Shell and Tube Heat Exchanger October 7, 2003 Cycle 2 Group 1A Frank Fadenholz Jennifer Fadenholz...
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Transcript of Shell and Tube Heat Exchanger October 7, 2003 Cycle 2 Group 1A Frank Fadenholz Jennifer Fadenholz...
![Page 1: Shell and Tube Heat Exchanger October 7, 2003 Cycle 2 Group 1A Frank Fadenholz Jennifer Fadenholz Christian Woods Angel Taylor.](https://reader030.fdocuments.us/reader030/viewer/2022032706/56649ca25503460f949615e0/html5/thumbnails/1.jpg)
Shell and Tube Heat Shell and Tube Heat ExchangerExchanger
October 7, 2003October 7, 2003Cycle 2Cycle 2
Group 1AGroup 1AFrank FadenholzFrank Fadenholz
Jennifer FadenholzJennifer FadenholzChristian WoodsChristian Woods
Angel TaylorAngel Taylor
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OutlineOutline
• ObjectivesObjectives
• BackgroundBackground
• Experimental StrategyExperimental Strategy
• ResultsResults
• Error AnalysisError Analysis
• ConclusionsConclusions
• RecommendationsRecommendations
• ReferencesReferences
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Objectives and Objectives and BackgroundBackground
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ObjectivesObjectives
• Operate shell and tube heat exchanger Operate shell and tube heat exchanger varying steam flowvarying steam flow
• Determine the outside overall heat transfer Determine the outside overall heat transfer coefficient (Ucoefficient (Uoo))
• Determine shellside heat transfer (QDetermine shellside heat transfer (QSSSS))
• Determine tubeside heat transfer (QDetermine tubeside heat transfer (QTSTS))
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Heat Exchanger BackgroundHeat Exchanger Background
• Exchange heat between fluidsExchange heat between fluids
• Latent heat and sensible heat transferLatent heat and sensible heat transfer
• Common to chemical process industryCommon to chemical process industry
• Types of heat exchangersTypes of heat exchangers– Air CooledAir Cooled– Double PipeDouble Pipe– Spiral Plate and TubeSpiral Plate and Tube– Shell and TubeShell and Tube
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Heat Exchanger BackgroundHeat Exchanger Background
Shell and Tube Heat ExchangersShell and Tube Heat Exchangers
• Account for 60% of heat exchangers in use todayAccount for 60% of heat exchangers in use today
• Can handle large flows, low temperatures and Can handle large flows, low temperatures and pressures, high temperatures and pressurespressures, high temperatures and pressures
• Our shell and tube heat exchangerOur shell and tube heat exchanger– Basco Type 500 U-tube Water HeaterBasco Type 500 U-tube Water Heater– 1 Shell Pass1 Shell Pass– 16 Tubes16 Tubes
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Experimental StrategyExperimental Strategy
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ST-V1
FT-01
EmergencyShutdown
Vavle
CompressedAir Steam
Hot Water Outlet
TT-04
TT-03
PG-07
Con
densate
ColdWaterInlet
EmergencyShutdown
Valve ST-V3
PRV-05
PG-06 FT-02
E-01
Figure 1. Unit Operations Lab: Shell and Tube Heat Exchanger(Group 1A)
ST-V4
ST-V2
ST-V5
FV-02
TV-04
T
Should make Labels Larger
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Experimental StrategyExperimental Strategy
• 5 Runs Total5 Runs Total• Varied Steam Valve (TV-04) PositionVaried Steam Valve (TV-04) Position
– 105% open105% open– 75% open75% open– 65% open65% open– 60% open60% open– 52% open52% open
• Cooling water flow rate constantCooling water flow rate constant
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Experimental StrategyExperimental Strategy
• Measured VariablesMeasured Variables– Condensate flowCondensate flow– Condensate temperatureCondensate temperature– Cooling water flowCooling water flow– Cooling water inlet temperatureCooling water inlet temperature– Cooling water outlet temperatureCooling water outlet temperature
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Heat Exchanger Heat Exchanger CalculationsCalculations
• Heat transfer rate Heat transfer rate QQTSTS = mCp = mCpT T
QQSSSS = m = mH + mCpH + mCpTT
• Overall heat transfer coefficientOverall heat transfer coefficient UUoo = Q = QSSSS/(A/(Aoo**TTLMLM))
Log mean temperatureLog mean temperature TTLM LM = = ((T((Thihi-T-Tcoco) – (T) – (Thoho – T – Tcici)) / ln[(T)) / ln[(Thihi – T – Tcoco) – (T) – (Thoho – T – Tcici)])]
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Simplified Process Flow Simplified Process Flow DiagramDiagram
Thi
Tho
Tci TcoQout, TSQin, TS
Qin, SS
Qout, SS
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ResultsResults
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Experimental ResultsExperimental Results
Steam Valve% Open
Heat Transfer
Rate (QTS)(btu/hr)
Heat Transfer Rate (QSS)(btu/hr)
Overall Heat Transfer
Coefficient (Uo)
(btu/lb*F*hr)
105% 276489 275350 211
75% 250275 254588 201
65% 183357 181872 148
60% 134200 133777 112
52% 98289 93757 78
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90000
140000
190000
240000
290000
75 125 175 225 275Condensate Mass Out
(lb/hr)
Hat
e T
rans
fer
Rat
e (b
tu/h
r)
Q-Shellside Q-Tubeside
Steam vs. Heat Transfer Rate (QSteam vs. Heat Transfer Rate (QTSTS, , QQSSSS))
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Steam vs. Overall Heat Transfer Steam vs. Overall Heat Transfer CoefficientCoefficient
50
100
150
200
250
300
50 100 150 200 250 300
Condensate Mass Out (lb/hr)
Hea
t Tra
nsfe
r C
oeffi
cien
t (b
tu/lb
*F*h
r)
U inside U outside
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Error AnalysisError Analysis
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Propagation of ErrorPropagation of Error
• Determine the accuracy of measured Determine the accuracy of measured variablesvariables
• Apply the propagation of error equation to Apply the propagation of error equation to each functioneach function
21
1
2
k
ii
i
xx
yy
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Variable Measurement Variable Measurement AccuracyAccuracy
• Flow rate of the steam +/- 5 lb/hrFlow rate of the steam +/- 5 lb/hr
• Flow rate of the cooling water +/- 50 Flow rate of the cooling water +/- 50 lb/hrlb/hr
• Temperature readings +/- 2 Temperature readings +/- 2 °°FF
• Largest sources of error Largest sources of error – Mass flow rate of the steam Mass flow rate of the steam – Mass flow rate of the cooling waterMass flow rate of the cooling water
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Calculated Error ValuesCalculated Error Values
• ∆∆QQTS TS ≈ +/- 1,000 btu/hr≈ +/- 1,000 btu/hr
• ∆∆QQSS SS ≈ +/- 50,000 btu/hr≈ +/- 50,000 btu/hr
• ∆∆UUo o ≈ +/- 4 btu/lb ≈ +/- 4 btu/lb °°F hrF hr
• ∆∆UUi i ≈ +/- 4 to +/- 1.6 btu/lb ≈ +/- 4 to +/- 1.6 btu/lb °°F hrF hr
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Propagation of Error Heat Propagation of Error Heat TransferTransfer
90000
140000
190000240000
290000
340000
75 125 175 225 275
Condensate Mass Out (lb/hr)
He
at
Tra
nsf
er
Ra
te
(btu
/hr)
Q-tubeside Q-shellside
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Propagation of Error Heat Propagation of Error Heat Transfer CoefficientTransfer Coefficient
50
100
150
200
250
300
50 100 150 200 250 300
Condensate Mass Out (lb/hr)
Hea
t Tra
nsfe
r C
oeffi
cien
t (b
tu/lb
*F*h
r)
U inside U outside
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Conclusions Conclusions and and
RecommendationsRecommendations
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ConclusionsConclusions
• QQTSTS, Q, QSSSS, U, Uoo all increase as the steam flow all increase as the steam flow rate increasesrate increases
• QQTSTS, Q, QSSSS, U, Uoo all have a linear relationship all have a linear relationship with the mass flow rate of the steamwith the mass flow rate of the steam
• Heat transfer rate of the tube side is Heat transfer rate of the tube side is equal to the heat transfer rate of the equal to the heat transfer rate of the shell sideshell side
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RecommendationsRecommendations
• Operation RecommendationOperation Recommendation– Operate the shell and tube heat Operate the shell and tube heat
exchanger at approximately 75% for exchanger at approximately 75% for sufficient heat transfer and economic sufficient heat transfer and economic efficiencyefficiency
• Experiment RecommendationsExperiment Recommendations– Monitor pressure gauge (PG-07) at low Monitor pressure gauge (PG-07) at low
steam rates to prevent a vacuumsteam rates to prevent a vacuum
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ReferencesReferences
• API Heat Transfer. Shell and Tube Heat Exchanger PictureAPI Heat Transfer. Shell and Tube Heat Exchanger Picturewww.apiheattransfer.com/en/Products/HeatExchangers/www.apiheattransfer.com/en/Products/HeatExchangers/ShellAndTube/ShellAndTube/
• Georgia Tech. Georgia Tech. Propagation of ErrorPropagation of Error. . www.swiki.che.gatech.edu/CHE4200. August 2002.www.swiki.che.gatech.edu/CHE4200. August 2002.
• Geankoplis, Christie J. Geankoplis, Christie J. Transport Processes and Unit Transport Processes and Unit OperationsOperations, 3rd ed. Englewood Cliffs, NJ. Prentice-Hall , 3rd ed. Englewood Cliffs, NJ. Prentice-Hall Publishing, Inc. 1993.Publishing, Inc. 1993.
• Heald, C. C. Heald, C. C. Cameron Hydraulic DataCameron Hydraulic Data. Liberty Corner, NJ. . Liberty Corner, NJ. Ingersoll-Dresser Pump Co. 1998.Ingersoll-Dresser Pump Co. 1998.
• Peters, Timmerhaus, West. Peters, Timmerhaus, West. Plant Design and Economics for Plant Design and Economics for Chemical EngineersChemical Engineers, 5th ed. New York, NY. McGaw-Hill Co. , 5th ed. New York, NY. McGaw-Hill Co. Inc., 2003.Inc., 2003.
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