HYSYS-Report Ammonia Plant
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Reporte de hysys util para el conocimiento de plantas de amonaco urea.
Transcript of HYSYS-Report Ammonia Plant
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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
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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
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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
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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
Aspen Technology Inc. Aspen HYSYS Version 8.4 (30.0.0.8433) Page 4 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: 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------------------------------------------
Aspen Technology Inc. Aspen HYSYS Version 8.4 (30.0.0.8433) Page 5 of 21
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63* Specified by user.Licensed to: LEGENDS
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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
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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------------------------------------------
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63* Specified by user.Licensed to: LEGENDS
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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
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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
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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
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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
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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
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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
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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
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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
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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
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63* Specified by user.Licensed to: LEGENDS
