tsr 79 v i lllllll eieeeiiiiiiee · rho-inf free-stream density, lbm/ft 3 rn reference nose radius,...

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NOLD ENGINEERING DEVELOPMENT CENTER ARNOLD AS TN FI 20/4 ... S PACE SHUTTLE ORBITER SILTS PODFLOW ANGULARITY AND AERODYNAMIC-ETC(U) UNCLASSIFIED AEDDCT TSR R 79 "V V N I lllllll EIEEEIIIIIIEE

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Page 1: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

NOLD ENGINEERING DEVELOPMENT CENTER ARNOLD AS TN FI 20/4

... S PACE SHUTTLE ORBITER SILTS POD FLOW ANGULARITY AND AERODYNAMIC-ETC(U)

UNCLASSIFIED AEDDCTT S R

R7 9 "V

V N

I lllllll

EIEEEIIIIIIEE

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AEDC-TSR-79-V70

___- SPACE SHUTTLE ORBITER SILTS POD FLOWANGULARITY AND AERODYNAMIC HEATING

_(OH-102A AND OH-400)

K. W. N~utt

___ARO, Inc. O~TIC____ ELECTE

__ A---- ____ November 1979

__ Final Report for Period October 1978 - October 1979

Approved for public release; distribution unlimited.

ARNOLD. ENGINEERING DEVELOPMENT CENTERARNOLD AIR FORCE STATION, TENNESSEE

AIR FORCE SYSTEMS COMMANDUNITED STATES AIR FORCE

80 7 3 114

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NOTICES

When U. S. Government drawings, specifications, or other data are used for any purpose otherthan a definitely related Government procurement operation, the Government thereby incurs noresponsibility nor any obligation whatsoever, and the fact that the Government may haveformulated, furnished, or in any way supplied the said drawings, specifications, or other data, isnot to be regarded by implication or otherwise, or in any manner licensing the holder or any -

other person or corporation, or conveying any rights or permission to manufacture, use, or sellagany patented invention that may in any way be related thereto.

References to named commerical prc~ducts in this report are not to be considered in any sensej as an indorsement of the product by the United States Air Force or the Government.

APPROVAL STATEMENT

This report has been reviewed and approved.

JOSEPH F. PAWLICK, Jr., Lt. Col, USAFTest Director, VKF DivisionDirectorate of Test Operations

Approved for publication:

FOR THE COMMANDER -

iAMES D. SANDERS, Colonel, USAFDeputy of Operations -

Page 4: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

IIUNCLASSIFIED

REPORTDOCUMENTATION PAGE READ INSTRUCTIONSBEFORE COMPLETING FORM

.. REP.ORT NUMER .GOVT ACCESSION NO. 3. IPIEN'S CATALOG NUMBER

EDC-TSR-79=-V70 7 '9V&PROCVEDE -adgtibigjaw- , - -- , --- --. TP Of RE~qRT &PRO OEE

PACE SHUTTLE ORBITER SILTS POD FLOW ANGULARITY AND/pFinal ,Kep r or oct 0 78-RODYNAMIC HaTING'TtSTS (OH-1 2A AftDOH-400), Oct M79

" "UT 0. CONTRACT OR GRANT NUMBER(s)

/6'K. W.r utt ARO, Inc., a Sverdrup CorporationCompahy -

9. PERFORMING ORGANIZATIO*4 NAME AND ADDRESS 10. PROGRAM ELEMENT. PROJECT, TASK

Arnold Engineering Development Center/DO AREA & WORK UNIT NUMBERS

Air Force Systems Command Program Element 921E01Arnold Air Force Station, TN 37389

1I. CONTROLLING OFFICE NAME AND ADDRESS

NASA/Johnson Space Center (ES3) Novenbr_ _ 107

Houston, TX 77058 13. NUMBER OF PAGES49

14. MONITORING AGENCY NAME & ADDRESS(II dlfterent Irom Controlllng Office) 15. SECURITY CLASS. (of this report)

UNCLASSIFIED1S&. DECL ASSI FICATION 'DOWNGRAOING

SCHEDULE N/A

1|6. DISTRIBUTION STATE=MENT (of this 'Report)

Approved for public release; distribution unlimited.

17. DISTRIBUTION STATEMENT (of the abstract entered In Block 20, if different from Report)

IS. SUPPLEMENTARY NOTES

Available in Defense Technical Information Center (DTIC).

19. KEY WORDS (Continue on reverse aide If necessary and Identify by block number)

heat transfer SILTS podoil flowflow field probespace shuttle orbiterhypersonic testing20 BSTRACT (Continue o reves.. side If necessary and identify by block number)

Heat transfer, flow field, and oil flow tests were conducted on a 0.0175 scalemodel of the space shuttle orbiter. The tests were conducted at Mach 8.iv-thte&,

( AEDC -HXRqrsoni" Tunnzl B. The objective of the tests was to determine theaerodynamic heating distribution on the orbiter SILTS tail configuration and toobtain flow field total pressure and total temperature measurements at the loca-tion of the leading edge of the vertical ta . T", testsmere conducted at free-stream Reynolds numbers ranging from Zx L6 3.2 xj10, per ft. The model

jangle of attack was varied from -5 to 5 deg and from 30 to 40 degrees. . . JDD , JAN 73 1473 EDITION OF I NOV S IS OBSOLETE ' "

UNCLASSIFIED ,

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CONTENTS

NOMENCLATURE ............ ........................ 31.0 INTRODUCTION ............ ........................ 62.0 APPARATUS

2.1 Test Facility .............................. 72.2 Test Articles ...... ..................... 7

2.2.1 Flow Angularity Test (OH-102A) ........... 72.2.2 SILTS Pod Test (OH-400) ...... ............. 8

2.3 Test Instrumentation ........ ................. 8

3.0 TEST DESCRIPTION3.1 Test Conditions and Procedures- 9.............

3.1.1 General ......... ..................... 93.1.2 Data Acquisition ........ ................ 10

3.2 Data Reduction ....... ..................... . .113.3 Uncertainty of Measurements ..... .............. ... 13

4.0 DATA PACKAGE PRESENTATION ..... ............... ..... 13

REFERENCES .......... ......................... ... 14

APPENDIXES

I. ILLUSTRATIONS

FigureI. Tunnel B ................................. 162. 56-0 Model Installation ....... .................. . 173. Vertical Tail for Flow Angularity ..... .............. ... 184. Photograph of 56-) Model Vertical Tail ... ........... ... 195. Photograph of 92-0 Model Vertical Tail Configurations. . . 206. Comparison of Vertical Tail Configurations .. ......... ... 217. Photograph of 92-0 Model Installation .... ............ ... 228. 92- Model Installation ....... .................. ... 239. Photograph of 92-$ Model Installation for Probe Phase . . 2510. Thermocouple Locationson 0.0175 Scale Vertical Tail. ..... 2611. Thermocouple Locations on 0.0525 Scale Vertical Tail .. 2712. Overhead Probe Survey Mechanism ..... ................13. Shielded Thermocouple Probe ...... ................. ... 3014. Probe Holder .......... .........................15. Flow Field Probe Alignment with Optical Overlay. .......... 3216. Data Repeatability on Leading Edge of 0.0525 Scale Tail.. 3317. Representative Probe Measurements ..... .............. ... 34

iI

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CONTENTS

P age

[I. TABLES

Table1. Estimated Uncertainties .. ........... ....... 372. Model Thermocouple Locations. .. .......... ..... 393. Test Summary. ......................... 414. Probe Angle at the Vertical Tail*LeadingEdge.... .. .. ..

III. REFERENCE HEAT TRANSFER CONDITIONS .............. 46

IV. SAMPLE TABULATED DATA

1. Heat-Transfer Data ........................ 48

2. Flow Field Probe Data .. ....... ............ 49

Ll

2

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NOMENCLATURE

ALPHA Model angle of attack, deg

ALPHA-PREBEND Sting prebend angle, deg

ALPHA-SECTOR Tunnel sector angle, deg

ALPT Angle pitch drive unit makes with respectto the tunnel centerline, deg

b Model skin thickness, in. or ft

BV Height of model vertical tail(see Fig. 3), in.

CONFIG Code used to define model configuration

CONSTANT SET The set of thermocouples recorded during atunnel injection (see Table 2)

c Model skin material specific heat, Btu/ibm0R

CV Vertical tail chord (see Fig. 3), in.

DTWDT Time rate of change of wall temperature, *R/sec

FLOW ANGLE Angle of flow with respect to the leading edgeof the vertical tail (see Fig. 3), deg

GROUP Data identification number

Hla Local heat-transfer coefficient

HREF Reference heat-transfer coefficient based on Fayand Riddell theory. See Appendix III

H(TO) Heat-transfer coefficient based on TO (see Eq. 1),Btu/ft 2-sec- 0R

H(0.9 TO) Heat-transfer coeffLcient based on 0.9 TO,Btu/ft2-sec-*R

MACH NO., M Free-stream Mach number

MODEL Model designation

MU-INF Free stream viscosity, lbf-sec/ft2

MUO Viscosity conditions baled on stagnationI temperature, lbf-sec/ft

3

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P-INF Free-stream static pressure, psia

PO Tunnel stilling chamber pressure, psia

P02 Stagnation pressure downstream of a normalshock, psia

PPN Total pressure measured by probe PPN, N - Ior 2 (see Fig. 14), psia

QDOT Heat-transfer rate, (w b cp)(DTWDT), Btu/ft 2-sec

Q-INF Free-stream dynamic pressure, psia

R Radius of 0.0525 scale SILTS pod dome,R = 0.56 in., (see Fig. 11), in.

RE/FT Free-stream Reynolds number

RHO-INF Free-stream density, lbm/ft3

RN Reference nose radius, (0.0175 ft or 0.0525 ft,

determined by model scale)

ROLL-SECTOR Tunnel sector roll position, deg

S Surface distance on 0.0525 scale SILTS pod(see Fig. 11)

SILTS SCALE Scale of vertical tail on the OH-400 Test

(0.0175 or 0.0525)

STFR Stanton number based on HREF (see Appendix III)

SWITCH POSITION Designates the position of the thermocoupleselector switch

t Time from start of model injection cycle, sec

StI iTime when initial model wall temperature was

recor(ied before model injection, sec

TC NO Thermocouple number

THETA Angular position of thermocouples on the SILTS

pod o1 the 0.0525 scale vertical tail (seeFig. I L), deg

4

Lpl

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T-INF Free-stream temperature, OR

TO Tunnel stilling chamber temperature, OR

TTN Total temperature measured by probe TTN,

N = 1 or 2 (see Fig. 14), OR

TW Model wall temperature at midpoint of datainterval, OR

TWi Initial model wall temperature beforeinjection, OR

V-INF Free-stream velocity, ft/sec

w Model skin material density, lbm/ft3

X Longitudinal coordinate of vertical tail(see Fig. 3), in.

XT Tunnel longitudinal axis coordinate (seeFig. 12b), in.

Y Lateral tunnel axis coordinate (see Fig.

12b), in.

YAW Yaw angle of model, deg

Z Model scale vertical coordinate (seeFig. 3), in.

ZT Tunnel vertical axis coordinate (seeFig. 12a), in.

I

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1.0 INTRODUCTION

The work reported herein was conducted at the Arnold Engineering

Development Center (AEDC), Air Force Systems Command (AFSC), by ARO,

Inc., AEDC Division (a Sverdrup Corporation Company), contract operatorof AEDC, AFSC, Arnold Air Force Station, Tennessee. The work was

sponsored by the Johnson Space Center (NASA-JSC(ES3)), Houston, Texas,

under Program Element 921E-01. Rockwell International (RI), Space

Division, Downey, California was responsible for test planning and data

analysis. The project monitor for NASA-JSC(ES3) was Mrs. Dorothy B. Lee

and the test engineer for Rockwell International was Mr. Jim Collins.

The overall objective of the tests was to measure heat transfer

coefficients on the SILTS* pod of a scaled space shuttle orbiter

model. The SILTS pod houses an infrared sensor which will be used

during flight tests to obtain orbiter leeside surface temperature

distributions. Since the pod, which mounts on the top of the

vertical tail, is in the wake of the orbiter, flow conditions

approaching the tail are needed to permit data analysis and extra-

polation to flight conditions. Therefore, flow angularity, local

pitot pressure and local total temperature measurements were added

to the usual heating rate measurements.

The test was conducted in two phases in the 50-in. diam HypersonicWind Tunnel (B) at the von Kairman Gas Dynamics Facility (VKF). The first

phase was an oil flow study to determine the flow angularity at theleading edge of the space shuttle orbiter vertical tail. This phase wasdesignated by NASA/Rockwell International as the OH-102A test and was

conducted on October 9, 25, and November 29, 1978. The objective of thesecond phase was to determine aerodynamic heating distributions on the

orbiter SILTS tail configuration and to obtain total pressure and totaltemperature measurements at the leading edge of the vertical tail. Thisphase was designated as the OH-400 test and was conducted during theperiod October 5, 8 and 9, 1979. Both phases of the test were completedunder ARO Project No. V41B-65.

*Shuttle Infrared Leeside Temperature Sensor

6

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The tests were conducted at a nominal Mach number of 8, with freestreamReynolds numbers varying between 0.5 x 106 and 3.7 x 106 per ft. Model anglesof attack ranged from 30 to 40 deg for all phases of the test. In addition,heating distribueion data were also obtained at angles of attack ranging from-5 to 5 deg.

Copies of all test data have been transmitted to Rockwell International.A data tape will be transmitted to Chrysler Corporation Space Division fortheir Dataman system. Inquiries to obtain copies of the test data should bedirected to NASA-JSC(ES3), Houston, Texas 77058. A microfilm record has beenretained in the VKF at AEDC.

2.0 APPARATUS

2.1 TEST FACILITY

Tunnel B (Fig. 1) is a closed circuit hypersonic wind tunnel with a 50-in.diam test section. Two axisymmetric contoured nozzles are available to provideMach numbers of 6 and 8 and the tunnel may be operated continuously over arange of pressure levels from 20 to 300 psia at Mach number 6, and 50 to 900psia at Mach number 8, with air supplied by the VKF main compressor plant.Stagnation temperatures sufficient to avoid air liquefaction in the test section(up to 1,3500R) are obtained through the use of a natural gas fired combustionheater. The entire tunnel (throat, nozzle, test section, and diffuser) is cooledby integral, external water jackets. The tunnel is equipped with a modelinjection system, which allows removal of the model from the test section whilethe tunnel remains in operation. A description of the tunnel may be found inRef. 1.

2.2 TEST ARTICLES

2.2.1 Flow Angularity Test (OH-102A)

The flow angularity data for the OH-102A test were obtained using theRockwell 56-f model. This model was a 0.0175 scale phase change paint modelthat was modified by the addition of a new vertical tail. The new verticaltail was constructed of stainless steel with the pilot's left side being aflat slab that was coincident with the orbiter centerline. A sketch of the56-0 model installation in the tunnel is presented in Fig. 2. The tip of thevertical tail extends past the theoretical tip (Z = 14.275 in.) to stationZ - 15.025 in. as shown in Fig. 3. The tail extends past the theoreticaltip to study the flow angle in the area of the SILTS pod. A photograph ofthe vertical tail with a typical oil flow pattern is shown in Fig. 4.

7.

-T-17

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2.2.2 SILTS Pod Test (OH-400)

The model used for the OH-400 test was the 0.0175 scale Rockwell92- orbiter model fitted with two different vertical tails. A photo-graph of the two vertical tail configurations is shown in Fig. 5. Oneconfiguration was a 0.0175 scale of the vertical tail and the SILTSpod. The second configuration was a 0.0525 scale vertical taii andSILTS pod that was truncated at the trailing edge to conform to the0.0175 scale outline. A sketch comparing the outlines of these twoconfigurations is shown in Fig. 6. The centerline of the 0.0525scale SILTS pod is at the full span of the 0.0175 scale tail. Thelarger scale SILTS pod was tested to gain better definition of theheating distribution on the SILTS pod. Both vertical tail configurationswere fabricated from 17-4PH stainless steel and instrumented withtnermocouples. A photograph or the 9L-p model with the U.UJZJ scalevertical tail installed is shown in Fig. 7. A sketch of the 92-4 modelinstallation for both angle of attack ranges is presented in Fig. 8.

The 92-4 model was also used during the total pressure and totaltemperature probe phase. For these measurements the vertical tailwas removed and a cover plate inserted to provide a smooth contour.A photograph of the 92- model installed for the probe phase is shownin Fig. 9.2.3 TEST INSTRUMENTATION

The instrumentation, recording devices, and calibration methodsused to measure the primary tunnel and test data parameters are listedin Table la along with the estimated measurement uncertainties. The

range and estimated uncertainties for primary parameters that werecalculated from the measured parameters are listed in Table lb.

The model temperatures were measured with Chromel-constantanthermocouples. The 0.0175 scale vertical tail and SILTS pod was instru-mented with 43 thermocouples. The thermocouple locations are shownin Fig. 10 with coordinates and skin thicknesses listed in Table'2a.Thermocouples are on the pilot's left side of the tail. The 0.0525scale vertical tail and SILTS pod was instrumented with 77 thermocouples.The locationsof these thermocouples are shown in Fig. 11 with coordinatesand skin thicknesses presented in Table 2b. Thermocouples werelocated symmetrically about the SILTS pod but are only located on thepilot's left side of the tail.

The flow field measurements were obtained by using the overhead probedrive system illustrated-in Fig. 12 that was designed and fabricated bythe VKF. The unit is designated the "X-Y-Z" probe drive and can be mountedabove the window opening on top of either Tunnel. B or C. The X-Y-Z drivemotors are located on top of the tunnel. In addition, the mechanism has the

8

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capability for pitching the probe holder 10 to -25 deg (ALPT) relativeto the tunnel centerline. To minimize pressure stabilization time, thepressure transducers were mounted as close to the probes as possiblein the area provided behind the water cooled shield.

Two total pressure (PPI and PP2) probes were used during the flowfield measurement. The two total pressure probes were fabricatedfrom 0.0937 in. OD 1/4 hard stainless steel with a 0.015 in. wallthickness. The tip of the probe had a 15 deg bevel relative to theouter surface of the probe. Each probe was connected to a 15-psidDruck model PDCR-22 differential pressure transducer that was calibratedfor l-psid and 10-psid full scale. A near-vacuum reference pressure wasused in conjunction with the differential pressure transducers. Thereference pressure was measured with a Hastings absolute pressuretransducer.

Two total temperature probes were used to measure the local stag-nation temperature. These were single shielded thermocouple probeswith a Chromef - Alumel® thermocouple. The probe dimensions arepresented in Fig. 13.

A special probe holder was fabricated to mount the pressure andtemperature probes. A sketch of the probe holder is shown in Fig. 14.The probes were mounted in the tunnel with a 22 deg prebend when ALPTwas zero. The position of PP1 was set at the centerline of the tunnelwhen the probe drive reading of Y equaled zero.

3.0 TEST DESCRIPTION

3.1 TEST CONDITIONS AND PROCEDURES

3.1.1 General

The test was conducted at a nominal Mach number of 8 in Tunnel B.A summary of the specific test conditions is given below.

MACH No. PO, psia TO, OR Q-INF, psia P-INF, psia RE/FTxl0 6

7.90 100 1250 0.5 0.01 0.57.94 205 1250 1.0 0.02 1.07.98 435 1300 2.0 0.05 2.07.99 670 1320 3.1 0.07 3.08.00 850 1350 3.9 0.09 3.7

A more detailed test summary showing all configurations tested andthe variables for each is presented in Table 3.

9

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In the VKF contLnuous flow wind tunnels (A, 8, C), the model ismounted on a sting su.,, :t mechanism in an installation tank directlyunderneath the tunnel test section. The tank is separated from thetunnel by a pair of fairing doors and a safety door. When closed, thefairing doors, except for a slot for the pitch sector, cover theopening to the tank and the safety door seals the tunnel from the tankarea. After the model is prepared for a data run, the personnel accessdoor to the installation tank is closed, the tank is vented to thetunnel flow, the safety and fairing doors are opened, the model isinjected into the airstream, and the fairing doors are closed. Afterthe data are obtained, the model is retracted into the tank and thesequence is reversed with the tank being vented to atmosphere to allowaccess to the model in preparation for the next run, if necessary.The sequence is repeated for each configuration change.

3.1.2 Data Acquisition

Oil flow photographs were taken with Varitron Model E 70mmsequence cameras mounted outside the test section windows.Three cameras were used to provide photographic data on the OH-102Atest and only one camera was used on the OH-400 test. An automaticcamera control system was utilized to provide automatic shuttersequencing of 1 or 2 sec intervals.

The initial step pricr to recording the thin-skin thermocoupledata was to cool the model uniformly to approximately 70'F with highpressure air. Once the cooling cycle was complete, the desired modelattitude was established in the tank prior to injection. With thedesired tunnel free stream conditions established, the model was theninjected into the tunnel. At lift-off, the initial temperature, (TWi),for each thermocouple of the selected Constant Set was recorded.The data acquisition sequence was initiated at lift-off and continuedfor approximately 4 seconds after the model reached tunnel centerline.After each injection, the model was retracted and the cycle wasrepeated to cool the model to an isothermal state.

A Beckman® 210 analog-to-digital converter was used in conjunctionwith a Digital Equipment Corp.®(DEC) PDP-11 computer and a DEC-10computer to record the temperature data. The Beckman ®convertersampled the output of each thermocouple approximately 15 times persecond.

The flow field measurements were made with the probe tips positionedin the plane of the leading edge of the vertical tail. Since thevertical tail was removed for these measurements, the followingprocedure was employed. An optical overlay of the vertical tail wasmarked with a grid showing the value of Z/BV as a percentage of theleading edge distance. A photograph of the model with the overlaysuperimposed is presented in Fig. 15. This overlay was mounted on an

10

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adjustable plate in the schlieren system and was aligned with the model.During the.alignment, the 0.0175 scale vertical tail was installed onthe model and the overlay was properly marked to insure that the overlaywas coincident with the tail leading edge. The Y position of the probedrive was calibrated so that when probe PP1 was aligned with the center-

line of the vertical tail, the value of Y equalled zero

Two types of probe measurements were recorded during the OH-400

test. The first type of probe measurements were freestream calibrations.These data were obtained with the model removed from the tunnUl. Withthe probes in the tunnel freestream the probe angle with respect to thetunnel centerline was varied from -3 to 21 degrees in 3 deg increments.At each position the value of both pressure and both temperature probeswere recorded. This provided a calibration of the probe sensitivity

to flow angle misalignment. The second type were the probe measure-ments at the plane of the leading edge. With the model positioned inthe tunnel at the desired angle of attack the overlay was adjusted toalign with the model. The desired probe angle at each position withrelation to the leading edge of the vertical tail was determined fromthe oil flow photographs on the OH-102A test. These angles are listedin Table 4. For each position along the leading edge (Z/BV) the desiredprobe angle was set and then the probe tip was driven to the desiredZ/BV location. All four probe measurements (2 pressure, 2 temperature)and a photograph as shown in Fig. 15, were recorded for each data point.

3.2 DATA REDUCTION

The reduction of thin-skin thermocouple data utilizes the calori-meter heat balance, which, in coefficient form is

H(TO) = wbc DTWDT (1)p TO-TW

Radiation and conduction losses are neglected in this heat balance,and data reduction simply requires evaluation of DTWDT from the tempera-

ture-time data and determination of model material properties. For thepresent tests, radiation effects were negligible; however, conductioneffects were potentially significant in several regions of the model.To permit identification of these regions and improve evaluation of thedata, the following procedure was used.

Separation of variables and integration of Eq, (1), assuming constant

w, b, c and TO yieldsp

H(TO) (t t ti) (2)WbC t = n (2)

P.1

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Since H(TO)wbcp is a constant, plotting Zn (TO-TWi)/(TO-TW ) versustime will give a straight line if conduction is negligible. Thus, devia-tions from a straight line can be interpreted as conduction effects.

The data were evaluated in this manner and, generally, a reasonablylinear portion of the curve could be found for all thermocouples. Alinear least-squares curve fit of in (TO-TWi)/(TO-TW) versus time wasapplied to the data. The data reduction time is typically started atcenterline. However, the data for the thermocouples on the verticaltail leading edge were reduced starting 0.5 seconds prior to centerlinefor the 0.0175 scale tail and 0.61 seconds prior to centerline for the0.0525 scale tail. This was done to reduce the data on these thermo-

couples before conduction errors became significant. The curve fitextended for a time span which was a function of the heating rate, asshown on the following list.

Range Number of Points Time Span, sec

DTWDT > 32 5 0.27

16 < DTWDT 32 7 0,41

8 < DTWDT 16 9 0.54

4 < DTWDT 8 13 0.82

2 < DTWDTE 4 17 1.09

1 < DTWDT 2 25 1.63

DTWDT 5 1 41 2.72

In general, the time spans given above were adequate to keep the

evaluation of the right-hand side of Eq. (2) within the linear region.The value of cp is not constant, as assumed, and the relation

cp = 0.0797 + (5.556 x 10 5) TW, (17-4 PH stainless steel) (3)

was used with the computed value of TW at the midpoint of the curve fit.The maximum variation of cp over any curve fit was less than 1.5 percent.Thus, the assumption of constant cp was reasonable. The value of density

used for the 17-4 PH stainless steel skin was, w = 490 ibm/ft 3, and, theskin thickness, b, for each thermocouple is listed in Table 2.

The heat-transfer coefficient calculated from Eq. 2 was normalizedusing the Fay-Riddell stagnation point coefficient, HREF, based on anose radius of 1.0 foot (scaled down to the scale of the vertical tail,i.e. RN - 0.0175 or 0.0525). (see Appendix III)

The pressure transducers used for the probe measurements were cali-brated prior to each operational shift, and as required,with a knownpressure differential and their readings recorded. A zero pressuredifferential is applied across each transducer and the zero readings arerecorded. Prom,these data scale factors for each transducer foreach range are calculated, Probe pressures are calculated from differ-enti4l pressure readings using the calibrated scale factors, plus a

reference pressure (near vacuum),

12

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3. 3 UNCERTAINTY OF MEASUREMENTS

In general, instrumentation calibrations and data uncertaintyestimates were made using methods recognized by the National Bureau ofStandards (NBS). Measurement uncertainty is a combination of bias andprecision errors defined as:

U t (B + t 95S)

where B is the bias limit, S is the sample standard deviation, and t9is the 95th percentile point for the two-tailed Student's "t" distri-bution (95-percent conf idence interval), which for sample sizes greaterthan 30 is taken equal to 2.

Estimates of the measured data uncertainties for this test aregiven in Table Ia. The data uncertainties for the measurements aredetermined from in-place calibrations through the data recording systemand data reduction program.

Propagation of the bias and precision errors of measured data throughthe calculated data was made in accordance with Ref. 2 and the resultsare given in Table lb.

4.0 DATA PACKAGE PRESENTATION

Oil flow photographs and plots of flow 'angle as a function of thepercentage of distance along the vertical tail leading edge were trans-mitted to Rockwell at the completion of the OH-102A test. A typicaloil flow photograph was presented in Fig. 4.

The final tabulated heating and flow field probe data were trans-mitted with this report to NASA-JSC and Rockwell International. Theoil flow photographs obtained on the OH-400 test have been sent toRockwell International. Sample tabulated data of the heat transfer andflow field probe measur-ements are presented in Appendix IV.

Representative daia, along with the leading edge of the 0.0525scale vertical tail and SILTS pod,are presented in Fig. 16. Data fromtwo groups are present,-d as a sample of data repeatability. Representa-tive data from the probei measurements are presented in Fig. 17.

13

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REFERENCES

1I. Test Facilities Handbook (Eleventh Edition). "von Karman GasDynamics Facility, Vol. 3." Arnold Engineering DevelopmentCenter, June 1979.

2. Abernethy, R. B. and Thompson, J. W. "Handbook Uncertainty in Gas TurbineMeasurements." AEDC-TR-73-5 (AD755356), February 1973.

-i 14

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APPENDIX I

-e ILLUSTRATIONS

.15

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Screen ~ ~ ~ ~ ~ b Tunnel NozeScinTest sectionDfuerScin

Tank 1. Tunnel en

16i

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cq0

0 r- r-

'.4 eqV-4 04

0 04,40

0-44

gr 4

r4

11 0M

.4-4

-a 02

Q C4

4J M to

V ~,- ___"__ v4- 4

I 4. C. ton

m Lo

4

0 0d

lu c

4- 1 0U

C'HI00

17

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jii44

'14

4 beo cq

ki) 000e

4 j VIwo 00 co -40 to

t. -cI4 - 4 J 1-4

0 be

0 cc4.44

4J 90

00 0en

A00

Page 23: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

cc.

-4

Hz

-a

04

-4

1~9

* ___________________________________________________ ______________________________

Page 24: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

CD2

CZ)

'-4

0 0)

02

Page 25: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

Id

U .4

0

.4

*1 * .4

-44

-4

.Cto)

U.%4

r44Id)

e4.

212

-AELIM0

Page 26: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

22

Page 27: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

0 -

01 f-4

00IA

00-4k x -4x10 Z11

.. N

P-4A

I- tM m 0

*4~-

C.)l41~

030

00 4)00 x0 bD

400 bOM

0.14 4

.44

to

-4-*tto

z 23

Page 28: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

I 04

11

00 z

OD- X , U -4

0. 1- 1-4

1K>Ar4 %4+ V4'

0010X 0 w-*'

~ ~tto4

r-4 M..j

Q0

zO 039b

M. to

to0 9_ __ __4J1

P40001++

cs + 24

Page 29: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

71

25

Page 30: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

4o

9;z

t-'

4

E-4

P4

it S 26

Page 31: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

01-4

0. 0 . o 1-- 0- c

0-- - 0; N - IN o n 0 - ,

is

I9O \ .- 1

0

7 -4.

I.8

P4

4

27

Page 32: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

0

-4

4

4.)

V

'.4

0 u

4-4W

-a W~ 0 2

> 04v44 :0-

-44

C,3

0

0

0

'-4ba r4

a)04

0+

0

-4

-4

-4 A

28

Page 33: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

0

131

I-00

04 "0

0 -q

00 "I)~4V4

r~4J

-H C)

/V _4 C

4-)- r-4X4~ u~I I ~ I 4

................ih0.il

Page 34: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

cmJ

Ig.4

0- 1I 0

d S

20 V

o %*0

0 V

10 ..4

300

Page 35: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

* -1

C.'V

010

* .. 4 /31-~-

Page 36: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

71]

I i I I r Iii I Bi hf' AIi n i I 1 1 h Opt I ~I i v' I

Page 37: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

44

o; 0 C .Y

0

-E-

100

0 - 0 0 0-

o 0

4 4J

4D 0

0

o to

(01*) P4

33.L) H

o

.44

330

c. . , • ..... 1_ "-- i '' U 4,. " --,3'0'- , - '

Page 38: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

4.)

- -- - - - - - - : -

0.- - ' 54

04o) 0

0

c0)

-7-* -- 7

.0

0 0 0 0

-4

04

34

Page 39: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

4r

qgo

-44

* ~OO

-44

354

Page 40: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

APPENDIX 11

TABLES

36

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1 -0 -.-

10 -. 0 ol T10-C6~

Ow3

OK I +1 I

W* +1 +

+1 oo co00

0,j 04 . , 0 - 5 ~ ~ - I.

0,3, I" 040

1 0. 440

OD041 A3 15

MIN. 0

0100 31- 00. ft000

1 4 0 0 0 0 D 0 3o

0

3 44

00 A**fl4f '

-~ 0 ~ N -N N NO3o.,)o353 ~ N e~ 000a

*~ 4 0' 0 * , + r

3.+ +53

0 +4+ +4 4 +37

Page 42: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

90 vi 06 r. U

0 - ~~ 00 0,

.T Ij n 0 +-- +1- 0 IO

luao ~U d 0

00 +1 0

JO 0.0.d 0

U 44 +1 44 0

4.4m00

toll~fl o +

1444 tjwe N~v

~10 0 ~ U1P+4I

4.4 38

Page 43: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

TABLE 2. Model Thermocouple Locations

a. 0.0175 Scale Vertical Tail

(CONSTANT SET 111)

'PC No. X,/Cv Z /3 V b, TC No. X/CV Z/BV bi nches~ inches

1 0.1 .70 .015 22 0.00 0.~ 5 .0163 0.30 .021 24 0.210 .0216

4 ,.70 .021 25 0.30 .019_5 0 .90 .020 -- 26 0.40 j0 9

6 0.00 6 871 050.7 00 28 0.701

8 0.20 .02 29 0.00 0.90 .020.9 0.30 .020 30 0.10 I.01610 _ 0.40 .021 .019

11 05 020 32 50.01612 0. 020D 33 0.70 1.019~

10.0.0201 34 0.90 I.02 1.14 0.00 .8 .018 35 0.10 0.937 .01615 0.10 4.0181 36 0.38 0*41023~16 06-.20 6 .02 37 0.60 0.25 .017117 0.30 .020 38 0.70 0.949818 0.40 I .020 39 0.80 0.4 19

10,0.019 40 -0.13 0.97oi20 0.70 I.020 4 1 0.00 1.02521 0.90 .020 42 0.18 .0201

43 0.10 1.00 .014

39

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TABLE 2. Concluded

b. 0.0525 Scale Vertical Tail

_(CONSTANT SET 211)

b, b,

TC No. X/CV Z/BV inches TC No. X/CV Z/BV inches

1 0.00 .817 .024 24 0.287 .883 .02262 0.052 .0203 25 0.00 .9 0 .0193 0.104 .0201 26 0.052 .0234 0.156 .0208 27 0.104 .0205 0.209 .0225 28 0.156 .0226 0.287 .0232 29 0.209 , .02187 0.00 .833 .022 30 0.00 .917 .0208 0.104 .0205 31 0.052 .02159 0.209 .0232 32 0.104 .019510 0.00 .8"0 .022 33 0.156 .02111 0.052 .020 34 0.209 ' .021512 0.104 .0208 35 0.00 .933 .022313 0.156 .0212 36 0.052 .022114 0.209 .0235 37 0.104 .02115 0.287 i .0225 38 0.156 .021516 0.00 .8 7 .0223 39 0.209 i* .022817 0.104 .0218 40 0.00 .950 .018818 0.209 1 .0235 41 0.052 j .023719 0.00 .813 .020 42 0.104 .021320 0.052 .0235 43 0.156 I .02221 0.104 .022 44 0.209 i .021822 0. 156 .023 45 0.287 i .021523 0.209 .0228 46 0.00 .956 .021

TC No. THETA, S/R b, TC No. THETA, S/R b,deg inches deg inches

47 180 1.178 .021 63 215 0.393 .01848 0.785 .016 64 j 0.785 .02049 1 0.393 .011 65 1.178 .02250 0 0.00 .022 66 - 2.269 .020551 0.393 .021 67 - 2.89 .018852 0.785 .014 68 3.513 .020453 1.178 .0125 69 4.114 .022254 2 0 1.178 .020 70 90 1.63 .02055 0.785 .023 71 1.996 .019856 0.393 .022 72 2.542 .02057 !0 0.393 .023 73 3.09 .02358 0.785 .023 74 3.619 .023259 1.178 .020 75 0 1.571 .021560 15 0.393 .024 76 2.542 .02261 0.785 .024 77 3.637 .02362 1.178 .024

40

Ma

Page 45: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

C eq Nq e) c 0t-

eq

41

* 0 e-4 k

F" 94-qc

-4

q4.0

- 0 N0

0 bi04r4 4

300

be) CV M Nt

41

Page 46: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

eq C;

00 ton t- goqi Ito~ to in

-I4

4.1 -04 11 - q )

o~~C Ci Ci .o Co - - C o - -4 -40 q t- 0eq r4 * Cr

I .4 Co Co (D eq eq

x *4

.4 :3 - 04'~~~~ 00 en 0 e .4' a o C C

5 CV)~ 54* - O Co Co q eq - - ~ -

0 0 -4t' eq 0as eq -

4J Q

*10 - - - - - - - - - - - -4

4) C0 -tocq ~~t (D0 C o s C -4 CO) eq3 CV) C s4s C C; o o C') m ~ -4 -4 -4 4

C: e. 0V v)

* 0

o 54

4) nf 0 to 0 in a '0 0 to I 0(5) C1 C41 m I mI (5) '

Cs e

to

-4

424

Page 47: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

0 1

*~0 0O) v~a ~~

C),

100

14 m

4J 00

0 0

04 t

14 0 toLO4fN ~ ~ ~ ~ r VC0 ) 0)0 ) 0

'.443

44 0

Page 48: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

0D 0-4 -4 -4 4

o4 4 4 -k e

0 -4

o 0 -4 -4 eq - 4 -4a m * -4 r4 r 4~ 1

4 -4 eqCf

09

P4 =-4")

00 0a F4

0p4~~~4 000 ~ q C

04 40&40 -4

140 01-4 04 G

a) 4) 04

WINI

Page 49: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

0)

a) C" a%, n -

Hn H~H H -Hl Hq H- H- H 4 C)

.0vo.cng Ll cn UN e\ %D

H H H H 04

\,oti-- N c H 0% C7, - f

ot

;-4 qn H H H- H 7 ON H

t- t- t - t C c-- .14Mc CV) c oj o cm t-re- q e- c - I

C))

x en vU 't Co

Lgo co CC) m- m0 0% m. '.4 ir j QTXe cne CMtj l u CM H~ H- Hi M -4

Cl2 0

a))

C; o

( n en i'' n en (n NO

H\ H

45

Page 50: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

APPENDIX III

REFERENCE HEAT-TRANSFER CONDITIONS

In presenting heat-transfer coefficient results, it is convenient

to use reference coefficients to normalize the data. Equilibrium stag-

nation point values derived from the work of Fay and Riddell* were used to

normalize the data obtained in this test. These reference coefficients

are given by:

8.17173(P02) 0 "5 0M)0"4[ - (P-INF)1 0.25 O.2235+(l.35xlO5)(TO+560

HREF P02

(RN) 0 . 5 (To)O. 1 5

sT = (RHO-INF) (V-INF) [0.2235 + 1.35 x 10-5 (TO + 560)

*Fay, J. A., and Riddell, F. R., "Theory of Stagnation Point Heat

Transfer in Dissociated Air," Journal of the Aeronautical Sciences,Vol. 25, No. 2, February 1958.

.4

i4

I

Page 51: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

APPENDIX 1V

SAMPLE TABULATED DATA

47

Page 52: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

J=40

COCO w a

41.00 a0

4, o o00 -9C4 UiS. -

0Xi 0 W Uaoe.j A 4 L . a"-

IJI.D w C v . 0 306

2ea 1.0 .

Ut .4 :0t C

ae 0 C4 SIe a o ~ w o

.30 45 0000000 0000CO d0 0 aa00 a 0 000 -000a

M. C- D aZ a U)---.c- 0 al0 Cc0 0 0 .o.0oacco 0 0 a 0 Cw. o2V U) o 0 00aCa000 c0 010 0 c 00000 00000 00e 000

I .

U0 5 0000000 000000o 00c0 0- 00 0 0 a00 o

I i U 0 0 0000000 00000000 000 0000. .0.- 1 :4 I. . C

0000 1 aOOOOOOCOOQO 0000000000 a00 000a

,C 0. W. c 0M. -a %0. In.-)

S2 v CV 0

10 C', 0, C, 11 ~ 3~- C> VI

a.. C:.a -0. . . *...c cZ 000a00 0000 0 C,00000e000 0 000 aa

a. 2Lo r- ES 0v % ' .-in

S.~~ a I- I I.V V ) . o 4a ' n.V ,.S 1S-~ mu S. .mi, . *. W, cc U: , "s we -, muW W

* ~ ~ g .*S- 0aWUCV-uUC... :iC.5 A -c., snm w05 0

U)! -tC-- SC t -n E~ O .. 0 a'0 .. v-ow n I4 - - - m

1. 01 C -Itc c!! 0 CM t~ DC I5

9L .. L aC 0 0 . t 0 01)~. 00. e0

Uo T 10 W:ISNc.5N.W~~?C ~fof b.C w

"C.o -c0o 4;1 *..f. 1"4 -W-.

.5Ih 2 at0w e4 ,O % .m 0W Z-.f f

It :4 . C2 wo

0ch dc au. 10 Vt

b~SCA 4" N . S. o)daS a.0 5..U fUr5t.4 n..CI ~ 00..u

Page 53: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

JOEO U

0 40

.- ar.

a.L1 a.

4Qib9 0. C*C

9L

a a-

-. --

&Jm a Uao4

-C z. * -~O.f

L~ IL

S Cr4

4. ae

I his

0m u

*- c

aa &aW" I W. 0

AS b.9 & 1 ~ O O

V. 0

Uu- a '

4. .1..&L v

w 49

.II ME4

Page 54: TSR 79 V I lllllll EIEEEIIIIIIEE · RHO-INF Free-stream density, lbm/ft 3 RN Reference nose radius, (0.0175 ft or 0.0525 ft, determined by model scale) ROLL-SECTOR Tunnel sector roll

I