simulation repor1 lab 3
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Simulation Report
File Name: New ProjectCompany:Customer:Project:Job No:Prepared By:Report Date: 10/22/2015 10:37:20 AMUnit Set: Field
File: New Project.vmpiCON v8.0
Main Flowsheet....................................................................................................................................................3Material Streams.............................................................................................................................................3Energy Streams...............................................................................................................................................9Conv Reactors...............................................................................................................................................11Coolers............................................................................................................................................................13Heaters.............................................................................................................................................................14Separators......................................................................................................................................................15
*Bold face throughout the report denotes specified values.*Italic face throughout the report denotes recycle values.
Customer: JobNo: Project:
Prepared by:
RootThermo (Thermodynamic Model)
Main Data
Property Package Name Advanced_Peng-Robinson Compound Count 3
Compounds
n-HEPTANE TOLUENE HYDROGEN
File: New Project.vmpApril-21-23 iCON v8.0 Page 2 of 15
Customer: JobNo: Project:
Prepared by:
/stream_A (Material Stream)
Prop Pkg: Advanced Peng-Robinson
Connections
Material Inlets
Connection Up Stream Unit OpIn ---- ----
Material Outlets
Connection Down Stream Unit OpOut heater ----
Natural Gas / Component Content
Water [lb/MMSCF] 0.00 Sulfur (Total) [grain/100SCF] 0.00Mercaptans [grain/100SCF] 0.00 H2S [grain/100SCF] 0.00CO2 [Fraction] 0.00 N2 [Fraction] 0.00H2 [ppm] 0.00 O2 [ppm] 0.00
Settings / Eq. Results Configuration
Include Bulk Liq. in Eq. Results False View Component Free Compositions FalseName for Component Free Cmp. Free Exclude from Component Free
n-HEPTANE 0.00 TOLUENE 0.00 HYDROGEN 0.00
Equilibrium Results
Bulk Vapour Liquid01.00 0.00 1.00
T [F] 65.00 65.00 65.00P [psia] 14.692 14.692 14.692Mole Flow [lbmol/h] 100.00 0.00 100.00Mass Flow [lb/h] 10020.19 0.00 10020.19Mole Fraction [Fraction] n-HEPTANE 1.00 1.00 1.00 TOLUENE 0.00 0.00 0.00 HYDROGEN 0.00 0.00 0.00Mass Fraction [Fraction] n-HEPTANE 1.00 1.00 1.00 TOLUENE 0.00 0.00 0.00 HYDROGEN 0.00 0.00 0.00MoleFlows [lbmol/h] n-HEPTANE 100.00 0.00 100.00 TOLUENE 0.00 0.00 0.00 HYDROGEN 0.00 0.00 0.00MassFlows [lb/h] n-HEPTANE 10020.19 0.00 10020.19 TOLUENE 0.00 0.00 0.00 HYDROGEN 0.00 0.00 0.00
File: New Project.vmpApril-21-23 iCON v8.0 Page 3 of 15
Customer: JobNo: Project:
Prepared by:
/stream_B (Material Stream)
Prop Pkg: Advanced Peng-Robinson
Connections
Material Inlets
Connection Up Stream Unit OpIn heater ----
Material Outlets
Connection Down Stream Unit OpOut catalytic_reactor ----
Natural Gas / Component Content
Water [lb/MMSCF] 0.00 Sulfur (Total) [grain/100SCF] 0.00Mercaptans [grain/100SCF] 0.00 H2S [grain/100SCF] 0.00CO2 [Fraction] 0.00 N2 [Fraction] 0.00H2 [ppm] 0.00 O2 [ppm] 0.00
Settings / Eq. Results Configuration
Include Bulk Liq. in Eq. Results False View Component Free Compositions FalseName for Component Free Cmp. Free Exclude from Component Free
n-HEPTANE 0.00 TOLUENE 0.00 HYDROGEN 0.00
Equilibrium Results
Bulk Vapour Liquid01.00 1.00 0.00
T [F] 800.00 800.00 800.00P [psia] 14.692 14.692 14.692Mole Flow [lbmol/h] 100.00 100.00 0.00Mass Flow [lb/h] 10020.19 10020.19 0.00Mole Fraction [Fraction] n-HEPTANE 1.00 1.00 1.00 TOLUENE 0.00 0.00 0.00 HYDROGEN 0.00 0.00 0.00Mass Fraction [Fraction] n-HEPTANE 1.00 1.00 1.00 TOLUENE 0.00 0.00 0.00 HYDROGEN 0.00 0.00 0.00MoleFlows [lbmol/h] n-HEPTANE 100.00 100.00 0.00 TOLUENE 0.00 0.00 0.00 HYDROGEN 0.00 0.00 0.00MassFlows [lb/h] n-HEPTANE 10020.19 10020.19 0.00 TOLUENE 0.00 0.00 0.00 HYDROGEN 0.00 0.00 0.00
File: New Project.vmpApril-21-23 iCON v8.0 Page 4 of 15
Customer: JobNo: Project:
Prepared by:
/stream_C (Material Stream)
Prop Pkg: Advanced Peng-Robinson
Connections
Material Inlets
Connection Up Stream Unit OpIn catalytic_reactor ----
Material Outlets
Connection Down Stream Unit OpOut cooler ----
Natural Gas / Component Content
Water [lb/MMSCF] 0.00 Sulfur (Total) [grain/100SCF] 0.00Mercaptans [grain/100SCF] 0.00 H2S [grain/100SCF] 0.00CO2 [Fraction] 0.00 N2 [Fraction] 0.00H2 [ppm] 3.75E+05 O2 [ppm] 0.00E+00
Settings / Eq. Results Configuration
Include Bulk Liq. in Eq. Results False View Component Free Compositions FalseName for Component Free Cmp. Free Exclude from Component Free
n-HEPTANE 0.00E+00 TOLUENE 0.00E+00 HYDROGEN 0.00E+00
Equilibrium Results
Bulk Vapour Liquid01.00 1.00 0.00
T [F] 800.00 800.00 800.00P [psia] 14.692 14.692 14.692Mole Flow [lbmol/h] 160.00 160.00 0.00Mass Flow [lb/h] 10020.19 10020.19 0.00Mole Fraction [Fraction] n-HEPTANE 0.5313 0.5313 0.5312 TOLUENE 0.0938 0.0938 0.0937 HYDROGEN 0.3750 0.3750 0.3750Mass Fraction [Fraction] n-HEPTANE 0.8500 0.8500 0.8500 TOLUENE 0.1379 0.1379 0.1379 HYDROGEN 0.0121 0.0121 0.0121MoleFlows [lbmol/h] n-HEPTANE 85.00 85.00 0.00 TOLUENE 15.00 15.00 0.00 HYDROGEN 60.00 60.00 0.00MassFlows [lb/h] n-HEPTANE 8517.16 8517.16 0.00 TOLUENE 1382.08 1382.08 0.00 HYDROGEN 120.95 120.95 0.00
File: New Project.vmpApril-21-23 iCON v8.0 Page 5 of 15
Customer: JobNo: Project:
Prepared by:
/stream_D (Material Stream)
Prop Pkg: Advanced Peng-Robinson
Connections
Material Inlets
Connection Up Stream Unit OpIn cooler ----
Material Outlets
Connection Down Stream Unit OpOut separator ----
Natural Gas / Component Content
Water [lb/MMSCF] 0.00 Sulfur (Total) [grain/100SCF] 0.00Mercaptans [grain/100SCF] 0.00 H2S [grain/100SCF] 0.00CO2 [Fraction] 0.00 N2 [Fraction] 0.00H2 [ppm] 3.75E+05 O2 [ppm] 0.00E+00
Settings / Eq. Results Configuration
Include Bulk Liq. in Eq. Results False View Component Free Compositions FalseName for Component Free Cmp. Free Exclude from Component Free
n-HEPTANE 0.00E+00 TOLUENE 0.00E+00 HYDROGEN 0.00E+00
Equilibrium Results
Bulk Vapour Liquid01.00 0.39 0.61
T [F] 65.00 65.00 65.00P [psia] 14.692 14.692 14.692Mole Flow [lbmol/h] 160.00 62.65 97.35Mass Flow [lb/h] 10020.19 388.77 9631.43Mole Fraction [Fraction] n-HEPTANE 0.5313 0.0378 0.8488 TOLUENE 0.0938 0.0053 0.1507 HYDROGEN 0.3750 0.9569 0.0005Mass Fraction [Fraction] n-HEPTANE 0.8500 0.6106 0.8597 TOLUENE 0.1379 0.0785 0.1403 HYDROGEN 0.0121 0.3109 0.0000MoleFlows [lbmol/h] n-HEPTANE 85.00 2.37 82.63 TOLUENE 15.00 0.33 14.67 HYDROGEN 60.00 59.95 0.05MassFlows [lb/h] n-HEPTANE 8517.16 237.38 8279.78 TOLUENE 1382.08 30.54 1351.54 HYDROGEN 120.95 120.85 0.10
File: New Project.vmpApril-21-23 iCON v8.0 Page 6 of 15
Customer: JobNo: Project:
Prepared by:
/stream_E (Material Stream)
Prop Pkg: Advanced Peng-Robinson
Connections
Material Inlets
Connection Up Stream Unit OpIn separator ----
Material Outlets
Connection Down Stream Unit OpOut ---- ----
Natural Gas / Component Content
Water [lb/MMSCF] 0.00 Sulfur (Total) [grain/100SCF] 0.00Mercaptans [grain/100SCF] 0.00 H2S [grain/100SCF] 0.00CO2 [Fraction] 0.00 N2 [Fraction] 0.00H2 [ppm] 9.57E+05 O2 [ppm] 0.00E+00
Settings / Eq. Results Configuration
Include Bulk Liq. in Eq. Results False View Component Free Compositions FalseName for Component Free Cmp. Free Exclude from Component Free
n-HEPTANE 0.00E+00 TOLUENE 0.00E+00 HYDROGEN 0.00E+00
Equilibrium Results
Bulk Vapour Liquid01.00 1.00 0.00
T [F] 65.00 65.00 65.00P [psia] 14.692 14.692 14.692Mole Flow [lbmol/h] 62.65 62.65 0.00Mass Flow [lb/h] 388.77 388.77 0.00Mole Fraction [Fraction] n-HEPTANE 0.0378 0.0378 0.8488 TOLUENE 0.0053 0.0053 0.1507 HYDROGEN 0.9569 0.9569 0.0005Mass Fraction [Fraction] n-HEPTANE 0.6106 0.6106 0.8597 TOLUENE 0.0785 0.0785 0.1403 HYDROGEN 0.3109 0.3109 0.0000MoleFlows [lbmol/h] n-HEPTANE 2.37 2.37 0.00 TOLUENE 0.33 0.33 0.00 HYDROGEN 59.95 59.95 0.00MassFlows [lb/h] n-HEPTANE 237.38 237.38 0.00 TOLUENE 30.54 30.54 0.00 HYDROGEN 120.85 120.85 0.00
File: New Project.vmpApril-21-23 iCON v8.0 Page 7 of 15
Customer: JobNo: Project:
Prepared by:
/stream_F (Material Stream)
Prop Pkg: Advanced Peng-Robinson
Connections
Material Inlets
Connection Up Stream Unit OpIn separator ----
Material Outlets
Connection Down Stream Unit OpOut ---- ----
Natural Gas / Component Content
Water [lb/MMSCF] 0.00 Sulfur (Total) [grain/100SCF] 0.00Mercaptans [grain/100SCF] 0.00 H2S [grain/100SCF] 0.00CO2 [Fraction] 0.00 N2 [Fraction] 0.00H2 [ppm] 518.20 O2 [ppm] 0.00
Settings / Eq. Results Configuration
Include Bulk Liq. in Eq. Results False View Component Free Compositions FalseName for Component Free Cmp. Free Exclude from Component Free
n-HEPTANE 0.00 TOLUENE 0.00 HYDROGEN 0.00
Equilibrium Results
Bulk Vapour Liquid01.00 0.00 1.00
T [F] 65.00 65.00 65.00P [psia] 14.692 14.692 14.692Mole Flow [lbmol/h] 97.35 0.00 97.35Mass Flow [lb/h] 9631.43 0.00 9631.43Mole Fraction [Fraction] n-HEPTANE 0.8488 0.0378 0.8488 TOLUENE 0.1507 0.0053 0.1507 HYDROGEN 5.18E-04 9.57E-01 5.18E-04Mass Fraction [Fraction] n-HEPTANE 0.8597 0.6106 0.8597 TOLUENE 0.1403 0.0785 0.1403 HYDROGEN 1.06E-05 3.11E-01 1.06E-05MoleFlows [lbmol/h] n-HEPTANE 82.63 0.00 82.63 TOLUENE 14.67 0.00 14.67 HYDROGEN 0.05 0.00 0.05MassFlows [lb/h] n-HEPTANE 8279.78 0.00 8279.78 TOLUENE 1351.54 0.00 1351.54 HYDROGEN 0.10 0.00 0.10
File: New Project.vmpApril-21-23 iCON v8.0 Page 8 of 15
Customer: JobNo: Project:
Prepared by:
/Q-1 (Energy Stream)
Prop Pkg: Advanced Peng-Robinson
Connections
Energy Streams
Connection ValueIn [Btu/h] ---- 5884805.6004Out [Btu/h] /heater.InQ 5884805.6004
File: New Project.vmpApril-21-23 iCON v8.0 Page 9 of 15
Customer: JobNo: Project:
Prepared by:
/Q-2 (Energy Stream)
Prop Pkg: Advanced Peng-Robinson
Connections
Energy Streams
Connection ValueIn [Btu/h] /cooler.OutQ 5942071.9447Out [Btu/h] ---- 5942071.9447
File: New Project.vmpApril-21-23 iCON v8.0 Page 10 of 15
Customer: JobNo: Project:
Prepared by:
/catalytic_reactor (Conv Reactor)
Prop Pkg: Advanced Peng-Robinson
Connections
Material Inlets
Connection Up Stream Unit OpIn stream_B heater
Material Outlets
Connection Down Stream Unit OpOut stream_C cooler
Energy Streams
Connection ValueOutQ [Btu/h] ---- -1630754.6084
Summary / Main Data
OutQ [Btu/h] -1630754.6084 Delta P [psi] 0.00Rxn0_Conversion [Fraction] 0.1500
Summary / Configuration
Split Phases False
Material
In OutVapFrac 1.00 1.00T [F] 800.00 800.00P [psia] 14.692 14.692Mole Flow [lbmol/h] 100.00 160.00Mass Flow [lb/h] 10020.19 10020.19Energy [Btu/h] 5551142.6423 5753508.1162Mole Fraction [Fraction] n-HEPTANE 1.00 0.5313 TOLUENE 0.00 0.0938 HYDROGEN 0.00 0.3750Mass Fraction [Fraction] n-HEPTANE 1.00 0.8500 TOLUENE 0.00 0.1379 HYDROGEN 0.00 0.0121MoleFlows [lbmol/h] n-HEPTANE 100.00 85.00 TOLUENE 0.00 15.00 HYDROGEN 0.00 60.00MassFlows [lb/h] n-HEPTANE 10020.19 8517.16 TOLUENE 0.00 1382.08 HYDROGEN 0.00 120.95
Settings / Settings
File: New Project.vmpApril-21-23 iCON v8.0 Page 11 of 15
Customer: JobNo: Project:
Prepared by:
Liquid Ports 1 Q Exothermic Is Positive True
Settings / Phase Settings
Liquid Ports 1 Add Solid Port False
Reactions
Rxn0Rxn Name Rxn_1Base Comp n-HEPTANERxn0_Conversion [Fraction] 0.1500Solution Order 0n-HEPTANE -1TOLUENE 1HYDROGEN 4Balance 0.000H Rx'n(25C) [Btu/lbmol] 102321.96
File: New Project.vmpApril-21-23 iCON v8.0 Page 12 of 15
Customer: JobNo: Project:
Prepared by:
/cooler (Cooler)
Prop Pkg: Advanced Peng-Robinson
OutQ [Btu/h]Delta P [psi]
OutQ [Btu/h] ---- -1630754.6084
Material
In OutVapFrac 1.00 0.3916T [F] 800.00 65.00P [psia] 14.692 14.692Mole Flow [lbmol/h] 160.00 160.00Mass Flow [lb/h] 10020.19 10020.19Energy [Btu/h] 5753508.1162 -188563.8285Mole Fraction [Fraction] n-HEPTANE 0.5313 0.5313 TOLUENE 0.0938 0.0938 HYDROGEN 0.3750 0.3750Mass Fraction [Fraction] n-HEPTANE 0.8500 0.8500 TOLUENE 0.1379 0.1379 HYDROGEN 0.0121 0.0121MoleFlows [lbmol/h] n-HEPTANE 85.00 85.00 TOLUENE 15.00 15.00 HYDROGEN 60.00 60.00MassFlows [lb/h] n-HEPTANE 8517.16 8517.16 TOLUENE 1382.08 1382.08 HYDROGEN 120.95 120.95
File: New Project.vmpApril-21-23 iCON v8.0 Page 13 of 15
Customer: JobNo: Project:
Prepared by:
/heater (Heater)
Prop Pkg: Advanced Peng-Robinson
InQ [Btu/h]Delta P [psi]
OutQ [Btu/h] ---- -1630754.6084
Material
In OutVapFrac 0.00 1.00T [F] 65.00 800.00P [psia] 14.692 14.692Mole Flow [lbmol/h] 100.00 100.00Mass Flow [lb/h] 10020.19 10020.19Energy [Btu/h] -333662.9581 5551142.6423Mole Fraction [Fraction] n-HEPTANE 1.00 1.00 TOLUENE 0.00 0.00 HYDROGEN 0.00 0.00Mass Fraction [Fraction] n-HEPTANE 1.00 1.00 TOLUENE 0.00 0.00 HYDROGEN 0.00 0.00MoleFlows [lbmol/h] n-HEPTANE 100.00 100.00 TOLUENE 0.00 0.00 HYDROGEN 0.00 0.00MassFlows [lb/h] n-HEPTANE 10020.19 10020.19 TOLUENE 0.00 0.00 HYDROGEN 0.00 0.00
File: New Project.vmpApril-21-23 iCON v8.0 Page 14 of 15
Customer: JobNo: Project:
Prepared by:
/separator (Separator)
Prop Pkg: Advanced Peng-Robinson
Connections
Material Inlets
Connection Up Stream Unit OpIn stream_D cooler
Material Outlets
Connection Down Stream Unit OpLiq0 stream_F ----Vap stream_E ----
Material
In Liq0 VapVapFrac 0.3916 0.00 1.00T [F] 65.00 65.00 65.00P [psia] 14.692 14.692 14.692Mole Flow [lbmol/h] 160.00 97.35 62.65Mass Flow [lb/h] 10020.19 9631.43 388.77Energy [Btu/h] -188563.8285 -425572.3471 237008.5163Mole Fraction [Fraction] n-HEPTANE 0.5313 0.8488 0.0378 TOLUENE 0.0938 0.1507 0.0053 HYDROGEN 0.3750 5.18E-04 0.9569Mass Fraction [Fraction] n-HEPTANE 0.8500 0.8597 0.6106 TOLUENE 0.1379 0.1403 0.0785 HYDROGEN 0.0121 1.06E-05 0.3109MoleFlows [lbmol/h] n-HEPTANE 85.00 82.63 2.37 TOLUENE 15.00 14.67 0.33 HYDROGEN 60.00 0.05 59.95MassFlows [lb/h] n-HEPTANE 8517.16 8279.78 237.38 TOLUENE 1382.08 1351.54 30.54 HYDROGEN 120.95 0.10 120.85
Settings / Settings
Order Liq. Phases by Key Cmp True Key Cmp. in 2nd Liquid WATERMin Key Cmp. in 2nd Liquid [Fraction] 0.5000
File: New Project.vmpApril-21-23 iCON v8.0 Page 15 of 15