team members: allen baragar dustin thompson jose membreno katelyn this

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Team Members: Allen Baragar Dustin Thompson Jose Membreno Katelyn This MECT 4275 Spring 2014 Industrial Advisors: Paul Tyllick- System Interface Supervisor, Technip USA Keith Wingfield- CAA Tech Center Engineering Consultant Chris LeBlanc- VP of Sales and Marketing, Lime Instruments Instructor: Professor Raresh Pascali Faculty Advisor: Dr. Mehendra L. Joshi

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MECT 4275 Spring 2014. Team Members: Allen Baragar Dustin Thompson Jose Membreno Katelyn This. Instructor: Professor Raresh Pascali Faculty Advisor: Dr. Mehendra L. Joshi. Industrial Advisors: Paul Tyllick - System Interface Supervisor, Technip USA - PowerPoint PPT Presentation

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Page 1: Team Members:        Allen  Baragar Dustin Thompson Jose  Membreno Katelyn This

Team Members: Allen BaragarDustin ThompsonJose MembrenoKatelyn This

MECT 4275Spring 2014

Industrial Advisors:Paul Tyllick- System Interface Supervisor, Technip USA

Keith Wingfield- CAA Tech Center Engineering Consultant

Chris LeBlanc- VP of Sales and Marketing, Lime Instruments

Instructor: Professor Raresh Pascali

Faculty Advisor:Dr. Mehendra L. Joshi

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Outline

• Objective/Goals• Purpose• Market Research

▫ Online survey▫ Current market offerings

• Design and Analysis▫ System Schematic▫ Thermodynamic Analysis▫ Parts

• Laboratory Experiments• Budget• Risk Matrix• Gantt Chart• Sponsorship• Lessons Learned• Questions

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Objective

•Create a compact, portable steam power plant trainer that will aid in the understanding of the Rankine cycle and automated system control

Goals• Achieve fully automated system control• Rolling frame for ease of transport

▫ Dimensions of 4x2x3.5 feet• Deliver the product complete with multiple lab

experiments• Produce an aesthetically pleasing product

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Purpose

•Many students find difficulty understanding thermodynamics without being able to apply theory to real world application

•Steam power plants account for roughly 78% of the world’s electricity

•Students will learn the automated control system and will obtain a working knowledge of how to check transducer readings

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Online Survey

• Using Survey Monkey ▫ 110 respondents ▫ 10 questions

• Questions: 1. What is your age?2. What type of engineering degree do you have?3. What is the highest level of school or degree you have completed?4. Did you take thermodynamics?5. If so, did it require a lab section?6. Did your thermodynamics class/lab include steam power plant training

station?7. Did you find the training equipment useful?8. If the training equipment was not useful, why?9. If you did not have training equipment, would you have liked to have one? Would it have been beneficial?10. What is your alma mater?

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Market Research ResultsDid you take Thermodynamics?

YesNo

12%

88%

If you took thermodynamics, did it require a lab section?

Yes

No

N/A64%

25%11%

Did your lab include a steam power plant training station?

YesNoN/A

25%

67%

8%

75%

25%

Did you find the training equipment useful?

YesNo

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Current Market Offerings

$33,000 $40,000Unknown Price $175,000-350,000

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System Schematic

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Analysis

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Analysis

win = 0.339 Btu/lbm qin = 123.0 Btu/lbm wout = 225.0 Btu/lbm qout = 898.3 Btu/lbm

Assumptions:

T1 = 110°F

P2 = 25 psi

P1 = 4 psi

Assumptions: Fluid is super heated

when it exits the boiler

Assumptions:

T3 = 350°F

P3 = 100 psi

Assumptions: Fluid is a saturated

mixture

T4 = 153°F

P4 = 4 psi

Rankine Cycle Analysis

Idealization: q = 0

w = h2-h1= v(p2-p1)

Idealization: w = 0

q = h3-h2

Idealization: q = 0

w = h4-h3

Idealization: w = 0

q = h4-h1

(1)-(2) (2)-(3) (3)-(4) (4)-(1)

Isentropic Compression in Pump

Constant Pressure Heat Addition in Boiler

Isentropic Expansion in Turbine

Constant Pressure Heat Rejection in Condenser

qin = 1123.035 Btu/lbm

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Control Systems

Specifications UnknownPrice to be determined Specifications Unknown

Price to be determinedWorks with Inline-instant Steam Generator

Price to be determined

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System Schematic

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Steam Generator

Infinity FluidsInline-instant Steam Generator

220V$2600.00

Model Number A (in) B (in) C (FNPT Std.) D (in) Watts (kW) Volts Phases AMPS CRES-SG-12-0010-K 12 9.75 1/4 2.0 1.0 120 1 8CRES-SG-12-0020-K 12 9.75 1/4 2.0 2.0 120 1 17CRES-SG-12-0040-K 16 13.25 1/4 3.0 4.0 240 1 17CRES-SG-12-0060-K 16 13.25 1/4 3.0 6.0 240 1 25

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Recirculating Pump

Price Unknown

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Flow Meter

BlancettTurbine Flow Meter

-150°F-375°F3/8 to 10in bore sizes

Accuracy: 1%$375.00

Simple Float style units or high

resolution digital units

Price Unknown

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Condenser

Price: $800

http://www.infinityfluids.com/documents/CRES-HXS-GA_PKG1.pdf

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DC Motor

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Turbine Pump

Purchasing v.s. Manufacturing

Rankin Rollers

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Control Valves

¼” Inlet-OutletFull Port Ball Valve

0-2000 psi$695.00

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Safety Pressure Valve

AquatrolInlet: ¼”

Overall Height: 2-7/8”Pressure Range: 0-200 psi

Temperature Range: 0-406°FASME Section VIII/CRN

$75.00

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Thermal Couples

¼” OD probeFlow-Through Thermocouple

Temp range: -418-500°F$152.10

¼” OD probeFlow-Through Thermocouple

Temp range: -330-2460°F$132.00

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Pressure Transducers

Celerity¼” input & output connection

Pressure Range: 250 psi$59.99

AST American Sensor TechDifferential Pressure Transducer

Pressure Range: 5,000 psi$495.00

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Analog Display Gauges

Pressure Range: 0-50 psi

Temp Range: -40-250˚F

$38.70

Temp Range: 32-250˚F

Price Unknown

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Lab Experiments

•Plot power curve▫Watts vs. Flow rate▫Watts vs. % Valve

•Calculate cooling tower efficiency

•Calculate condenser efficiency

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Budget

Low High ActualElectric Boi ler 1,000$ 3,000$ 2,000$ Turbine Pump 250$ 1,000$ Reci rculating Pump 200$ 450$ Condenser 40$ 235$ 800$ Flanges and Elbow Joints 125$ 175$ Pipe Reducer (2) 15$ 50$ DC Motor 200$ 400$ Safety Pressure Va lve 50$ 100$ Solenoid/Bal l Va lve 20$ 100$ Pressure Transducers 60$ 495$ Thermal Couples 132$ 153$ Control System 500$ 5,000$ *DonatedFlow Meter 300$ 4,000$ Piping 90$ 170$ Frame Materia l 150$ 220$ Welding 50$ 200$ DonatedCool ing Tower 100$ 600$ DonatedTotal 3,282$ 16,348$

Expected Costs

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Risk Matrix

Risks1 Injury2 Not meeting funding requirements3 Poor design due to calculation error4 Fail to finish project5 NW-Campus lab power capacity6 Outsourcing cost7 Team logistics8 Software Hardware interface issues9 Noise issues

10 Long lead times11 Manufacturing issues

Severity

Catastrophic 4 1,2 10  

Severe 11 8

High 3

Medium 7 5 6

Low 9

Low Possible High Very High Definite

Likelihood

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WBS Steam Power Plant Trainer

WBS

(45%)Market/Technical Research

(90%) Gaging Interest

(100%)Market Offerings

(100%)Scout Vendors

(100%)Spec’ing parts

(85%)Parts

pricing

(90%)Narrow choices

(85%)Automated Control

(70%)

Design/Analysis

(89%)Create Basic

Design Schematic

(100%)Part Design

(75%)Thermodynamic analysis

(90%)Boiler

selection

(95%)Condenser Selection

(95%)Design Lab

Experiments

(80%)

Fabrication and

Assembly

(0%) Parts acquisition

(0%)Frame

(0%)Secure Main

components

(0%)Assemble piping

(0%)Wiring

(0%)

Testing

(0%)

Automated control test

(0%)Boiler test

(0%)Valve testing

(0%)Sensor testing

(0%)

0% 40% 60% 80% 100%

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Gantt Chart

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Current Sponsors

Sponsorship Package

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Lessons Learned

•Make efficient use of your time.

•Trust but verify.

• If it sounds too good to be true it probably is.

•Doesn’t hurt to ask any company for donations.

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Contact Us

•Online:▫http://cot-mect4276.tech.uh.edu/~kathis▫www.rankinrollers.com

•Facebook: ▫facebook.com/RankinRoller

•Email:▫[email protected]

Page 42: Team Members:        Allen  Baragar Dustin Thompson Jose  Membreno Katelyn This

Questions?