caso37f2012-detailed report.xls

Index1 Input File

2 Solution History

3 Main

Input File$ Generated by PRO/II Keyword Generation System <version 8.0>$ Generated on: Mon Jan 30 10:56:56 2012TITLE PRINT STREAM=ALL, RATE=LV,GV, FRACTION=M DIMENSION SI, TEMP=C, PRES=KG/CM2, TIME=DAY, FLENGTH=CM, & ENERGY=CAL, WORK=KCAL/HR, CONDUCT=CAL/H, HTCOEF=KC/H, & FOUL=HMC/K, VISCOSITY=CP OUTDIMENSION REPLACE, ENGLISH, TIME=DAY, ENERGY=KWH, WORK=KW, & STDTEMP=60.0008, STDPRES=14.6959, PBASIS=14.6959 SEQUENCE SIMSCICOMPONENT DATA LIBID 1,METHANE/2,N2/3,H2O/4,AIRTHERMODYNAMIC DATA METHOD SYSTEM=PR, SET=PR01, DEFAULTSTREAM DATA PROPERTY STREAM=S1, TEMPERATURE=22, PRESSURE=45, PHASE=M, & RATE(GV)=3.53961E6, COMPOSITION(M)=1,73.58/2,26.42 PROPERTY STREAM=S18, TEMPERATURE=30, PRESSURE=10, PHASE=M, & RATE(WT)=4.32219E7, COMPOSITION(M)=3,100UNIT OPERATIONS COMPRESSOR UID=C1 FEED S1 PRODUCT V=S2 OPERATION CALCULATION=ASME, PRES=80, EFF=75 HXRIG UID=E1 TYPE TEMA=AES, ORIENTATION=HORI, FLOW=COUN TUBES FEED=S3, M=S4, LENGTH=2.4384, NUMBER=3200, PATTERN=90 SHELL FEED=S18, M=S19, SERIES=2 VALVE UID=V2 FEED S7 PRODUCT M=S8 OPERATION PRESSURE=45 MEMBRANE UID=MEM1 FEED S8 PRODUCT S9,S11 RPARM =10,21500,4.8301,1.4617 HXRIG UID=E3 TYPE TEMA=AES, ORIENTATION=HORI, FLOW=COUN TUBES FEED=S4, M=S5, LENGTH=4.572, NUMBER=1600, PATTERN=90 SHELL FEED=S9, M=S10, SERIES=2 MEMBRANE UID=MEM2 FEED S11 PRODUCT S12,S15 RPARM =10,16000,4.8301,1.4617 HXRIG UID=E4 TUBES FEED=S5, M=S6, LENGTH=4.572, NUMBER=1600, PATTERN=90 SHELL FEED=S12, M=S13 VALVE UID=V1 FEED S15

Index

PRODUCT M=S16 OPERATION PRESSURE=5 HXRIG UID=E5 TYPE TEMA=AES, ORIENTATION=HORI, FLOW=COUN TUBES FEED=S6, M=S7, LENGTH=4.572, NUMBER=1600, PATTERN=90, & FOUL=0.00020482 SHELL FEED=S16, M=S17, FOUL=0.00020482 HXCALC HTCMETHOD=CHEN COMPRESSOR UID=C2 FEED S13 PRODUCT V=S14 OPERATION CALCULATION=ASME, PRES=80, EFF=75 MIXER UID=M1 FEED S2,S14 PRODUCT M=S3END

Solution History SIMULATION SCIENCES INC. R PAGE H-1 PROJECT PRO/II VERSION 8.0 ELEC V6.6 PROBLEM CALCULATION HISTORY 01/30/12 Your license will expire in -42 days. Please contact your IPASSI sales represe

*** PROBLEM SOLUTION BEGINS FEED FLASH COMPLETE UNIT 2 SOLVED - 'C1 ' Loop 1 BEGINS - 'LOOP1 ' UNIT 3 SOLVED - 'E1 ' UNIT 9 SOLVED - 'V2 ' UNIT 1 SOLVED - 'MEM1 ' UNIT 5 SOLVED - 'E3 ' UNIT 7 SOLVED - 'MEM2 ' UNIT 11 SOLVED - 'E4 ' UNIT 6 SOLVED - 'V1 ' UNIT 12 SOLVED - 'E5 ' UNIT 10 SOLVED - 'C2 ' UNIT 8 SOLVED - 'M1 ' MAX ERRORS: X=2.74E-6 (S15) T=-.214 (S16) P=.00215 (S10) Loop 1 SOLVED after 1 trials *** PROBLEM SOLUTION REACHED *** THIS RUN USED 183.75 PRO/II SIMULATION UNITS *** RUN STATISTICS STARTED 10:37:42 01/30/12 NO ERRORS FINISHED 10:37:42 01/30/12 NO WARNINGS RUN TIMES NO MESSAGES INTERACTIVE 0 MIN, 0.00 SEC CALCULATIONS 0 MIN, 0.42 SEC TOTAL 0 MIN, 0.42 SEC

Index

=========

Compressor (Detailed) UOM C1Name C1Description C1Thermodynamic System PR01Feed Streams S1Product Streams S2Product Stream Phases S14 N/A S2 VaporOutlet Temperature F 177.29708432Outlet Pressure psia 1137.86699232461Pressure Increase psi 497.816769256653Pressure ratio 1.777777667Efficiency - adiabatic 75Efficiency - polytropic 76.68412631Head - adiabatic ft 24886.8375557743Head - polytropic ft 25445.6719291339Head - actual ft 33182.4500656168Work - theoretical kW 2612.16122Work - polytropic kW 2670.817346Work - actual kW 3482.881626Isentropic coefficient 1.388650937Polytropic coefficient 1.549882498Aftercooler Duty kW-hr / day N/AAftercooler Outlet Temperature F N/AAftercooler Pressure drop psi N/AInlet Temperature F 71.59998902Inlet Pressure psia 640.050223067953Inlet Enthalpy kW-hr / day 88362.1278Inlet Entropy kW-hr / F lb 0.0006345033208079Inlet Vapor Frac fraction 1Inlet Liquid Frac fraction 0Inlet CP kW-hr / lb-mol F 0.0026593279162459Inlet Cv kW-hr / lb-mol F 0.0018243543682705Inlet CP/CV Ratio 1.457681667Actual Vol Flow at Inlet ft3 / day 2895183.51349477Isentropic Temperature F 155.9770853Isentropic Pressure psia 1137.86699232461Isentropic Enthalpy kW-hr / day 151053.99708Isentropic Entropy kW-hr / F lb 0.0006345033232578Isentropic Vapor Frac fraction 1Isentropic Liquid Frac fraction 0Outlet Temperature F 177.29708432Outlet Pressure psia 1137.86699232461Outlet Enthalpy kW-hr / day 171951.27708Outlet Entropy kW-hr / F lb 0.0006394938895092Outlet Vapor Frac fraction 1Outlet Liquid Frac fraction 0Outlet CP kW-hr / lb-mol F 0.0028157396732124Outlet Cv kW-hr / lb-mol F 0.0019690850826555Outlet CP/CV Ratio 1.429973594

Index

Feed Total Mass Rate lb / day 6686435.36274008Feed Total Enthalpy kW-hr / day 88362.1278Product Total Mass Rate lb / day 6686435.36274008Product Total Enthalpy kW-hr / day 171951.27708

HxRig (Detailed) UOM E1HX Name E1HX Description E1Shell Side Thermo Method PR01Tube Side Thermo Method PR01Shell Side Feed Stream(s) S18Shell Side Product Stream(s) S19Tube Side Feed Stream(s) S3Tube Side Product Stream(s) S4

2

1

2Orientation(Selected) HorizontalFlow Configuration(Selected) CountercurrentTEMA Type Front(Selected) ATEMA Type Shell(Selected) ETEMA Type Rear(Selected) STube Inside Diameter(User Input) ft 0.0486666659448819Tube Wall Thickness(User Input) ft 0.0069166665616798Tube Length(User Input) ft 8.0000000984252Tube Outside Diameter(User Input) ft 0.0624999990485564Tube Pitch(User Input) in 0.99999998503937Tube Pitch Pattern(Selected) Square - 90 degreesTube Sheet Thickness(User Input) in 11.9511503937008Baffle Type(Selected) SingleBaffle Geometry(Selected) CutBaffle Cut Fraction(User Input) 0.2Baffle Center Spacing(User Input) in 13.7999997913386Inlet Baffle Spacing(User Input) in 14.4244258110236Outlet Baffle Spacing(User Input) in 14.4244258110236Baffle Thickness in 0.374999994370079Number of Sealing Strips 0Number of Baffles 5Tubes in Baffle Windows Tubes In Window

1Two Phase HTC Method(Selected) ChenTube Side Coefficient(User Input) BTU/hr-ft2-F 162.678666915569Tube Side Scale Factor(User Input) 1

hr-ft2-F/BTU 0.001999999898359

ft 0Shell Side Coefficient(User Input) BTU/hr-ft2-F 2298.47064769841Shell Side Scale Factor(User Input) 1Shell Side Fouling Resistance hr-ft2-F/BTU 0.001999999898359

Number of Shells in Series(User Input)

Number of Shells in Parallel(User Input)

Number of Tube Passes per Shell(User Input)

Overall U Value Scale Factor(User Input)

Tube Side Fouling Resistance(User Input)

Tube Side Fouling Thickness(User Input)

ft 0

1

BBM

1

BellTube Material(Selected) Carbon SteelTube material Name CARB STLTube Material Density(User Input) lb / ft3 490.809952115558

BTU/hr-ft-F 29.9871731167015Shell Material(Selected) Carbon SteelShell Material Name CARB STLShell Material Density(User Input) lb / ft3 490.809952115558

in 15.2499997716535

in 13.2499997992126

in 23.2499996496063

in 27.2499995905512

in 0Duty kW-hr / day 270522.86784LMTD F 58.967176824LMTD Correction factor (Ft) 0.9751242383MTD (Ft * LMTD) F 57.50032338U Value with Fouling BTU/hr-ft2-F 75.9956448982611U Value without Fouling BTU/hr-ft2-F 116.412327913833Required U-Value BTU/hr-ft2-F 75.9957926371811Exchanger Area ft2 8801.58515979032U*A BTU/hr-F 668882.139492386Tube Bundle Weight lb 21580.4935294273Empty Shell Weight lb 23533.6162674827Shell Weight with Water lb 56147.5689165594Number of Tubes per Shell 3200Tube Side product temperature F 95.24187932Tube Side pressure drop per shell psi 0.927032987950269Tube Side Feed Pressure psia 1137.86699232461Tube Side Product Pressure psia 1136.01287209417Tube Side velocity ft / sec 11.2397497014436Tube Minimum Design Veloctiy ft / sec 0Tube Maximum Design Velocity ft / sec 999.999984908137Tube Side Fouling Factor 0.3522199821Tube Side design pressure psia 1199.9985265622Fin Efficiency 1Tube Side Reynolds number 179021.4048Tube Side Prandtl number 0.8258408441Tube Wall Resistance hr-ft2-F/BTU 0.0002607075145648

Shell Side Fouling Thickness(User Input)

Tube Side DP Scale Factor(User Input)

Tube Side Pressure Drop Method(Selected)

Shell Side DP Scale Factor(User Input)

Shell Side Pressure Drop Method(Selected)

Tube Material Conductivity(User Input)

Tube Inlet Nozzle Inside Diameter(User Input)

Tube Outlet Nozzle Inside Diameter(User Input)

Shell Inlet Nozzle Inside Diameter(User Input)

Shell Outlet Nozzle Inside Diameter(User Input)

Shell Outlet Nozzle Length(User Input)

Tube Side Feed Density lb / ft3 2.79422457354564Tube Side Feed Specific Gravity 0.3971428942Tube Side Product Density lb / ft3 4.01475937058158Tube Side Product Specific Gravity 0.3971428942Tube Side Feed Vapor Viscosity cP 0.01718053689Tube Side Product Vapor Viscosity cP 0.01367717118Shell Side Product Temperature F 95.7111728Shell Side Pressure Drop per Shell psi 19.4012139653882Shell Side Feed Pressure psia 142.233374040576Shell Side Product Pressure psia 103.430798824034Shell Side Velocity ft / sec 6.32610674540682Shell Side Minimum Velocity ft / sec 0Shell Side Maximum Velocity ft / sec 999.999984908137Shell Side Fouling Required hr-ft2-F/BTU 0.0019999743160525Area per shell ft2 4400.78402419728Shell Inlet Nozzle rv2 lb / ft / sec 2 2251.65499257483Shell Side Prandtl number 5.066834597Shell Side Reynolds number 70539.67991Shell Side Feed Density lb / ft3 62.1448547715776Shell Side Feed Specific Gravity 0.9999999725Shell Side Product Density lb / ft3 62.0387534963036Shell Side Product Specific Gravity 0.9999999725Shell Side Feed Liquid Viscosity cP 0.7969852972Shell Side Product Liquid Viscosity cP 0.7126218371Shell Side Feed Liquid Therm. Cond BTU/hr-ft-F 0.356595141557946

BTU/hr-ft-F 0.360528998116413Shell Side Mixed Feed Temparature F 85.9999890200001Shell Side Mixed Feed Pressure psia 142.233374040576Shell Side Feed Total Mass Rate lb / day 95288197.0249916Shell Side Feed Total Enthalpy kW-hr / day 1508248.17192

Shell Side Mixed Feed Stream Phase WaterShell Side Mixed Feed Vapor Frac. fraction 0Shell Side Mixed Feed Vapor CP BTU/lb-F 0Shell Side Mixed Feed Liquid CP BTU/lb-F 0.997648407375561

F 95.7111728Shell Side Mixed Product Pressure psia 103.430798824034Shell Side Product Total Mass Rate lb / day 95288197.0249916Shell Side Product Total Enthalpy kW-hr / day 1778779.47792

Water

Shell Side Mixed Product Vapor Frac. fraction 0Shell Side Mixed Product Vapor CP BTU/lb-F 0Shell Side Mixed Product Liquid CP BTU/lb-F 0.997436043278877Tube Side Mixed Feed Temparature F 282.0936839Tube Side Mixed Feed Pressure psia 1137.86699232461Tube Side Feed Total Mass Rate lb / day 9839688.88043881Tube Side Feed Total Enthalpy kW-hr / day 403981.8972

Tube Side Mixed Feed Stream Phase VaporTube Side Mixed Feed Vapor Frac. fraction 1

Shell Side Product Liquid Therm. Cond

Shell Side Mixed Product Temparature

Shell Side Mixed Product Stream Phase

Tube Side Mixed Feed Vapor CP 2.135799125Tube Side Mixed Feed Liquid CP 0

F 95.24187932Tube Side Mixed Product Pressure psia 1136.01287209417Tube Side Product Total Mass Rate lb / day 9839688.88043881Tube Side Product Total Enthalpy kW-hr / day 133457.901216

Vapor

Tube Side Mixed Product Vapor Frac. fraction 1Tube Side Mixed Product Vapor CP 2.120516123Tube Side Mixed Product Liquid CP 0


2

1

2Orientation(Selected) HorizontalFlow Configuration(Selected) CountercurrentTEMA Type Front(Selected) ATEMA Type Shell(Selected) ETEMA Type Rear(Selected) STube Inside Diameter(User Input) ft 0.0486666659448819Tube Wall Thickness(User Input) ft 0.0069166665616798Tube Length(User Input) ft 15.0000000885827Tube Outside Diameter(User Input) ft 0.0624999990485564Tube Pitch(User Input) in 0.99999998503937Tube Pitch Pattern(Selected) Square - 90 degreesTube Sheet Thickness(User Input) in 8.66025390944882Baffle Type(Selected) SingleBaffle Geometry(Selected) CutBaffle Cut Fraction(User Input) 0.2Baffle Center Spacing(User Input) in 9.9999998503937Inlet Baffle Spacing(User Input) in 10.6698746968504Outlet Baffle Spacing(User Input) in 10.6698746968504Baffle Thickness in 0.249999996259843Number of Sealing Strips 0Number of Baffles 16Tubes in Baffle Windows Tubes In Window

1Two Phase HTC Method(Selected) Chen

Tube Side Mixed Product Temparature

Tube Side Mixed Product Stream Phase





Tube Side Coefficient(User Input) BTU/hr-ft2-F 261.517911648991Tube Side Scale Factor(User Input) 1

hr-ft2-F/BTU 0.001999999898359


ft 0

1

BBM

1



in 13.2499997992126

in 13.2499997992126

in 23.2499996496063

in 23.2499996496063

in 0Duty kW-hr / day 46677.848376LMTD F 18.41788089LMTD Correction factor (Ft) 0.6095626801MTD (Ft * LMTD) F 11.2268528424U Value with Fouling BTU/hr-ft2-F 65.9150544180788U Value without Fouling BTU/hr-ft2-F 94.3169524819223Required U-Value BTU/hr-ft2-F 65.8889073941665Exchanger Area ft2 8967.76229831114U*A BTU/hr-F 591110.539176194Tube Bundle Weight lb 21964.7971304609Empty Shell Weight lb 17831.3596403817Shell Weight with Water lb 50750.0821663521Number of Tubes per Shell 1600Tube Side product temperature F 63.39759908Tube Side pressure drop per shell psi 2.28333372590199Tube Side Feed Pressure psia 1136.01287209417Tube Side Product Pressure psia 1131.44619943261














Tube Side velocity ft / sec 18.2893028937008Tube Minimum Design Veloctiy ft / sec 0Tube Maximum Design Velocity ft / sec 999.999984908137Tube Side Fouling Factor 0.3522199821Tube Side design pressure psia 1199.9985265622Fin Efficiency 1Tube Side Reynolds number 414912.3294Tube Side Prandtl number 0.9015105224Tube Wall Resistance hr-ft2-F/BTU 0.0002607075145648Tube Side Feed Density lb / ft3 4.01475937058158Tube Side Feed Specific Gravity 0.3971428942Tube Side Product Density lb / ft3 4.35420639954012Tube Side Product Specific Gravity 0.3971428942Tube Side Feed Vapor Viscosity cP 0.01367717118Tube Side Product Vapor Viscosity cP 0.013035715Shell Side Product Temperature F 88.78108784Shell Side Pressure Drop per Shell psi 51.3217561307428Shell Side Feed Pressure psia 142.233377231405Shell Side Product Pressure psia 39.6052740486979Shell Side Velocity ft / sec 117.179436909449Shell Side Minimum Velocity ft / sec 0Shell Side Maximum Velocity ft / sec 999.999984908137Shell Side Fouling Required hr-ft2-F/BTU 0.0020060203003804Area per shell ft2 4485.66051042485Shell Inlet Nozzle rv2 lb / ft / sec 2 687.8629672675Shell Side Prandtl number 0.7554851991Shell Side Reynolds number 402441.988Shell Side Latent Heat kW-hr / lb 0Shell Side Feed Density lb / ft3 0.502680827886531Shell Side Feed Specific Gravity 0.3523651316Shell Side Product Density lb / ft3 0.120645746364996Shell Side Product Specific Gravity 0.3523651316Shell Side Feed Vapor Viscosity cP 0.0113789868Shell Side Product Vapor Viscosity cP 0.01265331314Shell Side Mixed Feed Temparature F 23.32548554Shell Side Mixed Feed Pressure psia 142.233377231405Shell Side Feed Total Mass Rate lb / day 4736774.77528704Shell Side Feed Total Enthalpy kW-hr / day 67808.209632

Shell Side Mixed Feed Stream Phase VaporShell Side Mixed Feed Vapor Frac. fraction 1Shell Side Mixed Feed Vapor CP BTU/lb-F 0.468610697191172Shell Side Mixed Feed Liquid CP BTU/lb-F 0


Vapor

Shell Side Mixed Product Vapor Frac. fraction 1Shell Side Mixed Product Vapor CP BTU/lb-F 0.470329798175217Shell Side Mixed Product Liquid CP BTU/lb-F 0



Tube Side Mixed Feed Temparature F 95.24187932Tube Side Mixed Feed Pressure psia 1136.01287209417Tube Side Feed Total Mass Rate lb / day 9839688.88043881Tube Side Feed Total Enthalpy kW-hr / day 133457.901216

Tube Side Mixed Feed Stream Phase VaporTube Side Mixed Feed Vapor Frac. fraction 1Tube Side Mixed Feed Vapor CP 2.120516123Tube Side Mixed Feed Liquid CP 0


Vapor



1

1

2Orientation(Selected) HorizontalFlow Configuration(Selected) CountercurrentTEMA Type Front(Selected) ATEMA Type Shell(Selected) ETEMA Type Rear(Selected) STube Inside Diameter(User Input) ft 0.0486666659448819Tube Wall Thickness(User Input) ft 0.0069166665616798Tube Length(User Input) ft 15.0000000885827Tube Outside Diameter(User Input) ft 0.0624999990485564Tube Pitch(User Input) in 0.99999998503937Tube Pitch Pattern(Selected) Square - 90 degreesTube Sheet Thickness(User Input) in 8.66025390944882Baffle Type(Selected) SingleBaffle Geometry(Selected) CutBaffle Cut Fraction(User Input) 0.2Baffle Center Spacing(User Input) in 9.9999998503937Inlet Baffle Spacing(User Input) in 10.6698746968504Outlet Baffle Spacing(User Input) in 10.6698746968504






Baffle Thickness in 0.249999996259843Number of Sealing Strips 0Number of Baffles 16Tubes in Baffle Windows Tubes In Window


hr-ft2-F/BTU 0.001999999898359


ft 0

1

BBM

1



in 13.2499997992126

in 13.2499997992126

in 21.2499996811024

in 21.2499996811024

in 0Duty kW-hr / day 13825.374564LMTD F 14.8282332498LMTD Correction factor (Ft) 0.5282509774MTD (Ft * LMTD) F 7.8330287088U Value with Fouling BTU/hr-ft2-F 55.9430621528426U Value without Fouling BTU/hr-ft2-F 75.1494105412574Required U-Value BTU/hr-ft2-F 55.94183277976Exchanger Area ft2 4485.56193771999U*A BTU/hr-F 250936.06981254Tube Bundle Weight lb 21964.7971304609















Empty Shell Weight lb 17831.3596403817Shell Weight with Water lb 50750.0821663521Number of Tubes per Shell 1600Tube Side product temperature F 54.0683088800001Tube Side pressure drop per shell psi 2.15192253682507Tube Side Feed Pressure psia 1131.44619943261Tube Side Product Pressure psia 1129.29427275206Tube Side velocity ft / sec 17.3554145374016Tube Minimum Design Veloctiy ft / sec 0Tube Maximum Design Velocity ft / sec 999.999984908137Tube Side Fouling Factor 0.3522199821Tube Side design pressure psia 1199.9985265622Fin Efficiency 1Tube Side Reynolds number 428307.9797Tube Side Prandtl number 0.926679991Tube Wall Resistance hr-ft2-F/BTU 0.0002607075145648Tube Side Feed Density lb / ft3 4.35420639954012Tube Side Feed Specific Gravity 0.3971428942Tube Side Product Density lb / ft3 4.46509027007288Tube Side Product Specific Gravity 0.3971428942Tube Side Feed Vapor Viscosity cP 0.013035715Tube Side Product Vapor Viscosity cP 0.01284494655Shell Side Product Temperature F 57.73142156Shell Side Pressure Drop per Shell psi 14.1433500861524Shell Side Feed Pressure psia 142.233377231405Shell Side Product Pressure psia 128.090132390395Shell Side Velocity ft / sec 48.8665904855643Shell Side Minimum Velocity ft / sec 0Shell Side Maximum Velocity ft / sec 999.999984908137Shell Side Fouling Required hr-ft2-F/BTU 0.0020003927193232Area per shell ft2 4485.66051042485Shell Inlet Nozzle rv2 lb / ft / sec 2 404.969195632374Shell Side Prandtl number 0.7698227795Shell Side Reynolds number 255485.7368Shell Side Latent Heat kW-hr / lb 0Shell Side Feed Density lb / ft3 0.542226964660727Shell Side Feed Specific Gravity 0.3995928194Shell Side Product Density lb / ft3 0.452792072551135Shell Side Product Specific Gravity 0.3995928194Shell Side Feed Vapor Viscosity cP 0.01224835746Shell Side Product Vapor Viscosity cP 0.01296346647Shell Side Mixed Feed Temparature F 23.32548554Shell Side Mixed Feed Pressure psia 142.233377231405Shell Side Feed Total Mass Rate lb / day 3153254.94058096Shell Side Feed Total Enthalpy kW-hr / day 32122.217376

Shell Side Mixed Feed Stream Phase VaporShell Side Mixed Feed Vapor Frac. fraction 1Shell Side Mixed Feed Vapor CP BTU/lb-F 0.423432499283462Shell Side Mixed Feed Liquid CP BTU/lb-F 0

F 57.73142156Shell Side Mixed Product Pressure psia 128.090132390395Shell Side Product Total Mass Rate lb / day 3153254.94058096


Shell Side Product Total Enthalpy kW-hr / day 45947.649672

Vapor

Shell Side Mixed Product Vapor Frac. fraction 1Shell Side Mixed Product Vapor CP BTU/lb-F 0.42568320316232Shell Side Mixed Product Liquid CP BTU/lb-F 0Tube Side Mixed Feed Temparature F 63.39759908Tube Side Mixed Feed Pressure psia 1131.44619943261Tube Side Feed Total Mass Rate lb / day 9839688.88043881Tube Side Feed Total Enthalpy kW-hr / day 86779.85796



Vapor



1

1

2Orientation(Selected) HorizontalFlow Configuration(Selected) CountercurrentTEMA Type Front(Selected) ATEMA Type Shell(Selected) ETEMA Type Rear(Selected) STube Inside Diameter(User Input) ft 0.0486666659448819Tube Wall Thickness(User Input) ft 0.0069166665616798Tube Length(User Input) ft 15.0000000885827Tube Outside Diameter(User Input) ft 0.0624999990485564Tube Pitch(User Input) in 0.99999998503937Tube Pitch Pattern(Selected) Square - 90 degrees







Tube Sheet Thickness(User Input) in 8.66025390944882Baffle Type(Selected) SingleBaffle Geometry(Selected) CutBaffle Cut Fraction(User Input) 0.2Baffle Center Spacing(User Input) in 9.9999998503937Inlet Baffle Spacing(User Input) in 10.6698746968504Outlet Baffle Spacing(User Input) in 10.6698746968504Baffle Thickness in 0.249999996259843Number of Sealing Strips 0Number of Baffles 16Tubes in Baffle Windows Tubes In Window


hr-ft2-F/BTU 0.000999999996593


ft 0

1

BBM

1



in 13.2499997992126

in 13.2499997992126

in 21.2499996811024

in 23.2499996496063

in 0Duty kW-hr / day 10210.8813816LMTD F 18.26876268LMTD Correction factor (Ft) 0.3918407077















MTD (Ft * LMTD) F 7.1584449012U Value with Fouling BTU/hr-ft2-F 45.2083827616206U Value without Fouling BTU/hr-ft2-F 50.4145468858418Required U-Value BTU/hr-ft2-F 45.2099521508349Exchanger Area ft2 4485.81622767833U*A BTU/hr-F 202796.496672208Tube Bundle Weight lb 21964.7971304609Empty Shell Weight lb 17831.3596403817Shell Weight with Water lb 50750.0821663521Number of Tubes per Shell 1600Tube Side product temperature F 47.20506188Tube Side pressure drop per shell psi 2.10192591040152Tube Side Feed Pressure psia 1129.29427275206Tube Side Product Pressure psia 1127.19234665166Tube Side velocity ft / sec 16.9795656660105Tube Minimum Design Veloctiy ft / sec 0Tube Maximum Design Velocity ft / sec 999.999984908137Tube Side Fouling Factor 0.1761099994Tube Side design pressure psia 1199.9985265622Fin Efficiency 1Tube Side Reynolds number 433875.5606Tube Side Prandtl number 0.9380773187Tube Wall Resistance hr-ft2-F/BTU 0.0002607075145648Tube Side Feed Density lb / ft3 4.46509027007288Tube Side Feed Specific Gravity 0.3971428942Tube Side Product Density lb / ft3 4.54942473639058Tube Side Product Specific Gravity 0.3971428942Tube Side Feed Vapor Viscosity cP 0.01284494655Tube Side Product Vapor Viscosity cP 0.01270375327Shell Side Product Temperature F 50.4018428Shell Side Pressure Drop per Shell psi 9.23954972181773Shell Side Feed Pressure psia 71.1166870202879Shell Side Product Pressure psia 61.8771394218218Shell Side Velocity ft / sec 48.9120603018373Shell Side Minimum Velocity ft / sec 0Shell Side Maximum Velocity ft / sec 999.999984908137Shell Side Fouling Required hr-ft2-F/BTU 0.0009992321509284Area per shell ft2 4485.66051042485Shell Inlet Nozzle rv2 lb / ft / sec 2 242.072254411718Shell Side Prandtl number 0.7573918658Shell Side Reynolds number 137981.5109Shell Side Feed Density lb / ft3 0.346782519868376Shell Side Feed Specific Gravity 0.5663957744Shell Side Product Density lb / ft3 0.267866266113648Shell Side Product Specific Gravity 0.5663957744Shell Side Feed Vapor Viscosity cP 0.01376534385Shell Side Product Vapor Viscosity cP 0.01508864191Shell Side Mixed Feed Temparature F -4.97283862Shell Side Mixed Feed Pressure psia 71.1166870202879Shell Side Feed Total Mass Rate lb / day 1949659.07123582Shell Side Feed Total Enthalpy kW-hr / day -2392.29585432

Shell Side Mixed Feed Stream Phase VaporShell Side Mixed Feed Vapor Frac. fraction 1

Shell Side Mixed Feed Vapor CP BTU/lb-F 0.319276576144072Shell Side Mixed Feed Liquid CP BTU/lb-F 0


Vapor

Shell Side Mixed Product Vapor Frac. fraction 1Shell Side Mixed Product Vapor CP BTU/lb-F 0.320963914684246Shell Side Mixed Product Liquid CP BTU/lb-F 0Tube Side Mixed Feed Temparature F 54.0683088800001Tube Side Mixed Feed Pressure psia 1129.29427275206Tube Side Feed Total Mass Rate lb / day 9839688.88043881Tube Side Feed Total Enthalpy kW-hr / day 72954.42576



Vapor


Mixer (Detailed) UOM M1Name M1Description M1Thermodynamic System PR01Feed Streams S2 , S14Product Streams S3Product Stream Phases S3 VaporPressure Drop(User Input) psi N/APressure(User Input) psia N/ATemperature F 282.00620408Pressure psia 1137.86699232461Pressure Drop psi 0Mole Frac. Vapor fraction 1Mole Frac. Free Water fraction 0Mole Frac. Liquid fraction 0Mole Frac Solids fraction 0Product Tolal Molar Rate lb-mol / day 511429.097437345Feed Total Mass Rate lb / day 9839690.30332105Feed Total Enthalpy kW-hr / day 403853.37816





Product Total Mass Rate lb / day 9839690.30332105Product Total Enthalpy kW-hr / day 403853.37816

MembraneSep (Detailed) UOM MEM1Name MEM1Description MEM1Thermodynamic System PR01Feed Stream(s) S8Product Stream(s) S9 , S11Pressure Above Membrane psia 640.050223067953Permeate Side Pressure psia 142.233377231405Membrane Area ft2 231424.173600422Operating Temperature F 23.32548554

METHANE 1.461742043 N2 0 H2O 0 AIR 4.830103874

Valve (Detailed) UOM V1Name V1Description V1Thermodynamic System PR01Feed Streams S15Product Streams S16Product Stream Phases S8 N/A S16 VaporPressure Drop(User Input) psi N/APressure(User Input) psia 71.1166870202879Temperature F -4.97283862Pressure psia 71.1166870202879Pressure Drop psi 568.933510521033Mole Frac Vapor fraction 1Mole Frac Liquid fraction 0Mole Frac Free Water fraction 0Mole Frac Solids fraction 0Tolal Molar Rate lb-mol / day 82700.6808705621Feed Total Mass Rate lb / day 1949659.07123582Feed Total Enthalpy kW-hr / day -2392.29585384Product Total Mass Rate lb / day 1949659.07123582Product Total Enthalpy kW-hr / day -2392.29585432

Stream (Detailed) UOM S1Name S1Description S1Phase VaporThermodynamic System PR01Total Molar Rate lb-mol / day 348153.477796787Total Mass Rate lb / day 6686435.36274008Total Std. Liq. Rate ft3 / day 270738.470306566Total Std. Vap. Rate ft3 / day 124999890.406083Temperature F 71.59998902

Permeation Constant in Input units [Volume/[Area*Time*Pressure]

Pressure psia 640.050223067953Total Molecular Weight 19.20542459Total Enthalpy kW-hr / day 88362.1278Total Specific Enthalpy kW-hr / lb 0.0132151322767733Vapor Mole Fraction fraction 1Total Liquid Mole Fraction fraction 0Liquid Mole Fraction fraction 0Water Mole Fraction fraction 0

1.700574142

Total Reduced Pressure (Kay's Rule) 1.030537511Total Acentric Factor 0.01846289149Total UOP K factor 14.47057477Total Std. Liq. Density lb / ft3 24.697027193906Total Std. Liq. Specific Gravity 0.3959978105Total Std. API 225.825208Total Molar Component Rates lb-mol / day METHANE 256171.330393834 N2 91982.1473267606 H2O 0 AIR 0Total Molar Component Fractions fraction METHANE 0.7358000043 N2 0.2641999957 H2O 0 AIR 0Vapor Molar Rate lb-mol / day 348153.477796787Vapor Mass Rate lb / day 6686435.36274008Vapor Act. Vol. Rate ft3 / day 2895183.51349477Vapor Std. Vol. Rate ft3 / day 124999889.216122Vapor Specific Gravity 0.6630791533Vapor Molecular Weight 19.20542459Vapor Specific Enthalpy kW-hr / lb 0.0132151322767733Vapor CP BTU/lb-F 0.472471246536735Vapor Z (from density) 0.9335583878Vapor Act. Density lb / ft3 2.30950312200748Vapor Std. Density lb / ft3 0.0534915303192097Vapor Composition fraction METHANE 0.7358000043 N2 0.2641999957 H2O 0 AIR 0Vapor Component Rate lb-mol / day METHANE 256171.330393834 N2 91982.1473267606 H2O 0 AIR 0Liquid Molar Rate lb-mol / day N/ALiquid Mass Rate lb / day N/ALiquid Vol. Rate ft3 / day N/ALiquid Std Vol. Rate ft3 / day N/ALiquid Std. Specific Gravity N/ALiquid Molecular Weight N/A

Total Reduced Temperature (Kay's Rule)

Liquid Specific Enthalpy kW-hr / lb N/ALiquid CP BTU/lb-F N/ALiquid Std. Density lb / ft3 N/ALiquid Act. Density lb / ft3 N/ALiquid Z (from density) N/ALiquid Composition fraction METHANE N/A N2 N/A H2O N/A AIR N/ALiquid Component Rate lb-mol / day METHANE N/A N2 N/A H2O N/A AIR N/AFree Water Mole Rate lb-mol / day N/AWater Mole Fraction fraction N/A

C2C2C2

PR01S13S14

VaporN/A

493.620512361137.866992324611009.77685996322

8.88333059875

79.65424424117398.319652231

124683.65902231156531.092880577

5811.0766286171.6922277748.1021711.3180319171.411580382

N/AN/AN/A

57.73142156128.090132390395

45947.6496720.0006802748731052

10

0.00240933313610270.0017786096864692

1.3546159996964024.17541468

401.006981661137.86699232461

185413.4887440.0006802748730352

10

493.620512361137.86699232461

231902.100960.0006965381651396

10

0.00314062870354610.0024707214205978

1.271138331

3153254.9405809645947.649672

3153254.94058096231902.10096

MEM2MEM2MEM2PR01

S11S12 , S15

640.050197541321142.233377231405172222.640818919

23.32548554

1.46169996300

4.83010006

V2V2V2

PR01S7S8

VaporN/AN/A

640.05022306795323.32548482

640.050223067953487.140780679821

1000

511428.959720639839688.88043881

63051.0542889839688.88043881

63051.054312

S10 S11 S12 S13S10 S11 S12 S13S10 S11 S12 S13

Vapor Vapor Vapor VaporPR01 PR01 PR01 PR01

265452.657895201 245976.317825711 163275.619773894 163275.6197738944736774.77528704 5102914.34134641 3153254.94058096 3153254.94058096215544.980697181 181722.202429786 126528.836393249 126528.83639324995307257.4989494 88314535.8086514 58621946.5944365 58621946.5944365

88.78108784 23.32548554 23.32548554 57.73142156

39.6052740486979 640.050197541321 142.233377231405 128.09013239039517.84414145 20.74555138 19.31246652 19.31246652

114486.25296 17533.9863768 32122.217232 45947.6496720.0241696636175549 0.0034360730373958 0.010187002905977 0.0145714985183482

1 1 1 10 0 0 00 0 0 00 0 0 0

1.684530173 1.623511129 1.551193308 1.661691768

0.06180025414 1.069048345 0.2295831356 0.20675410230.01548647728 0.02183034318 0.01869693618 0.01869693618

16.42668545 12.56699051 14.32845426 14.3284542621.9758064467699 28.0808523824774 24.9212355851585 24.9212355851585

0.3523651316 0.4502548413 0.3995928194 0.3995928194270.0720834 182.7664709 222.6104673 222.6104673

225506.741953121 149342.588498563 118678.200728055 118678.20072805539945.9116943861 96633.7207746168 44597.4276745622 44597.4276745622

0 0 0 00 0 0 0

0.8495177396 0.6071421419 0.726858063 0.7268580630.1504822442 0.3928578231 0.2731419898 0.2731419898

0 0 0 00 0 0 0

265452.657895201 245976.317825711 163275.619773894 163275.6197738944736774.77528704 5102914.34134641 3153254.94058096 3153254.9405809639261846.5100347 1832031.01188054 5815378.329012 6964024.1754146895307256.6141068 88314534.9848324 58621946.0452239 58621946.0452239

0.6160800112 0.7162529823 0.6667748417 0.666774841717.84414145 20.74555138 19.31246652 19.31246652

0.0241696636175549 0.0034360730373958 0.010187002905977 0.01457149851834820.470329798175217 0.430371348285087 0.423406016050444 0.42568320316232

0.9952590138 0.9197035138 0.9773552267 0.98393031750.120645746364996 2.78538644099844 0.542226964660727 0.452792072551135

0.0497000432538053 0.0577811380889327 0.0537896667191513 0.0537896667191513

0.8495177534 0.6071421632 0.7268580246 0.72685802460.1504822466 0.3928578368 0.2731419754 0.2731419754

0 0 0 00 0 0 0

225506.745572232 149342.593717702 118678.194461278 118678.19446127839945.9123420166 96633.7241461049 44597.4253126158 44597.4253126158

0 0 0 00 0 0 0

N/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/A

N/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/A

N/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/A


S14 S15 S16 S17S14 S15 S16 S17S14 S15 S16 S17


163275.619773894 82700.6808705621 82700.6808705621 82700.68087056213153254.94058096 1949659.07123582 1949659.07123582 1949659.07123582126528.836393249 55193.3525808263 55193.3525808263 55193.352580826358621946.5944365 29692583.0325212 29692583.0325212 29692583.0325212

493.62051236 23.32548554 -4.97283862 50.4018428

1137.86699232461 640.050197541321 71.1166870202879 61.877139421821819.31246652 23.57488537 23.57488537 23.57488537

231902.10096 -2392.29581832 -2392.29585432 7818.6281760.0735437208155371 -0.001227032896528 -0.00122703291505 0.004010254043048

1 1 1 10 0 0 00 0 0 00 0 0 0

3.06159769 1.78809293 1.683329976 1.88833205

1.836665044 1.147849444 0.1275388242 0.11096885890.01869693618 0.0280166167 0.0280166167 0.0280166167

14.32845426 9.71811041 9.71811041 9.7181104124.9212355851585 35.3241646010884 35.3241646010884 35.3241646010884

0.3995928194 0.5663957744 0.5663957744 0.5663957744222.6104673 118.3253102 118.3253102 118.3253102

118678.200728055 30664.3856180885 30664.3856180885 30664.385618088544597.4276745622 52036.2931000547 52036.2931000547 52036.2931000547

0 0 0 00 0 0 0

0.726858063 0.3707875836 0.3707875836 0.37078758360.2731419898 0.6292123903 0.6292123903 0.6292123903

0 0 0 00 0 0 0

163275.619773894 82700.6808705621 82700.6808705621 82700.68087056213153254.94058096 1949659.07123582 1949659.07123582 1949659.071235821482056.14523059 631762.457195526 5622137.68032518 7278479.2956856258621946.0452239 29692582.7518125 29692582.7518125 29692582.7518125

0.6667748417 0.813937487 0.813937487 0.81393748719.31246652 23.57488537 23.57488537 23.57488537

0.0735437208155371 -0.001227032896528 -0.00122703291505 0.0040102540430480.554889179325499 0.35632178346231 0.319276576144072 0.320963914684246

1.009594325 0.943306984 0.9907840853 0.99487335672.12762178398258 3.08606351909412 0.346782519868376 0.267866266113648

0.0537896667191513 0.0656614848240075 0.0656614848240075 0.0656614848240075

0.7268580246 0.3707875933 0.3707875933 0.37078759330.2731419754 0.6292124067 0.6292124067 0.6292124067

0 0 0 00 0 0 0

118678.194461278 30664.3864181026 30664.3864181026 30664.386418102644597.4253126158 52036.2944524595 52036.2944524595 52036.2944524595

0 0 0 00 0 0 0


S18 S19 S2 S3S18 S19 S2 S3S18 S19 S2 S3

Water Water Vapor VaporPR01 PR01 PR01 PR01

5289298.76378772 5289298.76378772 348153.477796787 511429.09743734595288197.0249916 95288197.0249916 6686435.36274008 9839690.303321051527872.89488892 1527872.89488892 270738.470306566 397267.3067913511899052596.62181 1899052596.62181 124999890.406083 183621837.00051985.9999890200001 95.7111728 177.29708432 282.00620408

142.233374040576 103.430798824034 1137.86699232461 1137.8669923246118.01527977 18.01527977 19.20542459 19.23959812

1508248.17192 1778779.47792 171951.27708 403853.378160.015828279039516 0.0186673641983842 0.025716434500564 0.0410433017294778

0 0 1 11 1 0 00 0 0 01 1 0 0

0.4684530027 0.4767899706 2.038906348 2.376592138

0.04446451952 0.03233418883 1.832066573 1.8335321480.3448610008 0.3448610008 0.01846289149 0.01853761112

8.757604226 8.757604226 14.47057477 14.4250304362.366573391694 62.366573391694 24.697027193906 24.7684371140596

0.9999999725 0.9999999725 0.3959978105 0.397142813710.00000389 10.00000389 225.825208 224.795003

0 0 256171.330393834 374849.5311028410 0 91982.1473267606 136579.575001323

5289298.76378772 5289298.76378772 0 00 0 0 0

0 0 0.7358000043 0.73294525660 0 0.2641999957 0.26705476021 1 0 00 0 0 0

N/A N/A 348153.477796787 511429.097437345N/A N/A 6686435.36274008 9839690.30332105N/A N/A 1997342.85087986 3520961.17866009N/A N/A 124999889.216122 183621835.261346N/A N/A 0.6630791533 0.6642590154N/A N/A 19.20542459 19.23959812N/A N/A 0.025716434500564 0.0410433017294778N/A N/A 0.500260244578198 0.510112061001242N/A N/A 0.9549788363 0.9842157571N/A N/A 3.34766530472828 2.79460346422049N/A N/A 0.0534915303192097 0.0535867114663465

N/A N/A 0.7358000043 0.7329452443N/A N/A 0.2641999957 0.2670547557N/A N/A 0 0N/A N/A 0 0

N/A N/A 256171.330393834 374849.524817016N/A N/A 91982.1473267606 136579.57269652N/A N/A 0 0N/A N/A 0 0N/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/AN/A N/A N/A N/A




5289298.76378772 5289298.76378772 N/A N/A1 1 N/A N/A

S4 S5 S6 S7S4 S5 S6 S7S4 S5 S6 S7


511428.95972063 511428.95972063 511428.95972063 511428.959720639839688.88043881 9839688.88043881 9839688.88043881 9839688.88043881397267.168572831 397267.168572831 397267.168572831 397267.168572831183621787.510356 183621787.510356 183621787.510356 183621787.510356

95.24187932 63.39759908 54.0683088800001 47.20506188

1136.01287209417 1131.44619943261 1129.29427275206 1127.1923466516619.23960052 19.23960052 19.23960052 19.23960052

133457.901216 86779.85796 72954.42576 62743.5018720.0135632236788869 0.0088193701069103 0.0074143020828886 0.0063765737546783

1 1 1 10 0 0 00 0 0 00 0 0 0

1.778133504 1.676093191 1.646198853 1.624206588

1.830544565 1.823185935 1.819718371 1.8163313760.01853761637 0.01853761637 0.01853761637 0.01853761637

14.42502724 14.42502724 14.42502724 14.4250272424.768442139524 24.768442139524 24.768442139524 24.768442139524

0.3971428942 0.3971428942 0.3971428942 0.3971428942224.7949308 224.7949308 224.7949308 224.7949308

374849.32443253 374849.32443253 374849.32443253 374849.32443253136579.63957389 136579.63957389 136579.63957389 136579.63957389

0 0 0 00 0 0 0

0.73294505 0.73294505 0.73294505 0.732945050.2670549584 0.2670549584 0.2670549584 0.2670549584

0 0 0 00 0 0 0

511428.95972063 511428.95972063 511428.95972063 511428.959720639839688.88043881 9839688.88043881 9839688.88043881 9839688.880438812450878.86272297 2259812.23146884 2203693.15849122 2162842.43609152183621785.771183 183621785.771183 183621785.771183 183621785.771183

0.6642590983 0.6642590983 0.6642590983 0.664259098319.23960052 19.23960052 19.23960052 19.23960052

0.0135632236788869 0.0088193701069103 0.0074143020828886 0.00637657375467830.506476574710996 0.516799133944779 0.521021730677367 0.524528383490972

0.9141829489 0.8906364894 0.8826089709 0.87634281224.01475937058158 4.35420639954012 4.46509027007288 4.54942473639058

0.0535867181461563 0.0535867181461563 0.0535867181461563 0.0535867181461563

0.7329450438 0.7329450438 0.7329450438 0.73294504380.2670549562 0.2670549562 0.2670549562 0.2670549562

0 0 0 00 0 0 0

374849.321194377 374849.321194377 374849.321194377 374849.321194377136579.638431013 136579.638431013 136579.638431013 136579.638431013

0 0 0 00 0 0 0


S8 S9S8 S9S8 S9

Vapor VaporPR01 PR01

511428.95972063 265452.6578952019839688.88043881 4736774.77528704397267.168572831 215544.980697181183621787.510356 95307257.4989494

23.32548482 23.32548554

640.050223067953 142.23337723140519.23960052 17.84414145

63051.054312 67808.2108080.0064078300725507 0.0143152702060458

1 10 00 00 0

1.547687995 1.483487748

1.031361955 0.22194162450.01853761637 0.01548647728

14.42502724 16.4266854524.768442139524 21.9758064467699

0.3971428942 0.3523651316224.7949308 270.0720834

374849.32443253 225506.741953121136579.63957389 39945.9116943861

0 00 0

0.73294505 0.84951773960.2670549584 0.1504822442

0 00 0

511428.95972063 265452.6578952019839688.88043881 4736774.775287043749206.35397236 9423026.52925991183621785.771183 95307256.6141068

0.6642590983 0.616080011219.23960052 17.84414145

0.0064078300725507 0.01431527020604580.480057588372982 0.468575362806917

0.9052371465 0.97409012922.6244724747867 0.502680827886531

0.0535867181461563 0.0497000432538053

0.7329450438 0.84951775340.2670549562 0.1504822466

0 00 0

374849.321194377 225506.745572232136579.638431013 39945.9123420166

0 00 0

N/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/A

N/A N/AN/A N/AN/A N/AN/A N/AN/A N/A

N/A N/AN/A N/AN/A N/AN/A N/A

N/A N/AN/A N/AN/A N/AN/A N/AN/A N/AN/A N/A

caso37f2012-detailed report.xls

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