HYSYS-Report Ammonia Plant

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: INICIAL FEED GASFluid Package: Basis-1

Property Package: Peng-Robinson

CONDITIONS

Vapour / Phase FractionTemperature: (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)Liq Vol Flow @Std Cond (barrel/day)

Overall1.0000

120.0 *

834.9 *

43937.710e+004 *

1.669e+004-3.489e+004

36.77-1.533e+0087.092e+006 *

Vapour Phase1.0000

120.0834.94393

7.710e+0041.669e+004

-3.489e+00436.77

-1.533e+0087.092e+006

COMPOSITION

Overall Phase Vapour Fraction 1.0000

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

3999.8262 *

284.6789 *

1.2740 *

81.5816 *

25.8320 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

MOLE FRACTION

0.9105 *

0.0648 *

0.0003 *

0.0186 *

0.0059 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

MASS FLOW (lb/hr)

64168.8123 *

8560.2658 *

56.1807 *

3590.3813 *

723.6311 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

MASS FRACTION

0.8323 *

0.1110 *

0.0007 *

0.0466 *

0.0094 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

LIQUID VOLUMEFLOW (barrel/day)

14675.7115 *

1647.9438 *

7.5923 *

297.8712 *

61.4468 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

LIQUID VOLUMEFRACTION

0.8793 *

0.0987 *

0.0005 *

0.0178 *

0.0037 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

0.0000 *

Total 4393.1927 1.0000 77099.2712 1.0000 16690.5656 1.0000

Vapour Phase Phase Fraction 1.000

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

3999.8262284.6789

1.274081.581625.8320

0.00000.00000.00000.00000.00000.00000.00000.00000.0000

MOLE FRACTION

0.91050.06480.00030.01860.00590.00000.00000.00000.00000.00000.00000.00000.00000.0000

MASS FLOW (lb/hr)

64168.81238560.2658

56.18073590.3813

723.63110.00000.00000.00000.00000.00000.00000.00000.00000.0000

MASS FRACTION

0.83230.11100.00070.04660.00940.00000.00000.00000.00000.00000.00000.00000.00000.0000

LIQUID VOLUMEFLOW (barrel/day)

14675.71151647.9438

7.5923297.8712

61.44680.00000.00000.00000.00000.00000.00000.00000.00000.0000

LIQUID VOLUMEFRACTION

0.87930.09870.00050.01780.00370.00000.00000.00000.00000.00000.00000.00000.00000.0000

Total 4393.1927 1.0000 77099.2712 1.0000 16690.5656 1.0000

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63* Specified by user.Licensed to: LEGENDS

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: INICIAL FEED GAS (continueFluid Package: Basis-1

Property Package: Peng-Robinson

K VALUE

COMPONENTSMethane

EthanePropane

CO2Nitrogen

H2OMercury

HydrogenArgon

COS_Vapour

H2SOxygen

Ammonia

MIXED------------------------------------------

LIGHT------------------------------------------

HEAVY------------------------------------------

UNIT OPERATIONS

FEED TOSaturate with water: op-100

PRODUCT FROM LOGICAL CONNECTION

UTILITIES

( No utilities reference this stream )

PROCESS UTILITY

Material Stream: Water to hidratateFluid Package: Basis-1

Property Package: Peng-Robinson

CONDITIONS

Vapour / Phase FractionTemperature: (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)Liq Vol Flow @Std Cond (barrel/day)

Overall0.0000

120.0 *

834.9 *

2.197e-0043.380e-003 *

2.319e-004-1.222e+005

14.24-22.93

2.281e-004 *

Aqueous Phase1.0000

120.0834.9

1.876e-0043.380e-0032.319e-004

-1.222e+00514.24

-22.932.281e-004

COMPOSITION

Overall Phase Vapour Fraction 0.0000

COMPONENTS

MethaneEthanePropaneCO2Nitrogen

MOLAR FLOW (lbmole/hr)

0.00000.00000.00000.00000.0000

MOLE FRACTION

0.00000.00000.00000.00000.0000

MASS FLOW (lb/hr)

0.00000.00000.00000.00000.0000

MASS FRACTION

0.00000.00000.00000.00000.0000

LIQUID VOLUMEFLOW (barrel/day)

0.00000.00000.00000.00000.0000

LIQUID VOLUMEFRACTION

0.00000.00000.00000.00000.0000

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63* Specified by user.Licensed to: LEGENDS

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: Water to hidratate (continuedFluid Package: Basis-1

Property Package: Peng-Robinson

COMPOSITION

Overall Phase (continued) Vapour Fraction 0.0000

COMPONENTS

H2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

0.00020.00000.00000.00000.00000.00000.00000.00000.0000

MOLE FRACTION

1.00000.00000.00000.00000.00000.00000.00000.00000.0000

MASS FLOW (lb/hr)

0.00400.00000.00000.00000.00000.00000.00000.00000.0000

MASS FRACTION

1.00000.00000.00000.00000.00000.00000.00000.00000.0000

LIQUID VOLUMEFLOW (barrel/day)

0.00030.00000.00000.00000.00000.00000.00000.00000.0000

LIQUID VOLUMEFRACTION

1.00000.00000.00000.00000.00000.00000.00000.00000.0000

Total 0.0002 1.0000 0.0040 1.0000 0.0003 1.0000

Aqueous Phase Phase Fraction 1.000

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

0.00000.00000.00000.00000.00000.00020.00000.00000.00000.00000.00000.00000.00000.0000

MOLE FRACTION

0.00000.00000.00000.00000.00001.00000.00000.00000.00000.00000.00000.00000.00000.0000

MASS FLOW (lb/hr)

0.00000.00000.00000.00000.00000.00340.00000.00000.00000.00000.00000.00000.00000.0000

MASS FRACTION

0.00000.00000.00000.00000.00001.00000.00000.00000.00000.00000.00000.00000.00000.0000

LIQUID VOLUMEFLOW (barrel/day)

0.00000.00000.00000.00000.00000.00020.00000.00000.00000.00000.00000.00000.00000.0000

LIQUID VOLUMEFRACTION

0.00000.00000.00000.00000.00001.00000.00000.00000.00000.00000.00000.00000.00000.0000

Total 0.0002 1.0000 0.0034 1.0000 0.0002 1.0000

K VALUE

COMPONENTSMethane

EthanePropane

CO2Nitrogen

H2OMercury

HydrogenArgon

COS_Vapour

H2SOxygen

Ammonia

MIXED---------------

0.0000------------------------

LIGHT------------------------------------------

HEAVY---------------

0.0000------------------------

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63* Specified by user.Licensed to: LEGENDS

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: Water to hidratate (continuedFluid Package: Basis-1

Property Package: Peng-Robinson

UNIT OPERATIONS

FEED TOSaturate with water: op-100

PRODUCT FROM LOGICAL CONNECTION

UTILITIES

( No utilities reference this stream )

PROCESS UTILITY

Material Stream: HIDROTRATADOR PRODUCTFluid Package: Basis-1

Property Package: Peng-Robinson

CONDITIONS

Vapour / Phase FractionTemperature: (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)Liq Vol Flow @Std Cond (barrel/day)

Overall1.0000

699.8834.93460

6.001e+0041.298e+004

-2.709e+00444.68

-9.374e+0075.587e+006 *

Vapour Phase1.0000

699.8834.93460

6.001e+0041.298e+004

-2.709e+00444.68

-9.374e+0075.587e+006

Liquid Phase0.0000

699.8834.9

0.00000.00000.0000

-2.709e+00444.68

0.00000.0000

COMPOSITION

Overall Phase Vapour Fraction 1.0000

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

3062.4313217.9619

0.975462.462242.8000

0.00020.0000

68.85114.93950.00000.00120.00190.00000.0000

MOLE FRACTION

0.88500.06300.00030.01810.01240.00000.00000.01990.00140.00000.00000.00000.00000.0000

MASS FLOW (lb/hr)

49130.27976554.0913

43.01432748.94351198.9574

0.00300.0000

138.8038197.3237

0.00000.04000.06380.00000.0000

MASS FRACTION

0.81870.10920.00070.04580.02000.00000.00000.00230.00330.00000.00000.00000.00000.0000

LIQUID VOLUMEFLOW (barrel/day)

11236.32781261.7335

5.8130228.0625101.8088

0.00020.0000

136.04949.86100.00000.00150.00550.00000.0000

LIQUID VOLUMEFRACTION

0.86570.09720.00040.01760.00780.00000.00000.01050.00080.00000.00000.00000.00000.0000

Total 3460.4248 1.0000 60011.5204 1.0000 12979.6632 1.0000

Vapour Phase Phase Fraction 1.000

COMPONENTS

MethaneEthanePropane

MOLAR FLOW (lbmole/hr)

3062.4313217.9619

0.9754

MOLE FRACTION

0.88500.06300.0003

MASS FLOW (lb/hr)

49130.27976554.0913

43.0143

MASS FRACTION

0.81870.10920.0007

LIQUID VOLUMEFLOW (barrel/day)

11236.32781261.7335

5.8130

LIQUID VOLUMEFRACTION

0.86570.09720.0004

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63* Specified by user.Licensed to: LEGENDS

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: HIDROTRATADOR PRODUCTFluid Package: Basis-1

Property Package: Peng-Robinson

COMPOSITION

Vapour Phase (continued) Phase Fraction 1.000

COMPONENTS

CO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

62.462242.8000

0.00020.0000

68.85114.93950.00000.00120.00190.00000.0000

MOLE FRACTION

0.01810.01240.00000.00000.01990.00140.00000.00000.00000.00000.0000

MASS FLOW (lb/hr)

2748.94351198.9574

0.00300.0000

138.8038197.3237

0.00000.04000.06380.00000.0000

MASS FRACTION

0.04580.02000.00000.00000.00230.00330.00000.00000.00000.00000.0000

LIQUID VOLUMEFLOW (barrel/day)

228.0625101.8088

0.00020.0000

136.04949.86100.00000.00150.00550.00000.0000

LIQUID VOLUMEFRACTION

0.01760.00780.00000.00000.01050.00080.00000.00000.00000.00000.0000

Total 3460.4248 1.0000 60011.5204 1.0000 12979.6632 1.0000

Liquid Phase Phase Fraction 0.0000

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

MOLE FRACTION

0.88500.06300.00030.01810.01240.00000.00000.01990.00140.00000.00000.00000.00000.0000

MASS FLOW (lb/hr)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

MASS FRACTION

0.81870.10920.00070.04580.02000.00000.00000.00230.00330.00000.00000.00000.00000.0000

LIQUID VOLUMEFLOW (barrel/day)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

LIQUID VOLUMEFRACTION

0.86570.09720.00040.01760.00780.00000.00000.01050.00080.00000.00000.00000.00000.0000

Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000

K VALUE

COMPONENTSMethane

EthanePropane

CO2Nitrogen

H2OMercury

HydrogenArgon

COS_Vapour

H2SOxygen

Ammonia

MIXED1.0001.0001.0001.0001.0001.000

---1.0001.000

---1.0001.000

------

LIGHT1.0001.0001.0001.0001.0001.000

---1.0001.000

---1.0001.000

------

HEAVY------------------------------------------

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63* Specified by user.Licensed to: LEGENDS

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: HIDROTRATADOR PRODUCTFluid Package: Basis-1

Property Package: Peng-Robinson

UNIT OPERATIONS

FEED TOComponent Splitter: Desulfurizador

PRODUCT FROMConversion Reactor: Hidrotratador

LOGICAL CONNECTION

UTILITIES

( No utilities reference this stream )

PROCESS UTILITY

Material Stream: REF. PRIMARIO PRODUCTFluid Package: Basis-1

Property Package: Peng-Robinson

CONDITIONS

Vapour / Phase FractionTemperature: (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)Liq Vol Flow @Std Cond (barrel/day)

Overall1.0000

1344 *

583.21.733e+0042.341e+0053.457e+004

-4.472e+00441.60

-7.749e+0082.794e+007 *

Vapour Phase1.0000

1344583.2

1.733e+0042.341e+0053.457e+004

-4.472e+00441.60

-7.749e+0082.794e+007

Liquid Phase0.0000

1344583.2

0.00000.00000.0000

-4.472e+00441.60

0.00000.0000

COMPOSITION

Overall Phase Vapour Fraction 1.0000

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

1224.972587.1847

0.39021322.9235

42.80006304.8388

0.00007499.6712

4.9395840.3075

0.00120.00000.00000.0000

MOLE FRACTION

0.07070.00500.00000.07630.00250.36390.00000.43280.00030.04850.00000.00000.00000.0000

MASS FLOW (lb/hr)

19652.11192621.6365

17.205758221.4678

1198.9574113582.3036

0.000015119.3374

197.323723537.7706

0.04000.00000.00000.0000

MASS FRACTION

0.08390.01120.00010.24870.00510.48510.00000.06460.00080.10050.00000.00000.00000.0000

LIQUID VOLUMEFLOW (barrel/day)

4494.5311504.6934

2.32524830.2671

101.80887792.9966

0.000014819.3121

9.86102016.1646

0.00150.00000.00000.0000

LIQUID VOLUMEFRACTION

0.13000.01460.00010.13970.00290.22540.00000.42870.00030.05830.00000.00000.00000.0000

Total 17328.0292 1.0000 234148.1546 1.0000 34571.9615 1.0000

Vapour Phase Phase Fraction 1.000

COMPONENTS

MethaneEthanePropane

MOLAR FLOW (lbmole/hr)

1224.972587.1847

0.3902

MOLE FRACTION

0.07070.00500.0000

MASS FLOW (lb/hr)

19652.11192621.6365

17.2057

MASS FRACTION

0.08390.01120.0001

LIQUID VOLUMEFLOW (barrel/day)

4494.5311504.6934

2.3252

LIQUID VOLUMEFRACTION

0.13000.01460.0001

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63* Specified by user.Licensed to: LEGENDS

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: REF. PRIMARIO PRODUCT (cFluid Package: Basis-1

Property Package: Peng-Robinson

COMPOSITION

Vapour Phase (continued) Phase Fraction 1.000

COMPONENTS

CO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

1322.923542.8000

6304.83880.0000

7499.67124.9395

840.30750.00120.00000.00000.0000

MOLE FRACTION

0.07630.00250.36390.00000.43280.00030.04850.00000.00000.00000.0000

MASS FLOW (lb/hr)

58221.46781198.9574

113582.30360.0000

15119.3374197.3237

23537.77060.04000.00000.00000.0000

MASS FRACTION

0.24870.00510.48510.00000.06460.00080.10050.00000.00000.00000.0000

LIQUID VOLUMEFLOW (barrel/day)

4830.2671101.8088

7792.99660.0000

14819.31219.8610

2016.16460.00150.00000.00000.0000

LIQUID VOLUMEFRACTION

0.13970.00290.22540.00000.42870.00030.05830.00000.00000.00000.0000

Total 17328.0292 1.0000 234148.1546 1.0000 34571.9615 1.0000

Liquid Phase Phase Fraction 0.0000

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

MOLE FRACTION

0.07070.00500.00000.07630.00250.36390.00000.43280.00030.04850.00000.00000.00000.0000

MASS FLOW (lb/hr)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

MASS FRACTION

0.08390.01120.00010.24870.00510.48510.00000.06460.00080.10050.00000.00000.00000.0000

LIQUID VOLUMEFLOW (barrel/day)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

LIQUID VOLUMEFRACTION

0.13000.01460.00010.13970.00290.22540.00000.42870.00030.05830.00000.00000.00000.0000

Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000

K VALUE

COMPONENTSMethane

EthanePropane

CO2Nitrogen

H2OMercury

HydrogenArgon

COS_Vapour

H2SOxygen

Ammonia

MIXED1.0001.0001.0001.0001.0001.000

---1.0001.0001.0001.000

---------

LIGHT1.0001.0001.0001.0001.0001.000

---1.0001.0001.0001.000

---------

HEAVY------------------------------------------

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63* Specified by user.Licensed to: LEGENDS

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: REF. PRIMARIO PRODUCT (cFluid Package: Basis-1

Property Package: Peng-Robinson

UNIT OPERATIONS

FEED TOMixer: MIX-103

PRODUCT FROMConversion Reactor: Reformado Primario

LOGICAL CONNECTION

UTILITIES

( No utilities reference this stream )

PROCESS UTILITY

Material Stream: REF. SECUNDARIO PRODUCFluid Package: Basis-1

Property Package: Peng-Robinson

CONDITIONS

Vapour / Phase FractionTemperature: (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)Liq Vol Flow @Std Cond (barrel/day)

Overall1.0000

1645 *

571.82.643e+0044.257e+0055.383e+004

-2.390e+00441.00

-6.317e+0084.269e+007 *

Vapour Phase1.0000

1645571.8

2.643e+0044.257e+0055.383e+004

-2.390e+00441.00

-6.317e+0084.269e+007

Liquid Phase0.0000

1645571.8

0.00000.00000.0000

-2.390e+00441.00

0.00000.0000

COMPOSITION

Overall Phase Vapour Fraction 1.0000

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

0.00000.00000.3902

1745.20615145.14485570.0496

0.000011190.7099

11.08221819.8469

0.00120.0000

949.23070.0000

MOLE FRACTION

0.00000.00000.00000.06600.19470.21070.00000.42340.00040.06890.00000.00000.03590.0000

MASS FLOW (lb/hr)

0.00000.0000

17.205776805.9982

144130.9432100345.0028

0.000022560.4715

442.711550975.5515

0.04000.0000

30375.38320.0000

MASS FRACTION

0.00000.00000.00000.18040.33860.23570.00000.05300.00100.11980.00000.00000.07140.0000

LIQUID VOLUMEFLOW (barrel/day)

0.00000.00002.3252

6372.108212238.8038

6884.77200.0000

22112.785822.1239

4366.39060.00150.0000

1828.18400.0000

LIQUID VOLUMEFRACTION

0.00000.00000.00000.11840.22740.12790.00000.41080.00040.08110.00000.00000.03400.0000

Total 26431.6616 1.0000 425653.3076 1.0000 53827.4950 1.0000

Vapour Phase Phase Fraction 1.000

COMPONENTS

MethaneEthanePropane

MOLAR FLOW (lbmole/hr)

0.00000.00000.3902

MOLE FRACTION

0.00000.00000.0000

MASS FLOW (lb/hr)

0.00000.0000

17.2057

MASS FRACTION

0.00000.00000.0000

LIQUID VOLUMEFLOW (barrel/day)

0.00000.00002.3252

LIQUID VOLUMEFRACTION

0.00000.00000.0000

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63* Specified by user.Licensed to: LEGENDS

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: REF. SECUNDARIO PRODUCFluid Package: Basis-1

Property Package: Peng-Robinson

COMPOSITION

Vapour Phase (continued) Phase Fraction 1.000

COMPONENTS

CO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

1745.20615145.14485570.0496

0.000011190.7099

11.08221819.8469

0.00120.0000

949.23070.0000

MOLE FRACTION

0.06600.19470.21070.00000.42340.00040.06890.00000.00000.03590.0000

MASS FLOW (lb/hr)

76805.9982144130.9432100345.0028

0.000022560.4715

442.711550975.5515

0.04000.0000

30375.38320.0000

MASS FRACTION

0.18040.33860.23570.00000.05300.00100.11980.00000.00000.07140.0000

LIQUID VOLUMEFLOW (barrel/day)

6372.108212238.8038

6884.77200.0000

22112.785822.1239

4366.39060.00150.0000

1828.18400.0000

LIQUID VOLUMEFRACTION

0.11840.22740.12790.00000.41080.00040.08110.00000.00000.03400.0000

Total 26431.6616 1.0000 425653.3076 1.0000 53827.4950 1.0000

Liquid Phase Phase Fraction 0.0000

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

MOLE FRACTION

0.00000.00000.00000.06600.19470.21070.00000.42340.00040.06890.00000.00000.03590.0000

MASS FLOW (lb/hr)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

MASS FRACTION

0.00000.00000.00000.18040.33860.23570.00000.05300.00100.11980.00000.00000.07140.0000

LIQUID VOLUMEFLOW (barrel/day)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

LIQUID VOLUMEFRACTION

0.00000.00000.00000.11840.22740.12790.00000.41080.00040.08110.00000.00000.03400.0000

Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000

K VALUE

COMPONENTSMethane

EthanePropane

CO2Nitrogen

H2OMercury

HydrogenArgon

COS_Vapour

H2SOxygen

Ammonia

MIXED------

1.0001.0001.0001.000

---1.0001.0001.0001.000

---1.000

---

LIGHT------

1.0001.0001.0001.000

---1.0001.0001.0001.000

---1.000

---

HEAVY------------------------------------------

Aspen Technology Inc. Aspen HYSYS Version 8.4 (30.0.0.8433) Page 9 of 21

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63* Specified by user.Licensed to: LEGENDS

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: REF. SECUNDARIO PRODUCFluid Package: Basis-1

Property Package: Peng-Robinson

UNIT OPERATIONS

FEED TOLNG: LNG-100

PRODUCT FROMConversion Reactor: Reformado Secundario

LOGICAL CONNECTION

UTILITIES

( No utilities reference this stream )

PROCESS UTILITY

Material Stream: HTS PRODUCTFluid Package: Basis-1

Property Package: Peng-Robinson

CONDITIONS

Vapour / Phase FractionTemperature: (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)Liq Vol Flow @Std Cond (barrel/day)

Overall1.0000

415.6571.8

2.643e+0044.257e+0055.491e+004

-3.431e+00433.66

-9.069e+0084.270e+007 *

Vapour Phase1.0000

415.6571.8

2.643e+0044.257e+0055.491e+004

-3.431e+00433.66

-9.069e+0084.270e+007

Aqueous Phase0.0000

415.6571.8

0.00000.00000.0000

-1.161e+00522.35

0.00000.0000

COMPOSITION

Overall Phase Vapour Fraction 1.0000

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

0.00000.00000.3902

2291.16025145.14485024.0955

0.000011736.6640

11.08221273.8929

0.00120.0000

949.23070.0000

MOLE FRACTION

0.00000.00000.00000.08670.19470.19010.00000.44400.00040.04820.00000.00000.03590.0000

MASS FLOW (lb/hr)

0.00000.0000

17.2057100833.2740144130.9432

90509.58520.0000

23661.1150442.7115

35682.88600.04000.0000

30375.38320.0000

MASS FRACTION

0.00000.00000.00000.23690.33860.21260.00000.05560.00100.08380.00000.00000.07140.0000

LIQUID VOLUMEFLOW (barrel/day)

0.00000.00002.3252

8365.499312238.8038

6209.95410.0000

23191.588322.1239

3056.47340.00150.0000

1828.18400.0000

LIQUID VOLUMEFRACTION

0.00000.00000.00000.15230.22290.11310.00000.42230.00040.05570.00000.00000.03330.0000

Total 26431.6616 1.0000 425653.1438 1.0000 54914.9535 1.0000

Vapour Phase Phase Fraction 1.000

COMPONENTS

MethaneEthanePropane

MOLAR FLOW (lbmole/hr)

0.00000.00000.3902

MOLE FRACTION

0.00000.00000.0000

MASS FLOW (lb/hr)

0.00000.0000

17.2057

MASS FRACTION

0.00000.00000.0000

LIQUID VOLUMEFLOW (barrel/day)

0.00000.00002.3252

LIQUID VOLUMEFRACTION

0.00000.00000.0000

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63* Specified by user.Licensed to: LEGENDS

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: HTS PRODUCT (continued)Fluid Package: Basis-1

Property Package: Peng-Robinson

COMPOSITION

Vapour Phase (continued) Phase Fraction 1.000

COMPONENTS

CO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

2291.16025145.14485024.0955

0.000011736.6640

11.08221273.8929

0.00120.0000

949.23070.0000

MOLE FRACTION

0.08670.19470.19010.00000.44400.00040.04820.00000.00000.03590.0000

MASS FLOW (lb/hr)

100833.2740144130.9432

90509.58520.0000

23661.1150442.7115

35682.88600.04000.0000

30375.38320.0000

MASS FRACTION

0.23690.33860.21260.00000.05560.00100.08380.00000.00000.07140.0000

LIQUID VOLUMEFLOW (barrel/day)

8365.499312238.8038

6209.95410.0000

23191.588322.1239

3056.47340.00150.0000

1828.18400.0000

LIQUID VOLUMEFRACTION

0.15230.22290.11310.00000.42230.00040.05570.00000.00000.03330.0000

Total 26431.6616 1.0000 425653.1438 1.0000 54914.9535 1.0000

Aqueous Phase Phase Fraction 0.0000

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

MOLE FRACTION

0.00000.00000.00000.00150.00040.99510.00000.00200.00000.00020.00060.00000.00020.0000

MASS FLOW (lb/hr)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

MASS FRACTION

0.00000.00000.00000.00360.00070.99380.00000.00020.00000.00030.00110.00000.00040.0000

LIQUID VOLUMEFLOW (barrel/day)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

LIQUID VOLUMEFRACTION

0.00000.00000.00000.00430.00080.99040.00000.00310.00000.00030.00060.00000.00040.0000

Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000

K VALUE

COMPONENTSMethane

EthanePropane

CO2Nitrogen

H2OMercury

HydrogenArgon

COS_Vapour

H2SOxygen

Ammonia

MIXED------

2.236e+00458.60455.4

0.1910---

226.1665.9289.9

7.818e-005---

150.0---

LIGHT------------------------------------------

HEAVY------

2.236e+00458.60455.4

0.1910---

226.1665.9289.9

7.818e-005---

150.0---

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63* Specified by user.Licensed to: LEGENDS

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: HTS PRODUCT (continued)Fluid Package: Basis-1

Property Package: Peng-Robinson

UNIT OPERATIONS

FEED TOCooler: E-102

PRODUCT FROMConversion Reactor: HTS Converter

LOGICAL CONNECTION

UTILITIES

( No utilities reference this stream )

PROCESS UTILITY

Material Stream: LTS PRODUCTFluid Package: Basis-1

Property Package: Peng-Robinson

CONDITIONS

Vapour / Phase FractionTemperature: (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)Liq Vol Flow @Std Cond (barrel/day)

Overall1.0000

513.2550.4

2.643e+0044.257e+0055.745e+004

-3.435e+00433.92

-9.079e+0084.272e+007 *

Vapour Phase1.0000

513.2550.4

2.643e+0044.257e+0055.745e+004

-3.435e+00433.92

-9.079e+0084.272e+007

Aqueous Phase0.0000

513.2550.4

0.00000.00000.0000

-1.122e+00525.33

0.00000.0000

COMPOSITION

Overall Phase Vapour Fraction 1.0000

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

0.00000.00000.3902

3565.05305145.14483750.2026

0.000013010.5568

11.08220.00000.00120.0000

949.23070.0000

MOLE FRACTION

0.00000.00000.00000.13490.19470.14190.00000.49220.00040.00000.00000.00000.03590.0000

MASS FLOW (lb/hr)

0.00000.0000

17.2057156896.9174144130.9432

67560.27740.0000

26229.2830442.7115

0.00000.04000.0000

30375.38320.0000

MASS FRACTION

0.00000.00000.00000.36860.33860.15870.00000.06160.00100.00000.00000.00000.07140.0000

LIQUID VOLUMEFLOW (barrel/day)

0.00000.00002.3252

13016.745412238.8038

4635.37890.0000

25708.794022.1239

0.00000.00150.0000

1828.18400.0000

LIQUID VOLUMEFRACTION

0.00000.00000.00000.22660.21300.08070.00000.44750.00040.00000.00000.00000.03180.0000

Total 26431.6616 1.0000 425652.7614 1.0000 57452.3568 1.0000

Vapour Phase Phase Fraction 1.000

COMPONENTS

MethaneEthanePropane

MOLAR FLOW (lbmole/hr)

0.00000.00000.3902

MOLE FRACTION

0.00000.00000.0000

MASS FLOW (lb/hr)

0.00000.0000

17.2057

MASS FRACTION

0.00000.00000.0000

LIQUID VOLUMEFLOW (barrel/day)

0.00000.00002.3252

LIQUID VOLUMEFRACTION

0.00000.00000.0000

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63* Specified by user.Licensed to: LEGENDS

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: LTS PRODUCT (continued)Fluid Package: Basis-1

Property Package: Peng-Robinson

COMPOSITION

Vapour Phase (continued) Phase Fraction 1.000

COMPONENTS

CO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

3565.05305145.14483750.2026

0.000013010.5568

11.08220.00000.00120.0000

949.23070.0000

MOLE FRACTION

0.13490.19470.14190.00000.49220.00040.00000.00000.00000.03590.0000

MASS FLOW (lb/hr)

156896.9174144130.9432

67560.27740.0000

26229.2830442.7115

0.00000.04000.0000

30375.38320.0000

MASS FRACTION

0.36860.33860.15870.00000.06160.00100.00000.00000.00000.07140.0000

LIQUID VOLUMEFLOW (barrel/day)

13016.745412238.8038

4635.37890.0000

25708.794022.1239

0.00000.00150.0000

1828.18400.0000

LIQUID VOLUMEFRACTION

0.22660.21300.08070.00000.44750.00040.00000.00000.00000.03180.0000

Total 26431.6616 1.0000 425652.7614 1.0000 57452.3568 1.0000

Aqueous Phase Phase Fraction 0.0000

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

MOLE FRACTION

0.00000.00000.00000.00980.00270.97210.00000.01350.00000.00000.00040.00000.00140.0000

MASS FLOW (lb/hr)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

MASS FRACTION

0.00000.00000.00000.02390.00420.96710.00000.00150.00000.00000.00070.00000.00250.0000

LIQUID VOLUMEFLOW (barrel/day)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

LIQUID VOLUMEFRACTION

0.00000.00000.00000.02820.00510.94320.00000.02090.00000.00000.00040.00000.00210.0000

Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000

K VALUE

COMPONENTSMethane

EthanePropane

CO2Nitrogen

H2OMercury

HydrogenArgon

COS_Vapour

H2SOxygen

Ammonia

MIXED------

727.113.7071.03

0.1460---

36.4777.16

---1.162e-004

---25.46

---

LIGHT------------------------------------------

HEAVY------

727.113.7071.03

0.1460---

36.4777.16

---1.162e-004

---25.46

---

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63* Specified by user.Licensed to: LEGENDS

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: LTS PRODUCT (continued)Fluid Package: Basis-1

Property Package: Peng-Robinson

UNIT OPERATIONS

FEED TOCooler: E-103

PRODUCT FROMConversion Reactor: LTS Converter

LOGICAL CONNECTION

UTILITIES

( No utilities reference this stream )

PROCESS UTILITY

Material Stream: METHANATOR PRODUCTFluid Package: Basis-1

Property Package: Peng-Robinson

CONDITIONS

Vapour / Phase FractionTemperature: (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)Liq Vol Flow @Std Cond (barrel/day)

Overall1.0000

706.1530.5

1.799e+0041.786e+0053.766e+004

206331.27

3.712e+0072.912e+007 *

Vapour Phase1.0000

706.1530.5

1.799e+0041.786e+0053.766e+004

206331.27

3.712e+0072.912e+007

Liquid Phase0.0000

706.1530.5

0.00000.00000.0000

206331.27

0.00000.0000

COMPOSITION

Overall Phase Vapour Fraction 1.0000

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

178.04610.00000.39020.0000

5144.9065356.0921

0.000012298.1095

11.08220.00000.00000.00000.00000.0000

MOLE FRACTION

0.00990.00000.00000.00000.28600.01980.00000.68370.00060.00000.00000.00000.00000.0000

MASS FLOW (lb/hr)

2856.37520.0000

17.20570.0000

144124.26816415.0355

0.000024792.9892

442.71070.00000.00000.00000.00000.0000

MASS FRACTION

0.01600.00000.00010.00000.80670.03590.00000.13880.00250.00000.00000.00000.00000.0000

LIQUID VOLUMEFLOW (barrel/day)

653.26660.00002.32520.0000

12238.2370440.1421

0.000024301.0018

22.12380.00000.00000.00000.00000.0000

LIQUID VOLUMEFRACTION

0.01730.00000.00010.00000.32500.01170.00000.64530.00060.00000.00000.00000.00000.0000

Total 17988.6266 1.0000 178648.5846 1.0000 37657.0965 1.0000

Vapour Phase Phase Fraction 1.000

COMPONENTS

MethaneEthanePropane

MOLAR FLOW (lbmole/hr)

178.04610.00000.3902

MOLE FRACTION

0.00990.00000.0000

MASS FLOW (lb/hr)

2856.37520.0000

17.2057

MASS FRACTION

0.01600.00000.0001

LIQUID VOLUMEFLOW (barrel/day)

653.26660.00002.3252

LIQUID VOLUMEFRACTION

0.01730.00000.0001

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63* Specified by user.Licensed to: LEGENDS

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: METHANATOR PRODUCT (cFluid Package: Basis-1

Property Package: Peng-Robinson

COMPOSITION

Vapour Phase (continued) Phase Fraction 1.000

COMPONENTS

CO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

0.00005144.9065

356.09210.0000

12298.109511.0822

0.00000.00000.00000.00000.0000

MOLE FRACTION

0.00000.28600.01980.00000.68370.00060.00000.00000.00000.00000.0000

MASS FLOW (lb/hr)

0.0000144124.2681

6415.03550.0000

24792.9892442.7107

0.00000.00000.00000.00000.0000

MASS FRACTION

0.00000.80670.03590.00000.13880.00250.00000.00000.00000.00000.0000

LIQUID VOLUMEFLOW (barrel/day)

0.000012238.2370

440.14210.0000

24301.001822.1238

0.00000.00000.00000.00000.0000

LIQUID VOLUMEFRACTION

0.00000.32500.01170.00000.64530.00060.00000.00000.00000.00000.0000

Total 17988.6266 1.0000 178648.5846 1.0000 37657.0965 1.0000

Liquid Phase Phase Fraction 0.0000

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

MOLE FRACTION

0.00990.00000.00000.00000.28600.01980.00000.68370.00060.00000.00000.00000.00000.0000

MASS FLOW (lb/hr)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

MASS FRACTION

0.01600.00000.00010.00000.80670.03590.00000.13880.00250.00000.00000.00000.00000.0000

LIQUID VOLUMEFLOW (barrel/day)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

LIQUID VOLUMEFRACTION

0.01730.00000.00010.00000.32500.01170.00000.64530.00060.00000.00000.00000.00000.0000

Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000

K VALUE

COMPONENTSMethane

EthanePropane

CO2Nitrogen

H2OMercury

HydrogenArgon

COS_Vapour

H2SOxygen

Ammonia

MIXED1.000

---1.000

---1.0001.000

---1.0001.000

---------------

LIGHT1.000

---1.000

---1.0001.000

---1.0001.000

---------------

HEAVY------------------------------------------

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63* Specified by user.Licensed to: LEGENDS

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: METHANATOR PRODUCT (cFluid Package: Basis-1

Property Package: Peng-Robinson

UNIT OPERATIONS

FEED TOLNG: LNG-101

PRODUCT FROMConversion Reactor: METHANATOR

LOGICAL CONNECTION

UTILITIES

( No utilities reference this stream )

PROCESS UTILITY

Material Stream: PURIFIER FINAL STREAMFluid Package: Basis-1

Property Package: Peng-Robinson

CONDITIONS

Vapour / Phase FractionTemperature: (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)Liq Vol Flow @Std Cond (barrel/day)

Overall1.0000-8.60750.00

1.763e+0041.722e+0053.721e+004

-914.328.96

-1.612e+0072.855e+007 *

Vapour Phase1.0000-8.60750.00

1.763e+0041.722e+0053.721e+004

-914.328.96

-1.612e+0072.855e+007

COMPOSITION

Overall Phase Vapour Fraction 1.0000

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

177.98690.00000.00410.0000

5144.81850.00000.0000

12298.104111.0817

0.00000.00000.00000.00000.0000

MOLE FRACTION

0.01010.00000.00000.00000.29180.00000.00000.69750.00060.00000.00000.00000.00000.0000

MASS FLOW (lb/hr)

2855.42530.00000.18290.0000

144121.80400.00000.0000

24792.9782442.6905

0.00000.00000.00000.00000.0000

MASS FRACTION

0.01660.00000.00000.00000.83690.00000.00000.14400.00260.00000.00000.00000.00000.0000

LIQUID VOLUMEFLOW (barrel/day)

653.04930.00000.02470.0000

12238.02780.00000.0000

24300.991022.1228

0.00000.00000.00000.00000.0000

LIQUID VOLUMEFRACTION

0.01750.00000.00000.00000.32890.00000.00000.65300.00060.00000.00000.00000.00000.0000

Total 17631.9953 1.0000 172213.0810 1.0000 37214.2157 1.0000

Vapour Phase Phase Fraction 1.000

COMPONENTS

MethaneEthanePropane

MOLAR FLOW (lbmole/hr)

177.98690.00000.0041

MOLE FRACTION

0.01010.00000.0000

MASS FLOW (lb/hr)

2855.42530.00000.1829

MASS FRACTION

0.01660.00000.0000

LIQUID VOLUMEFLOW (barrel/day)

653.04930.00000.0247

LIQUID VOLUMEFRACTION

0.01750.00000.0000

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63* Specified by user.Licensed to: LEGENDS

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: PURIFIER FINAL STREAM (cFluid Package: Basis-1

Property Package: Peng-Robinson

COMPOSITION

Vapour Phase (continued) Phase Fraction 1.000

COMPONENTS

CO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

0.00005144.8185

0.00000.0000

12298.104111.0817

0.00000.00000.00000.00000.0000

MOLE FRACTION

0.00000.29180.00000.00000.69750.00060.00000.00000.00000.00000.0000

MASS FLOW (lb/hr)

0.0000144121.8040

0.00000.0000

24792.9782442.6905

0.00000.00000.00000.00000.0000

MASS FRACTION

0.00000.83690.00000.00000.14400.00260.00000.00000.00000.00000.0000

LIQUID VOLUMEFLOW (barrel/day)

0.000012238.0278

0.00000.0000

24300.991022.1228

0.00000.00000.00000.00000.0000

LIQUID VOLUMEFRACTION

0.00000.32890.00000.00000.65300.00060.00000.00000.00000.00000.0000

Total 17631.9953 1.0000 172213.0810 1.0000 37214.2157 1.0000

K VALUE

COMPONENTSMethane

EthanePropane

CO2Nitrogen

H2OMercury

HydrogenArgon

COS_Vapour

H2SOxygen

Ammonia

MIXED------------------------------------------

LIGHT------------------------------------------

HEAVY------------------------------------------

UNIT OPERATIONS

FEED TOCompressor: K-101

PRODUCT FROMLNG: LNG-103

LOGICAL CONNECTION

UTILITIES

( No utilities reference this stream )

PROCESS UTILITY

Material Stream: AMMONIA CONVERTER PROFluid Package: Basis-1

Property Package: Peng-Robinson

CONDITIONS

Vapour / Phase FractionTemperature: (F)Pressure: (psia)

Overall1.0000

784.32247

Vapour Phase1.0000

784.32247

Liquid Phase0.0000

784.32247

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63* Specified by user.Licensed to: LEGENDS

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: AMMONIA CONVERTER PROFluid Package: Basis-1

Property Package: Peng-Robinson

CONDITIONS

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)Liq Vol Flow @Std Cond (barrel/day)

Overall4.552e+0041.142e+0061.091e+005

-599.735.07

-2.730e+0077.358e+007 *

Vapour Phase4.552e+0041.142e+0061.091e+005

-599.735.07

-2.730e+0077.358e+007

Liquid Phase0.00000.00000.0000-598.735.07

0.00000.0000

COMPOSITION

Overall Phase Vapour Fraction 1.0000

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

3778.05630.00000.01980.0000

33362.74860.00000.0000

-0.0000175.5354

0.00000.00000.00000.0000

8198.7360

MOLE FRACTION

0.08300.00000.00000.00000.73300.00000.0000

-0.00000.00390.00000.00000.00000.00000.1801

MASS FLOW (lb/hr)

60610.97960.00000.87470.0000

934590.69380.00000.0000

-0.00007012.2902

0.00000.00000.00000.0000

139624.4805

MASS FRACTION

0.05310.00000.00000.00000.81850.00000.0000

-0.00000.00610.00000.00000.00000.00000.1223

LIQUID VOLUMEFLOW (barrel/day)

13862.01830.00000.11820.0000

79360.28120.00000.0000

-0.0000350.4294

0.00000.00000.00000.0000

15518.5014

LIQUID VOLUMEFRACTION

0.12710.00000.00000.00000.72750.00000.0000

-0.00000.00320.00000.00000.00000.00000.1423

Total 45515.0963 1.0000 1.141839319e+06 1.0000 109091.3485 1.0000

Vapour Phase Phase Fraction 1.000

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

3778.05630.00000.01980.0000

33362.74860.00000.0000

-0.0000175.5354

0.00000.00000.00000.0000

8198.7360

MOLE FRACTION

0.08300.00000.00000.00000.73300.00000.0000

-0.00000.00390.00000.00000.00000.00000.1801

MASS FLOW (lb/hr)

60610.97960.00000.87470.0000

934590.69380.00000.0000

-0.00007012.2902

0.00000.00000.00000.0000

139624.4805

MASS FRACTION

0.05310.00000.00000.00000.81850.00000.0000

-0.00000.00610.00000.00000.00000.00000.1223

LIQUID VOLUMEFLOW (barrel/day)

13862.01830.00000.11820.0000

79360.28120.00000.0000

-0.0000350.4294

0.00000.00000.00000.0000

15518.5014

LIQUID VOLUMEFRACTION

0.12710.00000.00000.00000.72750.00000.0000

-0.00000.00320.00000.00000.00000.00000.1423

Total 45515.0963 1.0000 1.141839319e+06 1.0000 109091.3485 1.0000

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63* Specified by user.Licensed to: LEGENDS

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: AMMONIA CONVERTER PROFluid Package: Basis-1

Property Package: Peng-Robinson

COMPOSITION

Liquid Phase Phase Fraction 0.0000

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

MOLE FRACTION

0.08300.00000.00000.00000.73310.00000.00000.00000.00390.00000.00000.00000.00000.1801

MASS FLOW (lb/hr)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

MASS FRACTION

0.05310.00000.00000.00000.81850.00000.00000.00000.00610.00000.00000.00000.00000.1222

LIQUID VOLUMEFLOW (barrel/day)

0.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.00000.0000

LIQUID VOLUMEFRACTION

0.12710.00000.00000.00000.72750.00000.00000.00000.00320.00000.00000.00000.00000.1422

Total 0.0000 1.0000 0.0000 1.0000 0.0000 1.0000

K VALUE

COMPONENTSMethane

EthanePropane

CO2Nitrogen

H2OMercury

HydrogenArgon

COS_Vapour

H2SOxygen

Ammonia

MIXED1.000

---1.000

---0.9999

---------

1.000------------

1.000

LIGHT1.000

---1.000

---0.9999

---------

1.000------------

1.000

HEAVY------------------------------------------

UNIT OPERATIONS

FEED TOLNG: LNG-106

PRODUCT FROMConversion Reactor: AMMONIA CONVERTER

LOGICAL CONNECTION

UTILITIES

( No utilities reference this stream )

PROCESS UTILITY

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63* Specified by user.Licensed to: LEGENDS

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: 1200 MTD WARM NH3 TO URFluid Package: Basis-1

Property Package: Peng-Robinson

CONDITIONS

Vapour / Phase FractionTemperature: (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)Liq Vol Flow @Std Cond (barrel/day)

Overall0.0022

98.60 *

312.92937

5.006e+0045594

-2.826e+00420.43

-8.301e+0075633 *

Vapour Phase0.0022

98.60312.96.484118.014.84

-2.025e+00436.17

-1.313e+00518.24

Liquid Phase0.9978

98.60312.92931

4.994e+0045579

-2.828e+00420.39

-8.288e+0075617

COMPOSITION

Overall Phase Vapour Fraction 0.0022

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

19.06100.00000.00150.00001.57860.00000.00000.00001.95030.00000.00000.00000.0000

2914.4086

MOLE FRACTION

0.00650.00000.00000.00000.00050.00000.00000.00000.00070.00000.00000.00000.00000.9923

MASS FLOW (lb/hr)

305.79440.00000.06720.0000

44.22080.00000.00000.0000

77.90910.00000.00000.00000.0000

49632.3803

MASS FRACTION

0.00610.00000.00000.00000.00090.00000.00000.00000.00160.00000.00000.00000.00000.9915

LIQUID VOLUMEFLOW (barrel/day)

69.93660.00000.00910.00003.75500.00000.00000.00003.89340.00000.00000.00000.0000

5516.3690

LIQUID VOLUMEFRACTION

0.01250.00000.00000.00000.00070.00000.00000.00000.00070.00000.00000.00000.00000.9861

Total 2937.0000 1.0000 50060.3718 1.0000 5593.9631 1.0000

Vapour Phase Phase Fraction 2.208e-003

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

1.27980.00000.00000.00000.58240.00000.00000.00000.10570.00000.00000.00000.00004.5157

MOLE FRACTION

0.19740.00000.00000.00000.08980.00000.00000.00000.01630.00000.00000.00000.00000.6965

MASS FLOW (lb/hr)

20.53090.00000.00030.0000

16.31580.00000.00000.00004.22170.00000.00000.00000.0000

76.9027

MASS FRACTION

0.17400.00000.00000.00000.13830.00000.00000.00000.03580.00000.00000.00000.00000.6519

LIQUID VOLUMEFLOW (barrel/day)

4.69550.00000.00000.00001.38540.00000.00000.00000.21100.00000.00000.00000.00008.5473

LIQUID VOLUMEFRACTION

0.31640.00000.00000.00000.09340.00000.00000.00000.01420.00000.00000.00000.00000.5760

Total 6.4836 1.0000 117.9714 1.0000 14.8393 1.0000

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63* Specified by user.Licensed to: LEGENDS

LEGENDSBurlington, MAUSA

Case Name: Amoniaco Final.hsc

Unit Set: Field

Date/Time: Wed May 20 07:02:54 2015

Material Stream: 1200 MTD WARM NH3 TO URFluid Package: Basis-1

Property Package: Peng-Robinson

COMPOSITION

Liquid Phase Phase Fraction 0.9978

COMPONENTS

MethaneEthanePropaneCO2NitrogenH2OMercuryHydrogenArgonCOS_VapourH2SOxygenAmmonia

MOLAR FLOW (lbmole/hr)

17.78130.00000.00150.00000.99610.00000.00000.00001.84460.00000.00000.00000.0000

2909.8929

MOLE FRACTION

0.00610.00000.00000.00000.00030.00000.00000.00000.00060.00000.00000.00000.00000.9930

MASS FLOW (lb/hr)

285.26350.00000.06690.0000

27.90500.00000.00000.0000

73.68740.00000.00000.00000.0000

49555.4776

MASS FRACTION

0.00570.00000.00000.00000.00060.00000.00000.00000.00150.00000.00000.00000.00000.9923

LIQUID VOLUMEFLOW (barrel/day)

65.24110.00000.00900.00002.36950.00000.00000.00003.68240.00000.00000.00000.0000

5507.8217

LIQUID VOLUMEFRACTION

0.01170.00000.00000.00000.00040.00000.00000.00000.00070.00000.00000.00000.00000.9872

Total 2930.5164 1.0000 49942.4004 1.0000 5579.1238 1.0000

K VALUE

COMPONENTSMethane

EthanePropane

CO2Nitrogen

H2OMercury

HydrogenArgon

COS_Vapour

H2SOxygen

Ammonia

MIXED32.53

---2.245

---264.3

---------

25.90------------

0.7014

LIGHT32.53

---2.245

---264.3

---------

25.90------------

0.7014

HEAVY------------------------------------------

UNIT OPERATIONS

FEED TO PRODUCT FROMHeater: E-110

LOGICAL CONNECTION

UTILITIES

( No utilities reference this stream )

PROCESS UTILITY

Aspen Technology Inc. Aspen HYSYS Version 8.4 (30.0.0.8433) Page 21 of 21

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63* Specified by user.Licensed to: LEGENDS