Balance Materia Economizador

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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* Specified by user.Licensed to: LEGENDS



Unit Set: Field


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)

(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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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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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


---

---

1.191.191.191.191.191.191.191.191.19

Viscosity (cP)

---

---

0.130.130.130.130.130.130.130.130.13


---

---

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)

---

---

---

---

---


---

---

---

---

---

Viscosity (cP)

---

---

---

---

---


---

---

---

---

---


---

---

---

---

---


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Unit Set: Field


Air cooler: AC-100 (continued)PERFORMANCE TABLE

Heavy Liquid Phase

Mass Flow (lb/hr)

---

---

---

---

---

---

Density (lb/ft3)

---

---

---

---

---

---


---

---

---

---

---

---

Viscosity (cP)

---

---

---

---

---

---


---

---

---

---

---

---


---

---

---

---

---

---

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


---

---

1.191.191.191.191.191.191.191.191.19

Viscosity (cP)

---

---

0.130.130.130.130.130.130.130.130.13


---

---

0.280.280.280.280.280.280.280.280.28


---

---

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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Unit Set: Field


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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Unit Set: Field


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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Unit Set: Field


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)


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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Unit Set: Field


Workbook: Case (Main) (continued)Material Streams (continued) Fluid Pkg: All

NameVapour FractionTemperaturePressureMolar FlowMass FlowLiquid Volume FlowHeat Flow

(F)(psia)

(lbmole/hr)(lb/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


(F)(psia)

(lbmole/hr)(lb/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


(F)(psia)

(lbmole/hr)(lb/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


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


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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Unit Set: Field


Workbook: Case (Main) (continued)Compositions (continued) Fluid Pkg: All


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 *


11No 500.0 *


15No 500.0 *


19No 500.0 *


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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Unit Set: Field


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



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

Name 5 7 q100Aspen Technology Inc. Aspen HYSYS Version 8.4 (30.0.0.8433) Page 11 of 168

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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.





(Btu/lb)


(Btu/lb)

(Btu/lb)(psia)

(Cost/s)(ACFM)


(MMSCFD)(lb/ft3)

(USGPM)

(psia)

(Btu/lbmole)(cSt)



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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Unit Set: Field


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


(cP)(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


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


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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Unit Set: Field


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


Parameters


User Variables

RATING

Curves



Flow Limits



Surge Flow Rate --- Field Flow Rate 1.650e+004 ACFM Stone Wall Flow --- Compressor Volume 0.0000 ft3

Nozzle Paramaters



100.16400.00000.0000

110.16400.00000.0000

Inertia


WORKSHEET


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Unit Set: Field


Compressor: K-101 (continued)Conditions


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





(Btu/lb)


(Btu/lb)

(Btu/lb)(psia)

(Cost/s)(ACFM)


(MMSCFD)(lb/ft3)

(USGPM)

(psia)

(Btu/lbmole)(cSt)


(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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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)


(cP)(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


5.174e+0045.532e+0045.174e+0045.532e+004

7580


59671.0121.3281.243

---

---

Power/Torque


59670.00000.00005967


---

---

---

---

DYNAMICS



1.518e+0077580

201.6---

ActiveNot Active

ActiveNot Active


5.532e+0045.532e+0041.650e+004

---


No

Holdup Details

Phase

VapourLiquid

Aqueous


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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Unit Set: Field


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


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



Flow Limits




Nozzle Paramaters



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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Unit Set: Field


Compressor: K-102 (continued)Inertia


WORKSHEET

Conditions


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.





(Btu/lb)


(Btu/lb)

(Btu/lb)(psia)

(Cost/s)(ACFM)


(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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Unit Set: Field



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)



(cP)(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


913.6915.0913.6915.0

7575


130.71.0001.1921.130

---

---

Power/Torque


130.70.00000.0000130.7


---

---

---

---

DYNAMICS



3.326e+0057575

1.000---

ActiveNot Active

ActiveNot Active


915.0915.0

2.312e+004---


No

Holdup Details

Phase

Vapour


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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Unit Set: Field


Compressor: K-102 (continued)Phase

LiquidAqueous


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


Parameters


User Variables

RATING

Curves



Flow Limits




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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Unit Set: Field


Compressor: K-103 (continued)


180.16400.00000.0000

190.16400.00000.0000

Inertia


WORKSHEET

Conditions


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





(Btu/lb)


(Btu/lb)

(Btu/lb)(psia)

(Cost/s)(ACFM)


(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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Unit Set: Field



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)




(cP)(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


6.784e+0047.110e+0046.784e+0047.110e+004

7579


40931.0021.4061.292

---

---

Power/Torque


40930.00000.00004093


---

---

---

---

DYNAMICS



1.042e+0077579

99.03---

ActiveNot Active

ActiveNot Active


7.110e+0047.110e+0041.322e+004

---


NoAspen Technology Inc. Aspen HYSYS Version 8.4 (30.0.0.8433) Page 22 of 168

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Unit Set: Field


Compressor: K-103 (continued)Holdup Details

Phase

VapourLiquid

Aqueous


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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Unit Set: Field


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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Unit Set: Field


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)





(Btu/lb)


(Btu/lb)

(Btu/lb)(psia)

(Cost/s)(ACFM)


(MMSCFD)(lb/ft3)

(USGPM)

(psia)

(Btu/lbmole)(cSt)




(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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Unit Set: Field


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


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---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

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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Unit Set: Field


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


---

---

---

---

---

---

---

---

---

---

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)

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---


---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

Viscosity (cP)

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---


---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---


---

---

---

---

---

---

---

---

---

---

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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Unit Set: Field



Cold Composite

Vapour PhaseCold Composite


---

---

---

---

---

---

---

---

---

---

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)

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---


---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

Viscosity (cP)

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---


---

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---


---

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---

---

---

---

---

---

---

---

---

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

---

---

---

---

---

---

---

---

---

---


1

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34

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Unit Set: Field



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)

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---


---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

Viscosity (cP)

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---

---


---

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---


---

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---

---

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---

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---

---

---

---

---

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

---

---

---

---

---

---

---

---

---

---


1

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Unit Set: Field



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)

---

---

---

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---

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---

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---

---

---

---

---

---

---

---

---

---

Density (lb/ft3)

---

---

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---

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---

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---

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---

---

---

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---

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---

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---

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---

---

---

---

---

---

---

Viscosity (cP)

---

---

---

---

---

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---

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Molecular Wt

---

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---

---

---

---

---

---

---

---

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

---

---

---

---

---

---

---

---

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1

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Unit Set: Field



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

---

---

---

---

---

---

---

---

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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


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UA (Btu/F-hr)

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---

---

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---

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Molar Vap Frac

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---

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---

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---

Mass Vap Frac

0.00000.00000.00000.00000.00000.00000.00000.0000


---

---

---

---

---

---

---

---

Delta Temp (F)

0.06410.54180.54511.18081.18972.21352.23514.6146


1

2

34

5

67

891011

12

1314

15

1617

18192021

22

2324

25

2627

2829303132333435363738394041

42

4344

45

4647

48495051

52

5354

55

5657

585960616263




Unit Set: Field



Hot Composite

Overall PhaseHot Composite

UA (Btu/F-hr)

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---

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---

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Molar Vap Frac

---

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---

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---

Mass Vap Frac

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000


---

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---

---

---

---

---

---

---

---

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Delta Temp (F)

4.682017.824518.293460.936062.774282.9272

120.3631123.7501189.7116191.8765257.6183323.3610

Vapour PhaseHot Composite

Mass Flow (lb/hr)

---

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---

---

---

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Molecular Wt

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Density (lb/ft3)

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Viscosity (cP)

---

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---

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Z Factor

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Pseudo Pc (psia)

---

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---

---

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---

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Pseudo Tc (F)

-221.89-221.89-221.89-221.89-221.89-221.89-221.89-221.89

Pseudo Zc

---

---

---

---

---

---

---

---

Pseudo Omega

---

---

---

---

---

---

---

---


1

2

34

5

67

891011

12

1314

15

1617

18192021

22

2324

25

2627

2829303132333435363738394041

42

4344

45

4647

48495051

52

5354

55

5657

585960616263




Unit Set: Field



Hot Composite

Vapour PhaseHot Composite


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Z Factor

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Pseudo Pc (psia)

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---

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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

---

---

---

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Pseudo Omega

---

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Light Liquid PhaseHot Composite

Mass Flow (lb/hr)

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Density (lb/ft3)

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---

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Viscosity (cP)

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---

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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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---

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Pseudo Omega

---

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1

2

34

5

67

891011

12

1314

15

1617

18192021

22

2324

25

2627

2829303132333435363738394041

42

4344

45

4647

48495051

52

5354

55

5657

585960616263




Unit Set: F

Balance Materia Economizador

Documents

Transcript of Balance Materia Economizador