues related to

migration of thorium particles at high temperature [26].

5. Working Gas. IROrCa2D’s working gas is Xenon – there are several factors in the

code which are gas specific, including collision cross-section, collision and

ionization frequencies, thermal conductivity, etc. These all required updating to

the corresponding properties for Argon.

5.2 Experimental Methods

In this section is described the experimental equipment and methods by which

data was collected throughout the course of the research. Where appropriate, details are

given on experimental setup, design, and equipment descriptions including manufacturer

and model numbers. It should be noted that typically operating an LFA thruster with

chamber background pressures on the order of 10-3 torr and greater is considered to

produce unreliable data, particularly where thrust is concerned [35]. This is caused by an

unpredictable interaction between the background chamber atmosphere, and the plasma

exhaust plume which extends many anode diameters downstream due to the large

magnetic fields present in such devices. Since the flow rates of the cathode under study

are relatively high, this produces a high interior cathode pressure – for all factors of

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consideration in this study, as long as the condition of Pcathode >> Pchamber is maintained,

that is interior cathode pressure is large compared to the chamber pressure, no adverse

effects are expected on cathode performance. In such flow regimes, a “sonic condition” is

created at the cathode exit which prevents the chamber atmosphere from having any

significant interaction with the IPC. In addition, the present research is not concerned

with thrust measurements, thus the objectives of the experiment are not expected to be

sensitive to the chamber background pressure; this correlation has been experimentally

verified by previous researchers [7]. In practice, the flow inside the cathode ranges from

continuum to transitional, thus the conditions at the exit are more complex then simple

sonic conditions of a continuum flow, however the effect of limiting chamber atmosphere

interaction with the IPC is the same.

The experimental section of this work was conducted in a 12 in by 12 in

cylindrical vacuum chamber, connected to a single roughing pump. The chamber and

much of the experimental equipment are bolted to the top of a 4 ft by 6 ft optical bench,

under which resides the vacuum pump, high current power supply and a Neslab Coolflow

CFT-33 water chiller used to cool the anode. Typical chamber operating pressures are in

the 10’s of mTorr range. Although state of the art LFA thrusters use vaporized Lithium

propellant, when this work was moved from JPL to USC, it was decided that the added

complexities involved in safe handling, pumping, component cleaning, and safe disposal

of Lithium and its reaction products were beyond the resources available to this study. It

was for this reason that Argon was used for all experiments. It has been shown that

information and models derived from studies conducted with Argon propellant are easy

applied to Li-LFA’s.

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The high voltage starter supply is a “home built” plasma discharge device,

constructed by Robert Toomath at JPL in 1985 for MPD testing. Its range is 0 to 850

Volts, and 0 to 4 Amps (during plasma discharge), with a peak power output of 1.2 kW.

Three high current power supplies were used during the course of the research. The first

was a Hewlett Packard model Harrison 6475A DC power supply, with a range of 0 to 110

Volts, and 0 to 100 Amps; the second a Miller, Gold star 400SS constant current DC

welding power source. The third power supply was used during the acquisition of much

of the data, a EMS 10-250 from Lambda. All electrode components were custom made.

The entirety of the vacuum side components were mounted to the chamber door, which

was attached to a linear slide allowing the entire experiment to be removed from the

Figure 19. Vacuum chamber w/ door open – early iteration of cathode setup

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chamber permitting 360 degree unobstructed access to the vacuum side equipment. An

early iteration of the internal chamber experimental setup clearly showing the cathode

and anode arrangement can been seen in Figure 19, and in schematic form in Figure 22

and in Figure 23.

The anode was a Copper cylinder measuring 2.55 inch long by ~2.0 inch inner

diameter. Brazed to the anode exterior is a helical coil of Copper tubing, through which

water flows to an exterior air cooled chiller stored under the optical bench - this was

designed to remove excess heat from the anode and maintain an anode operating

temperature far below the melting temperature of Copper.

Figure 20. Vacuum chamber, side view

The numerical model developed requires experimental inputs, plasma data for

which much be collected at the downstream boundary: plasma potential and plasma

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density at the cathode exit plane were collected with a purpose built Langmuir probe, and

analyzed by oscilloscope. The propellant flow rate was measured with an MKS mass

flow meter. For measurements of the plasma potential and plasma density a Langmuir

probe was designed and employed. All chamber flanges and feedthroughs use ISO

standard Conflat connections or Klampflange connections. For temperature measurement,

a Leeds and Northrup disappearing filament optical pyrometer was employed.

Langmuir Plasma Probe

The Langmuir probe consists of Tungsten wire covered by a non conducting

ceramic tube, leaving only a few millimeters of the wire exposed to the plasma [11, 16].

The probe is attached to the end of a fast acting pneumatic linear actuator, which moves a

stainless steel shaft at a speed of 0.55 m/s a total of 500 mm. The linear actuator is bolted

to the center flange of the door, with the piston and control valve on the atmosphere side.

On the vacuum side is a set of stainless steel bellows, which seal the piston, and on the

end of which is the mounting plate that serves as the mechanical interface between the

linear actuator and the plasma probe. A small aluminum collar is bolted to the mounting

plate and the ceramic tube of the probe is slid into the collar and held in place with

setscrews.

The high speed of the pneumatic linear actuator is necessary to ensure a small

resonance time of the probe in the dense plasma region. If the probe were to remain in the

dense plasma for too long, it would become hot and being to thermioniclly emit electrons,

which would thus make it an “emitting probe” increasing the complexity of diagnostics.

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The characteristics of an emitting probe are somewhat different than those of a non-

emitting probe, and generally more complex to work with, and thus it was desirable to

avoid such a situation.

The probe is assumed to be a perfect absorber of all ions and electrons reaching

its surface, and any secondary electron emission due to interaction with the surface is

neglected. Further, it is assumed that the velocity of the electrons and ions at the edge

between the bulk plasma and the probe sheath can be accurately described by a

Maxwellian distribution. The surface of the probe exposed to the plasma has been sized

so that it may approximate (to a reasonable degree) an infinitely long cylinder.

Concerning Langmuir probe diagnostics, there are two approximation models commonly

used, the small sheath size approximation, and the orbital-motion-limited (OML)

approach, each appropriate to a particular regime in which one intends to probe

depending upon the relative size of the Debye length to the probe dimensions. Thus we

have:

p

D

p

D

Small sheath approximation: ~ 10

Orbital-motion-limited: ~ 3

r

λ

>

> (4.2.1)

The Debye length is given as:

o b eD 2

e

k Tn q

ελ = (4.2.2)

For the plasma in these experiments the Debye length was on the order of 10-6 m, and the

probe was sized such that the ratio of probe dimension to Debye length was~103 m, thus

the small plasma sheath analysis model is appropriate. The model centers on the fact that

the sheath surrounding any object in a plasma is on the order of a few Debye lengths in

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thickness. When the probe is introduced into the plasma, the total surface area over which

current will be collected will in actuality be the outer surface of the sheath, not that of the

probe. If the sheath thickness is small compared to the probe dimensions, the total surface

area of the sheath will be (to a good approximation) nearly identical to that of the probe

itself, allowing this difference to be ignored, and thus in computations the area of current

collection is the directly measurable/controllable area of the probe.

The construction of the probe consists of a single central Tungsten wire, 0.25 mm

in diameter, which is inserted in a ceramic cylinder with a center hole just slightly larger.

The end of the ceramic tube is sealed with Omega Bond, leaving 2 mm of exposed

Tungsten wire, as seen schematically in Figure 21. On the back end of the probe, the

Tungsten wire is crimped to shielded Copper wire, which is run to the to the oscilloscope

through a feedthrough in the chamber door. The ceramic tube is held in a small aluminum

collar (which is bolted to the vacuum side of the pneumatic piston) by a pair of set

screws. Several iterations of probe design were required to achieve a reliable device with

satisfactory performance, design changes guided by empirical results.

Figure 21: Construction of Langmuir probe end tip.

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The aluminum probe collar is bolted to the end of the vacuum side of the pneumatic

piston, and the whole plasma probe assembly is usually in a retracted position, as seen in

the schematic in Figure 22. In the retracted position, the probe tip sits 500 mm

downstream of the cathode exit plane, and on centerline. The pneumatic piston pressure

is set to ensure that the probe will travel the full extension in less than 1 ms. When the

piston is activated, the probe travels through the large cylindrical anode, stops at the

center of the cathode exit plane such that the exposed probe tip is bisected by the exit

Figure 22: Layout of vacuum side experimental components, Langmuir probe in

retracted position.

plane. Once in position (as seen in Figure 23), the bias voltage of the probe is pulsed

from 0 to 50 to 0 Volts relative to ground, at which point the probe collects current.

The pulsing of the bias voltage was done manually, with a single sweep of 0 to 50

Volts and back to 0 Volts. The maximum bias voltage necessary to cover the entire range

of electron energies necessary for a full analysis was empirically determined to be

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Figure 23: Layout of vacuum side experimental components, Langmuir probe in

fully extended position.

approximately 50 Volts. The current is measured by recoding the voltage drop across a

resistor through which the current flows – the resistor voltage drop, and the probe bias

voltage are measured and recorded by the oscilloscope. The data is stored locally on the

oscilloscope and later exported to PC for analysis. Once the pulse is complete, the probe

is retracted, with the whole event taking less 2 seconds to completion. Once this trace has

been accomplished, the bias voltage is reversed and the procedure is followed again, this

time the probe bias voltage is pulsed from 0 to -50 and back to 0 Volts, relative to

ground. This enables a complete profile of collected current over a bias voltage range of -

50 to + 50 Volts, relative to ground. To correlate the plasma reading to the potential of

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the electrode, the total discharge voltage and voltage of the cathode relative to ground are

recorded for each trace. The vacuum chamber is also at ground potential.

Figure 24: Electrical schematic of the Langmuir probe circuit.

As a result of the pulsing of the probe bias voltage, each side (polarity relative to

ground) of the trace will record data for the ramping up to peak bias voltage, and the

ramping down. A sample Langmuir probe trace is show in Figure 25. This “double trace”

can be see on the data recorded by the oscilloscope, and is most clearly visible for the

positive value of collected current. As the probe begins to collect current, the impact of

the charged particles on the probe will cause an increase in temperature. If the heat load

is high enough, the probe will then being to emit electrons thermionicly. This emission of

electrons will interfere with the collection of current from the plasma resulting in a net

collection of fewer electrons when biased positively, thus compromising the reliable use

of the probe.

This effect of reduced electron collection from a hot probe can be seen in the

positive bias portion of the trace shown in Figure 25. This section of the collected data is

ignored, and it is only the data following the classical “I-V” curve of Langmuir theory

that is analyzed (this is the upper potion of the data in Figure 25 for positive values of

Probe Bias Voltage). An additional example of a sample trace recorded form the

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Langmuir probe can be seen in chapter 7. The data for each pulse is recorded in separate

files, and combined during analysis. It this process which results in the irregularities seen

near the 0 Volts line in the plots.

bias voltage vs Ln of signal current

-10

-9

-8

-7

-6

-5

-4

-3

-2

-1

0-60 -50 -40 -30 -20 -10 0 10 20 30 40 50 60

Series1

electronretardationelectron saturation

Figure 25: Langmuir probe data trace, 2 mm Tantalum cathode, 100 sccm, 35 Amp

discharge. “Double Trace” effects of the voltage pulse are clearly visible

Cathode Stage

It is necessary to have a profile of the plasma potential and density at the exit

plane of the cathode – these numbers are experimental input for the numerical model and

serve as boundary conditions. For input to the IROrCa2D model, plasma measurements

were taken at only one location, on centerline at the orifice boundary. Measurements at a

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single location proved to be acceptable due to the size of the orifice in relation to the

computational domain. In the current study, the “orifice diameter” is in fact the diameter

of the entire cathode, thus it becomes necessary to obtain a more complete profile in

order to accurately represent the relevant plasma properties at the exit plane. To obtain

this profile, measurements at three different radial positions along the exit plane were

planned to be taken:

• Centerline, r = 0

• r = R/3

• r = 2R/3

The obtaining of these profiles were plagued with equipment failures during the

experiment. As a result, data was primarily taken on centerline (r = 0 ), with some

additional data gathered at the r = R/3 location. These difficulties are expanded upon in

the final chapter.

The probes movement is restrained to that of the linear positioner, and its

movement is parallel to the axis of the cathode. Due to the restraint it is necessary to

move the cathode assembly itself, while taking readings at the same spot in space with

the Langmuir probe. This is accomplished by mounting the cathode assembly to a 2 axis

stage, with one manually operated micrometer driven axis, only accessible from inside

the chamber, and one motor driven axis with external control. Prior to closing the

chamber the cathode is centered such that the probe will hit the center of the cathode exit

plane, on axis with the cathode. Once the chamber is closed, the stage can then be

repositioned horizontally on a single axis via the motor assembly. Due to the small size of

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the cathode, it is necessary to move the stage only a few millimeters to probe at the

desired locations.

The stage (without the cathode) assembly is shown in Figure 26. The anode is

mounted directly to the chamber door and is stationary.

Figure 26. Two-axis Stage to which the cathode is mounted

Optical Pyrometery

The chamber is oriented such that there is a window 3.75 inch in diameter at a 90o

angle to the cathode (and chamber) center line, allowing full observational access to the

full length of the cathode from outside the chamber. The eyepiece of the optical

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pyrometer is attached to a small stand to elevate it to level of the cathode, and is bolted to

the optical bench.

Temperature measurements are taken manually, at 2 mm intervals along the

whole length of the cathode, beginning at the exit plane and ending 40 mm upstream.

Figure 27. Chamber and optical pyrometer

The optical pyrometer and horizontal position assembly can be seen above in

Figure 27, in its physical relation to the chamber. The position assembly is activated

manually to obtain the desired translation of the pyrometer’s axial location along the

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cathode. The optical pyrometer used is a single wavelength Leeds and Northrup

Disappearing Filament Optical Pyrometer, model # 8622-C.

The pyrometer contains a filament of Tungsten which is superimposed over the

image of the object whose temperature is to be measured. A red notch filter in the

pyrometer limits the light passing through to 650 nm. The operator varies the current

passing through the filament until its brightness matches that of the target object, at

which point a reading of the temperature of the filament is made from the pyrometer,

which is the “brightness temperature”, Tb , of the target object. The pyrometer is

calibrated to display the effective blackbody temperature of the target object.

The target object is in reality an imperfect blackbody, often modeled as a

“graybody” with an emissivity less than that of a true blackbody (whose ε=1), and so a

correction must be made to account for the difference. “In effect, we ask the question,

“What temperature would a graybody (an imperfect blackbody) with emissivity ε require

in order to be as bright at wavelength = 650 nm as a blackbody at temperature Tb?” The

answer comes from the Planck distribution law. Equating the brightness of a graybody

with an equivalent blackbody we get” [40]:

2 2

grey5 5

b grey b brightness

2 1 2 1

exp 1 exp 1

hc hchc hc

k T k T

π ε πλ λ

λ λ

⎡ ⎤ ⎡ ⎤⎢ ⎥ ⎢ ⎥⎢ ⎥ ⎢ ⎥=⎢ ⎥ ⎢ ⎥⎛ ⎞ ⎛ ⎞⎢ ⎥ ⎢ ⎥− −⎜ ⎟ ⎜ ⎟⎜ ⎟ ⎜ ⎟⎢ ⎥ ⎢ ⎥⎝ ⎠ ⎝ ⎠⎣ ⎦ ⎣ ⎦

(4.2.3)

Solving for the temperature of the graybody we have:

greyb

grey,effective brightness

,

ln exp 1 1

hcT k

T

α α λαε

= =⎡ ⎤⎡ ⎤⎛ ⎞⎢ ⎥− +⎢ ⎥⎜ ⎟⎜ ⎟⎢ ⎥⎢ ⎥⎝ ⎠⎣ ⎦⎣ ⎦

(4.2.4)

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Where the actual emissivity of the target graybody object has been replaced with the

effective emissivity, to account for losses like the transmission factor of the vacuum

chamber window. At 650nm light, the emissivity of the Tungsten cathodes is taken as

0.37, the emissivity used for the Tantalum cathodes is 0.36 [2]. The transmission factor of

the quartz window is 0.93, thus the effective emissivity’s of the cathode are:

• Tungsten: εeff = 0.3441

• Tantalum: εeff = 0.3348

Cathodes

Several cathodes were used during the course of this research, varying in

geometries, construction and material. Initial facility shakedown tests were conducted

with Tantalum cathodes, measuring 57.2 mm long, 5.4 mm outer diameter and 0.5 mm

wall thickness – no data was recorded with these cathodes.

Four Tungsten cathodes were the center focus of the research, from which

discharge plasma measurements were made. These had the following dimensions:

• Cathodes A and B measured 60 mm in length, with a 6 mm inner diameter

and a 0.5 mm wall thickness.

i. Cathode A initial mass: 86.71 g

ii. Cathode B initial mass: 82.45 g

• Cathodes C and D measured 60 mm in length, with a 10 mm inner

diameter and a 0.5 mm wall thickness.

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i. Cathode C initial mass: 92.76 g

ii. Cathode D initial mass: 97.99 g

All Tungsten cathodes were electron beam welded to Molybdenum flanges measuring 6.1

mm in thickness and 38.1 mm in diameter. These flanges could then be bolted to the front

of a stainless steel mating flange as part of the gas feed assembly. The four Tungsten

cathodes constructed for this study were all manufactured by Ultramet, a refractory

metals processing house in Pacoima, California. The cathode fixtures consist of a

cylindrical tube of pure Tungsten electron beam welded to a mating flange of

Molybdenum.

When problems arose with the Tungsten cathodes, several smaller Tantalum

cathodes were employed to obtain the required temperature and plasma data. These

cathodes were all of identical geometry, measuring 38 mm in length, 3.22 mm outer

diameter, 2.0 mm inner diameter, 0.6 mm wall thickness with a 0.5 mm long taper at the

downstream end. The 10 mm diameter Tungsten, and 2 mm diameter Tantalum cathodes

can be seen in Figure 28.

Figure 28: 10 mm diameter Tungsten cathodes and 2 mm diameter Tantalum cathodes

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Signal Processing and Data Acquisition (DAQ)

In consideration of the large common mode voltages and high current of the arc-

ignition and steady state discharge phase, it was necessary to isolate all data and

measurement signals from the experiment to the data acquisition electronics. To this end,

inductive coupling was used to measure the discharge voltage, the discharge current and

the current from the Langmuir probe. The electrical schematic of the experiment can be

seen in Figure 29.

Figure 29: Layout of the power supply and diagnostic electronic systems.

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For measurement of the discharge current, a commercially available Rogosky coil

was employed with a straightforward connection to the DAQ equipment. Isolation and

measurement of the discharge voltage posed additional restrictions, specifically the

avoidance of measurement during the high voltage arc-ignition phase due to the

limitations of the measurement circuitry. An interlock switch on the ignition power

supply was installed to prevent the voltage interface with the DAQ equipment during the

ignition phase. A voltage divider reduced the arc voltage by a factor of 12.7, after which

a 1:1 V/V isolation amplifier provided the inductive coupling to he DAQ system. Plasma

probe data was measured and recorded with an oscilloscope, Tektronix model number

TDS 644A, 5 mhz with a max sample rate of 2 GS/s.

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Chapter 6: Single Channel Hollow Cathode model

6.1 Assumptions

Modeling begins with assumptions, the researchers speculations of valid

approximations, which closely describe the phenomena under study without undue or

adverse simplification. In the cathode and conditions under consideration in this work,

the generated plasma modeled as a quasi-neutral, highly collisional, highly ionized fluid

governed by the well-known magnetohydrodynamic (MHD) equations. The plasma is

understood to be composed of three particle species (neutrals, positively charged ions,

and electrons) of a single gaseous species (Argon), and modeled with a continuum nature,

not a rarefied flow (densities inside MPD thruster hollow cathodes reach 10’s of Torr,

and the mean free path is small in comparison to the cathode diameter, Kn ~ O 0.01).

Further, all heavy particles are assumed to be in thermal equilibrium, Tions = Tneutrals, and

Figure 30. Computational zone

L

D

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the neutrals are assumed to be slow in comparison to the charged particle, with electron

speeds much greater than ion or neutral speeds.

The region of the cathode in the computational model is shown in Figure 30, and

the computational zone extends axially from the cathode exit plane at the downstream

end, to some user defined distance L upstream, and radially to include all volume inside

the cathode diameter D, up to but not including the sheath (which is handled as a

boundary condition).

The mechanisms by which transport of mass, momentum and energy are

achieved, are all modeled as classical two body collisions, ion-neutral (i-n), electron-

neutral (e-n), electron-ion (e-i). Anomalous factors are not believed to play any

significant role in the transport processes and are not taken into consideration [42].

The choice of a fluidic approach is perhaps of some debate, and may call into

question the accuracy of the model predictions. The gas introduced through the cathode is

exiting to a much lower (chamber) pressure, and thus the flow becomes choked and

leaves the cathode at sonic speeds. Whether the gas is considered to be in free molecular

flow or continuum flow is determined by the Knudsen number (Kn), which is the ratio of

the particles’ mean free path (distance traveled between collisions with other particles) to

a characteristic length of the geometry in question (in this case, the cathode diameter).

particle b nn 2

cathode cathode n n 2k TK

D D P dλ

π= = (4.1.1)

As an example, for ground state Argon gas (atomic diameter = 1.76x10-10m) flowing

through a 6 mm diameter cathode, at 2,000 K and at a pressure of 10 torr, the Knudsen

number = approximately 2.5x10-2.

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For flows with a Knudsen number greater than 1, the flow is free molecular (rarefied),

and if the Knudsen number is less than 0.01, the flow is a viscous continuum. In the case

at hand, with Kn ~ O 0.01, the SCHC is operating exclusively in neither regime, but is in

the transitional flow regime between free-molecular and viscous continuum. Indeed in

practice, MPD SCHC’s operate almost exclusively in the transition regime. Since there

are no well agreed upon (or validated) transitional flow theories (and for hereditary

reasons), the author has chosen to model the flow as a viscous continuum. This is a

known shortcoming the in model, and improvements/modifications relevant to this issue

are left for future research. It should be noted that since, in practice, these devices operate

in a regime neither completely viscous nor rarefied, it may be permissible to describe

relevant processes by equations designed for either regime, depending upon convenience,

and maintain a reasonable degree of overall accuracy.

6.2 Governing Equations

Many authors have derived the equations governing the conservation laws of a

charged fluidic medium. These are the so-called Magneto-Hydrodynamic equations,

which macroscopically describe the motions of the particles in the fluid based upon the

Navier Stokes equations with the addition of electric and magnetic field terms arising

from the nature of charged particles. For reasons of compatibility with existing models,

the derivations here are based upon the work first presented by Braginskii [6], with the

noted assumptions.

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The plasma must obey the conservations laws, and is constrained by the

continuity equation for conservation of mass, the equation of motion for the conservation

of momentum, and the energy equation for the conservation of energy. In the derived

model, each species (electron, ion and neutral) is governed by its own set of conservation

equations, along with other equations describing the actions of charged particles in the

presence of an electric field. Equations of significance are boxed to highlight their

importance.

Conservation of Mass – Species Continuity Equation.

Conservation laws requires that N, the total number of particles in volume V, changes by

the flux of particles across the boundary of the volume, S, and the rate of sources + sinks

within the volume.

( )

V V surface

N ndV sources dV nu dSt t

∂ ∂∂ ∂

= = −∫ ∫ ∫ i (4.2.1)

From the divergence theorem we have:

( )Divergence Thm.

surface

ˆV

nu ndS nu dV←⎯⎯⎯⎯⎯→ ∇∫∫ ∫∫∫i i (4.2.2)

Substitution back into 6.1 yields:

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( ) ( )V v V

n dV sources dV nu dVt

∂= − ∇

∂∫ ∫ ∫ i (4.2.3)

Since this must hold for any arbitrary volume V, the argument of the integrals must be

equal, and thus we have the final form of the conservation equation:

( ) ( )n nsources nu nu nt t

∂ ∂= − ∇ → + ∇ =

∂ ∂i i (4.2.4)

There is a conservation equation for each species.

For ions we have:

( )ii i i e iz

n n u n nt

ν∂+ ∇ = =

∂i (4.2.5)

where

iz n iz en uν σ= (4.2.6)

For electrons:

( )ee e e e iz

n n u n nt

ν∂+ ∇ = =

∂i (4.2.7)

For neutrals; Note the sign change, when ions and electrons are born, neutrals are lost:

( )nn n e iz

n n nt

ν∂+ ∇ Γ = − = −

∂i , (4.2.8)

where ( )n n nn uΓ = , is the neutral particle flux.

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Conservation of Momentum – Species Equation of Motion

The most general equation of motion for any species ‘a’ colliding with species ‘b’,

including charged-particle collisions, in the absence of a (strong) magnetic field, is given

by:

( ) ( ) { }a aa a a a a a tensora

n um n u u q n E

t∂⎡ ⎤

+ ∇ = − ∇ ⋅ + ∇ ⋅ + Ω⎢ ⎥∂⎣ ⎦P Πi , (4.2.9)

( )

all otherspecies

aba-ba

m n uν⎡ ⎤Ω = − Δ⎣ ⎦∑ (4.2.10)

where the last term on the right hand side (Ω) is a summation over collisions with all

possible species and represents the gain/loss of momentum of particle ‘a’ colliding with

particle ‘b’ – thus for electrons, Ω describes the electron-ion collisions and the electron-

neutral collisions. mab is the reduced mass for a given pair of particles:

a b e hab ei ie e

a b e h

e h h h hen ne e in ni

e h h h

,

,2

m m m Mm m m mm m m M

m M M M Mm m m m mm M M M

= ∴ = = ≈+ +

= = ≈ = = ≈+ +

(4.2.11)

From here, the terms on the LHS are expanded:

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81

( ) ( ) ( ) ( )

( )

( )

aa

a a a aa a a a a a a a a a a a a

a a aa a a a a e,i a a a a

n

a aa a a

Dun

Dt

n

n u n um n u u m u n n u u u n ut t t

n Du Dum u n u n u m n m nt Dt Dt

n um n u

t

=

⎡ ⎤⎢ ⎥

∂⎡ ⎤ ∂ ∂⎢ ⎥+ ∇ = + + ∇ + ∇⎢ ⎥ ⎢ ⎥∂ ∂ ∂⎣ ⎦ ⎢ ⎥⎢ ⎥⎣ ⎦

⎡ ⎤⎢ ⎥∂⎛ ⎞= + ∇ + = ± +⎢ ⎥⎜ ⎟∂⎝ ⎠⎢ ⎥⎣ ⎦

∂+ ∇

i i i

i

i( )

{ }

aa e,i a a a a

n

aa a a a a e,i a a

n

and so

tensor

Duu u m n m nDt

Dum n q n E m nuDt

⎡ ⎤= ± +⎢ ⎥

⎣ ⎦

= − ∇ ⋅ + ∇ ⋅ + ΩP Π ∓

(4.2.12)

( ) ( ) ( )noting that: nuu u nu nu u∇ = ∇ + ∇i i i

Here a substitution of the general species continuity equation (for ions and electrons) is

made, it should be made particular note that the ionization term appears for plasmas not

fully ionized, and is often omitted by many authors for the case of low ionization

frequency. The ( )a aa a

Du u u uDt t

∂= + ∇

∂i term is the convective derivative, and accounts for

the changes in the fluid momentum due to localized changes, and the movement of the

fluid itself. {A note about the convective derivative: this represents the change in a fluidic

property with respect to time, in this case the velocity, in a frame of reference moving

with the fluid. Changes can occur due to the movement of the control-volume in which

the fluid element resides, or to more global changes that would occur even if the control-

volume were stationary. A useful example from reference [10] is “the density of cars near

a freeway entrance at rush hour. A driver will see the density around him increasing as he

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approaches the crowded freeway. This is the convective term ( )a au u∇i . At the same

time, the local streets may be filling with cars that enter from driveways, so that the

density will increase even if the observer does not move. This is the aut

∂∂

term. The total

increase seen by the observer is the sum of these effects.”}

The anisotropic viscosity tensor (∇ ⋅ Π ) accounts for stresses created by like-particle

interactions, which increases forces in each individual species-fluids. It is assumed that

these same-particle collisions do not give rise to significant diffusion, and thus the

anisotropic viscosity tensor term will be neglected for the charged particles. Also note

that the second term on the RHS is not a scalar, but P is the stress tensor for generalized

3D motion. The assumption of local thermal equilibrium is employed, so that the

distribution function (locally) is an isotropic Maxwellian, and thus the stress tensor can

be written:

P =p 0 00 p 00 0 p

⎜⎜

⎟⎟

, in which case the tensor can be replaced by a scalar times the unit

matrix, and a∇ ⋅ P becomes aP∇ , or the gradient of the local pressure, [10, 42].

Thus, for electrons, the steady state momentum equation becomes:

( )

( ) ( ) ( )

e ee e e e e e

e e e e e ei e i e e en e ee n

Du um n m n u uDt t

en E n eT m n u u m n u u m nuν ν

∂⎛ ⎞= + ∇ ≅⎜ ⎟∂⎝ ⎠− − ∇ − − + − −⎡ ⎤⎣ ⎦

i (4.2.13)

( ) ( ) ( ) ( )e e e e e e e e e ei e i e e en e ee nn m u u en E n eT m n u u m n u u m nuν ν∇ = − − ∇ − − + − −⎡ ⎤⎣ ⎦i (4.2.14)

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83

Likewise, for ions we have:

( )

( ) ( ) ( )

i ii i i i i i

hi i i e i ie i e i in i n h i2

Du uM n M n u uDt t

Men E n eT m n u u n u u M nuν ν

∂⎛ ⎞= + ∇ =⎜ ⎟∂⎝ ⎠⎡ ⎤− ∇ − − + − −⎢ ⎥⎣ ⎦

i (4.2.15)

( ) ( ) ( ) ( )hi i i i i i i e i ie i e i in i n h i2

MM n u u en E n eT m n u u n u u M nuν ν⎡ ⎤∇ = − ∇ − − + − −⎢ ⎥⎣ ⎦i

(4.2.16)

Again, for many situations (such as conventional hollow cathodes) the ionization

collision rate is so small in comparison to other terms, that the final terms on the RHS of

both of the above equations is often neglected. In LFA’s, the plasma is both highly

collision and highly ionized, and so the ionization terms must be included.

It is assumed that the acceleration of the plasma is achieved in regions exterior of

the cathode, and no substantial plasma acceleration takes place in the hollow region, thus

processes in the plasma inside that cathode are slow enough (in comparison to naνava,

recall the highly collisional nature of the MPD cathode plasma) that the inertia terms

( me uei∇( )ue → 0) can be neglected in both the ion and electron momentum equations.

Since we are interested in a steady-state condition, the second term in the convective

derivative is also 0. Following this, the final form of the steady-state momentum

equations can be expressed:

For electrons:

( ) ( ) ( ) ( )e e e e e e ei e e en e e iz i e e ei n e e en0 en E n eT u m n m n m n u m n u m nν ν ν ν ν= − − ∇ − + + + +

(4.2.17)

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and for ions:

( ) ( )h hi i i i e i ie h i iz i in e e i ie i in n0

2 2M Men E n eT u m n M n n u m n n uν ν ν ν ν⎛ ⎞ ⎛ ⎞= − ∇ − + + + +⎜ ⎟ ⎜ ⎟

⎝ ⎠ ⎝ ⎠

(4.2.18)

Combining the election and ion momentum equations yields:

( ) ( )e i e e e en e e iz

h hi i in h i iz n e e en i in

0 ...

2 2

P P u m n m n

M Mu n M n u m n n

ν ν

ν ν ν ν

= −∇ + − + −

⎛ ⎞ ⎛ ⎞+ + +⎜ ⎟ ⎜ ⎟⎝ ⎠ ⎝ ⎠

(4.2.19)

This equation will prove useful later in the formulation of the model.

For neutrals we must follow a slightly different thought path. Since the particles

are uncharged they are not affected by electric (or magnetic) fields, which can then be

neglected in the equation of motion, and thus the neutral particles obey the regular

Navier-Stokes equations describing fluidic motion:

( ) ( ) ( ) ( )

( ) ( ) ( )

n h n n n h n ni ni n i n ne ne n e n h iz n

n i

n e

hn h n n n h n ei n i n e ne e n h iz n

with ...

2

n M u u n eT n m u u n m u u n M u

u uu u

Mn M u u n eT n u u n m u n M u

ν ν ν

ν ν ν

∇ = −∇ − − + − +⎡ ⎤⎣ ⎦

∇ = −∇ − − + +

i

i

(4.2.20)

At this point we must consider how to evaluate the spatial gradient of velocity in

the convective derivative term. It can be a complex matter to numerically model the

neutral species behavior as described by the convective derivative, and thus it would be

desirable to neglect the term altogether. However, in order for this to be done, it must be

shown that the effects from this term are not significant when compared to the other

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85

terms in the momentum equation (as was the case for the ions and electrons). In

comparison to the collision terms we can write:

( ) ( )

( )

n nr z

n h n n n n

n h iz n iz n iz n

z r

n zn n

n nz

n h n n

n h iz n iz n iz

if , and then

1

u uu un M u u u u r zn M u u u

u uu uu u

z ru uun M u u z z

n M u u

ν ν ν

ν ν ν

∂ ∂+∇ ∇ ∂ ∂= =

≈∂ ∂∂ ∂

∂ ∂∇ ∂ ∂≈ ≈

i i

i

(4.2.21)

where we have assumed that the radial component of velocity is small compared to the

axial component.

The SCHC cathodes are in many respects a simple tube with a large L/D ratio.

The mass flow through the SCHC exits to the vacuum chamber at a pressure much lower

than is necessary to choke the flow and provide sonic conditions at the exit, which allows

us to use the equations for simple tube flow. However, as discussed in section 6.1, the

flow is transitional at the exit, and it is known that a simple sonic condition is not

accurate. From a transitional flow theory employed by Cassady et. al. [9] in description

of SCHC’s we can express the exit speed as a function of mass flow rate, exit pressure

and cathode temperature at the cathode exit, given by:

B cexit 2

exit h cPmk Tv

M rπ= (4.2.22)

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86

and from this we can gauge a maximum value for the axial acceleration of the

neutrals. For this discussion we will assume a cathode radius of 0.5cm, exit pressure of 1

torr with a mass flow rate of 0.05mg/s, and a cathode temperature of 2,500K. This yields

an exit velocity of:

( ) ( )

( )( ) ( )

25 -23

2B c

exit 2 2-26exit h c

kg m kg5*10 1.38*10 2500Ks s K m2,500 skgP 133Pa 6.64*10 0.005matom

mk TvM rπ π

− ⎛ ⎞⎜ ⎟⎝ ⎠= = ≅

(4.2.23)

If we assume a conservative cathode entrance speed of 10 percent of its exit speed, and a

cathode length of 5 cm, that gives us an estimated acceleration of 4.5*104 m/s2, which is

two orders of magnitude lower than the ionization-collision frequency for even a weakly

ionized plasma such as that of the NSTAR cathodes (as reported in [42]). Thus we can be

assured that the inequality expressed by equation 6.2.20 is reasonable, and ultimately the

spatial term of the convective derivative can be neglected in the neutral species

momentum equation.

Thus, for the equation of motion of neutrals we have:

( ) ( ) ( )

( ) ( )

hn h n n n h n ni n i n e ne e n h iz n

hn h n ni n i n e ne e n h iz n

2

02

Mn M u u n eT n u u n m u n M u

Mn eT n u u n m u n M u

ν ν ν

ν ν ν

∇ = −∇ − − + +

≅ −∇ − − + +

i (4.2.24)

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87

Speaking for a single collision, though neutrals do not gain significant momentum (due to

the large mass difference) during collisions with electrons, it is none the less important to

include the neutral-electron term here due to the highly collisional nature of the plasma.

Many individual collisions make up for low momentum transfer in any individual

encounter. Note the sign change of the last term on the RHS, which results from the

substitution of the neutral species mass conservation equation.

Conservation of Energy – General Species Energy Equation

The general form of the energy equation, describing the transport of energy

(internal + kinetic) among particles of species ‘a’, in the presence of particles of species

‘b’, is given by:

( )2 2a a a a

a a a a a a a ab a a

other species

a a a aβ a a aβ=b

3 52 2 2 2

n m n mu n T u n T u u qt

e n E u R u Q S

⎧ ⎫∂ ⎛ ⎞ ⎛ ⎞+ + ∇ + + Π + =⎨ ⎬⎜ ⎟ ⎜ ⎟∂ ⎝ ⎠ ⎝ ⎠⎩ ⎭

+ + +∑

i i

i i (4.2.25)

Where, as previously mentioned, the anisotropic viscosity tensor has been neglected.

The first term on the left hand side represents the change in the total amount of energy

possessed by the particles in a volume, both kinetic and thermal. The second term on the

LHS is the total flux of energy across the boundary of the volume. Terms on the RHS

represent the energy gained/lost due to particle interactions with the electric field, energy

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88

gained/lost due to the “friction force” associated with collisions, and finally, the heat

generated due to the presence of particles of divergent temperature.

Gathering the kinetic energy terms, and substituting the dot product of the species

momentum equation with ua , yields:

( ) ( )

22a a a a a

a a a a a a

kinetic energy terms

2aa a a a , a a a iz a a

3 52 2 2 2

a

e in

DuDt

n m n m up p u q u ut t

um n u u u u p n m u Q St

ν

=

⎧ ⎫⎛ ⎞∂ ∂⎪ ⎪⎛ ⎞⎛ ⎞ ⎛ ⎞+ ∇ + + + ∇ =⎨ ⎬⎜ ⎟⎜ ⎟ ⎜ ⎟ ⎜ ⎟∂ ∂⎝ ⎠ ⎝ ⎠ ⎝ ⎠⎪ ⎪⎝ ⎠⎩ ⎭

∂⎡ ⎤+ ∇ + ∇ + −⎢ ⎥∂⎣ ⎦

i i

i i i ∓ (4.2.26)

Substitution of the species continuity equation into the above eqn will reduce the term in

curly brackets on the LHS:

( )

( )

,

22a a a a a

a a

22 2 2a a a

a a a a a a a a

22 2a a a

a a a a a a

2 2

2

2e i izn

n

n m n m uu ut

m n uu n u n u n u ut t

m n un u u n u ut t

ν=±

⎧ ⎫⎛ ⎞∂⎪ ⎪⎛ ⎞ + ∇ =⎨ ⎬⎜ ⎟⎜ ⎟∂ ⎝ ⎠⎪ ⎪⎝ ⎠⎩ ⎭⎡ ⎤∂ ∂

+ + ∇ + ∇⎢ ⎥∂ ∂⎣ ⎦⎡ ⎤⎢ ⎥

⎛ ⎞∂ ∂⎛ ⎞⎢ ⎥= + ∇ + + ∇⎜ ⎟⎜ ⎟⎢ ⎥∂ ∂⎝ ⎠ ⎝ ⎠⎢ ⎥⎢ ⎥⎣ ⎦

i

i i

i i

(4.2.27)

Further, it can be shown that:

∂u∂t

iu + ui∇( )u⎡⎣ ⎤⎦iu =ui∇u2

2+

12

∂u2

∂t (4.2.28)

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89

Using these relations, we arrive at a general expression for the transport of internal

energy for species ‘a’ in the presence of species ‘b’ of different temperature.

For ions and electrons this is:

2a a a a a a a a iz a a a

3 5 12 2 2

p p u q u p m n u Q St

ν∂ ⎛ ⎞ ⎛ ⎞+ ∇ + − ∇ − = −⎜ ⎟ ⎜ ⎟∂ ⎝ ⎠ ⎝ ⎠i i (4.2.29)

For neutrals:

2a a a a a a a a iz a a a

3 5 12 2 2

p p u q u p m n u Q St

ν∂ ⎛ ⎞ ⎛ ⎞+ ∇ + − ∇ + = −⎜ ⎟ ⎜ ⎟∂ ⎝ ⎠ ⎝ ⎠i i

Electron Energy Transport Equation

To derive the expression describing the transport of energy among electrons, we

can use the relation je = −eneue to produce:

( )e e 2e e e e e e e e e iz e e e

e

3 5 12 2 2

n Tn eT T j T j m n u Q S

t nκ ν

∇∂ ⎛ ⎞ ⎛ ⎞− ∇ + ∇ + − = −⎜ ⎟ ⎜ ⎟∂ ⎝ ⎠ ⎝ ⎠i i (4.2.30)

Qe represents energy exchange, of both thermal and kinetic energy, from electrons to

other species during inelastic and elastic collisions, and Se represents energy exchange

from electrons to other species during collisions resulting in ionization and excitation

(inelastic collisions only). Considering the first term, one can recognize that heat energy

may be transferred to momentum (kinetic) energy between species. Since the Te>Th,

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90

electrons will loose thermal energy in collisions with heavy species particles. From

conservation of energy during collisions, we have:

Qab + Rab iua = − Qba + Rba iub( )⎯ →⎯ Qab + Qba = −Rab i ua − ub( )general

Qei + Rei iue = − Qie + Rieiui( )Qen + Ren iue = − Qne + Rne iun( )Qe = Qei + Qen = −Qie − Qne − Rei i ue − ui( )− Ren i ue − un( )

(4.2.31)

The thermal energy transferred between electrons and ions in inelastic collisions is given

by:

( )eie ie e e i

h

mQ n e T TM

ν≈ − (4.2.32)

The thermal energy transferred between electrons and neutrals in inelastic collisions is

given by:

( )ene ne e e n

h

mQ n e T TM

ν≈ − (4.2.33)

The total Qe is then:

( ) ( ) ( ) ( )ee ei en e e h ei e i en e n

h

3mQ n e T T R u u R u uM

ν ν⎡ ⎤

= − + − − − − −⎢ ⎥⎣ ⎦

i i (4.2.34)

The Se term is a general representation for the energy exchanged in collisions resulting in

ionization or excitation of heavy species. Previous researchers have experimentally

demonstrated that the plasma inside hollow cathodes is optically thick [41], thus the

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91

majority of de-excitation related radiation remains trapped in the plasma, and can be

ignored. For ionization events we have:

Se = neε (4.2.35)

where ε is the ionization energy of the ground state neutral atoms.

Combining the above equations, with the electron momentum equation and using the

assumptions that ue − ui ≈ ue and ue − un ≈ ue , yields the final expression for the

conservation of energy for the electrons:

( ) ( )

e e

2 ee e iz e e e e e e ei en e e h

h

32

1 5 32 2

n eTt

mm n u T j T E j n e T T neM

ν κ ν ν ε

∂ ⎛ ⎞ =⎜ ⎟∂ ⎝ ⎠⎡ ⎤+ ∇ + ∇ + − + − −⎢ ⎥⎣ ⎦

i i(4.2.36)

The left hand side describes the net local change in energy of the electrons. On the right

hand side the terms in brackets describe the local divergence of energy carried away by

the electron current and energy transfer by conduction through the “electron fluid”. The

Ei je term accounts for work done on the electrons by the electric field, and the fourth

term represents energy that is transferred from the electron fluid to the heavy species

through collisions, while the last term is energy lost to ionization processes.

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92

Heavy Species Energy Transport Equation

Since the ions and neutrals are assumed to be in thermal equilibrium, it is

convenient to combine the energy transfer equations of both species into a single

equation describing all heavy particles.

Ion energy equation

We begin with the general equation of energy transfer for species ‘a’, as given by eqn

6.2.19. Proceeding along a similar derivation to that of the electron energy equation,

using both the ion continuity equation (eqn. 6.2.5) and the ion momentum equation (eqn.

6.2.17), we arrive at an equation describing the transfer of internal energy for the ions:

2i i i i i i i iz i i i i

3 5 12 2 2

p p u q u p n M u Q St

ν∂ ⎛ ⎞ ⎛ ⎞+ ∇ + − ∇ − = −⎜ ⎟ ⎜ ⎟∂ ⎝ ⎠ ⎝ ⎠i i (4.2.37)

Neutral Species Energy Equation

Again, beginning with the general relation describing energy transfer for species ‘a’, as

given by eqn 6.2.19, and proceeding along a similar derivation to that of the electron

energy equation, using both the neutral continuity equation (eqn. 6.2.8) and the neutral

momentum equation (eqn. 6.2.18), we arrive at an equation describing the transfer of

internal energy for the neutral species:

2n n n n n n i iz h n n n

3 5 12 2 2

p p u q u p n M u Q St

ν∂ ⎛ ⎞ ⎛ ⎞+ ∇ + − ∇ + = −⎜ ⎟ ⎜ ⎟∂ ⎝ ⎠ ⎝ ⎠i i (4.2.38)

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93

Again, note the difference in the sign of the kinetic energy terms, which can be traced

back to the species continuity equations, for where ions are created, neutrals are lost.

Combined Heavy Species Energy Equation

Since the ions and neutrals are assumed to be in thermal equilibrium, Ti=Tn, it is

convenient to sum the ion and neutral species energy equations (eqns. 6.2.30 and 6.2.31)

to form a general equation for the transport of energy for heavy species:

( ) ( )

( )

i n i i n n i n

2 2hn i i i n n i n i n

3 5 ...2 2

...2

p p p u p u q qt

nM u u u p u p Q Q S S

∂ ⎡ ⎤+ + ∇ + + + +⎢ ⎥∂ ⎣ ⎦

− − ∇ − ∇ = + − −

i

i i (4.2.39)

where, again, Q represents the heat generated/lost in the ions and neutrals as a result of

collisions with other species. Any change in the thermal energy of a species due to

collisions with other species, results in a change in momentum (Kinetic) energy:

( ) ( )

( ) [ ]

( )( ) ( ) ( )

( )

( ) ( )2

,...

... 3

3

ab ab a ba ba b ab ba ab a b

i in ie n ni ne

i n in ni ie ne

ein i n ei en e e h

h

in i h in i n

ei n i h in i n ei en e e h

h

Q R u Q R u Q Q R u u

Q Q Q Q Q QQ Q Q Q Q Q

mR u u n e T TM

R n M u u

mQ Q n M u u n e T TM

ν ν

ν

ν ν ν

+ = − + ⎯⎯→ + = − −

= + = +

+ = + + + =

⎡ ⎤− − + + −⎢ ⎥

⎣ ⎦= −

+ = − + + −

i i i

i

⎡ ⎤⎢ ⎥⎣ ⎦

(4.2.40)

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Noting the following algebraic reorganizations:

32

∂∂t

pi + pn( )=32

e ∂Th

∂tnn + ni( )−

32

Th∇i ji + eΓn( ) (4.2.41)

with the substitution of the ion and neutral mass conservation equations, and:

− ui i∇pi + un i∇pn[ ]= −∇i Th ji + eΓn( )⎡⎣ ⎤⎦ + pi i∇ui + pn i∇un[ ] (4.2.42)

We can now gather all these terms and write the combined heavy species energy

equation:

( ) ( ) ( )

[ ] ( ) ( )

( ) ( )

2hi n i h in i n h i n h i n

2 2hh i i n n h i n n i

eei en e e h i n

h

3 32 2

3 ...2 2

... 3

Te n n n M u u T j e Tt

nMeT n u n u T j e u u

mn e T T S SM

ν κ κ

ν ν

∂ ⎡ ⎤+ = − − ∇ + Γ + ∇ +⎢ ⎥∂ ⎣ ⎦

− ∇ + ∇ + ∇ + Γ + − +

⎡ ⎤+ − − −⎢ ⎥

⎣ ⎦

i

i i i (4.2.43)

Remaining Equations:

Combining the electron and ion momentum equations (eqns. 6.2.16 and 6.2.17),

we can solve for the ion current density ji,

( ) ( ) h

e i e e en iz n e e en i in

iin

h iz

2

2

Me P P j m u e m n nj

M

ν ν ν ν

ν ν

⎛ ⎞− ∇ + + + + +⎜ ⎟⎝ ⎠=

⎛ ⎞+⎜ ⎟⎝ ⎠

(4.2.44)

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95

And substitution back into the ion continuity equation yields:

( ) ( ) h

e i e e e en iz n e e en i in

inh iz

2

2

ii iz

MP P u m n u m n nn nt M

ν ν ν νν

ν ν

⎡ ⎤⎛ ⎞−∇ + + + + +⎜ ⎟⎢ ⎥∂ ⎝ ⎠⎢ ⎥= −∇∂ ⎛ ⎞⎢ ⎥+⎜ ⎟⎢ ⎥⎝ ⎠⎣ ⎦

i (4.2.45)

[Note: There is a typographical error in reference 42, eqn 37, where the term in the

denominator should read 1+νizνin

⎛⎝

⎞⎠ ].

Multiplying the steady state ion and electron continuity equations by e and –e

respectively, and then adding the two terms will yield a relation between the electron and

ion current:

∇i neue( )= n⎡⎣ ⎤⎦ −e( )∇i niui( )= n⎡⎣ ⎤⎦ e( )

+⎯ →⎯ ∇i ji + je( )= 0 (4.2.46)

Which due to its form can be thought of as an equation governing the “conservation of

current”.

Rearranging the electron momentum equation yields an expression for the

electron current density je,:

( ) ( ) ( )

( ) ( )( )

( )( )

( )

e e e e e ei e i en e n e e iz e

2 2e e e e e ei i en n

ee ei en iz

e e e ei en izi ei e en ne 2

e ei en iz e

0

...

...

, where

en E e n T m n u u u u m n u

n e E e n T em n u uj

m

n T mj en uEjn n e

ν ν ν

ν νν ν ν

ν ν νν ν ηη η ν ν ν

= − − ∇ − − + − −⎡ ⎤⎣ ⎦

+ ∇ − +=

+ +

∇ + ++= + − =

+ +

(4.2.47)

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(where η is the plasma resistivity) which, when combined with the equation for current

conservation and E = −∇φ , yields:

( )

( )( )

( )( )

( )( )

i e

e e i ei e en ni

ei en iz

e e e en n eii

e ei en iz en ei iz

e e e en n eii

e ei en iz en

0

...

0

...

1 0

...

1

e

j j

n T j en uE jn

n T en uE jn

n T en u jn

ν νη η ν ν ν

ν νη η ν ν ν ν ν ν

ν νφη η ν ν ν ν

∇ + =

⎛ ⎞∇ +∇ + − + =⎜ ⎟⎜ ⎟+ +⎝ ⎠

⎡ ⎤∇ ⎛ ⎞∇ + − + − =⎢ ⎥⎜ ⎟+ + + +⎝ ⎠⎣ ⎦

∇⎛ ⎞∇∇ = ∇ − + −⎜ ⎟ + +⎝ ⎠

i

i

i

i iei izν ν

⎡ ⎤⎛ ⎞⎢ ⎥⎜ ⎟+ +⎝ ⎠⎣ ⎦

(4.2.48)

and since this must apply at any location the divergence arguments must be equal,

yielding an equation for the plasma potential:

( )

( )1e e e en n ei

ie ei en iz en ei iz

n T en u jn

ν νφη η ν ν ν ν ν ν

⎡ ⎤∇ ⎛ ⎞⎛ ⎞∇∇ = ∇ − + −⎢ ⎥⎜ ⎟⎜ ⎟ + + + +⎝ ⎠ ⎝ ⎠⎣ ⎦

i i (4.2.49)

6.3 Summary of Equations:

In the previous section, a complete derivation of the governing equations was

presented, along with assumptions the author has chosen based upon conditions relevant

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to the work at hand. For clarity, a summary of the equations which comprise the

numerical model is now presented:

( ) ( ) h

e i e e e en iz n e e en i in

inh iz

2

2

ii iz

MP P u m n u m n nn nt M

ν ν ν νν

ν ν

⎡ ⎤⎛ ⎞−∇ + + + + +⎜ ⎟⎢ ⎥∂ ⎝ ⎠⎢ ⎥= − ∇∂ ⎛ ⎞⎢ ⎥+⎜ ⎟⎢ ⎥⎝ ⎠⎣ ⎦

i (4.3.1)

( ) ( )2 ee e e e iz e e e e e e ei en e e h

h

3 1 5 32 2 2

mn eT m n u T j T E j n e T T net M

ν κ ν ν ε∂ ⎛ ⎞ ⎡ ⎤= + ∇ + ∇ + − + − −⎜ ⎟ ⎢ ⎥∂ ⎝ ⎠ ⎣ ⎦i i

(4.3.2)

( )( )

e e e en n eii

e ei en iz en ei iz

1n T en u j

nν νφ

η η ν ν ν ν ν ν⎡ ⎤∇ ⎛ ⎞⎛ ⎞∇

∇ = ∇ − + −⎢ ⎥⎜ ⎟⎜ ⎟ + + + +⎝ ⎠ ⎝ ⎠⎣ ⎦i i (4.3.3)

E φ= −∇ (4.3.4)

( ) ( ) h

e i e e en iz n e e en i in

iin

h iz

2

2

Me P P j m u e m n nj

M

ν ν ν ν

ν ν

⎛ ⎞− ∇ + + + + +⎜ ⎟⎝ ⎠=

⎛ ⎞+⎜ ⎟⎝ ⎠

(4.3.5)

( )( )

( )e e e ei en izi ei e en ne 2

e ei en iz e

,n T mj en uEj

n n eν ν νν ν η

η η ν ν ν∇ + ++

= + − =+ +

(4.3.6)

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98

( ) ( ) ( )

[ ] ( ) ( ) ( ) ( )

2hi n i h in i n h i n h i n

2 2 ehh i i n n h i n n i ei en e e h i n

h

3 32 2

3 32 2

Te n n n M u u T j e Tt

mnMeT n u n u T j e u u n e T T S SM

ν κ κ

ν ν

∂ ⎡ ⎤+ = − − ∇ + Γ + ∇ +⎢ ⎥∂ ⎣ ⎦⎡ ⎤

− ∇ + ∇ + ∇ + Γ + − + + − − −⎢ ⎥⎣ ⎦

i

i i i

(4.3.7)

( ) ( )hn h n ni n i n e ne e n h iz n0

2Mn eT n u u n m u n M uν ν ν= −∇ − − + + (4.3.8)

( )nn n n n iz

n n u n nt

ν∂+ ∇ = − = −

∂i (4.3.9)

This system of 9 equations, along with the relevant boundary conditions (discussed

below) is solved simultaneously to yield the 2-D, axisymetric profiles of the 9 relevant

plasma properties: je , ji ,ne = ni ,Te ,φ, E,Th ,nn ,un .

The numerical model solves the above equations in the cylindrical coordinate

system. Cathode geometry dictates that the plasma properties be azimuthally invariant,

and radially and axially dependent, thus:

∂Ψ∂φ

= 0, where Ψ is any physical quantity.

6.4 Numerical Methodology

The conservation equations comprising the cathode numerical model described in

the previous section are implemented using the finite volume method for numerical

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computation of partial differential equations. This method is commonly used in the

solution of computational fluid dynamics problems, and for the author it provides

compatibility with existing models.

In the finite volume method, divergence terms contained in model equations are

converted into surface integrals via the divergence theorem. Computation is then

achieved by evaluating the surface integrals as a total surface flux of the given property

across the faces of the cell-volume, thus all fluxes (vector quantities) are edge-centered

and are taken as the average value across the cell wall. Conversely, all scalar quantities

are cell-centered, and are evaluated at the center of the cell volume and taken as the

average value of the given property for the volume of the cell. For finite differencing,

second order accurate approximations are used.

The discretization of the cells and plasma parameters are such that each cell is

located by the node at its center, and has 4 edges with each edge located by a node at its

center. Each scalar parameter (cell centered value) has a calculated value at the central

node, and is assumed constant throughout the volume of the cell. If the value of a scalar

parameter is required at the edge nodes, a value is calculated via liner interpolation using

the cell centered values on either side of the edge in question, and thus a discontinuous

stepwise function is formed. This is shown for a single dimsneion in Figure 31, note the

linear interpolation for the edge centered scalar parameter. The mesh grid of the

computation region is a uniform distribution of cells measuring 0.5 mm by 0.5 mm. The

geometry of the computational region is uniquely calculated for the geometry of the

cathode as defined by the user input.

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Figure 31. Discretization scheme showing stepwise function for scalar values.

Finite Volume Method

In the finite volume method, the conservation principle in question is applied in

an integral form over a fixed (control) volume in space, which thus observes the discrete

nature of the computational model. Since we have started with the PDE versions of the

conservation laws, we will have to work backwards, and with appropriate application of

the divergence theorem we can arrive at the desired and appropriate integral form of the

equations. For the equations in question, which are solved in a 2D manner, volume

integrals employ a predetermined depth for the 3rd “volume” dimension. Thus each row

of cells has a unique third depth dimension which is calculated according to the user

input cathode geometry, and is a function of its radial distance from the centerline.

For the flux of a some quantity across a cell boundary, which arises in the

divergence of a scalar parameter calculated at a cell center, the flux vector is determined

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at all edge centers. In calculating the divergence of some quantity, we can take advantage

of the divergence theorem to transform the volume integral into a surface integral, as

shown in eqn 6.3.10. In the finite volume method, the surface integral can be evaluated as

the sum of surface integral argument as calculated at each surface. Note the summation

only includes 4 of the 6 surfaces of the cubic cell, this if because the plasma is

azimuthally invariant, and so there is no net flux (at any location) in the azimuthal

direction.

( ) ( ) ( )4

i i i rrr=1V S

ˆ ˆu dV u n dA u n A∇ = = Δ∑∫∫∫ ∫∫i i i (4.3.10)

In some equations, a slightly different form of this is encountered where the

argument of the volume integral is a scalar times the divergence of a vector. In this case,

the nature of the discretization scheme is to our advantage, as we have set the scalar

values constant throughout the volume of an individual cell (but discontinuous a the cell

boundaries). In this case, the scalar value may simply be pulled out of the integral, and

the divergence theorem applied as previously done:

( ) ( ) ( )4

i i i i i i rrr=1V S

ˆ ˆn u dV n u n dA n u n A∇ = = Δ∑∫∫∫ ∫∫i i i (4.3.11)

It is now possible to quantitatively describe the methodology by which the

theoretical model is evaluated numerically and the relevant plasma properties are solved

for. A detailed description of the numerical evaluation of each equation in the model, as

well as each equations boundary requirements, is contained in appendix A.

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6.5 Boundary Conditions by Boundary Location

The boundary condition requirements are set by the nature of the finite volume

method chosen for numerical computation, in which scalar quantities are cell centered

and flux (vector) quantities are edge centered. For vector quantities, the value of the flux

across the boundary of the computational zone is specified where these boundaries

coincide with the edges of cells. For scalar properties, which are cell centered, the value

of the property is specified for a layer of imaginary “ghost cells” which lie adjacent to the

outermost cells and are just outside the computation zone.

The computational zone is a (solid) cylindrical region with three physical

boundaries, two of which coincide with the physical geometry of the cathode. The up-

stream boundary is the entrance of the computational zone and is where the neutral gas

enters; the down-stream boundary coincides with the cathode exit plane, and the radial

boundary is the cathode wall, though not including the plasma sheath which is handled

separately.

Boundary 1: Gas entrance

(z = L, 0 < r < R)

At the upstream end of the computation region the neutral gas is introduced to the

emission zone at a flow rate determined by the experimental parameters. The neutral gas

mass influx is specified in the input to the model, and is determined by a value of the

neutral gas velocity and density at the boundary.

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The neutral gas fluxes into the computational zone with the relation:

n i nh cross

section

ˆ mn u nM A

Γ = =i (4.4.1)

The gas pressure upstream of the computational zone is experimentally measured,

and from this the boundary condition for the neutral particle velocity is calculated using

the above equation.

No net electron flux is permitted out of the upstream boundary:

jein̂upstream = 0 (4.4.2)

Ions diffuse out of the upstream boundary at the ion thermal speed:

ui in̂upstream =

kbTh

π Mh

⎯ →⎯ ji in̂upstream = enikbTh

π M h

(4.4.3)

The heavy species temperature is set constant across the boarder and is set equal to the

value of the cathode wall temperature at the downstream axial location.

Ti = Th = Twall[ ]upstream−boundary (4.4.4)

Further, it is assumed that the upstream boundary to the computational zone is far enough

away from the cathode exit that there is no plasma in this region.

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Boundary 2: Cathode Walls

(0 < z < L, r = R)

At the boundary of the cathode walls begins the plasma sheath region which

supplies electrons to the bulk plasma as the primary source of ionization, and receives

ions from the plasma as the primary source of cathode wall heating. Thermionic electron

emission current density is a function of the cathode wall temperature, the electric field at

the surface of the wall, and materials properties, and is governed by the well known

Richardson equation:

jth =ATwall

2

eφeffkbTwall

e (4.4.5)

Where A is a constant set by material properties, Twall is the cathode wall temperature and

φeff is the effective work-function of the cathode material. The cathode wall has a

material dependent value for the work-function φ, which can be effectively enhanced by

electric fields at the surface of the wall. This enhancement is seen as a change in the

work-function to an effective work-function φeff , termed the Schottky effect, and given by:

4

ceff i

o

eEφ φπε

= − (4.4.6)

where εo is the permittivity of free space and Ec is the value of the electric field at the

cathode wall.

The exact nature and details of the sheath region are somewhat involved and are

considered of prime importance to the problem of cathode temperature and lifetime. It is

the sheath which provides the main source of heat to the cathode walls in the form of ions

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gaining energy falling through the sheath potential drop, and then depositing this energy

as heat upon impact with the cathode wall. Once the ion has struck the cathode wall, it is

temporarily adsorbed on the surface, where it recombines with a wall-supplied electron,

takes on the thermal energy level of the wall and drifts off as a neutral particle and rejoins

the bulk plasma region, where it may again be ionized or drift out of the cathode. The

sheath is also the primary source of neutral gas ionization, supplying energy to the

thermioniclly-emitted electrons and giving them the ability to ionize neutrals via

collision. The final temperature of the cathode wall is determined by a balance between

the heat depositing phenomena (ion strike, reverse electrons, etc.), and those processes

which emit heat from the cathode (conduction through the base of the cathode, electron

emission, recombinations, convection, and other forms of radiation). The sheath serves as

the interface barrier between the IPC and the cathode wall, and its properties are

divergent with axial location. Previous authors [26] have developed detailed models

describing the related processes occurring in the cathode sheath region.

Though the sheath phenomena are of significant importance to the determination

of the cathode wall temperature, a sheath model is not included in the IPC/cathode model

described herein. Instead, the author has chosen to focus on processes limited to the IPC

plasma inside the cathode, and simply accept the cathode temperature profile as an input

to the model. Further, though the limitations of the model caused by this decision are

obvious, and though achievement of a combined plasma + sheath model are of prime

interest to cathode researchers (and to the author in particular), resource and time

constraints have forced the model to develop as in its current state. A combined plasma +

sheath model will be left as future work, possibly to be conducted in a follow-on to this

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study. With the cathode wall temperature profile as a model input, one can accurately

determine the electron emission from the cathode wall surface.

Boundary 3: Cathode Exit Plane

(z = 0, 0 < r < R)

The cathode exit plane marks the downstream end of the computation zone. At

this boundary, values of the plasma potential and plasma density must be specified –

these numbers are determined by experimental measurements and are inputs to the

model:

φexit = φmeasured , nexit = nmeasured (4.4.7)

Adiabatic boundary conditions are imposed on the heavy species temperature and the

electron temperature. The neutral species flux out of the computational zone through the

exit plane is determined from knowledge of the total mass flux into the cathode, and the

flux of ions leaving the cathode - the neutrals crossing the exit plane are thus calculated

as the difference.

Boundary 4: Cathode Centerline:

(0 < z < L, r = 0)

Since the computational zone is azimuthally invariant, it is thus unnecessary to

calculate plasma values over the entire physical volume. This therefore yields a two

dimensional computational grid with a centerline as the boundary in the limiting case of

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zero radial position. Numerical symmetry is thus imposed along the cathode centerline,

and no net flux of any property is permitted across this boundary.

6.6 Solution Procedure

In the numerical simulation, the steady state form of the summary equations are

solved, with the exception of equations 6.3.1 and 6.3.2 which are time marched to yield

steady state value of the electron (plasma) density and electron temperature, respectively.

The solution flow chart is as follows: Initial values of the plasma density, neutral

gas density, neutral gas velocity, electron temperature, heavy species temperature, plasma

potential, electric field and electron current are input. Along with these dependent values,

the experimental parameters are read into the model, giving cathode geometry, neutral

gas flow rate and boundary conditions. Initially, the program creates the appropriate grid

for the cathode geometry, and at each grid point, initial values for all parameters are

assigned, including “constants” such as collision frequencies and other transport

coefficients.

Equations 6.3.1 and 6.3.2 are time marched to yield new values of the plasma

density and electron temperature, at which point these new values are used to calculate all

new transport coefficients for each cell. This process repeats for a user defines number N

of loops, with N being empirically determined. After N iterations, new values of plasma

potential, electric field, electron current density, heavy species temperature, neutral gas

density and neutral gas velocity are calculated. These new parameters are then used to

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calculate new values of the transport coefficients, which are then fed into the subroutines

calculating the plasma density and temperature, and the process repeats all over again.

The program will loop for a large number of total iterations, at which point the

values for all dependent variables is at, or very near, steady state. Total program loop

number is determined empirically. A flow chart describing the solution procedure is

contained at the end of this document.

6.7 Connecting Theoretical Model and Experimental Work

The theoretical model of the IPC developed in this work requires experiment

specific inputs for use in the boundary conditions. Gas type and input flow velocity are

easily determined and can be gathered with relative ease. Calculated properties relevant

to the gas type such as collision frequencies, ionization frequencies and thermal

conductivity, are used in each cell parameter calculation.

The cathode surface temperature profile, the downstream plasma density and the

downstream plasma potential will require more involved means of measurement. The

cathode surface temperature profile is used to determine the thermionic emission current

off of the cathode wall, and the plasma density and potential are required as downstream

boundary conditions.

Experimental and theoretical work were largely carried out in parallel, with little

interdependency during development, and both can largely stand on their own as

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individual works of research. Figure 32 shows the relative progression of theory and

experimental work in a sample flow chart from progress reports to JPL.

Figure 32. Sample flow chart for theory and experimental work

The experimental work generated data correlating the input parameters of cathode

geometry, propellant type and flow rate, and discharge current with the operating

parameters of cathode temperature profile, discharge voltage, and downstream plasma

density and potential. These data were then used as input to the cathode model developed

in this work, and can be applied to several other cathode models, notably those previously

developed at JPL and Princeton University.

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Chapter 7: Experimental Results and Conclusions

In this chapter is presented the results of the Argon fed single channel hollow

cathode experiments and modeling work. Primary goals of the experimental portion of

this work are to correlate cathode performance with varying experimental parameters of

discharge current, flow rate, discharge voltage, as well as cathode geometry. Other

significant goals of the experiments are to provide input data as boundary conditions to

the computational model, specifically upstream total pressure, cathode wall temperature,

exit plane plasma potential and density, as well as electron temperature.

Three unique cathode designs were used in the study, two configurations made of

cylindrical Tungsten electron beam welded to a Molybdenum flange, and one of

Tantalum tube with a stainless steel base. Both high-voltage/low-current discharges, and

low-voltage/high-current discharges were examined.

7.1 Cathodes

Several cathodes were severely damaged and/or destroyed during the

experimental run, both Tungsten and Tantalum. The first of which was cathode A, a

Tungsten cathode 6 mm in interior diameter. After approximately 30 minutes of running

at 55 Amps the discharge began a low frequency oscillation (visually observed to be of

order 1 Hz) in current and brightness for 10’s of seconds before extinguishing itself.

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Following the shutdown, the discharge was reestablished again, though it was noticeably

unstable, and extinguished itself after less than five minutes of operation.

After this second involuntary termination, the cathode was unable to support

another discharge, and upon termination of the test it was discovered that significant

portions of the cathode material had been removed from the downstream half of the

cylindrical region up to approximately 4 mm from the exit plane. Also, cathode material

had been re-deposited in spaces covering approximately the middle third of the body. The

damage occurred in a highly irregular pattern, which can be seen in Figure 33, and close

up in Figure 34.

A post test analysis of the cathode, including observation under a scanning-

electron microscope, revealed trace amounts of hydrocarbons on the cathode. It is

believed that this material may have come from an epoxy used on mounting hardware

inside the chamber. It is unclear what role this contamination played (if any) in the rapid

and unusual erosion of the Tungsten material. Further analysis of the failure lead to the

conclusion that the most significant contributor to the rapid erosion was an unsteady

power output from the HP high-current discharge supply. Once in current-limited mode,

the supply’s output regulation proved incapable of driving a steady output arc-discharge.

Insufficient internal ballast resistance caused a rapid feedback loop in the supplies control

circuitry, resulting in high-frequency oscillations in voltage output, conducting power

through the cathode in excess of its ability to cool, resulting in excessive cathode material

evaporation.

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Figure 33. Damaged cathode and flange

Figure 34. Close-up of damaged cathode

Following the failure of the first 6 mm Tungsten cathode, the HP supply was replaced

with the Miller arc-welding power supply. Several successful tests with 2 mm ID

Tantalum cathodes were conducted with discharge currents of 13 Amps to 70 Amps to

ensure the viability of the new supply.

When the second 6 mm Tungsten cathode was installed, further difficulties were

encountered. When the high-voltage start supply was engaged, it was unable to heat the

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cathode enough to start significant thermionic emission, resulting in high-voltage (110-

130 volts), low-current discharges (3-4 Amps). Because the discharge voltage would not

fall low enough to match the 80 Volt open circuit level of the Miller supply (thus

allowing current to flow through the blocking diode connected in series with the Miller

supply), the high-current supply would not engage.

Several runs were conducted with the high-voltage/low-current discharge yielding

constructive data. After approximately 4 hours of operation a small hole developed at 22

mm upstream, eventually widening to an oval measuring 4 mm by 3 mm, at which point

the cathode could yield no further data useful to this research and was considered

destroyed (though it is worth noting that it would still conduct a discharge). Further

analysis of the cathode yielded significant thinning of the wall material in the region

around the oval, and downstream. The wall thinning was of such magnitude that after

minor post test handling, the cathode cracked into two peices – post test photographs of

this cathode can be seen in Figure 35, with a penny in frame for scale.

Figure 35: Up close view of 6 mm Tungsten cathode, post test.

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To address the inability of the discharge supply’s open circuit voltage to match

the high-voltage star supply’s discharge voltage, the Miller supply was finally replaced

with the Lambda high-current power supply, which was successfully used throughout the

remainder of the experiment. The Lambda supply showed very low-current ripple in

comparison to the Miller, and had an open circuit voltage capable of matching the

discharge voltage of the high-voltage supply. All of the plasma data measurements made

for the 2 mm Tantalum cathode were used with this supply.

A high-current discharge run was conducted with a 10 mm Tungsten cathode

using the Lambda high-current supply. It was discovered that in the existing facility, the

cathode discharge could not be maintained below ~400 sccm flow rate of Argon, or

below ~65 Amps of discharge current. Further, the excessive heating resulting from the

high discharge power proved to beyond the capabilities of the facility cooling systems.

Figure 36. 2 mm Tantalum and 10 mm Tungsten cathodes. Images are pre-

discharge.

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Figure 37. Comparison of exit planes of 2 mm Tantalum, and 10 mm Tungsten

cathodes. Images are pre-discharge.

A stable operating point of 440 sccm flow rate, 75 Amps and 37 Volt discharge

was empirically selected for the experimental run. During the course of the experiment, it

was quickly realized that the facilities were insufficient in design and cooling capacity to

handle the excessive temperatures resulting from the high power loads needed to sustain

a discharge with the 10 mm cathodes.

The heat loads caused melting/outgassing of several of the vacuum chamber o-

rings, and caused a deposition of material to coat the inner surface of the quartz window

through which the surface temperature measurements are made. The reduced

transmisivity of the window prevented accurate measurements to be made with the

optical pyrometer. In addition, the excessive heat loads damaged the langmuir probe and

so no plasma data was able to be gathered for the 10 mm cathodes.

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Figure 38. Close-up view of 2 mm Tantalum cathodes. Images are pre-discharge.

Post discharge images of the 10 mm diameter Tungsten cathode can be seen in

Figure 39. A grey substance of unknown composition was discovered covering sections

of the cathode in a highly irregular patter. The substance was easy to remove and was

very brittle. When touched, the substance and would fracture off of the cathode body.

This appeared to be similar to the substance discovered on the 6 mm Tungsten cathode A

after failure (seen in Figure 33 and Figure 34), but in far greater quantities. Observations

of the cathode tip showed significant melting and erosion, but not to the point of

preventing the ability to ignite or sustain a discharge. The bolts holding the cathode to the

upstream mating flange had melted in place and could not be removed, thus a post test

analysis of the mass loss of the cathode could not be completed.

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Figure 39: Images of the 10 mm diameter Tungsten cathode after operation at 2 kW.

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7.2 Observed Trends

High-Voltage / Low-Current Discharges

Analysis of several experimental runs of discharges characterized with high-

voltage drops and low-currents were conducted with a 6 mm diameter Tungsten. These

runs were a result of limitations of the arc ignition circuitry and power supplies. From the

collected data with these runs, one can draw several conclusions about the operation of

the single channel hollow cathode in a high-voltage discharge. First observations were of

the cathode temperature profile. In all temperature profiles shown, the cathode exit plane

is identical the cathode tip. i.e. in Figure 40, gas flow is from right to left. Additionally,

“distance upstream” refers to axial distance, along the cathode body, from the cathode

exit plane.

From the data collected during the high-voltage discharges, it is shown that the

location of maximum cathode temperature is dependant upon flow rate, and is show to be

approximately linearly related over the region shown in Figure 40.The data show in

Figure 40 was taken for the cathode shown in Figure 35. After the data for 150 sccm flow

rate was collected, the hole in the wall of the 6 mm cathode was discovered. (The data

150 sccm is thus not considered reliable, but is included for comparison.). The location of

the hole (and later, where the cathode cracked in half) which developed is coincident with

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the regions over which the peak temperature was. This is clear evidence of cathode

erosion leading to eventual failure at the location of the peak temperature.

Figure 40. Dependence of peak temperature location on flow rate, for high-voltage,

low-current discharge through 6 mm Tungsten cathode

Higher flow rates yield a location of peak temperature further downstream, a

trend that is in agreement with observations made by previous studies, and with varying

propellants [7, 8, 18]. As seen in Figure 40, the value of peak temperature appears to be

dependent upon flow rate for a given discharge current, with the peak temperature

increasing with increasing flow rate. This is a direct contradiction to conclusions drawn

by previous studies of single channel hollow cathodes using Lithium propellant at

Princeton University [8]. (Note that the data seen in Figure 40 is for a high-voltage low-

current discharge, where the large voltage drop plays a more significant role in plasma

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generation and cathode material erosion. Conclusions drawn in the Princeton study relied

upon data gathered from high-current arc discharges. Data for high-current discharges are

presented later in this chapter). It is not believed that the discharge medium plays a

significant role the apparent contradiction in trends from the two studies.

High-Current / Low-Voltage Discharges

Figure 41 through Figure 66 show data collected from high-current discharges in

2 mm diameter Tantalum cathodes over flow rates from 60 to 300 sccm, and discharge

currents of 15 to 45 Amps. Figure 41 through Figure 50 show the voltage of the discharge

and the power consumed by the discharge, graphed parametrically with both the

discharge current and the mass flow rate. One can see the non-linear nature of the

discharge voltage as it varies with the mass flow rate, displaying a trend similar to that

seen in the familiar Paschen curve. (Note that the Paschen curve describes the voltage

necessary for initial gas breakdown, not maintenance of an already established arc). From

these graphs notice that there is a minimum discharge voltage necessary to maintain the

arc (for a constant discharge current), thus there is a maximum in the discharge

efficiency. Since the thrust of an MPD thruster is primarily dependant upon the discharge

current, there is therefore a minimum voltage (and thus power) necessary for a desired

thrust level, controlled by the gas density inside the cathode.

As expected, the discharge voltage is a decreasing function of the current, shown

in , and the power consumed by the discharge increases with discharge current over all

rates shown. Figure 48 and Figure 49 show the discharge power as a function of the

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Figure 41. Discharge voltage vs. flow rate, 2 mm Tantalum cathode

Figure 42. Discharge voltage vs. flow rate, current as parameter, lower current

range. 2 mm Tantalum cathode

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Figure 43. Discharge voltage vs. flow rate, current as parameter, higher current

range. 2 mm Tantalum cathode

Figure 44: Discharge voltage vs. discharge current for a 2 mm Tantalum cathode

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Figure 45. Discharge voltage vs. discharge current, flow rate as parameter, low flow

rate range. 2 mm Tantalum cathode

Figure 46. Total Discharge Power vs. Flow rate, 2 mm diameter Tantalum cathode,

with discharge current as a parameter, lower current range

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Figure 47: Total Discharge Power vs. Flow rate, 2 mm diameter Tantalum cathode,

with discharge current as a parameter, higher current range

Figure 48: Discharge power vs. Discharge current, with mass flow rate as a

parameter, lower mass flow rate range. 2 mm Tantalum cathode.

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Figure 49: Discharge power vs. Discharge current, with mass flow rate as a

parameter, lower mass flow rate range. 2 mm Tantalum cathode.

Figure 50. Energy input per mass throughput, 2 mm Tantalum cathode

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discharge current, parametrically with mass flow rate. The discharge power is shown to

be a decreasing function of the discharge current

Figure 50 shows the power consumed by the discharge divided by the mass flow

rate, graphed as a function of the mass flow rate. From this one can see the energy

consumed by the discharge per unit of mass throughput, and thus get a measure of the

discharge efficiency. As the mass flow rate increases, the power consumed by each mass

unit of propellant decreases, thus the efficiency involved in propellant processing is

increasing. Comparing Figure 47 and Figure 50, notice that as the mass flow rate it

increased, the energy consumed per unit mass decreases, while the overall power of the

discharge increases.

The total resistance of the Argon plasma discharge is shown in Figure 51, as a

function of Argon mass flow rate, with discharge current as a parameter. For all values of

flow rates tested, the resistance has a minimum value determined by a combination of

flow rate and discharge current, displaying the same trend as the discharge voltage and

power. As the discharge current increases, the curve for resistance flattens out, thus

showing a weaker dependence upon the mass flow rate. Figure 52 shows the value of the

minimum resistance of the plasma discharge seen in the previous figure, as well as the

flow rate at which this minimum occurs, as a function of discharge current. The value of

the minimum plasma resistance is a decreasing function of the discharge current, and the

flow rate at which the minimum occurs increases as the discharge current increases.

As can be seen in Figure 53, at a constant flow rate, as the discharge current rises,

the plasma resistance decreases, showing the classic decreasing resistance of an arc

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Figure 51. Resistance of Argon plasma discharge vs. mass flow rate, discharge

current as a parameter

Figure 52: Value of minimum resistance of the Argon plasma discharge, and flow rate at which minimum resistance occurs, vs. discharge current

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Figure 53: Plasma resistance vs discharge current, Argon flow rate as a parameter,

2 mm Tantalum cathode discharge. This is the slope of the curves in the graphs of discharge voltage vs. current,

Figure 44 and Figure 45.

The decreasing resistance curve (negative differential resistance) is a well known

phenomena of arc discharge physics and is the reason for the requirement for ballast

resistance in any arc discharge power supply circuitry. As the current increases, the

voltages required to push the current through the arc decreases, but for power supply

regulation, the voltage must increase. Therefore, inclusion of a fixed value ballast resistor

is employed: as the current across the resistor increases, the voltage required to drive the

current across the resistor will increase. Placement of the ballast resistor in series with the

arc discharge results in the total differential resistance being positive, thus voltage

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increasing for increasing current. More information on plasma resistance is discussed

later in this chapter.

Figure 54 through Figure 57 show selected temperature profiles of 2 mm diameter

Tantalum cathodes operating at flow rates from 60 sccm to 120 sccm of Argon, in a high-

current discharge of 20 Amps. Each individual plot shows data collected over multiple

runs of identical discharge parameters; from these plots one can see the high degree of

repeatability in the temperature data.

From these plots the effects of the mass flow rate and discharge current on the

temperature profiles are identifiable. Increased mass flow rates will raise the density of

neutral gas inside the cathode. This increase in density yields peak temperatures further

downstream, and higher values of peak temperature. This effect is can also be seen in

orificed hollow cathodes [42, 43, 53], which maintain a relatively high and homogenous

pressure inside the cathode. In orificed hollow cathodes the peak temperature is always

seen at the very downstream limit of the cathode. The high pressures (density) inside the

orificed hollow cathodes make them analogous to running an open ended hollow cathode

at high flow rates. To make this relation more clear, imagine raising the flow rate of the

open ended cathode (moving the peak temperature further downstream) and seeing the

density of the gas inside the cathode continuously rise. Eventually the interior density

would rise to a point at which the location of peak temperature would move all the way

downstream to the tip of the cathode, and the wall temperature profile of the open ended

cathode would resemble that of the orificed cathode. While at constant discharge current,

the temperature of the cathode at the exit plane (cathode tip temperature) is seen to

increase with increasing flow rate.

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Figure 54: Axial temperature profile along 2 mm Tantalum cathode at 60 sccm flow

rate

Figure 55. Axial temperature profile along 2 mm Tantalum cathode at 70 sccm flow

rate

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Figure 56 Axial temperature profile along 2 mm Tantalum cathode at 100 sccm flow

rate

Figure 57. Axial temperature profile along 2 mm Tantalum cathode at 120 sccm

flow rate

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Figure 58. Location and magnitude of the peak temperature of 2 mm Tantalum

cathode, vs. flow rate

Figure 59: Peak temperature vs. mass flow rate, 2 mm Tantalum cathode

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From Figure 58 and Figure 59 the magnitude of the peak cathode wall

temperature does show a slight dependence upon the mass flow rate, with the peak

temperature increasing with increasing flow rate. This is trend is in contradiction with

previous solid rod and hollow cathode research [26, 7] which concluded the peak

temperature has no dependence upon mass flow rate. Even a slight trend in temperature

can be very important due to the thermionic emission current density’s extreme

sensitivity to surface temperature, as seen previously, a drop in temperature of just 1%

can cause a reduction in current density of ~25%.

Observing the axial temperature profile, moving upstream away from the exit

plane, the temperature rises to a maximum value at some distance “l” from the exit plane,

and then drops down as you approach the upstream gas inlet. In all experimental runs,

from the location of peak temperature, the axial temperature gradient is greater in

magnitude in the upstream direction (to regions of higher total gas pressure) than moving

towards the cathode exit plane.

It can be seen from Figure 61 that over the current ranges investigated in this

study, the location of the peak temperature shows no apparent dependence upon the

discharge current. This is inconsistent with previous high-current Tungsten hollow

cathode research in Lithium [8] medium, where increasing discharge current moved the

location of peak cathode temperature further upstream. The location of the peak

temperature moves downstream closer to the exit place of the cathode as the mass flow

rate is increased.

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Figure 60: Location of the maximum temperature of 2 mm Tantalum cathode vs.

mass flow rate

Figure 61: Location of Peak Temperature dependence upon current, flow rate as a

parameter, 2 mm Tantalum cathode

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Figure 62. Magnitude of peak temperature vs. discharge current, 2 mm Tantalum

cathode

Figure 60 displays the dependence of the location of the peak temperature upon the mass

flow rate. Raising the mass flow rate will push the peak temperature further downstream

towards the cathode exit plane. Again, it must be noted that the controlling factor in this

relation is the density of gas inside the cathode; Since the density of the gas inside the

cathode is not a uniform value, and will change with additional heating of the flow, the

mass flow rate simply presents a convenient (coupled) substitute for the measure of the

gas density for a given cathode geometry. This data presents addition verification of

previously reported trends.

The value of the peak in the cathode wall temperature profile is shown to be

weakly dependent upon the discharge current, with the temperature increasing with

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Figure 63: Wall temperature profile of 2 mm diameter Tantalum cathode at 20 Amp

discharge. increasing discharge current - a doubling in the discharge current yielding a

approximately 10% increase in peak temperature over the range shown in Figure 62.

Further examination of the data in Figure 62 yields insight to the influence of flow

rate (interior cathode gas density) on the magnitude of the peak temperature. It is

suggested from the data that the magnitude of the peak temperature is weakly dependent

upon the flow rate, with temperature increasing with increasing flow rate. This is a very

important relation due to the extreme sensitivity of the current emission on the cathode

wall temperature - reduction the peak temperature while keeping the discharge constant is

a key goal of achieving increased cathode lifetime.

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Figure 64: Wall temperature profile of 2 mm diameter Tantalum cathode at 25 amp

discharge, Argon mass flow rate as a parameter.

Figure 63 through Figure 66 show axial temperature profiles of the 2 mm

diameter Tantalum cathode, parametrically with flow rate and discharge current. The

dependence of the peak temperatures’ magnitude and location upon the mass flow rate

can again be seen in Figure 63 and Figure 64 where the temperature profile is shown at a

constant discharge current of 20 and 25 Amps, respectively, with the mass flow rate as a

parameter. Figure 65 and Figure 66 display the temperature profile at two set points of

mass flow rate, 90 and 110 sccm, parametrically with discharge current.

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Figure 65: Wall temperature profile of 2 mm diameter Tantalum cathode at 90 sccm

Argon mass flow rate, discharge current as a parameter.

Figure 66: Wall temperature profile of 2 mm diameter Tantalum cathode at 90 sccm

Argon mass flow rate, discharge current as a parameter.

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Figure 67. Pressure 40mm upstream inside 10 and 6 mm diameter cathode vs. flow

rate.

Values of internal-cathode total gas pressure at a location 40 mm upstream of the

exit plane are necessary as input to the computational model. Experimental measurements

of the stagnation pressure as a function of flow rate were conducted with a model-cathode

machined of aluminum stock, simulating the flow inside the 10 mm Tungsten in the

absence of any plasma. The discharge was not turned on during the pressure

measurements, and thus all components were are room temperature rather than the

elevated temperatures experienced during a high-current discharge test. The lower

component temperature (specifically the aluminum gas feed lines, which conduct heat to

the propellant before it reaches the cathode) leads to a lower temperature of the neutral

gas entering the cathode, and thus a lower pressure. This discrepancy is a known

limitation of the computational model. The pressure measurements seen in Figure 67

were made with an MKS Baratron pressure transducer.

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Plasma Data

Figure 68: Sample of raw data from Langmuir probe trace, 2 mm Tantalum

cathode, 150 sccm, 30 Amp discharge

The trends observed in discharge plasma properties experimentally collected by

Langmuir probing during high-current discharges with a 2 mm diameter Tantalum

cathode are presented in this section. The data presented in Figure 68 through Figure 76

were all collected at a point 1 cm downstream from the cathode exit plane, on the cathode

centerline (refer to chapter 5 for diagram and explanation of Langmuir probe system

design and operation). At this location the electrons have undergone many collisions, and

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Figure 69: Electron Temperature vs. Discharge current, Mass flow rate as

parameter. 2 mm Tantalum cathode are expected to be well thermalized. Figure 68 shows raw data from a sample Langmuir

probe trace. From observation of the trace for positive collected current values, one can

clearly see the double trace from the bias voltage pulse (refer to chapter 5 for more

detailed explanation of Langmuir probe analysis procedure).

As the discharge current is increased, the data shows that the electron temperature

of the plasma will decrease, as seen in Figure 69. This can be better understood by

consideration of the source of energy of the electrons: the voltage drop across the cathode

sheath in the IPC. Figure 43 and Figure 45 show that as the discharge current is

increased, the discharge voltage will decrease, reducing the sheath drop and thus reducing

the initial energy of electrons leaving the sheath and entering the bulk plasma. The

observation of reduced electron temperature measured downstream of the cathode exit

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Figure 70: Plasma Density vs. Discharge current, discharge current as parameter. 2

mm Tantalum cathode

plane is a direct effect of this reduction in initial energy at the time of electron injection

into the bulk plasma. Figure 72 shows the data for the plasma potential as it varies with

discharge current. In addition, re-presented in this figure for comparison is the variance

of the discharge voltage with discharge current for selected values of mass flow rate. The

data correlating the relationship between the plasma potential and the discharge current

shows a variance in the trends.

The data for the lower flow rates tested clearly shows the potential to be a

decreasing function of discharge current, though as the flow rate is increased, the trend

appears to reverse, with the potential showing a weakly dependent proportionality to the

discharge current. Adding to this, the data for the total discharge voltage vs. the discharge

current (presented earlier in this chapter) revel the discharge voltage to be a decreasing

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Figure 71: Plasma ionization fraction vs. discharge current at location 10 cm

downstream of 2 mm Tantalum cathode.

function of discharge current over all values of mass flow rate tested. With this in mind, it

is unclear if the reversal in the trend of plasma potential is a real effect, or a result of

measurement/analysis error. From the data gathered in this study, a clear, repeatable and

reliable relation between the plasma potential and the discharge current cannot be

determined. Increasing the discharge current will raise the peak temperature of the

cathode, as well as the average temperature of the cathode as shown previously. This

increase in temperature yields an increase in electrons emitted thermionically from the

cathode surface which end up in the bulk plasma. These additional electrons will collide

with the neutrals, and since there are no additional neutral particles, the resulting effect is

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Figure 72: Plasma Potential (phi) and Discharge Voltage (DV) vs. Discharge

Current, Mass Flow rate as parameter. 2 mm Tantalum cathode

a rise in the electron neutral collision frequency, thus increasing the ionization fraction of

the plasma, and the density of the plasma. These effects can be seen in Figure 70 and

Figure 71. It is seen in Figure 73 that increasing the mass flow rate corresponds to a

decrease in the electron temperature. Consider flow rates to the right of the minimum

seen in Figure 42 and Figure 43. Raising the mass flow rate will introduce more neutral

particles in the bulk plasma, which increases the electron neutral collision frequency.

Each collision reduces the energy of an electron until it becomes thermalized with the

neutrals – the more collisions the lower the thermalized electron temperature (while

simultaneously raising the neutral species temperature). Therefore, increased interior gas

density results in an increase in the number of inelastic collisions, which drain energy

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Figure 73: Electron temperature vs. Mass flow rate, discharge current as

parameter. 2 mm Tantalum cathode

form the bulk electrons. This increase in electron neutral collision rate is seen as

additional resistance to the flow of the current through the plasma (shown previously),

requiring a rise in voltage to compensate. This increase in discharge voltage gives the

electrons additional energy upon ejection from the sheath into the bulk plasma.

Downstream of the cathode (where the plasma measurements in Figure 68

through Figure 76 have been made), the plasma is no longer in close proximity to (i.e.

many mean free path’s away from) the region dominated by sheath effects, and thus the

“cooling” process from the additional lower-energy neutrals will dominate. Following

this explanation, one would expect to see a decrease in the plasma potential, and a rise in

the plasma density and ionization fraction, trends which were observed experimentally

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Figure 74 : Plasma Potential vs. Mass Flow rate, discharge current as parameter. 2 mm Tantalum cathode

Figure 75: Plasma Density vs. Mass Flow rate, discharge current as parameter. 2

mm Tantalum cathode

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Figure 76: Plasma ionization fraction as a function of mass flow rate at location 10

cm downstream of 2 mm Tantalum cathode, discharge current as parameter

and shown in Figure 74, Figure 75 and Figure 76. The trend is very pronounced in the

graph of plasma density vs. mass flow rate, where a doubling of the flow rate yields an

approximately 4 to 5-fold increase in plasma density.

Work on solid rod cathodes [26] reported electron temperatures in the discharge

lower than those presented here, though the solid rod work was at higher flow rates and

significantly higher discharge current levels. The data presented here does confirm that

increasing both the discharge current and mass flow rate will decrease the electron

temperature of the discharge plasma. Thus the discrepancy in measurements of the

hollow cathode and the solid rod cathode discharge plasma electron temperature is

supported by these trends.

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The ionization fraction of the discharge plasma as shown in Figure 71 and Figure

76, are based upon measurements of the plasma taken on cathode centerline, 10 mm

downstream from the cathode exit plane. However, the total gas pressure measurements

used in the calculations were taken at a different location in the chamber, where the

pressure is known to be a different value than that at the location of plasma probing. Thus

the charts for ionization fraction presented here are for qualitative analysis only, and are

not considered to be quantitatively accurate.

One should also take particular note of the comparison between the data for total

discharge voltage (Figure 42 and Figure 43), and plasma potential (Figure 74), both as

functions of mass flow rate. Over the range of flow rates tested, a minimum in the trend

of discharge voltage is seen in the range of ~100 to 150 sccm, where there is no minimum

seen in the data for plasma potential.

7.3 Active Zone

Here is presented the observed trends of the properties of the active zone internal

to the cathode, based upon experimental data and theoretical extrapolation.

Understandings of the mechanisms controlling the active zone are key to the development

of mission capable cathodes, due to its relation to the peak cathode temperature (and

hence evaporation rate). Smaller active zones require higher surface current densities,

which in turn require higher cathode temperatures resulting in faster rates of material

erosion. From an efficiency standpoint, higher temperatures result in higher thermal

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Figure 77: Sample of analysis of thermionic emission profile data for active zone

calculations.

energy lost to the system from radiation, thus thermodynamic laws drive the active zone

to the smallest area possible – however for cathode lifetimes, it is desirable to increase

the width of the active zone.

For this analysis the active zone has been defined as the region of cathode wall

material responsible for 75% of the total thermionic emission of electrons from the

cathode. Further, as this analysis was designed to yield qualitative results, only emission

from the exterior cathode surface was considered. This decision was as result of a lack of

reliable data for the sheath drop profile along the cathode surface. The voltage across the

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Figure 78: Width of the active zone inside the cathode vs. mass flow rate

sheath will increase the thermionic emission from the cathode interior surface, through

the Shottkey effect as discussed previously. Rather than including errors by attempting to

make predictions of the Shottkey effect, it was decided to ignore interior thermionic

emission and the Shottkey effect altogether, and focus on exterior temperature profiles

only, thus yielding a strongly qualitative analysis. As a result of the construct of the

analysis, the actual width of the active zone is understood to be smaller than the values

shown in the plots below, though this should have no effect on trends brought forth from

the analysis.

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Figure 79: Width of the active zone vs. the discharge current, parametric with mass flow rate

From measured profiles of the cathode temperature, the thermionic current at each

data point was calculated. To employ numerical analysis, curve fitting of the data was

necessary, so the thermionic emission data was separated into 3 different regions (shown

in Figure 77), and polynomial curve fitting was applied to obtain an analytical description

of entire data set in piecewise functions. These curves were input to a computational

routine, which integrated over the profile to determine the width of the cathode material

responsible for 75% of the total current generation. For this analysis the active zone was

modeled as centering on the peak temperature and extending an equal distance upstream

and downstream.

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As can be seen in Figure 78 and Figure 79, the width of the active zone of the

cathode is a function of both flow rate and discharge current. Reasonable trend lines

show the width of the active zone to be a weakly increasing function of discharge current,

and an exponentially decreasing function of the mass flow rate. The width of the active

zone shows a dependence upon the discharge current, as seen in Figure 79, with a

doubling of the discharge current increasing the active zone width by approximately

50%. As was shown previously, increasing the discharge current will increase the peak

(and average) wall temperature of the cathode, resulting in additional electrons entering

the bulk plasma, but a decrease in the discharge (and sheath) voltage. The decreased

sheath voltage means a reduction in the energy per ion strike delivered to the surface, but

the ionization fraction is rising, so the total number of ions available to fall through the

sheath at any location inside the cathode increases. The net result of these competing

effects is additional heating of the cathode over a larger area, thus a larger active zone.

A reduction in the mass flow rate through the cathode results in an increase in the

width of the active zone. One can see from Figure 59 that for a constant current the peak

cathode wall temperature decreases with decreasing mass flow rate - to account for the

corresponding loss in thermionic current emission, the width of the active zone will

increases (and thus the temperature of the surrounding area will increase, flattening out

the wall temperature profile).

Reducing the mass flow rate will reduce the neutral gas density, and thus the

number of particles available inside the cathode to become charge carriers, which

decreases the plasma density (Figure 75). This decrease in plasma density means that the

total number of ions near the wall available to fall through the sheath and deposit energy

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to the wall has decreased, and this corresponds to an increase in the area over which the

plasma needs to “attach” to the wall and the ions deposit energy from wall strikes. The

result is the location of peak temperature moves further upstream and the region of

plasma attachment to the cathode wall increases.

This is a possible explanation for the superior operational characteristics of the

multi channel hollow cathodes (MCHC’s) reported in previous studies [7]. It has been

observed that for the same mass flow rates and discharge current, increasing the diameter

of the cathode will decrease the peak temperature, lengthening the active zone. This is the

same effect as discussed above because at a constant mass flow rate, increasing the

cathode diameter will reduce the density inside the cathode. Thus the peak temperature

and width of the active zone are controlled by the density of gas inside the cathode,

which can be controlled by cathode geometry and flow rate.

The MCHC devices are known to operate at lower temperatures. Studies at

Princeton have concluded that reduced losses through thermal radiation to be a key

contributing factor to the increased performance. Noticeably, a report detailing

comparison of SCHC and MCHC devices operating at the same total mass flow rate per

cross sectional open channel area is absent from the literature. Such a comparison would

yield valuable evidence to confirm the relationship seen in the present study.

A MCHC divides the total mass flow among many separate channels, reducing

the mass flow rate inside any given channel. It has been observed that at lower discharge

currents the plasma will attach to the central channels without also attaching to the

channels closer to the periphery. A measurement of the density of gas inside each channel

would provide useful insight to the performance of the MCHC. Due to boundary layer

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effects, and the physical impedance to the flow presented by the MCHC geometry, the

density of each channel is not expected to be uniform. Thus, lower density’s in the central

channels may be the cause of this phenomenon. Depending upon which side the of the

voltage vs flow rate curve the device is operating on, lower densities would provide

conditions permitting discharge at lower voltages and thus present a more efficient path

for the plasma attachment.

Previous research had modeled the active zone of the IPC as the region of plasma

attachment with a width is equal to 3 times the wall thickness of the cathode. This

constraint prevented the capture of the trend relations between the flow rate, discharge

current and active zone width, thus leading to the erroneous conclusion that processes in

the active zone are independent of mass flow rate. Additional work on the MCHC is

contained later in this chapter.

Note the effects of increasing either the discharge current or the mass flow rate.

Both conditions will result in higher peak cathode temperatures, although they will have

the opposite effect on the width of the active zone. Thus, peak temperature appears not to

be directly connected with the width of the active zone. However, the total discharge

voltage does appear to be connected. Temperature data was only taken for mass flow

rates on the left side of the minimum of the voltage vs. mass flow rate curves. Additional

information on how the active zone changes over the full range of the trend seen in

discharge voltage would provide useful information.

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Computational Predictions:

The code used in the study is a modified version of the IrOrca2D numerical model

developed for the NSTAR and NEXIS orificed hollow cathodes, which operates in the

continuum regime [42, 43, 44]. The open-ended cathodes in this study are known to

operate in the transition regime between continuum and free molecular flow. The choice

of IrOrca2D as the basis for the computational analysis tool was made for reasons of

domain similarity, resource availability, and the absence of a proven and well agreed

upon transitional flow model. Certain limitations were known to exist as a result of the

variance in operating regimes. Most noticeable among the compromises is the models

inability to converge for internal pressures below ~700 militorr. To avoid such problems

in the computational analysis, the downstream pressure boundary condition was

artificially raised to levels sufficient to ensure convergence. Thus the interior pressure

profile of the computational model is well above that experienced in the actually

experiment.

The original plan called for experimentally gathering profiles for the boundary

conditions at the cathode orifice plane from the acquisition of data at several radial

locations along the exit plane boundary. Once the discharge was established, it was

discovered that the positioning system necessary for establishing the profiles would fail

to operate under the extreme heat loads to which it was subjected during discharge

operation. Eventually the positioning system failed all together. As a result,

experimentally gathered plasma data for operating Tungsten cathodes are taken at the exit

plane, on centerline and two other radial positions, and full exit plane profiles were not

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able to be gathered. For the Tantalum cathodes, since the probe size was comparable to

the diameter of the cathode, it is believed that the presence of the probe at the exit plane

would significantly impeded the gas flow, introducing significant disturbances to the

plasma, and thus the measurements were taken on centerline, but 1 cm downstream of the

cathode exit.

Due to this inability to gather exit plane profiles, the data collected on centerline

was used as the value at all locations on the exit plane boundary in the numerical model.

In various iterations, this includes the plasma potential, plasma density, and electron

temperature.

Note that in all plots of the computation data, the axial line (z(cm)) is the distance

from the upstream boundary of the computation zone, thus the z axis for the model plots

are in the opposite direction as the experimental plots. In the computational plots, the

location at z = 4 cm is in fact the exit plane (or tip) or the cathode. Additionally, the

vertical axis gives the radial distance (in centimeters) from the centerline of the cathode.

All plots of computational data are for 6 mm diameter Tungsten cathodes, in a

high-voltage low-current plasma discharge, rendering direct comparison to the

experimental data (presented above) for 2 mm diameter Tantalum cathodes (in low-

voltage high-current discharge) somewhat difficult. Computational results from two case

studies, 215 sccm flow rate at 3.3 Amp discharge, and 185 sccm flow rate at 3.6 Amp

discharge, are presented below. Note that experimentally, the only operator-controllable

discharge parameter that was varied between the two rounds was the mass flow rate.

Figure 80 and Figure 86 show a peak plasma density near the cathode exit plane,

along with the corresponding contours of plasma potential seen in Figure 83 and Figure

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88, and heavy species temperature seen in Figure 85 and Figure 90. It was unexpected

that localized high plasma density regions existed near the upstream boundary of the

computation zone gas inlet, a previously unreported phenomenon.

Experimental evidence of this upstream plasma concentration was seen upon disassembly

of the cathode assembly after extended runs with the 10 mm cathode, when significant

Figure 80: Computed plasma density profile in 6 mm Tungsten cathode 3.3 Amp

121 Volt discharge, 215 sccm flow rate.

melting of the assembly was discovered near the upstream boundary, leading to the

strong likelihood of localized plasma in the gas inlet region. The damage to the upstream

cathode mating flange can be seen in Figure 81. Thermal conduction was determined to

be an unlikely source of the melting, as regions of higher thermal energy conductance

density did not exhibit the same destruction. Explanations as to the cause of the localized

peak plasma density have not yet been determined.

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There is a noticeable discrepancy between the cathode wall temperature

profiles input to the computational model, and the plasma density plots generated by the

model. Peak plasma generation and density is in the region of the active zone, which is

centered at the axial location of peak temperature. For the case of the 3.3 Amp discharge,

in the 6 mm Tungsten cathode with 215 sccm flow rate of Argon (temperature profiles

Figure 81; Damage of the rear mating flange after high power testing of the 10 mm

Tungsten cathode.

shown in Figure 40), the peak temperature is at an axial location of 26 mm upstream. In

Figure 80, the peak plasma density is seen at approximately 3 mm upstream of the

cathode exit plane. The difference is due to the requirement to artificially raise the

pressure inside the cathode to ensure the computation model’s numerical convergence.

Increasing the flow rate inside the cathode will displace the peak temperature further

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downstream, as is shown in the model output. Thus this discrepancy was expected, and

occurred as predicted. Figure 84 and Figure 89 displays the contour plots of the electron

temperature distribution inside the cathode. The profiles appears relatively flat, with peak

values near the exit plane of the cathode, and again a localized peak near the upstream

boundary condition.

Figure 82: Computed neutral particle density profile in 6 mm Tungsten cathode 3.3

Amp 121 Volt discharge, 215 sccm flow rate. Note that the values of computed electron temperatures are lower than those seen in the

experiment – for the 215 sccm run, the measured electron temperature at the exit plane

was approximately 5 eV, for the 185 sccm run, the measured electron temperature at the

exit plane was approximately 8 eV. These lower computed values of electron

temperatures seen in the computation plots are as a result of the artificially increased

internal cathode pressure in the model, and are consistent with experimental and

computation data for cathodes run at higher pressures than those in this experiment, as

shown by previous research [20, 26, 42, 43, 44]. The additional, relatively cold, heavy

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Figure 83: Computed plasma potential profile in 6 mm Tungsten cathode 3.3 Amp

121 Volt discharge, 215 sccm flow rate.

Figure 84: Computed electron temperature (eV) potential profile in 6 mm Tungsten

cathode 3.3 Amp 121 Volt discharge, 215 sccm flow rate.

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species particles will cool the electrons through collisions (both elastic and inelastic, with

the inelastic processes chiefly responsible for the transfer of energy from the electrons),

yielding a flatter profile. (Note that the Langmuir probe measurements taken for the 6

mm Tungsten cathodes, as input boundary conditions to the model, were among the first

iterations of probe designs and technique used in this study, and thus the confidence in

the reliability the results from those measurements is not as high as for later iterations. As

the study progressed, iteration in both Langmuir probe design and technique led to higher

confidence in probe results – unfortunately the 6 mm Tungsten cathodes were destroyed

very early in the experimental phase, thus, more-reliable Langmuir probing of the

Tungsten cathode discharge was not possible.)

Temperature contour plots of the heavy species can be seen in Figure 85 and

Figure 90. Localized peaks in the temperature can be seen near the upstream and

downstream boundaries correspond in position to locations of local maximums in the

plasma potential and plasma densities. This is expected, as the cooler neutrals will gain

energy from collisions with the electrons, the electrons gain energy moving through steep

plasma potential gradients. Thus regions of high potential gradients should show

significant transfer of energy through collisions, and thus the generation of plasma.

Data generated from the numerical model have permitted the mapping of the

internal plasma column of a single channel hollow cathode. The model has predicted the

distribution of the plasma density, plasma potential, neural gas density, heavy species

temperature, and electron temperature inside the cathode. Model results have shown the

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Figure 85: Computed heavy species temperature (K) profile in 6 mm Tungsten

cathode 3.3 Amp 121 Volt discharge, 215 sccm flow rate.

Figure 86: Computed plasma density profile in a 6 mm Tungsten cathode, 3.6 Amp

discharge, 185 sccm Argon flow rate.

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Figure 87: Computed neutral particle density profile in a 6 mm Tungsten cathode,

3.6 Amp discharge, 185 sccm Argon flow rate.

Figure 88: Computed plasma potential profile in a 6 mm Tungsten cathode, 3.6

Amp discharge, 185 sccm Argon flow rate.

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Figure 89: Computed electron temperature (eV) profile in a 6 mm Tungsten

cathode, 3.6 Amp discharge, 185 sccm Argon flow rate.

Figure 90: Computed heavy species temperature (K) profile in a 6 mm Tungsten

cathode, 3.6 Amp discharge, 185 sccm Argon flow rate.

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previously undiscovered presence of plasma generation further upstream of the cathode

active zone. In addition, previously unexpected experimental evidence was shown in

support of this prediction.

Figure 91 and Figure 92 show the computation results as the mass flow rate is

varied inside the cathode. For these plots the internal cathode pressure profile was

increased by a multiple, while all other input parameters remained unchanged. The results

were normalized, and baselined to the 185 sccm and 215 sccm flow rate cases,

respectivly. Peak values for the electron temperature, plasma potential, and plasma

density are shows as functions of the normalized pressure. Note that the model predicts

the correct trends in the electron temperature and the plasma potential. Trends shown in

the model are also consistent with previous research [20, 26, 42, 43, 44], which has

shown the decreased electron temperatures of higher-pressure cathode environments.

Unexplained are the predicted trends in plasma density. As presented earlier, experiments

show the plasma density to be an increasing function of the internal cathode pressure. As

the two plots show, the model predicts a decreasing trend. This inconsistency had not

been resolved.

The desired performance of MPD thrusters typically results in operating ranges of

mass flow ranges that place the cathode well within the transitional flow regime. The

physical characteristics of the regime will lead to expected limitations on any efforts to

study the cathode with models grounded in the equations of magnetohydrodynamics, or

any continuum flow based model. It is recommended that future attempts at predictive

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Figure 91: Normalized plasma parameters vs. normalized pressure. Baselined to 185 sccm case.

Figure 92: Normalized plasma parameters vs. normalized pressure. Baselined to 215

sccm case.

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capable modeling of the IPC begin with either an attempt to develop a transitional flow

model, or to employ a free molecular model.

Comparison of a free molecular flow model, with the computational results of this study,

will no doubt yield valuable insight leading to the determination of a more reliable

method of open-ended hollow cathode modeling. It may be that neither an continuum

model, or a free molecular flow model is appropriate, in which case a true transitional

flow model will be required.

7.4 Connection to Multi Channel Hollow Cathodes

Examination of the results of this study on single channel hollow cathodes can

yield valuable insight to multi channel hollow cathodes. Though literature on the MCHC

devices is scarce, with most of the work done being experimental and the writing

focusing on performance, previous studies have reported several trends in comparison to

the operation of the SCHC, under similar conditions, notably:

1. MCHC’s operate at lower temperatures with equal discharge current

2. MCHC’s operate at lower discharge voltages with identical current and flow rate

3. MCHC center channels light first, experience highest erosion, and at low

discharge currents may be the only channels to have significant plasma

attachment

4. A MCHC divide total mass flow among many separate channels reducing the

mass flow rate inside any given channel.

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Let us apply the insight gained from this SCHC study to these listed traits of the MCHC.

First , we must consider the gas flow in the region upstream of the numerous channels,

first seen in Figure 7 and reproduced here in Figure 93. The flow regime in this upstream

region will be continuum, thus boundary layer and viscous effects will cause a velocity

profile as shown in the figure, with the highest gas flow velocity along the centerline, and

the lowest at the periphery. The continuum flow will also result in a gas density profile

inverse in shape of the velocity profile, that is gas along the centerline will be the least

dense, and gas near the cathode wall will have the highest density.

Figure 93: Gas flow in MCHC upstream of channels

When the gas flow reaches the upstream boundary of the hollow channels, the

density profile results in a radial gradient in the gas density inside the channels – that is,

gas flow through the channels along the periphery will have the highest density, and gas

flow through the central channels will have the lowest density. Referencing the data in

Figure 42 and Figure 43, (specifically the region to the right of the minimum), recall that

reduced mass flow rate (gas density) will require a reduced discharge voltage. In the

MCHC devices, we see that the central channels will light first, and at lower current

levels, can sustain the entire arc discharge plasma attachment with out lighting any of the

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outer channels. This is as a result of the radial density gradient – the central channels

have the lowest gas density, thus the require the lowest voltage to maintain the discharge.

So the central channels light first, and can stay lit without the inclusion of outer channels,

because they present the most desirable (efficient) environment for sustaining an arc

discharge.

As the discharge current is raised, the wall temperature central channels will

increase. In an SCHC, increased wall temperature results in increased power lost due to

thermal radiation – (nearly) all power radiated by the exterior surface is a loss to the

system. In a MCHC, because all the channel walls are in physical contact with each other,

heat from the central channels is transferred away to the walls of other channels through

conduction, and any power radiated from the walls of one channel is adsorbed by the

walls of other channels. Thus, very little heat from the inner channels is a loss to the

system. An increase in the discharge current will raise the peak temperature of the central

channels, resulting in more heat transferred to outer channels, increasing the thermionic

emission from those regions, though the bulk of the discharge current will continue to be

carried by the central channels. This is why we see that the material of the central

channels shows the most erosion, as seen in Figure 9 and Figure 10, and reproduced here

in Figure 94. The tight thermal coupling among the channel walls is directly responsible

for reduced power losses from radiative cooling, resulting in a lower required discharge

power (thus voltage), in comparison to a SCHC of equal mass flow rate and discharge

current.

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Figure 94: Exit plane of MCHC before, and after operation. Note the increased

erosion in the central channels

The radial gas density gradient seen in the gas flow through the channels will

continue through out the duration of cathode operation, from ignition, through the point

at which the discharge current is large enough to require all channels to emit

thermionically. Correspondingly, there should be a radial gradient in the plasma density

and electron temperature of the discharge plasma among the channels. Thus, again

considering the relations discovered in the discharge plasma of the SCHC, the central

channels of the MCHC, having the highest discharge current and lowest interior gas

density, will have two competing effects governing the temperature of the electrons from

those channels – the higher discharge current will tend to decrease the electron

temperature, where as the lower gas density will tend to increase electron temperatures.

Direct experimental measurements are required to determine the dominant mechanism.

Also, it is unclear what, if any, difference will exist in the sheath drop amongst the

different channels. This possible difference in voltages can play a strong role governing

the efficiency of the discharge and the properties of the plasma discharge, as was seen for

the SCHC.

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Generally speaking, we would expect the width of the active zone the be the

highest in the central channels, thus showing that these regions spread the thermal

loading to a greater degree than channels lying close to the periphery. Referencing trends

discovered for the SCHC active zone width, the central channels carry the largest

discharge current, with the lowest gas density, both of which push towards higher active

zone widths. Direct measurements of wall temperatures inside an operation MCHC will

make confirmation of this hypothesis challenging. Also, speaking again of a potential

gradient in sheath drop among the channels, it is unclear how significant the contribution

from Shottkey effect is.

One can ask the question, would better performance be achieved by a MCHC with

many small channels, or just a few channels of larger diameter. While this question can

only be answered by experiment, the insight gained from this study suggests that the total

open cross sectional area of the cathode should be maximized in an effort to reduce the

peak operating temperature, but not so low as to pass the minimum in required discharge

voltage, entering an operating regime where discharge power increases rapidly with

decreasing mass flow rate.

7.5 Summary of Results

From the data collected in this research and others, the following conclusions can be

drawn about the operating characteristics of a single channel hollow cathode. Key

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conclusions are those concerning the thermal loading as seen in the trends of peak

cathode temperature and size of the active zone.

Magnitude of Peak Temperature:

• Magnitude of the peak temperature along the hollow cathode is weakly but clearly

dependant upon mass flow rate (interior gas density), with higher flow rates

resulting in higher peak temperatures. This is inconsistent with previous hollow

cathode research [9] where the magnitude of the peak cathode temperature was

concluded to be invariant with mass flow rate.

• Magnitude of the peak temperature along the hollow cathode is dependant upon

discharge current, with increasing discharge current yielding a higher peak

temperature.

• Magnitude of the peak temperature along the hollow cathode is dependant upon

the diameter of the cathode, with the peak temperature increasing with decreasing

cathode diameter for a constant mass flow rate. Note that this is a gas density

effect.

“Hot Spot” or “Active Zone”:

For the purposes of this analysis, the active zone is defined as the surface area of the

cathode responsible for 75 percent of the total thermionic emission of electron current.

• The active zone width increases as mass flow rate decreases. Lowering the flow

rate (density) will also increase the efficiency of the discharge by lowering the

discharge voltage. Lower discharge power can be achieved by varying the flow

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rate, to a minimum discharge power value unique for each combination of

discharge currents and electrode geometry. Lowering of the gas density beyond

this point will still yield longer lifetimes, but at the cost of efficiency. A balance

between power and lifetime will have to be chosen for optimal performance to

meet requirements for any missions choosing to use these cathodes. Note that

previous research [9] concluded the width of the active zone primarily depend

upon cathode wall thickness. Results of this study appear to contradict these

previous findings – in this study, the cathode wall thickness was not varied,

though changes in the discharge current and mass flow rate were able to yield

changes in the active zone width of up to 300 percent

• The active zone width increases as discharge current increases.

• The width of the active zone does not appear to be connected to the peak wall

temperature of the cathode.

• The width of the active zone appears to be controlled by the discharge voltage,

with a larger voltage resulting in a small active zone width. is determined by the

density of gas inside the hollow cathode. Lowering the flow rate (density) will

yield lower cathode temperature profiles, reducing cathode material erosion rates

and resulting in longer cathode lifetimes.

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Location of Peak Temperature:

• Location of the peak temperature along the hollow cathode is dependant upon

flow rate, with higher flow rates moving the peak temperature further down

stream. This trend is consistent over all flow rates tested.

• Location of the peak temperature along the hollow cathode is not dependant upon

discharge current.

• Location of the peak temperature along the hollow cathode is dependant upon the

diameter of the cathode, with the peak temperature moving further downstream

towards the exit plane with decreasing cathode diameter at constant mass flow

rate. Note that this is a gas pressure effect.

Temperature Gradient:

• The axial temperature gradient along the cathode is steeper upstream of the

location of peak temperature than it is downstream.

Discharge Voltage:

• The total discharge voltage is dependant upon the flow rate – for a given electrode

geometry and constant current, the discharge voltage displays a non-linear

dependence upon the flow rate, showing a minimum at a certain flow rate. Note

that previous research results only reported a decrease in discharge voltage with

increasing flow rate.

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• The total discharge voltage is dependant upon the discharge current, with a larger

current requiring a lower discharge voltage.

Power:

• The total power consumed by the cathode discharge is dependent upon the mass

flow rate (and thus the internal cathode pressure). For a constant current, at higher

mass flow rates, the power is an increasing function of increasing mass flow rate,

showing a somewhat linear trend over the range of flow rates tested. While at

lower flow rates, there is a minimum in the power consumed. At lower flow rates,

the discharge power shows an inverse relation, with power decreasing as mass

flow rate increases, to a minimum, beyond which the trend switches to increasing

discharge power. This trend is seen over all ranges of discharge currents tested

and is believed to continue for higher current levels beyond those seen in this

work

• The total power consumed by the cathode discharge is proportional to the

discharge current. For a given flow rate, higher currents consumed more power

over all flow rates tested.

• The power consumed by the discharge, per unit of mass flow rate, is a decreasing

function of the mass flow rate over all ranges tested.

For plasma parameters measured 1cm downstream of the cathode, along center line:

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Electron Temperature:

• The electron temperature decreases with increasing discharge current.

• The electron temperature decreases with increasing mass flow rate.

Plasma Potential:

• The plasma potential decreases as the mass flow rate increases.

• No clear dependence of the plasma potential upon the discharge current could be

determined

Plasma Density:

• The plasma density increases as the discharge current increases.

• The plasma density increases as the mass flow rate increases.

Plasma Generation

• Unexpected plasma generation was predicted in regions near the gas inlet of the

cathode. Experimental evidence was obtained to support the predictions.

• The ionization fraction of the discharge plasma increases with increasing mass

flow rate.

• The ionization fraction of the discharge plasma increases with increasing

discharge current.

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The key conclusion are useful to designers of high current cathodes of MPD thrusters

who’s primary focus is to maintain a set point thruster operating condition (discharge

current) and attain the lowest cathode material erosion rate by reducing peak operating

temperature. From the results of this study, superior cathode thermal performance can be

achieved by reducing the discharge voltage, or the gas density in the interior of the

cathode. Reduced gas density will reduce the peak cathode temperature and increase the

size of the active zone, thus achieving longer lifetimes by reducing the material erosion

rate. Reduced interior gas density can be achieved by a reduction of the mass flow rate, or

a change in the physical geometry of the cathode itself (cross sectional area). Reduction

of the discharge voltage increases the width of the active zone, reducing the thermal

loading on the cathode. For the MCHC’s seen as a possible solution to the erosion

problem, reduced peak operating temperature can again be achieved by reduction in

interior gas density, but designers must be aware of the increasing discharge power if gas

density falls too low. Methods which can increase the sheath drop across the cathode in

the upstream regions of the cathode may cause a distribution of the thermal loading.

Additionally, this work has demonstrated the limitations of a continuum flow /

MHD model in the analysis of high current SCHC’s. The operating regimes of cathodes

found in state-of-the-art MPD thrusters fall within the transitional regime. Thus, though

continuum flow models may provide usefully information for qualitative analysis for

such cathodes, they are inappropriate for quantitative performance predictions necessary

for mission planners and cathode designers.

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7.5 Suggestions for Future Work

The contained research has added to the growing database of knowledge of high-

current hollow cathodes, though a complete understanding of the operation of these

devices is far from complete. Much additional research into the performance

characteristics and lifetime of high-current hollow cathodes is necessary for deployment

of these devices on flight missions. The relation between the width of the active zone and

the discharge voltage could be significant. Additional measurements correlating the

effects of these two parameters are desirable.

Additional cathode geometries must be tested for both performance and lifetime

including comparison between the operating characteristics of the single channel hollow

cathode to the multi channel hollow cathode. In particular, the operation of a SCHC and a

MCHC with equal flow rate per unit of cross sectional area is necessary to demonstrate

the relation between gas density in the channels of the cathode and the peak operating

temperatures. In addition, a relation between the plasma potential and the mass flow rate

must be resolved, along with the identification modeling of the physics controlling the

relationship.

Multi-channel-hollow-cathodes show good potential for the future of high current

MPD thrusters, though more experimental work is clearly needed. In particular,

measurements of the plasma density, ionization fraction and electron temperature of the

discharge plasma from each channel would provide data required to validate hypothesis

made about MCHC operation in this work. Additionally, though it is a significant

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challenge, measurements of the wall temperature profiles on the inside of MCHC

channels are of prime importance.

One item of note from this researcher is an extremely high surface area geometry

structure capable of being manufactured at Ultramet. The geometry closely resembles

that of a sponge, and can be manufactured with refractory metals, specifically Tungsten.

This construction can allow for total interior surface areas of the cathode orders of

magnitude higher than the state of the art MCHC’s, allowing for correlation of available

surface area to cathode performance. This geometrical structure has several benefits:

Radiation from interior sections of the sponge-structure will be reabsorbed by other

cathode material, reducing losses and increasing efficiency. In addition, due to the

geometry of the structure any material upstream in the cathode removed from the

structure by evaporation has a high likelihood of being re-deposited elsewhere on the

interior structure further upstream, yielding reduced overall material losses, leading to

longer lifetimes. Determination of the peak operating temperatures and the distribution of

the active zone would present significant challenges in such an irregular geometry, as the

documented technique of measuring exterior cathode surface temperatures would not

yield reliable data about interior temperature and plasma distribution.

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39. Michael LaPointe, Pavlos Mikellides, “Design and Operation fo MW-Class MPD Thrusters at the NASA Glenn Research Center”. AIAA 2002-4113.

40. Maclsaac, Kanner and Anderson, “Basic Physics of the Incandescent Lamp”. The Physics Teacher, Vol. 37, December 1999.

41. A. Malik, P. Montarde, M. Haines, “Spectroscopic Measurements of Xenon Plasma in a Hollow Cathode”. Journal of Physics D: Applied Physics, Volume 33, # 16, 2000, pgs 2037-2048.

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Appendix A:

Evaluation of Governing Equations

A through evaluation of the method of translating analytical equations into a numerical

model is necessary to provide a solid understanding of the nature of the computation

solutions and required boundary conditions. In this section the numerical approximation

to each equation in the model will be laid bare for the purposes of developing a complete

understanding of the method of solution and requirements of boundary conditions. All

equations will refer to a generic sample computational grid shown below in Figure 95.

Figure 95: Example of a generic computational zone grid

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In general, the volume of each cell is unique, as is the area of each cell edge and

the distance from the center of one cell to the center of an adjacent cell. In the following

derivations, subscripts will represent parameter identification, and superscripts represent

time steps. In the following derivations, discussion of the transport properties (collision

frequencies, etc.) is neglected.

Plasma Density, ni=ne

Since the time dependent form of the electron conservation eqn is used in the

derivation of other equations, it must be solved in its time dependent form. By the finite

volume method, we can write the following for the ion continuity equation, where ne is

the parameter value at any cell location (i,j):

ee iz i

ee iz i

V V

1

1

n n jt e

n n dV j dVt e

ν

ν

∂− = − ∇

∂∂⎛ ⎞ ⎛ ⎞− = − ∇⎜ ⎟⎜ ⎟∂ ⎝ ⎠⎝ ⎠∫∫∫ ∫∫∫

i

i A.1)

According to the principles of the finite volume method and the divergence theorem, we

can observe the following numerical approximation:

( ) ( )

( ) ( )( )all cellfaces

cellface r1

ˆ

ˆ ˆ

i iV S

i irS

j dV j n dS

j n dS j n A=

∇ =

=

∫∫∫ ∫∫

∑∫∫

i i

i i A.2)

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188

Further, using a first order forward difference approximation, and assuming that the

argument of the volume integral represents the average value of that argument over the

differential volume region, we can write:

( )( )

( )( )

{ } { } ( )( )

all cellfaces

ee iz i i edger=1

all cellr+1 r edges

a ae ee iz i edge1

all

r+1 re e icell edge1cell

1 1 ˆ

...

1 ˆ

...

ˆ

V V

n n dV j dV j n At e e

n n n dxdydz j n At e

tn n u n AV

ν

ν

∂⎛ ⎞ ⎛ ⎞ ⎛ ⎞− = − ∇ = −⎜ ⎟ ⎜ ⎟⎜ ⎟∂ ⎝ ⎠ ⎝ ⎠⎝ ⎠

⎡ ⎤− ⎛ ⎞− = −⎜ ⎟⎢ ⎥Δ ⎝ ⎠⎣ ⎦

⎛ ⎞Δ= Δ⎜ ⎟⎜ ⎟Δ⎝ ⎠

∑∫∫∫ ∫∫∫

i i

i

i { } cell

edgesre iz cell

n tν+ Δ∑

A.3)

which will provide the values of the plasma density ne for any cell located in the grid at

position (i,j), at time step r+1. Thus the value of the plasma density is shown to be an

explicit function of known parameters calculated at the previous time step.

Boundary and initial conditions: From this last equation one can observe that the

value of the plasma density at a given cell (at the advanced time step) is a function of the

ion current (and hence plasma density), for the previous time step, evaluated at each edge

of the cell. Thus when the cell in question is on the boarder of the computational region,

the value of the plasma density and ion current at that edge are required. Thus values of

ion current at all boundaries of the computational zone are required for solutions of this

equation. At the upstream boundary condition ions are allowed to flux out of the

computational zone at the thermal speed

As can be seen from the above equation, the solution for the plasma density at the

next time step (r+1) requires the value of the plasma density at all locations at the

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189

previous time step. Thus prior to the first execution of this equation, we must assign an

initial value to the plasma density at each cell.

Plasma Temperature, Te

Starting with the electron energy equation and expanding the temporal derivative we have

the following

( ) ( )( )

( ) ( )

ee iz e e e

2e e iz e e iz

3 3 32 2 2

1 5 32 2

e ee e e e e

ee e e e e ei en e e h

h

n T Te n T e T n e T n n u nt t t t

mm n u T j T E j n e T T n eM

ν

ν κ ν ν ν ε

∂ ∂ ∂∂ ⎡ ⎤ ⎡ ⎤= + = − ∇ + =⎢ ⎥ ⎢ ⎥∂ ∂ ∂ ∂⎣ ⎦ ⎣ ⎦⎡ ⎤= + ∇ + ∇ + − + − −⎢ ⎥⎣ ⎦

i

i i A.4)

Substitution of the election continuity equation and rearranging terms yields

( )( ) ( )( ) 2e iz e

5 22 3

2 123 3

ee e e e e

e

e eei en e h iz e iz i i

h e

T T j T E jt en

m TT T n n u m uM n e

κ

ν ν ν ε ν ν

∂ ⎡ ⎤⎛ ⎞= ∇ + ∇ + −⎜ ⎟⎢ ⎥∂ ⎝ ⎠⎣ ⎦⎡ ⎤⎛ ⎞

+ − + + − ∇ −⎢ ⎥⎜ ⎟⎝ ⎠⎣ ⎦

i i

i A.5)

Application of finite volume method yields the followin:

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190

( ) ( )( ) ( )

ee e e e e

e eS

2e e ei i ei en e h iz e iz e iz e

e h eS

r+1 re e

cellvalue

e

2 5 2ˆ ...3 2 3

2 1ˆ... 23 3

...

2...3

V V

V

T dV T j T ndA E j dVt en en

T m Tn u ndA T T n m u dVn M n e

T T Vt

en

κ

ν ν ν ε ν ν

∂ ⎛ ⎞= + ∇ + +⎜ ⎟∂ ⎝ ⎠

⎡ ⎤⎛ ⎞− − + − + + −⎢ ⎥⎜ ⎟

⎝ ⎠⎣ ⎦⎧ ⎫−

Δ =⎨ ⎬Δ⎩ ⎭

⎛ ⎞⎜ ⎟⎝ ⎠

∫∫∫ ∫∫ ∫∫∫

∫∫ ∫∫∫

i i

i

( )

( )( ) ( )( )

all 4 cell edges

r re e e e e

cell avg value1 edge evalue for cell

rr 2e e

ei en e h iz e iz i i e iz eh e avg value

for cell

5 2ˆ ...2 3

2 1... 23 3

T j T n A E j Ven

m TT T n n u m u VM n e

κ

ν ν ν ε ν ν

⎧ ⎫⎧ ⎫+ ∇ Δ + Δ +⎨ ⎬ ⎨ ⎬⎩ ⎭ ⎩ ⎭

⎧ ⎫⎡ ⎤⎛ ⎞⎪ ⎪− + − + + − ∇ − Δ⎨ ⎬⎢ ⎥⎜ ⎟⎝ ⎠⎪ ⎪⎣ ⎦⎩ ⎭

∑ i i

i

A.6)

And finally, the new value for the electron temperature at the next time step (r+1) for a

given cell is determined from:

{ }

{ } ( )

( )( )

1cellvalue

all 4 cell edges

cell avg valuevalue cell 1 edge for cell atvalue time step 'r'

...

2 5 2ˆ... ...3 2 3

2... 23

re

r r re e e e e e

e e

reei en e h iz

h

T

T t T j T n A t E jen V en

mt T TM

κ

ν ν ν ε

+ =

⎛ ⎞ ⎧ ⎫⎧ ⎫+ Δ + ∇ Δ + Δ⎨ ⎬ ⎨ ⎬⎜ ⎟Δ ⎩ ⎭⎝ ⎠ ⎩ ⎭

⎛ ⎞− Δ + − + +⎜ ⎟

⎝ ⎠

∑ i i

( )( ) 2e iz e

avg valuefor cell attime step 'r'

13

re

e iz i ie

Tn n u m un e

ν ν⎧ ⎫⎪ ⎪− ∇ −⎨ ⎬⎪ ⎪⎩ ⎭

i

A.7)

Thus the value of the electron temperature is shown to be an explicit function of known

parameters.

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191

Boundary and initial conditions: From the above equation, notice that solutions for the

electron temperature at a given cell (at the advanced time step) requires the values of the

electron temperature, electron density and velocity, and electron temperature gradient

evaluated at each edge of the cell for the previous time step. Thus the values of these

parameters on all boundaries of the computation region are required for solutions to the

above equation.

As can be seen from the above equation, the solution for the electron temperature

at the next time step (r+1) requires the value of the electron temperature at all locations at

the previous time step. Thus prior to the first execution of this equation, we must assign

an initial value to the electron temperature at each cell.

Plasma Potential, φ

Values of the plasma potential can be found from solutions to the following equation:

( )e e e en ein i

e ei en iz en ei iz

1n T enu j

nν νφ

η η ν ν ν ν ν ν⎡ ⎤∇ ⎛ ⎞ ⎛ ⎞⎛ ⎞∇

∇ = ∇ − + −⎢ ⎥⎜ ⎟ ⎜ ⎟⎜ ⎟ + + + +⎝ ⎠ ⎝ ⎠ ⎝ ⎠⎣ ⎦i i

A.8)

Application of the finite volume method and the divergence theorem yields the following:

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192

( )( )

( )all celledges

1 edge

ˆ ˆ1

ˆ ˆ1

en n e

e e e en n eii

e ei en iz en ei izS S

u me

e e en n e eii

e en ei iz

n T en undA j ndAn

n T u mn A j nn e

νη

ν νφη η ν ν ν ν ν ν

ν νφη η η ν ν ν

=

⎡ ⎤⎢ ⎥⎢ ⎥∇ ⎛ ⎞∇

= − + −⎢ ⎥⎜ ⎟+ + + +⎝ ⎠⎢ ⎥⎢ ⎥⎢ ⎥⎣ ⎦

⎡ ⎤∇ ⎛ ⎞⎧ ⎫∇Δ = − + − Δ⎨ ⎬ ⎢ ⎥⎜ ⎟+ +⎩ ⎭ ⎝ ⎠⎣ ⎦

∫∫ ∫∫

i i

i iall celledges

1edge

A⎧ ⎫⎪ ⎪⎨ ⎬⎪ ⎪⎩ ⎭

A.9)

From here, the LHS must be evaluated further to yield the required insight:

all cell sides

1 edge 1 edge 3edge 2 edge 4

1, , , 1 , ,

½, , ½½, , ½

ˆS

i j i j i j i j i j

i j i ji j i j

A A A AndA Ax y x y

A Al l

φ φ φ φ φ φη η η η η η

φ φ φ φ φη η+ +

+ ++ +

⎛ ⎞ ⎛ ⎞⎛ ⎞ ⎛ ⎞ ⎛ ⎞∇ ∇ ∂ ∂ ∂ ∂• = = + + +⎜ ⎟ ⎜ ⎟⎜ ⎟ ⎜ ⎟ ⎜ ⎟∂ ∂ ∂ ∂⎝ ⎠ ⎝ ⎠ ⎝ ⎠⎝ ⎠ ⎝ ⎠

⎛ ⎞ ⎛ ⎞− −⎛ ⎞ ⎛ ⎞+ −⎜ ⎟ ⎜ ⎟⎜ ⎟ ⎜ ⎟⎜ ⎟ ⎜ ⎟Δ Δ⎝ ⎠ ⎝ ⎠⎝ ⎠ ⎝ ⎠=

∑∫∫

1,

½,½,

, , 1

, ½, ½

...

...

i j

i ji j

i j i j

i ji j

Al

Al

φη

φ φη

−−

−−

⎡ ⎤⎛ ⎞− ⎛ ⎞ −⎢ ⎥⎜ ⎟⎜ ⎟⎜ ⎟ Δ⎝ ⎠⎢ ⎥⎝ ⎠⎢ ⎥

⎛ ⎞− ⎛ ⎞⎢ ⎥⎜ ⎟⎜ ⎟⎢ ⎥⎜ ⎟ Δ⎝ ⎠⎝ ⎠⎣ ⎦

A.10)

further…

i,j

1 1 1 1i+ ,j i,j+ i- ,j i,j-2 2 2 2

i+1,j i,j+1 i,j-1 i-1,j1 1 1 1i+ ,j i,j+ i,j- i- ,j2 2 2 2

ˆS

ndA

A A A AL L L L

A A A AL L L L

φη

φη η η η

φ φ φ φη η η η

⎛ ⎞∇• =⎜ ⎟

⎝ ⎠⎡ ⎛ ⎞⎛ ⎞ ⎛ ⎞ ⎛ ⎞ ⎛ ⎞⎢ ⎜ ⎟− − − − +⎜ ⎟ ⎜ ⎟ ⎜ ⎟ ⎜ ⎟⎢ ⎜ ⎟Δ Δ Δ Δ⎝ ⎠ ⎝ ⎠ ⎝ ⎠ ⎝ ⎠⎝ ⎠= ⎢⎢ ⎛ ⎞ ⎛ ⎞ ⎛ ⎞ ⎛ ⎞

+ + +⎢ ⎜ ⎟ ⎜ ⎟ ⎜ ⎟ ⎜ ⎟Δ Δ Δ Δ⎝ ⎠ ⎝ ⎠ ⎝ ⎠ ⎝ ⎠⎢⎣

∫∫⎤⎥⎥⎥⎥⎥⎥⎦

A.11)

This is the final form of the numerical evaluation of the left hand side of the plasma

potential equation. Since the plasma potential equation is a steady state equation, all

properties are considered at the same “time step”, and though the equation is steady state

initial values are necessary.

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193

Boundary and initial conditions: Note that the plasma potential at a cell (i,j)

depends upon the values of the potential at the adjacent cells (above, below, left and

right), thus an initial value (which is in general a guess) of the plasma potential at all cells

must be known. However, once the equation is solved for a given cell (say i,j), the value

at an adjacent cell using the newly calculated value at cell (i,j) is then altered, (which in

tern would alter the solution at the original cell i,j). It is then obvious that a system of

liner equations is then formed (which can be put into a matrix), all of which must be

solved simultaneously. In the code, this is accomplished by using solver routines

contained in the Compaq Extended Math Library (CXML) which is made available

through the choice of compilers. The solution method employed is termed the least

squares conjugate gradient method, which is an iterative solver method useful when

working with sparsely populated matrices.

At the boundaries of the computational zone, values of the plasma potential are

necessary for “ghost cells” located outside the boundaries. Also required are values of the

plasma resistivity, neutral gas velocity, ion current density, and pressure gradient on the

boundaries of the computational zone. Two spatial boundary conditions in each direction

are imposed.

Electric Field Vector, E

The equation for the electric field is given by:

E φ= −∇

A.12)

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194

The numerical evaluation of the above equation is relatively straight forward:

{ } { } i+1,j i,jedgeedge

1i+ ,j1i+ ,j 2 cell (i+1,j) to (i,j)2

ˆ ˆ

E

E n nl

φ

φ φφ

= −∇

⎧ ⎫−⎪ ⎪= − ∇ = − ⎨ ⎬Δ⎪ ⎪⎩ ⎭i i A.13)

And so for any given edge (i + ½, j) the value of the electric field is found from the above

expression.

Boundary and initial conditions: From this it is shown that once values of the

plasma potential are known, the electric field is an explicit function of the plasma

potential (and geometric factors). Thus the value of the plasma potential in the “ghost”

cell locations must be known.

Ion Current Density Vector, ji

The equation for the ion current density is given by:

( ) ( ) he e h e e en iz n e e en i in

iin

h iz

2

2

Me n e T T m j u e n m nj

M

ν ν ν ν

ν ν

⎛ ⎞− ∇ + + + + +⎡ ⎤ ⎜ ⎟⎣ ⎦ ⎝ ⎠=⎛ ⎞+⎜ ⎟⎝ ⎠

A.14)

As with the electric field vector, the evaluation of the ion current density vector is

relatively straight forward:

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195

( ) ( )

{ }( ) ( )

he e h e e en iz n e e en i in

iin

h iz

he e h e e en iz n e e en i in

i 1edge i+ ,j2 inh iz

2

2

2ˆ ˆ

2

Me n e T T m j u e n m nj

M

Me n e T T m j u e n m nj n n

M

ν ν ν ν

ν ν

ν ν ν ν

ν ν

⎡ ⎤⎛ ⎞− ∇ + + + + +⎡ ⎤ ⎜ ⎟⎢ ⎣ ⎦ ⎥⎝ ⎠⎢ ⎥=⎛ ⎞⎢ ⎥+⎜ ⎟⎢ ⎥⎝ ⎠⎣ ⎦

⎧ ⎫⎡ ⎤⎛ ⎞− ∇ + + + + +⎡ ⎤ ⎜ ⎟⎪⎢ ⎣ ⎦ ⎥⎪ ⎝ ⎠⎢ ⎥= ⎨ ⎬⎛ ⎞⎢ ⎥⎪ +⎜ ⎟⎢ ⎥⎪ ⎝ ⎠⎣ ⎦⎩

i i

{ }

( ) ( )( ){ }

1edge i+ ,j2

edge i1i+ ,j in2

h izedge

1i+ ,j2

e h e hi+1,j i,jedge e en iz e

1i+ ,jcell (i+1,j) to (i,j) 2

he e en i in n

1ˆ *...

2

ˆ ...

...ˆ...

2

j nM

P P P Pe m j n

l

Me n m n u n

ν ν

ν ν

ν ν

⎪⎪

⎪⎪⎭

⎧ ⎫⎪ ⎪⎪ ⎪= ⎨ ⎬

⎛ ⎞⎪ ⎪+⎜ ⎟⎪ ⎪⎝ ⎠⎩ ⎭

+ − +⎧ ⎫⎪ ⎪− + +⎨ ⎬Δ⎪ ⎪⎩ ⎭

⎛ ⎞+ +⎜ ⎟⎝ ⎠

i

i

iedge

1i+ ,j2

⎡ ⎤⎢ ⎥⎢ ⎥⎢ ⎥

⎧ ⎫⎢ ⎥⎨ ⎬⎢ ⎥⎩ ⎭⎢ ⎥⎣ ⎦

A.15)

And so for any given edge (i + ½, j) the value of the ion current density vector is found

from the above equation, and thus the ion current density vector is found to be an explicit

function of known parameters.

Boundary and initial conditions: at the boundaries of the computational zone,

values of the electron current density vector, neutral gas velocity and the electron and

heavy species pressure gradient are required.

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196

Electron Current Density Vector, je

The electron current density vector is given by the following equation:

( )( )

( )e e e ei en izi ei e en ne 2

e ei en iz e

,n T mj en uEj

n n eν ν νν ν η

η η ν ν ν∇ + ++

= + − =+ + A.16)

Again, the numerical evaluation is relatively uncomplicated, as is shown:

( )( )

{ } ( )( ) ( )

{ }edge

1i+ ,j2

e e i ei e en ne

e ei en iz

e e ei e enedgee i n

1i+ ,j edgee ei en iz ei en iz21i+ ,j2

edgee1i+ ,j e2

ˆ ˆ

n T j en uEjn

n T enEj n j u nn

Ej nn

ν νη η ν ν ν

ν νη η ν ν ν ν ν ν

η η

∇ += + −

+ +

⎧ ⎫⎡ ⎤⎛ ⎞ ⎛ ⎞∇⎪ ⎪= + − −⎢ ⎥⎜ ⎟ ⎜ ⎟⎨ ⎬⎜ ⎟ ⎜ ⎟+ + + +⎢ ⎥⎝ ⎠ ⎝ ⎠⎪ ⎪⎣ ⎦⎩ ⎭

⎧ ⎫= +⎨ ⎬

⎩ ⎭

i i

i( ) ( )

( ) ( ) ( ) ( )

edge1i+ ,j2

e e e ei+1,j i,j

cell (i+1,j) to (i,j)

ei e eni n

edgeei en iz ei en iz1i+ ,j2

...

ˆ ˆ...

n T n T

l

enj n u nν νν ν ν ν ν ν

−⎧ ⎫⎧ ⎫ ⎪ ⎪ +⎨ ⎬ ⎨ ⎬Δ⎩ ⎭ ⎪ ⎪⎩ ⎭

⎧ ⎫⎛ ⎞ ⎛ ⎞⎪ ⎪− −⎜ ⎟ ⎜ ⎟⎨ ⎬⎜ ⎟ ⎜ ⎟+ + + +⎪ ⎪⎝ ⎠ ⎝ ⎠⎩ ⎭i i

A.17)

Heavy Species Temperature, Th

Values of the heavy species temperature are found from solutions to the steady

state heavy species energy equation, shown below:

( ) [ ]

( ) ( ) ( ) ( )

2i h in i n h i n i n h i i n n

2 2 ehh i n n i ei en e e h i n

h

302

3 32 2

n M u u T j e q q eT n u n u

mnMT j e u u n e T T S SM

ν

ν ν

⎡ ⎤= − − ∇ + Γ + + − ∇ + ∇ +⎢ ⎥⎣ ⎦⎡ ⎤

+ ∇ + Γ + − + + − − −⎢ ⎥⎣ ⎦

i i i

i A.18)

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197

Since this equation is rather large and cumbersome, it is important that the analysis is

carried out in full detail.

For the purposes of notation, the following substitutions are made:

( )

[ ] ( )

( ) ( ) ( )

2

2 2n i

3,2

3,2

, 32

0

i h in i n h i n i n

h i i n n h i n

h eei en e b e h i n

h

a n M u u b T j e q q

c eT n u n u d T j e

nM mf u u g n k T T S SM

a b c d f g

ν

ν ν

⎡ ⎤= − = ∇ + Γ + +⎢ ⎥⎣ ⎦

= ∇ + ∇ = ∇ + Γ

⎡ ⎤= − = + − − −⎢ ⎥

⎣ ⎦∴

= − − + + +

i

i i i

A.19)

Applying finite volume method to the heavy species energy equation yields:

{ }

( ) ( )

2 2i h in i n i h in i n avg cell

valueV

h i n i n h i n iV

0

V

3 32 2

V V V V V V

A B C D F G

adV bdV cdV ddV fdV gdV

A n M u u dV n M u u

B T j e q q dV T j e q

ν ν

= = = = = =

= − − + + +

= − = − Δ

⎡ ⎤= ∇ + Γ + + = + Γ + +⎢ ⎥⎣ ⎦

∫∫∫ ∫∫∫ ∫∫∫ ∫∫∫ ∫∫∫ ∫∫∫

∫∫∫

∫∫∫ i

[ ] { } { }

( ) { } ( )

( ) ( )

nS

avg cell avg celli i n n i i n nvalue value

V S S

avg cellh i n h i nvalue

V S

2 2 2 2h hn i n i

avg ceV

ˆ

ˆ ˆ

3 3 ˆ2 2

2 2

q ndA

C P u P u dV P u ndA P u ndA

D T j e dV T j e ndA

nM nMF u u dV u u V

⎡ ⎤⎢ ⎥⎣ ⎦

= ∇ + ∇ = +

= ∇ + Γ = + Γ

⎧ ⎫= − = − Δ⎨ ⎬⎩ ⎭

∫∫

∫∫∫ ∫∫ ∫∫

∫∫∫ ∫∫

∫∫∫

i

i i i i

i i

( ) ( )

( ) ( )

llvalue

eei en e e h i n

hV

eei en e b e h i n

h avg cellvalue

3 ...

... 3

bmG n k T T S S dVM

mn k T T S S VM

ν ν

ν ν

⎡ ⎤⎛ ⎞= + − − − =⎢ ⎥⎜ ⎟

⎝ ⎠⎣ ⎦⎧ ⎫⎡ ⎤⎛ ⎞⎪ ⎪+ − − − Δ⎨ ⎬⎢ ⎥⎜ ⎟

⎝ ⎠⎪ ⎪⎣ ⎦⎩ ⎭

∫∫∫

A.20)

Page 216: Theoretical and Experimental Investigation into High Current Hollow Cathode Arc Attachment

198

Further evaluation yields:

{ }

( ) ( ){ }

( ){ }

{ }

2 2

avg valuefor cellV

all edges of cell i,j

h edge1S

all edges of cell i,j

h i n edge1

avg celliv

V

3 3ˆ ˆ ...2 2

ˆ...

i h in i n i h in i n

h i n i n i n

A n M u u dV n M u u

B T j e q q ndA T j e n A

T n A

C P

ν ν

κ κ

= − = − Δ

⎡ ⎤= + Γ + + = + Γ Δ +⎢ ⎥⎣ ⎦

∇ + Δ

=

∫∫∫

∑∫∫

i i

i

{ } { } { }

{ } { }

{ } ( ) { }

all edges of cell i,j

avg celli n n i icell i,j edgealue value 1S Sall edges of cell i,j

n ncell i,j edge1

avg valueh i n h icell i,jof cellS

ˆ ˆ ˆ ...

ˆ...

3 3ˆ2 2

u ndA P u ndA P u n A

P u n A

D T j e ndA T j

+ = Δ +

Δ

= + Γ = + Γ

∑∫∫ ∫∫

∫∫

i i i

i

i ( ){ }

( ) ( )

( ) ( )

all edges of cell i,j

n edge1

2 2 2 2h hn i n i

avg cellV value

eei en e b e h i n

h avg valuefor cell

ˆ

2 2

3

e n A

nM nMF u u dV u u V

mG n k T T S S VM

ν ν

Δ

⎧ ⎫= − = − Δ⎨ ⎬⎩ ⎭

⎧ ⎫⎡ ⎤⎛ ⎞⎪ ⎪= + − − − Δ⎨ ⎬⎢ ⎥⎜ ⎟⎝ ⎠⎪ ⎪⎣ ⎦⎩ ⎭

∫∫∫

i

A.21)

Further

{ } { } { }

( ){ } ( ){ }

{ } { }

42 2

celli h in i n i h in i navg value cell i,ji,j a=1for cell edge a

all edges all edges of cell i,j of cell i,j

i i n n i n hedge edge1 1

i icell i,j edge

1V V4

3 ˆ ˆ2

ˆ

A n M u u n M u u

B Pu P u n A T n A

C P u n A

ν ν

κ κ

⎡ ⎤= − Δ = Δ −⎢ ⎥

⎣ ⎦

= + Δ + + ∇ Δ

= Δ

∑ ∑i i

i { } { }

{ } ( ){ }

( ) { }

all edges all edges of cell i,j of cell i,j

n ncell i,j edge1 1

all edges of cell i,j

h i i n ncell i,j edge1

2 2 2 2h hcell i,jn i n i

avg cell cellvalue i,j

ˆ

3 ˆ2

1V2 2 4

P u n A

D T e n u n u n A

nM nMF u u V u u

+ Δ

= + Δ

⎧ ⎫ ⎧ ⎫= − Δ = Δ −⎨ ⎬ ⎨ ⎬⎩ ⎭ ⎩ ⎭

∑ ∑

i

i

( ) ( )

4

edge aa=1

eei en e b e h i n

h avg valuefor cell

3mG n k T T S S VM

ν ν

⎡ ⎤⎢ ⎥⎣ ⎦

⎧ ⎫⎡ ⎤⎛ ⎞⎪ ⎪= + − − − Δ⎨ ⎬⎢ ⎥⎜ ⎟⎝ ⎠⎪ ⎪⎣ ⎦⎩ ⎭

A.22)

Page 217: Theoretical and Experimental Investigation into High Current Hollow Cathode Arc Attachment

199

Neutral Gas Velocity Vector, un

Values of the neutral gas velocity are found from solutions to the neutral species

momentum equation shown below:

( ) ( )h

n h n ni n i n e en e n h iz n02

Mn eT n u u n m u n M uν ν ν= −∇ − − + + A.23)

Numerical evaluation proceeds as follows:

Page 218: Theoretical and Experimental Investigation into High Current Hollow Cathode Arc Attachment

200

( )

( )

( )

ni hn h n n h iz n ni i n e en e

hn h n ni i n e en e

nni

n h iz

n nedgen 1i+ ,j2 ni

n h izedge

1i+ ,j2

ni

niiz

02 2

2 ˆ

2

ˆ 1ˆ * ...

2

...2

2

Mn eT u n M n u n m u

Mn eT n u n m uu n

n M

n eT nu n

l n M

νν ν ν

ν ν

νν

νν

ννν

⎛ ⎞= −∇ + − + +⎜ ⎟⎝ ⎠

⎡ ⎤∇ − −⎢ ⎥

⎢ ⎥=⎛ ⎞⎢ ⎥−⎜ ⎟⎢ ⎥⎝ ⎠⎣ ⎦

Δ= −

Δ ⎛ ⎞−⎜ ⎟⎝ ⎠

⎛ −⎜⎝

i

ii

{ }

( ) ( )

{ }

nei e

niiz edgeedge 1i+ ,j1i+ ,j 22

edgen 1i+ ,j2

cell celln n n ni+1,j i,j

nicell (i+1,j) to (i,j)n h iz

edge1i+ ,j2

niedgei 1i+ ,j2 niz

ˆ ˆ

2

ˆ

1 ...

2

ˆ...2

u n u n

u n

n eT n eT

l n M

u n

ννν

νν

ννν

−⎞ −⎟⎠

=

⎧ ⎫−⎧ ⎫⎪ ⎪⎪ ⎪⎪ ⎪ −⎨ ⎬⎨ ⎬Δ ⎛ ⎞⎪ ⎪⎪ ⎪−⎩ ⎭ ⎜ ⎟⎪ ⎪⎝ ⎠⎩ ⎭

i i

i

i { } needgee 1i+ ,j ni2iiz edgeedge 1i+ ,j1i+ ,j 22

ˆ

22

u n ννν

⎧ ⎫ ⎧ ⎫⎪ ⎪ ⎪ ⎪⎪ ⎪ −⎨ ⎬ ⎨ ⎬

⎛ ⎞⎪ ⎪ ⎪ ⎪−⎜ ⎟ ⎩ ⎭⎪ ⎪⎝ ⎠⎩ ⎭

i

A.24)

And the neutral gas velocity at a given cell edge can be found from the final expression

given above.

Boundary and initial conditions: Since this is a steady state equation, no initial

conditions are necessary. From the expression shown above one can see that the neutral

gas velocity vector at a given cell edge is an explicit function of known parameters at the

edge in question. On the boarders of the computational region values of the neutral

species pressure gradient, ion velocity and electron velocity are required. Computation of

Page 219: Theoretical and Experimental Investigation into High Current Hollow Cathode Arc Attachment

201

the neutral species pressure gradient on the boundaries requires the value of the neutral

species pressure in a ghost cell outside the computation zone and sharing a cell edge with

the edge for which the equation if being solved.

Neutral Gas Density, nn

Values of the neutral gas density are found from solutions to the neutral gas

continuity equation:

( )n

n n n izn n nt

ν∂+ ∇ Γ = − = −

∂i

A.25)

The neutral gas continuity equation is of similar form to the ion and electron continuity

equations, and so the application of numerical approximation and the solution procedure

are also similar:

( )

( ) ( ){ }

{ }

nn iz n

nn iz n n iz n

V V V s

all cellr+1 r edges

r rn navg valuen iz n n edgeof cell i,javg value 1

of cell i,j

r+1 rn n izcell i,j

( )

ˆ( )

ˆ

n nt

n dV n dV n dV ndAt

n n V n V n u n At

n n

ν

ν ν

ν

ν

∂= − − ∇ Γ

∂∂

= − − ∇ Γ = − − Γ∂

⎛ ⎞−Δ = − Δ − Δ⎜ ⎟Δ⎝ ⎠

= − Δ

∫∫∫ ∫∫∫ ∫∫∫ ∫∫

i

i i

i

( ) { } ( ){ }all celledges

ravg value n n edgeof cell i,j 1cell

ˆtt n u n AVΔ

− ΔΔ ∑ i

A.26)

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202

The value of the neutral gas density at a given time-step and location are shown to be an

explicit function of the neutral gas density at the same location, and the flux of neutrals

through the edges of the cell in question, both values taken at the previous time-step.

Boundary and initial conditions: An initial value of the neutral species density is

required at all cell centers and edges within the computational zone (found from linear

interpolation. Further, initial values of the neutral gas flux are required on all boundaries

of the computational zone, and all cell boundaries. Values of the neutral gas flux are

required on all boundaries of the computational zone.

The upstream boundary condition is found from

upn i nstream h xs

ˆ mn u nM A

Γ = =i A.27)

with the assumption that all particles entering the computational zone across the upstream

boundary are neutrals.

The downstream boundary condition for the flux of neutrals is determined by

subtracting the ion flux at the cathode exit place (found from the ion current equation)

from the total mass flux:

total i

downnstream h xs

ˆ m jnM A q

Γ = −i A.28)

For reasons of symmetry no flux of neutrals is permitted across the centerline boundary,

and since all neutrals that enter the wall sheath will strike the wall and re-enter the

computational zone, no net flux of neutrals occurs at the cathode wall boundary.

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203

Boundary Conditions – Summary

The computational region has 4 spatial boundaries: the cathode centerline, cathode exit

plane, cathode wall (emitting surface), and the gas inlet.

1: Centerline: On the centerline of the computational zone, due to azimuthally symmetry

no flux of any parameter is permitted across the cathode centerline

2: Cathode exit plane: At the downstream end of the computational zone, the plasma exits

the cathode region. Dirichlet boundary conditions are imposed on the border, where

values of the plasma potential and the plasma density are input from experiment.

Adiabatic conditions are imposed on both the electron temperature and the heavy species

temperature at this location.

Boundary conditions for the exit velocity of the neutral particles is calculated

from the transitional flow equation found in section 6.2 (eqn 6.2.21).

3: Cathode Wall: On the boundary between the plasma and the emitting surface, the

plasma sheath is formed. The region contained within the sheath is populated by ions

which drift in from the bulk plasma (along with neutrals) and electrons thermionically

emitted from the cathode surface. Additionally a small number of high energy electrons

in the tail end of the speed potential distribution will enter the sheath from the bulk

plasma. The sheath region is not included in this model, and the computation zone

extends to, but does not include, the pre-sheath region.

Page 222: Theoretical and Experimental Investigation into High Current Hollow Cathode Arc Attachment

204

The electron emission from the cathode wall is determined by the cathode wall

temperature and the potential drop across the sheath. Electrons capable of overcoming the

sheath potential will escape the plasma and be absorbed by the cathode wall:

e,absorb

8ˆ , where 4

eTee e

e

en eTj n c e cm

φ

π−

= − =i A.29)

Positive ions are assumed to escape the plasma at the Bohm velocity:

e

i, escape eh

ˆ eTj n enM

=i A.30)

When the ions reach the cathode wall, they will recombine with an electron and

re-enter the computational region as a neutral particle, with a temperature equal to the

wall temperature at that axial location. All neutral particles fluxing out of the

computational zone across this border will strike the wall and return, but there will be an

additional flux of neutrals back into the computation region from ion-wall-electron

recombination’s. Thus there is a net flux of neutrals into the computational region across

this boarder.

wall

n eh

ˆ eTn nM

Γ = −i A.31)

Conditions are also imposed on the heavy species temperature such that all heavy

particles on this boundary are at assumed to be at the same temperature as the wall.

Page 223: Theoretical and Experimental Investigation into High Current Hollow Cathode Arc Attachment

205

4: Gas Inlet: At the gas inlet, neutrals flux into the computational zone with a mass flow

rate as set by the experiment. No electron flux is permitted across this boarder, however

ions are permitted to escape at thermal speed.

ei e

h

e

ˆ

ˆ 0

eTj n enM

j n

=

=

i

i A.32)

Neumann boundary conditions are imposed for the temperature of the heavy species

particles, which are assumed to enter the computational zone with a temperature equal to

the wall temperature at the upstream boundary.

There is also an adiabatic boundary condition for the electron temperature

imposed at the upstream boundary.

Page 224: Theoretical and Experimental Investigation into High Current Hollow Cathode Arc Attachment

206

Appendix B:

Collision Frequencies

Several collision frequencies are referred to in this work, representing both elastic

and inelastic collisions. Each term represents a particular type of collision between two

specific particle species, where νab describes the frequency of a particular type of

interaction between particles of species ‘a’ and species ‘b’ and should not be miss-

interpreted as the sum total number of interactions between particles ‘a’ and ‘b’.

ab b ab abn cν σ= (B.33)

The electron-neutral collision frequency, νen, represents the rate of momentum

transfer via elastic collisions (averaged over all interactions, both large and small angle)

between electrons and neutrals. The collision cross section is calculated by an equation fit

to data gathered by Nakamura and Kurachi [48].

( )

( )

5 4 3 2 20en e e e e e

een e

e

5 4 3 2 20een n e e e e e

e

.0002 0.0061 0.059 - 0.1317 1.2949 0.3044 10

8

8 .0002 0.0061 0.059 - 0.1317 1.2949 0.3044 10

T T T T T

qTc cm

qTn T T T T Tm

σ

π

νπ

= − + + +

≅ =

= − + + +

(B.34)

Here, σen is in (m2) and Te is in (eV).

The electron-ion (coulomb) collision frequency, νei, represents the rate of

momentum transfer via elastic collisions (averaged over all interactions, both large and

small angle) between electrons and ions, governed by the coulomb interaction using the

coulomb logarithm weighting factor. Applying the form directly stated by reference [32],

we have:

Page 225: Theoretical and Experimental Investigation into High Current Hollow Cathode Arc Attachment

207

( )

( )

( )

12 eei 3

2e

6 ee3

e

ee

e

2.9*10 ln

1ln 23 ln 10 , 10eV2

ln 24 ln , 10eV

n

T

n TT

nT

T

ν −

= Λ

⎛ ⎞Λ = − <⎜ ⎟

⎝ ⎠⎛ ⎞

Λ = − >⎜ ⎟⎜ ⎟⎝ ⎠

(B.35)

The ion-neutral collision frequency is given by:

( )

( ) ( )( )

2hin n cex n cexin

h

2icex h

h

h

2 122

, 0.0001 7.49 0.73ln T2

xkTn u n e x erf xM x

uxkT

M

πν σ σπ

σ

−⎡ ⎤⎛ ⎞= = + +⎢ ⎥⎜ ⎟⎝ ⎠⎣ ⎦

≡ = − (B.36)

The above equation is taken from reference [42], the charge exchange cross section, σcex,

is given by data reported in reference [51], and is in m2.

The equation for the total ionization collision frequency is a summation of the ionization

from direct single collision events, and step-wise ionization, as derived in reference [22]:

i

e

7 / 2 7 / 2Total s ei i i i o

e e e

81 1 TqTI Ik k k k eT T m

ε

σπ

−⎡ ⎤ ⎡ ⎤⎛ ⎞ ⎛ ⎞⎢ ⎥ ⎢ ⎥= + ≈ + ≈ +⎜ ⎟ ⎜ ⎟⎢ ⎥ ⎢ ⎥⎝ ⎠ ⎝ ⎠⎣ ⎦ ⎣ ⎦

(B.37)

Where for Argon, we have σo = 1.9*10-21m2.

The final ionization rate, or the number of positive ions created per second per unit

volume, is given by:

i

Totaln e e,n u u kν σ σ= = (B.38)

Page 226: Theoretical and Experimental Investigation into High Current Hollow Cathode Arc Attachment

208

Appendix C:

Presented in appendix C are grayscale images of the contour plots generated from

the numerical model. Plasma distribution is for a 6mm diameter Tungsten cathode, in a

3.3 amp 121 volt discharge, with 215 sccm of Argon flow rate.

Figure 96: Computed plasma density profile in 6mm Tungsten cathode 3.3 amp 121

volt discharge, 215 sccm flow rate.

Page 227: Theoretical and Experimental Investigation into High Current Hollow Cathode Arc Attachment

209

Figure 97: Computed neutral particle density profile in 6mm Tungsten cathode 3.3

amp 121 volt discharge, 215 sccm flow rate.

Figure 98: Computed electron temperature (eV) potential profile in 6mm Tungsten

cathode 3.3 amp 121 volt discharge, 215 sccm flow rate.

Page 228: Theoretical and Experimental Investigation into High Current Hollow Cathode Arc Attachment

210

Figure 99: Computed plasma potential profiles in 6 mm Tungsten cathode, 3.3 Amp,

121 Volt discharge, 215 sccm flow rate

Figure 100: Computed heavy species temperature in 6 mm Tungsten cathode, 3.3

Amp, 121 Volt discharge, 215 sccm flow rate