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LEGENDSBurlington, MAUSA
Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Air cooler: AC-100
CONNECTIONS
Inlet Stream
STREAM NAME FROM UNIT OPERATION19 K-103Compressor
Outlet Stream
STREAM NAME TO UNIT OPERATION20 VLV-103Valve
DESIGN PARAMETERS
Pressure Drop: 2.000 psi * UA: -2.313e+006 Btu/F-hrInlet Air Temp: 77.00 F Outlet Air Temp: 214.6 FConfiguration: one tube row, one pass
User Variables
SIZING
Number of Fans 2 *FanSpeed (rpm)Speed (rpm)Max Acceleration (rpm)Design Speed (rpm)Design airflow (ACFM)Current airflow (ACFM)
Fan 060.0060.00
---
60.002.119e+0052.119e+005
Fan 160.0060.00
---
60.002.119e+0052.119e+005
NOZZLE PARAMETERS
Base Elevation Relative to Ground Level 0.0000 ft *
Diameter (ft)Elevation (Base) (ft)Elevation (Ground) (ft)
190.16400.00000.0000
200.16400.00000.0000
CONDITIONS
NameVapourTemperature (F)Pressure (psia)Molar Flow (lbmole/hr)Mass Flow (lb/hr)Std Ideal Liq Vol Flow (barrel/day)Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)Heat Flow (Btu/hr)
191.0000
240.2986131.0313
5261.210389598.4149
9958.3764-1.837e+004
38.59-9.6625e+07
200.0000 *
70.6000 *129.0313
5261.210389598.4149
9958.3764-2.888e+004
19.18-1.5197e+08
PROPERTIES
NameMolecular WeightMolar DensityMass DensityAct. Volume FlowMass Enthalpy
(lbmole/ft3)(lb/ft3)
(barrel/day)(Btu/lb)
1917.03
1.808e-0020.3079
1.244e+006-1078
2017.032.21237.67
1.017e+004-1696
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LEGENDSBurlington, MAUSA
Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Air cooler: AC-100 (continued)PROPERTIES
NameMass EntropyHeat CapacityMass Heat CapacityLHV Molar Basis (Std)HHV Molar Basis (Std)HHV Mass Basis (Std)CO2 LoadingCO2 Apparent Mole Conc.CO2 Apparent Wt. Conc.LHV Mass Basis (Std)Phase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Phase Fraction [Act. Vol. Basis]Mass ExergyPartial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole)(Btu/lbmole)
(Btu/lb)
(lbmole/ft3)(lbmol/lb)
(Btu/lb)
(Btu/lb)(psia)
(Cost/s)(ACFM)
(lbmole/ft3)(Btu/lbmole-F)
(MMSCFD)(lb/ft3)
(USGPM)
(psia)
(Btu/lbmole)(cSt)
(lb/ft3)(barrel/day)
(ft3/lbmole)(Btu/lb)
(dyne/cm)(Btu/hr-ft-F)
(cP)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)
(psia)(psia)
(barrel/day)
192.2669.453
0.55511.362e+0051.627e+005
9551---
---
---
79981.0001.0001.000144.0
0.00000.0000
48502.2589.45347.9238.46
---
0.964812.24
---
0.00001.2661.32189282.29738.22
1.002e+0040.0000
55.31524.3
1.0000---
2.245e-0021.133e-002
7.4670.4385
7.1560.4202
---
---
---
210.5210.5
1.002e+004-29.10
201.12620.201.186
1.362e+0051.627e+005
9551---
---
---
7998---
0.00000.0000
138.10.00000.0000
---
2.25820.2047.9238.46296.5
---
12.24---
0.00001.1091.1098942
0.216338.22
1.002e+0041.000
0.4521525.1
0.000026.87
0.28160.1305
18.211.06918.211.069
---
---
---
210.5210.5
1.002e+004-48.94
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LEGENDSBurlington, MAUSA
Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Air cooler: AC-100 (continued)PERFORMANCE RESULTS
Working Fluid Duty: -5.534e+007 Btu/hr Correction Factor: 0.1000UA: -2.313e+006 Btu/F-hr LMTD: -239.3 F *Feed Temp: 240.3 F Prod Temp: 70.60 F *Air Feed Temp: 77.00 F Air Prod Temp: 214.6 FVolumetric Air Flow: 4.238e+005 ACFM * Mass Air Flow: 1.659e+006 lb/hr *
PERFORMANCE TABLE
Overall Phase
Temperature (F)
240.30127.67
71.3071.2171.1371.0470.9570.8670.7870.6970.60
Pressure (psia)
131.03130.83130.63130.43130.23130.03129.83129.63129.43129.23129.03
Heat Flow (Btu/hr)
0.00-5534082.39
-11068164.78-16602247.17-22136329.57-27670411.96-33204494.35-38738576.74-44272659.13-49806741.52-55340823.91
Enthalpy (Btu/lbmole)
-18365.43-19417.29-20469.14-21521.00-22572.85-23624.70-24676.56-25728.41-26780.27-27832.12-28883.98
Vapour Fraction
1.00001.00000.94060.82290.70530.58760.47000.35250.23490.11750.0000
Vap Phase Mass Frac
1.00001.00000.94060.82290.70530.58760.47000.35250.23490.11750.0000
Heat of Vap (Btu/lbmole)
---
---
---
---
---
---
---
---
---
---
---
Vapour Phase
Mass Flow (lb/hr)
89598.4189598.4184279.2773733.7363190.0652650.6942114.4331581.0721050.0710523.96
---
Molecular Wt
17.0317.0317.0317.0317.0317.0317.0317.0317.0317.03
---
Density (lb/ft3)
0.310.380.430.420.420.420.420.420.420.42
---
Mass Sp Heat (Btu/lb-F)
0.560.540.540.540.540.540.540.540.540.54
---
Viscosity (cP)
0.010.010.010.010.010.010.010.010.010.01
---
Thermal Cond (Btu/hr-ft-F)
0.020.020.020.020.020.020.020.020.020.02
---
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LEGENDSBurlington, MAUSA
Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Air cooler: AC-100 (continued)PERFORMANCE TABLE
Vapour Phase
Std Gas Flow (MMSCFD)
47.8247.8244.9939.3633.7328.1022.4816.8611.24
5.62---
Z Factor
0.960.940.920.920.920.920.920.920.920.92
---
Pseudo Pc (psia)
1635.581635.581635.581635.581635.581635.581635.581635.581635.581635.58
---
Pseudo Tc (F)
270.32270.32270.32270.32270.32270.32270.32270.32270.32270.32
---
Pseudo Zc
0.270.270.270.270.270.270.270.270.270.27
---
Pseudo Omega
0.250.250.250.250.250.250.250.250.250.25
---
Light Liquid Phase
Mass Flow (lb/hr)
---
---
5319.1515864.6826408.3636947.7347483.9858017.3568548.3579074.4589598.41
Density (lb/ft3)
---
---
37.6437.6437.6437.6537.6537.6637.6637.6737.67
Mass Sp Heat (Btu/lb-F)
---
---
1.191.191.191.191.191.191.191.191.19
Viscosity (cP)
---
---
0.130.130.130.130.130.130.130.130.13
Thermal Cond (Btu/hr-ft-F)
---
---
0.280.280.280.280.280.280.280.280.28
Surface Tens (dyne/cm)
---
---
26.7826.7926.8126.8226.8326.8426.8526.8626.87
Molecular Wt
---
---
17.0317.0317.0317.0317.0317.0317.0317.0317.03
Sp Gravity
---
---
0.600.600.600.600.600.600.600.600.60
Pseudo Pc (psia)
---
---
1635.581635.581635.581635.581635.581635.581635.581635.581635.58
Pseudo Tc (F)
---
---
270.32270.32270.32270.32270.32270.32270.32270.32270.32
Pseudo Zc
---
---
0.270.270.270.270.270.270.270.270.27
Pseudo Omega
---
---
0.250.250.250.250.250.250.250.250.25
Heavy Liquid Phase
Mass Flow (lb/hr)
---
---
---
---
---
Density (lb/ft3)
---
---
---
---
---
Mass Sp Heat (Btu/lb-F)
---
---
---
---
---
Viscosity (cP)
---
---
---
---
---
Thermal Cond (Btu/hr-ft-F)
---
---
---
---
---
Surface Tens (dyne/cm)
---
---
---
---
---
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LEGENDSBurlington, MAUSA
Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Air cooler: AC-100 (continued)PERFORMANCE TABLE
Heavy Liquid Phase
Mass Flow (lb/hr)
---
---
---
---
---
---
Density (lb/ft3)
---
---
---
---
---
---
Mass Sp Heat (Btu/lb-F)
---
---
---
---
---
---
Viscosity (cP)
---
---
---
---
---
---
Thermal Cond (Btu/hr-ft-F)
---
---
---
---
---
---
Surface Tens (dyne/cm)
---
---
---
---
---
---
Molecular Wt
---
---
---
---
---
---
---
---
---
---
---
Sp Gravity
---
---
---
---
---
---
---
---
---
---
---
Pseudo Pc (psia)
---
---
---
---
---
---
---
---
---
---
---
Pseudo Tc (F)
---
---
---
---
---
---
---
---
---
---
---
Pseudo Zc
---
---
---
---
---
---
---
---
---
---
---
Pseudo Omega
---
---
---
---
---
---
---
---
---
---
---
Mixed Liquid Phase
Mass Flow (lb/hr)
---
---
5319.1515864.6826408.3636947.7347483.9858017.3568548.3579074.4589598.41
Density (lb/ft3)
---
---
37.6437.6437.6437.6537.6537.6637.6637.6737.67
Mass Sp Heat (Btu/lb-F)
---
---
1.191.191.191.191.191.191.191.191.19
Viscosity (cP)
---
---
0.130.130.130.130.130.130.130.130.13
Thermal Cond (Btu/hr-ft-F)
---
---
0.280.280.280.280.280.280.280.280.28
Surface Tens (dyne/cm)
---
---
26.7826.7926.8126.8226.8326.8426.8526.8626.87
Molecular Wt
---
---
17.0317.0317.0317.0317.0317.0317.0317.0317.03
Sp Gravity
---
---
0.600.600.600.600.600.600.600.600.60
Pseudo Pc (psia)
---
---
1635.581635.581635.581635.581635.581635.581635.581635.581635.58
Pseudo Tc (F)
---
---
270.32270.32270.32270.32270.32270.32270.32270.32270.32
Pseudo Zc
---
---
0.270.270.270.270.270.270.270.270.27
Pseudo Omega
---
---
0.250.250.250.250.250.250.250.250.25
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LEGENDSBurlington, MAUSA
Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Air cooler: AC-100 (continued)DYNAMICS
Models
UA (Btu/F-hr)Reference Air Flow (lb/hr)
-2.313e+006---
Reference Fluid Flow (lb/hr)Minimum Flow Scale Factor
---
0.0000 *
Dynamic Specifications
Delta P: 2.000 psi * Overall k: ---
Spec Zones
Zone
0 *
Pressure (psia)129.0 *
Pressure Drop
2.000 *
Spec
Not Active
Zone
0 *
Flow (lbmole/hr)
5261 *
k
---
Spec
Not Active
Dynamic Parameters
Number of ZonesFluid Volume (ft3)
1 *3.531
Mass Flow (lb/hr)Exit Temperature (F)
8.960e+00470.60 *
Holdup Details
Phase
VapourLiquid
Aqueous
Accumulation (lbmole/hr)
0.00000.00000.0000
Moles (lbmole)0.00000.00000.0000
Volume (ft3)
0.00000.00000.0000
Total 0.0000 0.0000 0.0000
Individual Zone Holdup: Zone 0
NOTES
Simulation Case: Case
STATUS MESSAGES
Tag: Main Minimum Severity: ---
Object StatusSeverity Source Messages
Calculation Levels
Name1234567
ActiveYesYesYesYesYesYesYes
Calculation Level500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *
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LEGENDSBurlington, MAUSA
Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Simulation Case: Case (continued)Name
89101112131415161718192021222324
FeederBlock_1ProductBlock_3ProductBlock_4
LNG-100 (GAS -METANO)LNG-102 (ETILENO-PROPANO)LNG-101 (METANO-ETILENO)
LNG-103V-100V-101K-100K-101K-102K-103K-104
VLV-100VLV-101VLV-102VLV-103
q100q101q102q103q104
AC-100MIX-100
ActiveYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYesYes
Calculation Level500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *500.0 *
Exported Connections, Exported Variables and Initial Input Expert Only Available in Template View
OVERALL MASS BALANCE
In Stream Count Mass Flow Out Stream Count Mass Flow
Total In MassFlow Total Out MassFlowMass Imbalance Rel Mass Imbalance Pct
OVERALL ENERGY BALANCE
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Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Simulation Case: Case (continued)InStream Count Energy Flow OutStream Count Energy Flow
Total In EnergyFlow Total Out EnergyFlowEnergy Imbalance Rel Energy Imbalance Pct
OVERALL UTILITY BALANCE
Utility Name Usage Info Energy Flow Mass Flow Cost
Hot Utility Summary
Utility FlowUtility CostCarbon Emiss.Carbon Fees
Cold Utility Summary
Utility FlowUtility CostCarbon Emiss.Carbon Fees
PROCESS CO2 EMISSIONS
Inlet Stream Count IFPP (1995) IFPP (2007) EPA (2009)
Total from InletsTotal Carbon Feesfrom Inlets (Cost/hr)
Outlet Stream Count IFPP (1995) IFPP (2007) EPA (2009)
Total from OutletsTotal Carbon Feesfrom Outlets (Cost/hr)
User Variables
Workbook: Case (Main)Material Streams Fluid Pkg: All
NameVapour FractionTemperaturePressureMolar FlowMass FlowLiquid Volume FlowHeat Flow
(F)(psia)
(lbmole/hr)(lb/hr)
(barrel/day)(Btu/hr)
11.0000
100.0 *60.00 *2196 *
3.646e+0048201
-7.080e+007
20.1000 *-222.358.002196
3.646e+0048201
-8.351e+007
31.0000-222.358.00219.63524805.9
-7.627e+006
40.0000-222.358.001976
3.294e+0047395
-7.589e+007
51.0000 *-223.458.00 *7036
1.129e+0052.581e+004
-2.444e+008NameVapour FractionTemperaturePressureMolar FlowMass FlowLiquid Volume FlowHeat Flow
(F)(psia)
(lbmole/hr)(lb/hr)
(barrel/day)(Btu/hr)
60.4407-222.360.007036
1.129e+0052.581e+004
-2.571e+008
71.0000-13.83431.07036
1.129e+0052.581e+004
-2.342e+008
80.0000 *-142.0 *429.07036
1.129e+0052.581e+004
-2.571e+008
90.3290-142.322.006105
1.713e+0053.060e+0041.012e+008
101.0000 *-145.520.00 *6105
1.713e+0053.060e+0041.241e+008
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Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Workbook: Case (Main) (continued)Material Streams (continued) Fluid Pkg: All
NameVapour FractionTemperaturePressureMolar FlowMass FlowLiquid Volume FlowHeat Flow
(F)(psia)
(lbmole/hr)(lb/hr)
(barrel/day)(Btu/hr)
111.0000
132.3221.66105
1.713e+0053.060e+0041.393e+008
120.0000 *-37.50 *219.66105
1.713e+0053.060e+0041.012e+008
130.1316-37.8617.005549
2.447e+0053.307e+004
-2.972e+008
141.0000 *-43.1015.00 *4818
2.125e+0052.871e+004
-2.250e+008
151.0000-38.2116.00 *4818
2.125e+0052.871e+004
-2.247e+008NameVapour FractionTemperaturePressureMolar FlowMass FlowLiquid Volume FlowHeat Flow
(F)(psia)
(lbmole/hr)(lb/hr)
(barrel/day)(Btu/hr)
160.0000 *
5.500 *42.625549
2.447e+0053.307e+004
-2.972e+008
170.1288
5.26034.005261
8.960e+0049958
-1.520e+008
181.0000 *
2.71032.00 *5261
8.960e+0049958
-1.070e+008
191.0000
240.3131.05261
8.960e+0049958
-9.663e+007
200.0000 *
70.60 *129.05261
8.960e+0049958
-1.520e+008NameVapour FractionTemperaturePressureMolar FlowMass FlowLiquid Volume FlowHeat Flow
(F)(psia)
(lbmole/hr)(lb/hr)
(barrel/day)(Btu/hr)
211.0000-37.8617.00730.3
3.220e+0044352
-3.406e+007
221.0000
40.7844.625549
2.447e+0053.307e+004
-2.523e+008
231.0000-38.2016.005549
2.447e+0053.307e+004
-2.587e+008
240.0000-37.8617.004818
2.125e+0052.871e+004
-2.631e+008
Compositions Fluid Pkg: AllNameComp Mole Frac (Methane)Comp Mole Frac (Ethane)Comp Mole Frac (Propane)Comp Mole Frac (Ammonia)Comp Mole Frac (Ethylene)
10.9700 *0.0200 *0.0100 *0.0000 *0.0000 *
20.97000.02000.01000.00000.0000
30.99980.00020.00000.00000.0000
40.96670.02220.01110.00000.0000
51.00000.00000.00000.00000.0000
NameComp Mole Frac (Methane)Comp Mole Frac (Ethane)Comp Mole Frac (Propane)Comp Mole Frac (Ammonia)Comp Mole Frac (Ethylene)
61.0000 *0.0000 *0.0000 *0.0000 *0.0000 *
71.00000.00000.00000.00000.0000
81.00000.00000.00000.00000.0000
90.0000 *0.0000 *0.0000 *0.0000 *1.0000 *
100.00000.00000.00000.00001.0000
NameComp Mole Frac (Methane)Comp Mole Frac (Ethane)Comp Mole Frac (Propane)Comp Mole Frac (Ammonia)Comp Mole Frac (Ethylene)
110.00000.00000.00000.00001.0000
120.00000.00000.00000.00001.0000
130.0000 *0.0000 *1.0000 *0.0000 *0.0000 *
140.00000.00001.00000.00000.0000
150.00000.00001.00000.00000.0000
NameComp Mole Frac (Methane)Comp Mole Frac (Ethane)Comp Mole Frac (Propane)Comp Mole Frac (Ammonia)Comp Mole Frac (Ethylene)
160.00000.00001.00000.00000.0000
170.0000 *0.0000 *0.0000 *1.0000 *0.0000 *
180.00000.00000.00001.00000.0000
190.00000.00000.00001.00000.0000
200.00000.00000.00001.00000.0000
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Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Workbook: Case (Main) (continued)Compositions (continued) Fluid Pkg: All
NameComp Mole Frac (Methane)Comp Mole Frac (Ethane)Comp Mole Frac (Propane)Comp Mole Frac (Ammonia)Comp Mole Frac (Ethylene)
210.00000.00001.00000.00000.0000
220.00000.00001.00000.00000.0000
230.00000.00001.00000.00000.0000
240.00000.00001.00000.00000.0000
Energy Streams Fluid Pkg: AllNameHeat Flow (Btu/hr)
q1001.023e+007
q1011.518e+007
q1023.326e+005
q1031.042e+007
q1046.466e+006
Unit OpsOperation Name Operation Type Feeds Products Ignored Calc Level
LNG-100 (GAS -METANO) LNG 16
25
No 500.0 *
LNG-102 (ETILENO-PROPANO)LNG 1124
1214
No 500.0 *
LNG-101 (METANO-ETILENO) LNG 79
810
No 500.0 *
LNG-103 LNG2217
1618
No 500.0 *
V-100 Separator2 4
3No 500.0 *
V-101 Separator13 24
21No 500.0 *
K-100 Compressor5q100
7No 500.0 *
K-101 Compressor10q101
11No 500.0 *
K-102 Compressor14q102
15No 500.0 *
K-103 Compressor18q103
19No 500.0 *
K-104 Compressor23q104
22No 500.0 *
VLV-100 Valve 8 6 No 500.0 *VLV-101 Valve 12 9 No 500.0 *VLV-102 Valve 16 13 No 500.0 *VLV-103 Valve 20 17 No 500.0 *AC-100 Air cooler 19 20 No 500.0 *
MIX-100 Mixer2115
23No 500.0 *
Feeder Block: FeederBlock_1( No Datasheets exist for this unit operation )
Compressor: K-100
DESIGN
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Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Compressor: K-100 (continued)Connections
Inlet Stream
STREAM NAME FROM UNIT OPERATION5 LNG-100 (GAS -METANO)LNG
Outlet Stream
STREAM NAME TO UNIT OPERATION7 LNG-101 (METANO-ETILENO)LNG
Energy Stream
STREAM NAME FROM UNIT OPERATIONq100
Parameters
Speed: --- Duty: 4.0209e+03 hpAdiabatic Eff.: 75.00 PolyTropic Eff.: 80.65Adiabatic Head: 5.290e+004 ft Polytropic Head: 5.689e+004 ftAdiabatic Fluid Head: 5.290e+004 lbf-ft/lbm Polytropic Fluid Head: 5.689e+004 lbf-ft/lbmPolytropic Exp. 1.434 Isentropic Exp. 1.309 Poly Head Factor 0.9970
User Variables
RATING
Curves
Compressor Speed: --- Efficiency: Adiabatic Curves Enabled: YesHead Offset: 0.0000 ft Efficiency Offset: 0.0000
Speed: Flow Head Efficiency (%)
Flow Limits
Surge Curve: InactiveSpeed Flow Speed Flow Speed Flow
Stone Wall Curve: InactiveSpeed Flow Speed Flow Speed Flow
Surge Flow Rate --- Field Flow Rate 4660 ACFM Stone Wall Flow --- Compressor Volume 0.0000 ft3
Nozzle Paramaters
Base Elevation Relative to Ground Level 0.0000 ft *
Diameter (ft)Elevation (Base) (ft)Elevation (Ground) (ft)
50.16400.00000.0000
70.16400.00000.0000
Inertia
Rotational inertia (lb-ft2) 142.4 Radius of gyration (ft) 0.6562Mass (lb) 330.7 Friction loss factor (rad/min) (lb-ft2/s) 0.1424
WORKSHEET
Conditions
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Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Compressor: K-100 (continued)Conditions
VapourTemperature (F)Pressure (psia)Molar Flow (lbmole/hr)Mass Flow (lb/hr)Std Ideal Liq Vol Flow (barrel/day)Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)Heat Flow (Btu/hr)
1.0000 *-223.3610
58.0000 *7035.5340
112870.369025813.9883
-3.474e+00434.23
-2.4441e+08
1.0000-13.8292430.9766
7035.5340112870.3690
25813.9883-3.329e+004
35.08-2.3418e+08
---
---
---
---
---
---
---
---
1.0231e+07
Properties
NameMolecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLHV Molar Basis (Std)HHV Molar Basis (Std)HHV Mass Basis (Std)CO2 LoadingCO2 Apparent Mole Conc.CO2 Apparent Wt. Conc.LHV Mass Basis (Std)Phase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Phase Fraction [Act. Vol. Basis]Mass ExergyPartial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.
(lbmole/ft3)(lb/ft3)
(barrel/day)(Btu/lb)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole)(Btu/lbmole)
(Btu/lb)
(lbmole/ft3)(lbmol/lb)
(Btu/lb)
(Btu/lb)(psia)
(Cost/s)(ACFM)
(lbmole/ft3)(Btu/lbmole-F)
(MMSCFD)(lb/ft3)
(USGPM)
(psia)
(Btu/lbmole)(cSt)
(lb/ft3)(barrel/day)
(ft3/lbmole)(Btu/lb)
516.04
2.516e-0020.4037
1.195e+006-21652.1338.596
0.53583.451e+0053.804e+0052.371e+004
---
---
---
2.151e+0041.0001.0001.000163.3
0.00000.0000
46601.1658.59664.0818.69
---
---
19.52---
0.00001.3001.4413249
0.83354.246e-0021.136e+007
0.000039.74202.5
716.04
0.10191.635
2.950e+005-20752.1879.528
0.59393.451e+0053.804e+0052.371e+004
---
---
---
2.151e+0041.0001.0001.000225.4
0.00000.0000
11501.1659.52864.0818.69
---
0.883619.52
---
0.00001.2631.5051826
0.39124.246e-0021.136e+007
0.00009.810113.8
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LEGENDSBurlington, MAUSA
Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Compressor: K-100 (continued)Properties
NamePhase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(dyne/cm)(Btu/hr-ft-F)
(cP)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)
(psia)(psia)
(barrel/day)
51.0000
---
7.128e-0035.390e-003
6.6110.4121
5.9670.3720
---
---
---
---
---
1.136e+007---
71.0000
---
1.720e-0021.025e-002
7.5420.4701
6.3310.3946
---
---
---
---
---
1.136e+007-63.95
PERFORMANCE
Results
Adiabatic Head (ft)Polytropic Head (ft)Adiabatic Fluid Head (lbf-ft/lbm)Polytropic Fluid Head (lbf-ft/lbm)Adiabatic EfficiencyPolytropic Efficiency
5.290e+0045.689e+0045.290e+0045.689e+004
7581
Power Consumed (hp)Polytropic Head FactorPolytropic ExponentIsentropic ExponentSpeed (rpm)
40210.99701.4341.309
---
---
Power/Torque
Total Rotor Power (hp)Transient Rotor Power (hp)Friction Power Loss (hp)Fluid Power (hp)
40210.00000.00004021
Total Rotor Torque (lbf-ft)Transient Rotor Torque (lbf-ft)Friction Torque Loss (lbf-ft)Fluid Torque (lbf-ft)
---
---
---
---
DYNAMICS
Dynamic Specifications
Duty (Btu/hr)Adiabatic EfficiencyPolytropic EfficiencyPressure Increase (psi)
1.023e+0077581
373.0---
ActiveNot Active
ActiveNot Active
Head (ft)Fluid Head (lbf-ft/lbm)Capacity (ACFM)Speed (rpm)Use Characteristic Curves
5.689e+0045.689e+004
4660---
Not ActiveNot ActiveNot ActiveNot Active
No
Holdup Details
Phase
VapourLiquid
Aqueous
Accumulation (lbmole/hr)
0.00000.00000.0000
Moles (lbmole)0.0000 *0.0000 *0.0000 *
Volume (ft3)
0.00000.00000.0000
Total 0.0000 0.0000 0.0000
NOTES
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Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Compressor: K-101
DESIGN
Connections
Inlet Stream
STREAM NAME FROM UNIT OPERATION10 LNG-101 (METANO-ETILENO)LNG
Outlet Stream
STREAM NAME TO UNIT OPERATION11 LNG-102 (ETILENO-PROPANO)LNG
Energy Stream
STREAM NAME FROM UNIT OPERATIONq101
Parameters
Speed: --- Duty: 5.9672e+03 hpAdiabatic Eff.: 75.00 PolyTropic Eff.: 80.19Adiabatic Head: 5.174e+004 ft Polytropic Head: 5.532e+004 ftAdiabatic Fluid Head: 5.174e+004 lbf-ft/lbm Polytropic Fluid Head: 5.532e+004 lbf-ft/lbmPolytropic Exp. 1.328 Isentropic Exp. 1.243 Poly Head Factor 1.012
User Variables
RATING
Curves
Compressor Speed: --- Efficiency: Adiabatic Curves Enabled: YesHead Offset: 0.0000 ft Efficiency Offset: 0.0000
Speed: Flow Head Efficiency (%)
Flow Limits
Surge Curve: InactiveSpeed Flow Speed Flow Speed Flow
Stone Wall Curve: InactiveSpeed Flow Speed Flow Speed Flow
Surge Flow Rate --- Field Flow Rate 1.650e+004 ACFM Stone Wall Flow --- Compressor Volume 0.0000 ft3
Nozzle Paramaters
Base Elevation Relative to Ground Level 0.0000 ft *
Diameter (ft)Elevation (Base) (ft)Elevation (Ground) (ft)
100.16400.00000.0000
110.16400.00000.0000
Inertia
Rotational inertia (lb-ft2) 142.4 Radius of gyration (ft) 0.6562Mass (lb) 330.7 Friction loss factor (rad/min) (lb-ft2/s) 0.1424
WORKSHEET
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Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Compressor: K-101 (continued)Conditions
NameVapourTemperature (F)Pressure (psia)Molar Flow (lbmole/hr)Mass Flow (lb/hr)Std Ideal Liq Vol Flow (barrel/day)Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)Heat Flow (Btu/hr)
101.0000 *
-145.484820.0000 *
6104.7861171262.4506
30600.28332.033e+004
36.361.2414e+08
111.0000
132.2958221.6210
6104.7861171262.4506
30600.28332.282e+004
37.461.3932e+08
q101---
---
---
---
---
---
---
---
1.5183e+07
Properties
NameMolecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLHV Molar Basis (Std)HHV Molar Basis (Std)HHV Mass Basis (Std)CO2 LoadingCO2 Apparent Mole Conc.CO2 Apparent Wt. Conc.LHV Mass Basis (Std)Phase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Phase Fraction [Act. Vol. Basis]Mass ExergyPartial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar Volume
(lbmole/ft3)(lb/ft3)
(barrel/day)(Btu/lb)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole)(Btu/lbmole)
(Btu/lb)
(lbmole/ft3)(lbmol/lb)
(Btu/lb)
(Btu/lb)(psia)
(Cost/s)(ACFM)
(lbmole/ft3)(Btu/lbmole-F)
(MMSCFD)(lb/ft3)
(USGPM)
(psia)
(Btu/lbmole)(cSt)
(lb/ft3)(barrel/day)
(ft3/lbmole)
1028.05
6.166e-0030.1730
4.232e+006724.81.2968.812
0.31415.690e+0056.043e+0052.154e+004
---
---
---
2.028e+0041.0001.0001.00033.01
0.00000.0000
1.650e+0040.8528
8.81255.6023.92
---
---
17.53---
0.00001.2911.33856622.166
7.461e-0029.812e+006
0.0000162.2
1128.05
3.773e-0021.058
6.916e+005813.51.33511.88
0.42335.690e+0056.043e+0052.154e+004
---
---
---
2.028e+0041.0001.0001.000100.6
0.00000.0000
26970.8528
11.8855.6023.92
---
0.924617.53
---
0.00001.2011.2954259
0.68617.461e-0029.812e+006
0.000026.50
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LEGENDSBurlington, MAUSA
Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Compressor: K-101 (continued)Properties
NameMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(Btu/lb)
(dyne/cm)(Btu/hr-ft-F)
(cP)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)
(psia)(psia)
(barrel/day)
10201.8
1.0000---
6.152e-0036.003e-003
6.8260.2433
6.5840.2347
---
---
---
---
---
9.812e+006-26.99
11151.8
1.0000---
1.496e-0021.163e-002
9.8900.3525
9.1740.3270
---
---
---
---
---
9.812e+006-34.80
PERFORMANCE
Results
Adiabatic Head (ft)Polytropic Head (ft)Adiabatic Fluid Head (lbf-ft/lbm)Polytropic Fluid Head (lbf-ft/lbm)Adiabatic EfficiencyPolytropic Efficiency
5.174e+0045.532e+0045.174e+0045.532e+004
7580
Power Consumed (hp)Polytropic Head FactorPolytropic ExponentIsentropic ExponentSpeed (rpm)
59671.0121.3281.243
---
---
Power/Torque
Total Rotor Power (hp)Transient Rotor Power (hp)Friction Power Loss (hp)Fluid Power (hp)
59670.00000.00005967
Total Rotor Torque (lbf-ft)Transient Rotor Torque (lbf-ft)Friction Torque Loss (lbf-ft)Fluid Torque (lbf-ft)
---
---
---
---
DYNAMICS
Dynamic Specifications
Duty (Btu/hr)Adiabatic EfficiencyPolytropic EfficiencyPressure Increase (psi)
1.518e+0077580
201.6---
ActiveNot Active
ActiveNot Active
Head (ft)Fluid Head (lbf-ft/lbm)Capacity (ACFM)Speed (rpm)Use Characteristic Curves
5.532e+0045.532e+0041.650e+004
---
Not ActiveNot ActiveNot ActiveNot Active
No
Holdup Details
Phase
VapourLiquid
Aqueous
Accumulation (lbmole/hr)
0.00000.00000.0000
Moles (lbmole)0.0000 *0.0000 *0.0000 *
Volume (ft3)
0.00000.00000.0000
Total 0.0000 0.0000 0.0000
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LEGENDSBurlington, MAUSA
Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Compressor: K-101 (continued)NOTES
Compressor: K-102
DESIGN
Connections
Inlet Stream
STREAM NAME FROM UNIT OPERATION14 LNG-102 (ETILENO-PROPANO)LNG
Outlet Stream
STREAM NAME TO UNIT OPERATION15 MIX-100Mixer
Energy Stream
STREAM NAME FROM UNIT OPERATIONq102
Parameters
Speed: --- Duty: 1.3072e+02 hpAdiabatic Eff.: 75.00 PolyTropic Eff.: 75.11Adiabatic Head: 913.6 ft Polytropic Head: 915.0 ftAdiabatic Fluid Head: 913.6 lbf-ft/lbm Polytropic Fluid Head: 915.0 lbf-ft/lbmPolytropic Exp. 1.192 Isentropic Exp. 1.130 Poly Head Factor 1.000
User Variables
RATING
Curves
Compressor Speed: --- Efficiency: Adiabatic Curves Enabled: YesHead Offset: 0.0000 ft Efficiency Offset: 0.0000
Speed: Flow Head Efficiency (%)
Flow Limits
Surge Curve: InactiveSpeed Flow Speed Flow Speed Flow
Stone Wall Curve: InactiveSpeed Flow Speed Flow Speed Flow
Surge Flow Rate --- Field Flow Rate 2.312e+004 ACFM Stone Wall Flow --- Compressor Volume 0.0000 ft3
Nozzle Paramaters
Base Elevation Relative to Ground Level 0.0000 ft *
Diameter (ft)Elevation (Base) (ft)Elevation (Ground) (ft)
140.16400.00000.0000
150.16400.00000.0000
InertiaAspen Technology Inc. Aspen HYSYS Version 8.4 (30.0.0.8433) Page 17 of 168
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LEGENDSBurlington, MAUSA
Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Compressor: K-102 (continued)Inertia
Rotational inertia (lb-ft2) 142.4 Radius of gyration (ft) 0.6562Mass (lb) 330.7 Friction loss factor (rad/min) (lb-ft2/s) 0.1424
WORKSHEET
Conditions
NameVapourTemperature (F)Pressure (psia)Molar Flow (lbmole/hr)Mass Flow (lb/hr)Std Ideal Liq Vol Flow (barrel/day)Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)Heat Flow (Btu/hr)
141.0000 *
-43.095415.0000 *
4818.2480212470.2848
28713.3867-4.670e+004
34.40-2.2501e+08
151.0000
-38.208916.0000 *
4818.2480212470.2848
28713.3867-4.663e+004
34.44-2.2468e+08
q102---
---
---
---
---
---
---
---
3.3261e+05
Properties
NameMolecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLHV Molar Basis (Std)HHV Molar Basis (Std)HHV Mass Basis (Std)CO2 LoadingCO2 Apparent Mole Conc.CO2 Apparent Wt. Conc.LHV Mass Basis (Std)Phase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Phase Fraction [Act. Vol. Basis]Mass ExergyPartial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.
(lbmole/ft3)(lb/ft3)
(barrel/day)(Btu/lb)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole)(Btu/lbmole)
(Btu/lb)
(lbmole/ft3)(lbmol/lb)
(Btu/lb)
(Btu/lb)(psia)
(Cost/s)(ACFM)
(lbmole/ft3)(Btu/lbmole-F)
(MMSCFD)(lb/ft3)
(USGPM)
(psia)
(Btu/lbmole)
1444.10
3.473e-0030.1532
5.930e+006-1059
0.780015.06
0.34168.792e+0059.497e+0052.154e+004
---
---
---
1.994e+0041.0001.0001.0006.238
0.00000.0000
2.312e+0040.7173
15.0643.8831.63
---
---
14.70---
0.00001.1521.1728034
1544.10
3.666e-0030.1617
5.618e+006-1057
0.780915.20
0.34468.792e+0059.497e+0052.154e+004
---
---
---
1.994e+0041.0001.0001.0007.305
0.00000.0000
2.190e+0040.7173
15.2043.8831.63
---
0.964914.70
---
0.00001.1501.1718008
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Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Compressor: K-102 (continued)Properties
NameKinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(cSt)(lb/ft3)
(barrel/day)
(ft3/lbmole)(Btu/lb)
(dyne/cm)(Btu/hr-ft-F)
(cP)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)
(psia)(psia)
(barrel/day)
142.56831.69
2.866e+0040.0000
287.9182.2
1.0000---
6.709e-0036.299e-003
13.080.2965
12.850.2914
---
---
---
189.0189.0
2.866e+004-18.70
152.46431.69
2.866e+0040.0000
272.8181.6
1.0000---
6.845e-0036.380e-003
13.210.2996
12.980.2943
---
---
---
189.0189.0
2.866e+004-19.56
PERFORMANCE
Results
Adiabatic Head (ft)Polytropic Head (ft)Adiabatic Fluid Head (lbf-ft/lbm)Polytropic Fluid Head (lbf-ft/lbm)Adiabatic EfficiencyPolytropic Efficiency
913.6915.0913.6915.0
7575
Power Consumed (hp)Polytropic Head FactorPolytropic ExponentIsentropic ExponentSpeed (rpm)
130.71.0001.1921.130
---
---
Power/Torque
Total Rotor Power (hp)Transient Rotor Power (hp)Friction Power Loss (hp)Fluid Power (hp)
130.70.00000.0000130.7
Total Rotor Torque (lbf-ft)Transient Rotor Torque (lbf-ft)Friction Torque Loss (lbf-ft)Fluid Torque (lbf-ft)
---
---
---
---
DYNAMICS
Dynamic Specifications
Duty (Btu/hr)Adiabatic EfficiencyPolytropic EfficiencyPressure Increase (psi)
3.326e+0057575
1.000---
ActiveNot Active
ActiveNot Active
Head (ft)Fluid Head (lbf-ft/lbm)Capacity (ACFM)Speed (rpm)Use Characteristic Curves
915.0915.0
2.312e+004---
Not ActiveNot ActiveNot ActiveNot Active
No
Holdup Details
Phase
Vapour
Accumulation (lbmole/hr)
0.0000
Moles (lbmole)0.0000 *
Volume (ft3)
0.0000Aspen Technology Inc. Aspen HYSYS Version 8.4 (30.0.0.8433) Page 19 of 168
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Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Compressor: K-102 (continued)Phase
LiquidAqueous
Accumulation (lbmole/hr)
0.00000.0000
Moles (lbmole)0.0000 *0.0000 *
Volume (ft3)
0.00000.0000
Total 0.0000 0.0000 0.0000
NOTES
Compressor: K-103
DESIGN
Connections
Inlet Stream
STREAM NAME FROM UNIT OPERATION18 LNG-103LNG
Outlet Stream
STREAM NAME TO UNIT OPERATION19 AC-100Air cooler
Energy Stream
STREAM NAME FROM UNIT OPERATIONq103
Parameters
Speed: --- Duty: 4.0934e+03 hpAdiabatic Eff.: 75.00 PolyTropic Eff.: 78.60Adiabatic Head: 6.784e+004 ft Polytropic Head: 7.110e+004 ftAdiabatic Fluid Head: 6.784e+004 lbf-ft/lbm Polytropic Fluid Head: 7.110e+004 lbf-ft/lbmPolytropic Exp. 1.406 Isentropic Exp. 1.292 Poly Head Factor 1.002
User Variables
RATING
Curves
Compressor Speed: --- Efficiency: Adiabatic Curves Enabled: YesHead Offset: 0.0000 ft Efficiency Offset: 0.0000
Speed: Flow Head Efficiency (%)
Flow Limits
Surge Curve: InactiveSpeed Flow Speed Flow Speed Flow
Stone Wall Curve: InactiveSpeed Flow Speed Flow Speed Flow
Surge Flow Rate --- Field Flow Rate 1.322e+004 ACFM Stone Wall Flow --- Compressor Volume 0.0000 ft3
Nozzle Paramaters
Base Elevation Relative to Ground Level 0.0000 ft *Aspen Technology Inc. Aspen HYSYS Version 8.4 (30.0.0.8433) Page 20 of 168
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Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Compressor: K-103 (continued)
Diameter (ft)Elevation (Base) (ft)Elevation (Ground) (ft)
180.16400.00000.0000
190.16400.00000.0000
Inertia
Rotational inertia (lb-ft2) 142.4 Radius of gyration (ft) 0.6562Mass (lb) 330.7 Friction loss factor (rad/min) (lb-ft2/s) 0.1424
WORKSHEET
Conditions
NameVapourTemperature (F)Pressure (psia)Molar Flow (lbmole/hr)Mass Flow (lb/hr)Std Ideal Liq Vol Flow (barrel/day)Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)Heat Flow (Btu/hr)
181.0000 *2.7105
32.0000 *5261.2103
89598.41499958.3764
-2.035e+00437.86
-1.0704e+08
191.0000
240.2986131.0313
5261.210389598.4149
9958.3764-1.837e+004
38.59-9.6625e+07
q103---
---
---
---
---
---
---
---
1.0415e+07
Properties
NameMolecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLHV Molar Basis (Std)HHV Molar Basis (Std)HHV Mass Basis (Std)CO2 LoadingCO2 Apparent Mole Conc.CO2 Apparent Wt. Conc.LHV Mass Basis (Std)Phase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Phase Fraction [Act. Vol. Basis]Mass ExergyPartial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson K
(lbmole/ft3)(lb/ft3)
(barrel/day)(Btu/lb)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole)(Btu/lbmole)
(Btu/lb)
(lbmole/ft3)(lbmol/lb)
(Btu/lb)
(Btu/lb)(psia)
(Cost/s)(ACFM)
(lbmole/ft3)(Btu/lbmole-F)
(MMSCFD)(lb/ft3)
(USGPM)
1817.03
6.634e-0030.1130
3.390e+006-11952.2238.532
0.50101.362e+0051.627e+005
9551---
---
---
79981.0001.0001.00050.93
0.00000.0000
1.322e+0042.2588.53247.9238.46
---
---
12.24
1917.03
1.808e-0020.3079
1.244e+006-10782.2669.453
0.55511.362e+0051.627e+005
9551---
---
---
79981.0001.0001.000144.0
0.00000.0000
48502.2589.45347.9238.46
---
0.964812.24
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Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Compressor: K-103 (continued)Properties
NameUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)CvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(psia)
(Btu/lbmole)(cSt)
(lb/ft3)(barrel/day)
(ft3/lbmole)(Btu/lb)
(dyne/cm)(Btu/hr-ft-F)
(cP)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)
(psia)(psia)
(barrel/day)
18---
0.00001.3031.34398513.94138.22
1.002e+0040.0000
150.7578.5
1.0000---
1.277e-0027.131e-003
6.5460.3844
6.3520.3730
---
---
---
210.5210.5
1.002e+004-22.36
19---
0.00001.2661.32189282.29738.22
1.002e+0040.0000
55.31524.3
1.0000---
2.245e-0021.133e-002
7.4670.4385
7.1560.4202
---
---
---
210.5210.5
1.002e+004-29.10
PERFORMANCE
Results
Adiabatic Head (ft)Polytropic Head (ft)Adiabatic Fluid Head (lbf-ft/lbm)Polytropic Fluid Head (lbf-ft/lbm)Adiabatic EfficiencyPolytropic Efficiency
6.784e+0047.110e+0046.784e+0047.110e+004
7579
Power Consumed (hp)Polytropic Head FactorPolytropic ExponentIsentropic ExponentSpeed (rpm)
40931.0021.4061.292
---
---
Power/Torque
Total Rotor Power (hp)Transient Rotor Power (hp)Friction Power Loss (hp)Fluid Power (hp)
40930.00000.00004093
Total Rotor Torque (lbf-ft)Transient Rotor Torque (lbf-ft)Friction Torque Loss (lbf-ft)Fluid Torque (lbf-ft)
---
---
---
---
DYNAMICS
Dynamic Specifications
Duty (Btu/hr)Adiabatic EfficiencyPolytropic EfficiencyPressure Increase (psi)
1.042e+0077579
99.03---
ActiveNot Active
ActiveNot Active
Head (ft)Fluid Head (lbf-ft/lbm)Capacity (ACFM)Speed (rpm)Use Characteristic Curves
7.110e+0047.110e+0041.322e+004
---
Not ActiveNot ActiveNot ActiveNot Active
NoAspen Technology Inc. Aspen HYSYS Version 8.4 (30.0.0.8433) Page 22 of 168
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Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
Compressor: K-103 (continued)Holdup Details
Phase
VapourLiquid
Aqueous
Accumulation (lbmole/hr)
0.00000.00000.0000
Moles (lbmole)0.0000 *0.0000 *0.0000 *
Volume (ft3)
0.00000.00000.0000
Total 0.0000 0.0000 0.0000
NOTES
LNG: LNG-100 (GAS -METANO)CONNECTIONS
Inlet Stream
STREAM NAME FROM UNIT OPERATION16 VLV-100Valve
Outlet Stream
STREAM NAME TO UNIT OPERATION2 V-100Separator5 K-100Compressor
PARAMETERS
Exchanger Parameters
Rating Method: Simple Weighted Shell Passes: ---
Exchange Details
Pass Name1-26-5
Intervals10 *10 *
Dew/Bubble Pt.OnOn
EquilibrateOffOff
Step TypeEqual EnthalpyEqual Enthalpy
Pressure ProfileConst dPdHConst dPdH
Specifications Summary
Name Type Value Curr Value Rel Error Active EstimateHeat Balance Duty 0.0000 Btu/hr -1.652e-004 Btu/hr -1.300e-011 On Off
Side Results
Pass Name
1-26-5
Inlet Temp (F)
100.0-222.3
Outlet Temp (F)
-222.3-223.4
Delta P (psi)
2.0002.000
Molar Flow (lbmole/hr)
21967036
Duty (Btu/hr)
-1.271e+0071.271e+007
Ua (Btu/F-hr)
8.585e+0068.585e+006
Hot/Cold
HotCold
Overall/Detailed Performance
Duty: 1.271e+07 Btu/hrHeat Leak: 0.000e-01 Btu/hr
UA Curv. Error: 2.137e+05 Btu/F-hrHot Pinch Temp: -222.3 F
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Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
LNG: LNG-100 (GAS -METANO) (continued)PARAMETERS
Overall/Detailed Performance
Heat Loss: 0.000e-01 Btu/hrUA: 8.585e+06 Btu/F-hrMin. Approach: 6.410e-002 FLmtd: 1.481 F
Cold Pinch Temp: -222.3 FCold Inlet Eqm Temp: -222.3 F *Hot Inlet Eqm Temp: 100.0 F *
SPECIFICATIONS
Heat Balance
Type: Duty Pass: Error Spec Value: 0.0000 Btu/hr
RATING
Sizing
Zone GeometryZone Number
Zone 0Width
3.281 ft *Length3.281 ft *
Zone Metal PropertiesZone Number
Zone 0Thermal Cond
92.45 Btu/hr-ft-F *Cp
0.2102 Btu/lb-F *Density
168.6 lb/ft3 *Zone Layers
Zone NumberZone 0
Number of Layers in Set2 *
Repeated Sets1 *
Layers
Zone 0Layer
L 0L 1
Perforation (%)0.00 *0.00 *
Height (ft)2.208e-002 *2.208e-002 *
Pitch (fins/m)530.0 *530.0 *
Fin Thick (ft)1.375e-003 *1.375e-003 *
Plate Thick (ft)4.000e-003 *4.000e-003 *
Heat Transfer
Zone 0Initial Metal Temp
77.00 F *Internal Heat Transfer
LayerL 0L 1
U CalculatorU specifiedU specified
U (Btu/hr-ft2-F)0.00000.0000
Ref Flow (lb/hr)---
---
Min Scale 0.00000.0000
Override UANoNo
Convective UA (Btu/F-hr)0.00000.0000
External Heat TransferLayer
L 0L 1
External T (F)77.00 *77.00 *
UA (Btu/F-hr)0.0000 *0.0000 *
Q1 (Btu/hr)0.0000 *0.0000 *
Q fixed (Btu/hr)0.0000 *0.0000 *
CONDITIONS
NameVapourTemperature (F)Pressure (psia)Molar Flow (lbmole/hr)Mass Flow (lb/hr)Std Ideal Liq Vol Flow (barrel/day)
11.0000
100.0000 *60.0000 *
2196 *3.646e+004
8201
60.4407
-222.320960.0000
70361.129e+0052.581e+004
20.1000 *
-222.256858.0000
21963.646e+004
8201
51.0000 *
-223.361058.0000 *
70361.129e+0052.581e+004
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Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
LNG: LNG-100 (GAS -METANO) (continued)CONDITIONS
Molar Enthalpy (Btu/lbmole)Molar Entropy (Btu/lbmole-F)Heat Flow (Btu/hr)
-3.224e+00441.68
-7.080e+007
-3.655e+00426.55
-2.571e+008
-3.803e+00421.92
-8.351e+007
-3.474e+00434.23
-2.444e+008
PROPERTIES
NameMolecular WeightMolar DensityMass DensityAct. Volume FlowMass EnthalpyMass EntropyHeat CapacityMass Heat CapacityLHV Molar Basis (Std)HHV Molar Basis (Std)HHV Mass Basis (Std)CO2 LoadingCO2 Apparent Mole Conc.CO2 Apparent Wt. Conc.LHV Mass Basis (Std)Phase Fraction [Vol. Basis]Phase Fraction [Mass Basis]Phase Fraction [Act. Vol. Basis]Mass ExergyPartial Pressure of CO2Cost Based on FlowAct. Gas FlowAvg. Liq. DensitySpecific HeatStd. Gas FlowStd. Ideal Liq. Mass DensityAct. Liq. FlowZ FactorWatson KUser PropertyPartial Pressure of H2SCp/(Cp - R)Cp/CvHeat of Vap.Kinematic ViscosityLiq. Mass Density (Std. Cond)Liq. Vol. Flow (Std. Cond)Liquid FractionMolar VolumeMass Heat of Vap.Phase Fraction [Molar Basis]Surface TensionThermal ConductivityViscosityCv (Semi-Ideal)Mass Cv (Semi-Ideal)
(lbmole/ft3)(lb/ft3)
(barrel/day)(Btu/lb)
(Btu/lb-F)(Btu/lbmole-F)
(Btu/lb-F)(Btu/lbmole)(Btu/lbmole)
(Btu/lb)
(lbmole/ft3)(lbmol/lb)
(Btu/lb)
(Btu/lb)(psia)
(Cost/s)(ACFM)
(lbmole/ft3)(Btu/lbmole-F)
(MMSCFD)(lb/ft3)
(USGPM)
(psia)
(Btu/lbmole)(cSt)
(lb/ft3)(barrel/day)
(ft3/lbmole)(Btu/lb)
(dyne/cm)(Btu/hr-ft-F)
(cP)(Btu/lbmole-F)
(Btu/lb-F)
116.60
1.008e-0020.1673
9.317e+005-19422.5108.985
0.54113.558e+0053.918e+0052.360e+004
---
---
---
2.143e+0041.0001.0001.00090.08
0.00000.0000
36331.1458.98520.0019.01
---
0.991519.37
---
0.00001.2841.29940544.371
4.396e-0023.546e+006
0.000099.25244.1
1.0000---
2.043e-0021.171e-002
6.9990.4215
616.04
5.771e-0020.9259
5.211e+005-22781.65511.85
0.73843.451e+0053.804e+0052.371e+004
---
---
---
2.151e+0040.44070.44070.9788
307.40.00000.0000
19891.16511.8564.0818.69322.0
---
19.52---
0.00001.2011.1123239
---
4.246e-0021.136e+007
0.559317.33201.9
0.44078.601
---
---
9.8610.6146
216.60
0.21783.617
4.310e+004-22901.32013.68
0.82383.558e+0053.918e+0052.360e+004
---
---
---
2.143e+0049.826e-0029.664e-002
0.8707380.1
0.00000.0000
146.31.14513.6820.0019.01162.5
---
19.37---
0.00001.1701.0224065
---
4.396e-0023.546e+006
0.90004.591244.8
0.10009.190
---
---
11.690.7042
516.04
2.516e-0020.4037
1.195e+006-21652.1338.596
0.53583.451e+0053.804e+0052.371e+004
---
---
---
2.151e+0041.0001.0001.000163.3
0.00000.0000
46601.1658.59664.0818.69
---
---
19.52---
0.00001.3001.4413249
0.83354.246e-0021.136e+007
0.000039.74202.5
1.0000---
7.128e-0035.390e-003
6.6110.4121
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Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
LNG: LNG-100 (GAS -METANO) (continued)PROPERTIES
NameCvMass CvCv (Ent. Method)Mass Cv (Ent. Method)Cp/Cv (Ent. Method)Reid VP at 37.8 CTrue VP at 37.8 CLiq. Vol. Flow - Sum(Std. Cond)Viscosity Index
(Btu/lbmole-F)(Btu/lb-F)
(Btu/lbmole-F)(Btu/lb-F)
(psia)(psia)
(barrel/day)
16.917
0.4166---
---
---
---
---
3.546e+006-8.614
610.66
0.6642---
---
---
---
---
1.136e+007---
213.38
0.8060---
---
---
---
---
3.546e+006-56.86
55.967
0.3720---
---
---
---
---
1.136e+007---
PERFORMANCE
PERFORMANCE TABLES
Cold Composite
Overall PhaseCold Composite
Temperature (F)
-222.32-222.43-222.43-222.53-222.53-222.63-222.64-222.74-222.74-222.84-222.84-222.95-222.95-222.99-223.05-223.05-223.15-223.16-223.26-223.36
Pressure (psia)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Heat Flow (Btu/hr)
0.001271299.401280117.692542598.792560235.373813898.193840353.065085197.585120470.746356496.986400588.437627796.387680706.128216766.198899095.778960823.80
10170395.1710210096.9011441694.5612712993.96
Enthalpy (Btu/lbmole)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
UA (Btu/F-hr)
---
---
---
---
---
---
---
---
---
---
Molar Vap Frac
---
---
---
---
---
---
---
---
---
---
Mass Vap Frac
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Heat of Vap. (Btu/lbmole)
---
---
---
---
---
---
---
---
---
---
Delta Temp (F)
0.06410.54180.54511.18081.18972.21352.23514.61464.6820
17.8245Aspen Technology Inc. Aspen HYSYS Version 8.4 (30.0.0.8433) Page 26 of 168
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LEGENDSBurlington, MAUSA
Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
LNG: LNG-100 (GAS -METANO) (continued)PERFORMANCE TABLES
Cold Composite
Overall PhaseCold Composite
UA (Btu/F-hr)
---
---
---
---
---
---
---
---
---
---
Molar Vap Frac
---
---
---
---
---
---
---
---
---
---
Mass Vap Frac
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Heat of Vap. (Btu/lbmole)
---
---
---
---
---
---
---
---
---
---
Delta Temp (F)
18.293460.936062.774282.9272
120.3631123.7501189.7116191.8765257.6183323.3610
Vapour PhaseCold Composite
Mass Flow (lb/hr)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Molecular Wt
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Density (lb/ft3)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Mass Sp Heat (Btu/lb-F)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Viscosity (cP)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Thermal Cond (Btu/hr-ft-F)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Std Gas Flow (MMSCFD)
---
---
---
---
---
---
---
---
---
---
Z Factor
---
---
---
---
---
---
---
---
---
---
Pseudo Pc (psia)
---
---
---
---
---
---
---
---
---
---
Pseudo Tc (F)
-222.43-222.43-222.43-222.43-222.43-222.43-222.43-222.43-222.43-222.43
Pseudo Zc
---
---
---
---
---
---
---
---
---
---
Pseudo Omega
---
---
---
---
---
---
---
---
---
---
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LEGENDSBurlington, MAUSA
Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
LNG: LNG-100 (GAS -METANO) (continued)PERFORMANCE TABLES
Cold Composite
Vapour PhaseCold Composite
Std Gas Flow (MMSCFD)
---
---
---
---
---
---
---
---
---
---
Z Factor
---
---
---
---
---
---
---
---
---
---
Pseudo Pc (psia)
---
---
---
---
---
---
---
---
---
---
Pseudo Tc (F)
-222.43-222.43-222.43-222.43-222.43-222.43-222.43-222.43-222.43-222.43
Pseudo Zc
---
---
---
---
---
---
---
---
---
---
Pseudo Omega
---
---
---
---
---
---
---
---
---
---
Light Liquid PhaseCold Composite
Mass Flow (lb/hr)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Density (lb/ft3)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Mass Sp Heat (Btu/lb-F)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Viscosity (cP)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Thermal Cond (Btu/hr-ft-F)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Surface Tens (dyne/cm)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Molecular Wt
---
---
---
---
---
---
---
---
---
---
Sp Gravity
---
---
---
---
---
---
---
---
---
---
Pseudo Pc (psia)
---
---
---
---
---
---
---
---
---
---
Pseudo Tc (F)
-222.43-222.43-222.43-222.43-222.43-222.43-222.43-222.43-222.43-222.43
Pseudo Zc
---
---
---
---
---
---
---
---
---
---
Pseudo Omega
---
---
---
---
---
---
---
---
---
---
Aspen Technology Inc. Aspen HYSYS Version 8.4 (30.0.0.8433) Page 28 of 168
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
LNG: LNG-100 (GAS -METANO) (continued)PERFORMANCE TABLES
Cold Composite
Light Liquid PhaseCold Composite
Molecular Wt
---
---
---
---
---
---
---
---
---
---
Sp Gravity
---
---
---
---
---
---
---
---
---
---
Pseudo Pc (psia)
---
---
---
---
---
---
---
---
---
---
Pseudo Tc (F)
-222.43-222.43-222.43-222.43-222.43-222.43-222.43-222.43-222.43-222.43
Pseudo Zc
---
---
---
---
---
---
---
---
---
---
Pseudo Omega
---
---
---
---
---
---
---
---
---
---
Heavy Liquid PhaseCold Composite
Mass Flow (lb/hr)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Density (lb/ft3)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Mass Sp Heat (Btu/lb-F)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Viscosity (cP)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Thermal Cond (Btu/hr-ft-F)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Surface Tens (dyne/cm)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Molecular Wt
---
---
---
---
---
---
---
---
---
---
Sp Gravity
---
---
---
---
---
---
---
---
---
---
Pseudo Pc (psia)
---
---
---
---
---
---
---
---
---
---
Pseudo Tc (F)
-222.53-222.53-222.53-222.53-222.53-222.53-222.53-222.53-222.53-222.53
Pseudo Zc
---
---
---
---
---
---
---
---
---
---
Pseudo Omega
---
---
---
---
---
---
---
---
---
---
Aspen Technology Inc. Aspen HYSYS Version 8.4 (30.0.0.8433) Page 29 of 168
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
LNG: LNG-100 (GAS -METANO) (continued)PERFORMANCE TABLES
Cold Composite
Heavy Liquid PhaseCold Composite
Molecular Wt
---
---
---
---
---
---
---
---
---
---
Sp Gravity
---
---
---
---
---
---
---
---
---
---
Pseudo Pc (psia)
---
---
---
---
---
---
---
---
---
---
Pseudo Tc (F)
-222.53-222.53-222.53-222.53-222.53-222.53-222.53-222.53-222.53-222.53
Pseudo Zc
---
---
---
---
---
---
---
---
---
---
Pseudo Omega
---
---
---
---
---
---
---
---
---
---
Mixed LiquidCold Composite
Mass Flow (lb/hr)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Density (lb/ft3)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Mass Sp Heat (Btu/lb-F)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Viscosity (cP)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Thermal Cond (Btu/hr-ft-F)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Surface Tens (dyne/cm)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Molecular Wt
---
---
---
---
---
---
---
---
---
---
Sp Gravity
---
---
---
---
---
---
---
---
---
---
Pseudo Pc (psia)
---
---
---
---
---
---
---
---
---
---
Pseudo Tc (F)
-222.53-222.53-222.53-222.53-222.53-222.53-222.53-222.53-222.53-222.53
Pseudo Zc
---
---
---
---
---
---
---
---
---
---
Pseudo Omega
---
---
---
---
---
---
---
---
---
---
Aspen Technology Inc. Aspen HYSYS Version 8.4 (30.0.0.8433) Page 30 of 168
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585960616263
* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
LNG: LNG-100 (GAS -METANO) (continued)PERFORMANCE TABLES
Cold Composite
Mixed LiquidCold Composite
Molecular Wt
---
---
---
---
---
---
---
---
---
---
Sp Gravity
---
---
---
---
---
---
---
---
---
---
Pseudo Pc (psia)
---
---
---
---
---
---
---
---
---
---
Pseudo Tc (F)
-222.53-222.53-222.53-222.53-222.53-222.53-222.53-222.53-222.53-222.53
Pseudo Zc
---
---
---
---
---
---
---
---
---
---
Pseudo Omega
---
---
---
---
---
---
---
---
---
---
Hot Composite
Overall PhaseHot Composite
Temperature (F)
-222.26-221.89-221.88-221.35-221.34-220.42-220.40-218.12-218.06-205.02-204.55-162.01-160.18-140.07-102.68
-99.30-33.44-31.2834.36
100.00
Pressure (psia)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Heat Flow (Btu/hr)
0.001271299.401280117.692542598.792560235.373813898.193840353.065085197.585120470.746356496.986400588.437627796.387680706.128216766.198899095.778960823.80
10170395.1710210096.9011441694.5612712993.96
Enthalpy (Btu/lbmole)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
UA (Btu/F-hr)
---
---
---
---
---
---
---
---
Molar Vap Frac
---
---
---
---
---
---
---
---
Mass Vap Frac
0.00000.00000.00000.00000.00000.00000.00000.0000
Heat of Vap. (Btu/lbmole)
---
---
---
---
---
---
---
---
Delta Temp (F)
0.06410.54180.54511.18081.18972.21352.23514.6146
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
LNG: LNG-100 (GAS -METANO) (continued)PERFORMANCE TABLES
Hot Composite
Overall PhaseHot Composite
UA (Btu/F-hr)
---
---
---
---
---
---
---
---
---
---
---
---
Molar Vap Frac
---
---
---
---
---
---
---
---
---
---
---
---
Mass Vap Frac
0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000
Heat of Vap. (Btu/lbmole)
---
---
---
---
---
---
---
---
---
---
---
---
Delta Temp (F)
4.682017.824518.293460.936062.774282.9272
120.3631123.7501189.7116191.8765257.6183323.3610
Vapour PhaseHot Composite
Mass Flow (lb/hr)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Molecular Wt
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Density (lb/ft3)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Mass Sp Heat (Btu/lb-F)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Viscosity (cP)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Thermal Cond (Btu/hr-ft-F)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Std Gas Flow (MMSCFD)
---
---
---
---
---
---
---
---
Z Factor
---
---
---
---
---
---
---
---
Pseudo Pc (psia)
---
---
---
---
---
---
---
---
Pseudo Tc (F)
-221.89-221.89-221.89-221.89-221.89-221.89-221.89-221.89
Pseudo Zc
---
---
---
---
---
---
---
---
Pseudo Omega
---
---
---
---
---
---
---
---
Aspen Technology Inc. Aspen HYSYS Version 8.4 (30.0.0.8433) Page 32 of 168
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2829303132333435363738394041
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5657
585960616263
* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: Field
Date/Time: Tue Feb 11 18:18:29 2014
LNG: LNG-100 (GAS -METANO) (continued)PERFORMANCE TABLES
Hot Composite
Vapour PhaseHot Composite
Std Gas Flow (MMSCFD)
---
---
---
---
---
---
---
---
---
---
---
---
Z Factor
---
---
---
---
---
---
---
---
---
---
---
---
Pseudo Pc (psia)
---
---
---
---
---
---
---
---
---
---
---
---
Pseudo Tc (F)
-221.89-221.89-221.89-221.89-221.89-221.89-221.89-221.89-221.89-221.89-221.89-221.89
Pseudo Zc
---
---
---
---
---
---
---
---
---
---
---
---
Pseudo Omega
---
---
---
---
---
---
---
---
---
---
---
---
Light Liquid PhaseHot Composite
Mass Flow (lb/hr)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Density (lb/ft3)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Mass Sp Heat (Btu/lb-F)
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
---
Viscosity (cP)
---
---
---
---
---
---
---
---
---
---
---
---
---
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Thermal Cond (Btu/hr-ft-F)
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Surface Tens (dyne/cm)
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Molecular Wt
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Sp Gravity
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Pseudo Pc (psia)
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Pseudo Tc (F)
-221.88-221.88-221.88-221.88-221.88-221.88-221.88-221.88
Pseudo Zc
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Pseudo Omega
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Aspen Technology Inc. Aspen HYSYS Version 8.4 (30.0.0.8433) Page 33 of 168
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* Specified by user.Licensed to: LEGENDS
LEGENDSBurlington, MAUSA
Case Name: ejercicio-economizador prueba 2.hsc
Unit Set: F
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