Hla Summary Report

Index 1 Input File 2 Solution History 3 Main

Index

Input File $ Generated by PRO/II Keyword Generation System $ Generated on: Thu Jan 23 19:30:18 2014 TITLE DIMENSION ENGLISH, TEMP=C, PRES=ATM, ENERGY=KJ, STDTEMP=15.556, & STDPRES=1 SEQUENCE SIMSCI CALCULATION RVPBASIS=APIN, TVP=37.778 COMPONENT DATA LIBID 1,BENZENE/2,OXYLENE/3,TOLUENE, BANK=SIMSCI,PROCESS ASSAY CONVERSION=API94, CURVEFIT=IMPROVED, KVRECONCILE=TAILS THERMODYNAMIC DATA METHOD SYSTEM=PR, SET=PR01, DEFAULT STREAM DATA PROPERTY STREAM=S1, TEMPERATURE=21.111, PRESSURE=1, PHASE=M, & COMPOSITION(WT,LB/H)=1,577.83/2,115.57/3,462.27 UNIT OPERATIONS SHORTCUT UID=SCD1 FEED S1 PRODUCT STREAM=S2, RATE(WT)=577.83, PHASE=L, DP=0 PRODUCT STREAM=S3, PHASE=L, DP=0 CONDENSER TYPE=TFIX, TEMPERATURE=50 EVALUATE MODEL=REFINE, TRIAL=50 FINDEX 2 SPEC STREAM=S2, RATE(WT,LB/H), COMP=1,WET, VALUE=577.83 SPEC STREAM=S2,PCT, COMP=1,WET, VALUE=100 HX UID=E2 HOT FEED=S3, M=S7 UTILITY WATER, TIN=26.667, TEMPERATURE=48.889 CONFIGURE COUNTER OPER HOCO=55.556 SHORTCUT UID=SCD2 FEED S7 PRODUCT STREAM=S4, RATE(WT)=462.27, PHASE=L, DP=0 PRODUCT STREAM=S5, PHASE=L, DP=0 CONDENSER TYPE=TFIX, TEMPERATURE=50 EVALUATE MODEL=REFINE, TRIAL=100, KEYLIGHT=2, KEYHEAVY=3, & RRMIN=2 FINDEX 2 SPEC STREAM=S4, RATE(WT,LB/H), COMP=3,WET, VALUE=462.27 SPEC STREAM=S4,PCT(WT), COMP=3,WET, VALUE=100 HX UID=E4 HOT FEED=S5, M=S9 UTILITY WATER, TIN=25, TEMPERATURE=49 CONFIGURE COUNTER OPER HOCI=25 END

Index

Solution History SIMULATION SCIENCES INC. R PAGE H-1 PROJECT PRO/II VERSION 8.1 ELEC V6.6 PROBLEM CALCULATION HISTORY 01/23/14

*** PROBLEM SOLUTION BEGINS FEED FLASH COMPLETE UNIT 1 SOLVED - 'SCD1 ' UNIT 4 SOLVED - 'E2 ' UNIT 2 SOLVED - 'SCD2 ' UNIT 6 SOLVED - 'E4 ' *** PROBLEM SOLUTION REACHED *** THIS RUN USED 52.93 PRO/II SIMULATION UNITS *** RUN STATISTICS STARTED 19:07:28 01/23/14 NO ERRORS FINISHED 19:07:29 01/23/14 NO WARNINGS RUN TIMES NO MESSAGES INTERACTIVE 0 MIN, 0.00 SEC CALCULATIONS 0 MIN, 0.25 SEC TOTAL 0 MIN, 0.25 SEC

Index

Hx (Summary)

UOM

HX Name HX Description Hot Side Thermo Method Cold Side Thermo Method Hot Side Feed Stream(s) Hot Side Product Stream(s) Cold Side Feed Stream(s) Cold Side Product Stream(s)

E2

E2 E2 PR01 PR01 S3 S7 N/A N/A

Product Stream Phases

S9 S7 Duty FT Factor LMTD MTD U*A U Value Area Hot Pressure Drop Hot Product Temperature Hot Product Liquid Fraction Cold Pressure Drop Cold Product Temperature Cold Product Liquid Fraction Utility Inlet Temperature Utility OutletTemperature Utility Saturation Pressure Utility Flowrate Utility Cp or Heat Value Zone Weighted LMTD ShortColumn (Summary)

Name Description Thermodynamic System Feed Streams Product Streams Fenske Minimum Trays Product Temperature[S2] Product Temperature[S3] Product Pressure[S2] Product Pressure[S3] Product Molar Rate[S2] Product Molar Rate[S3] Product Mass Rate[S2] Product Mass Rate[S3] Product Std. Liq Vol Rate[S2]

kJ / hr C C BTU/hr-F BTU/hr-ft2-F ft2 atm C fraction atm C fraction C C atm lb-mol / hr BTU/lb-F C UOM

C C atm atm lb-mol / hr lb-mol / hr lb / hr lb / hr ft3 / hr

N/A Liquid 5275.020283 0.992529212 71.63861332 71.10341644 39.06487795 N/A N/A 0 104.4444366 1 N/A N/A N/A 26.6666809 48.8888794 N/A 6.938308143 N/A N/A SCD1

SCD1 SCD1 PR01 S1 S2 , S3 14.60782669 49.9999939 114.7202258 0.999999969 0.999999969 7.3972999 6.105574927 577.9913737 577.6783897 10.49359765

Product Std. Liq Vol Rate[S3] Product Std. Vap Vol Rate[S2] Product Std. Vap Vol Rate[S3]

ft3 / hr ft3 / hr ft3 / hr

ShortColumn (Summary)

UOM

Name Description Thermodynamic System Feed Streams Product Streams Fenske Minimum Trays Minimum Reflux Ratio Feed Condition Q Operating Reflux Ratio Product Temperature[S4] Product Temperature[S5] Product Pressure[S4] Product Pressure[S5] Product Molar Rate[S4] Product Molar Rate[S5] Product Mass Rate[S4] Product Mass Rate[S5] Product Std. Liq Vol Rate[S4] Product Std. Liq Vol Rate[S5] Product Std. Vap Vol Rate[S4] Product Std. Vap Vol Rate[S5]

C C atm atm lb-mol / hr lb-mol / hr lb / hr lb / hr ft3 / hr ft3 / hr ft3 / hr ft3 / hr

Stream (Summary)

UOM

Name Description Phase Thermodynamic System Total Molar Rate Total Mass Rate Temperature Pressure Total Molecular Weight Total Specific Enthalpy Total Cp Total Molar Component Rates

lb-mol / hr lb / hr C atm kJ / lb BTU/lb-F lb-mol / hr

BENZENE OXYLENE TOLUENE

Total Molar Component Fractions

BENZENE OXYLENE TOLUENE Vapor Molar Rate Vapor Mass Rate Vapor Molecular Weight Vapor Mole Fraction

10.57095385 2807.15717 2316.968173 SCD2

SCD2 SCD2 PR01 S7 S4 , S5 17.74231013 4587.168514 1.056065776 2 * Minimum Reflux Ratio 49.9999939 144.4353528 0.999999969 0.999999969 5.020039918 1.08553501 462.4317551 115.2466335 8.482715181 2.088238647 1905.024973 411.9431992 S1

S1 S1 Liquid PR01 13.50287483 1155.670012 21.1111084 0.999999969 85.5869603 22.36391321 0.367430279 7.3972999 1.088563948 5.01701098

fraction

lb-mol / hr lb / hr fraction

0.54783148 0.080617199 0.371551321 N/A N/A N/A N/A

Vapor Specific Enthalpy Vapor CP Vapor Composition


Vapor Component Rate

BENZENE OXYLENE TOLUENE Total Liquid Molar Rate Total Liquid Mass Rate Total Liquid Molecular Weight Total Liquid Mole Fraction Total Liquid Specific Enthalpy Total Liquid CP Total Liquid Composition

BENZENE OXYLENE TOLUENE Liqud Molar Rate Liquid Cp Liquid Molecular Weight Liquid Mole Fraction Liquid Molar Enthalpy Liquid Composition

BENZENE OXYLENE TOLUENE Decant Water Mole Rate Decant Water Moleculat Weight Water Mole Fraction Decant Water Molar Enthalpy Decant Water Cp Liquid1 Mole Rate Liquid1 Mole Frac Liquid1 Molecular Weight Liquid1 Molar Enthalpy Liquid1 Cp Liquid1 Composition

lb-mol / hr

lb-mol / hr lb / hr fraction kJ / lb BTU/lb-F fraction

lb-mol / hr

lb-mol / hr BTU/lb-F fraction kJ / lb-mol fraction

7.3972999 1.088563948 5.01701098 N/A N/A N/A N/A N/A N/A N/A N/A

lb-mol / hr

lb-mol / hr fraction kJ / lb-mol BTU/lb-F lb-mol / hr fraction kJ / lb-mol BTU/lb-F fraction


Liquid1 Component Rate

N/A N/A N/A 13.50287483 1155.670012 85.5869603 1 22.36391321 0.367430279 0.54783148 0.080617199 0.371551321


Liquid Component Rate

N/A N/A N/A N/A N/A


Total Liquid Component Rate

kJ / lb BTU/lb-F fraction

N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A

lb-mol / hr

BENZENE OXYLENE TOLUENE Liquid2 Mole Rate Liquid2 Mole Frac Liquid2 Molecular Weight Liquid2 Molar Enthalpy Liquid1 Cp Liquid2 Composition

kJ / lb-mol BTU/lb-F fraction


Liquid2 Component Rate

lb-mol / hr fraction


N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A

lb-mol / hr N/A N/A N/A

E4

E4 E4 PR01 PR01 S5 S9 N/A N/A Liquid N/A 9646.958912 0.824152705 52.58044309 43.3343144 117.222588 N/A N/A 0 49.9999939 1 N/A N/A N/A 24.9999939 48.9999939 N/A 11.74885812 N/A N/A

S2

S3

S4

S5

S2 S2 Liquid PR01 7.3972999 577.9913737 49.9999939 0.999999969 78.13545232 44.93371203 0.390763635

S3 S3 Liquid PR01 6.105574927 577.6783897 114.7202258 0.999999969 94.61490466 95.85963331 0.473401834

S4 S4 Liquid PR01 5.020039918 462.4317551 49.9999939 0.999999969 92.11714701 42.29194369 0.401969787

S5 S5 Liquid PR01 1.08553501 115.2466335 144.4353528 0.999999969 106.1657455 123.8220598 0.512791388

7.385796733 1.06555E-09 0.011503166

0.011518196 1.088561258 5.005495474

0.011518196 0.003153951 5.00536777

3.17721E-13 1.085407233 0.000127777

0.998444951 1.44046E-10 0.001555049 N/A N/A N/A N/A

0.001886505 0.178289722 0.819823773 N/A N/A N/A N/A

0.002294443 0.000628272 0.997077285 N/A N/A N/A N/A

2.92686E-13 0.999882291 0.000117709 N/A N/A N/A N/A

N/A N/A

N/A N/A

N/A N/A

N/A N/A

N/A N/A N/A

N/A N/A N/A

N/A N/A N/A

N/A N/A N/A

N/A N/A N/A 7.3972999 577.9913737 78.13545232 1 44.93371203 0.390763635

N/A N/A N/A 6.105574927 577.6783897 94.61490466 1 95.85963331 0.473401834

N/A N/A N/A 5.020039918 462.4317551 92.11714701 1 42.29194369 0.401969787

N/A N/A N/A 1.08553501 115.2466335 106.1657455 1 123.8220598 0.512791388

0.998444951 1.44046E-10 0.001555049

0.001886505 0.178289722 0.819823773

0.002294443 0.000628272 0.997077285

2.92686E-13 0.999882291 0.000117709

7.385796733 1.06555E-09 0.011503166 N/A N/A N/A N/A N/A

0.011518196 1.088561258 5.005495474 N/A N/A N/A N/A N/A

0.011518196 0.003153951 5.00536777 N/A N/A N/A N/A N/A

3.17721E-13 1.085407233 0.000127777 N/A N/A N/A N/A N/A

N/A N/A N/A

N/A N/A N/A

N/A N/A N/A

N/A N/A N/A

N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A N/A




N/A N/A N/A

N/A N/A N/A

N/A N/A N/A

N/A N/A N/A

N/A N/A N/A N/A N/A N/A N/A N/A




N/A N/A N/A

N/A N/A N/A

N/A N/A N/A

N/A N/A N/A

N/A N/A N/A

N/A N/A N/A

N/A N/A N/A

N/A N/A N/A

S7

S9

S7 S7 Liquid PR01 6.105574927 577.6783897 104.4444366 0.999999969 94.61490466 86.72821971 0.462466155

S9 S9 Liquid PR01 1.08553501 115.2466335 49.9999939 0.999999969 106.1657455 40.1149821 0.421345492

0.011518196 1.088561258 5.005495474

3.17721E-13 1.085407233 0.000127777

0.001886505 0.178289722 0.819823773 N/A N/A N/A N/A

2.92686E-13 0.999882291 0.000117709 N/A N/A N/A N/A

N/A N/A

N/A N/A

N/A N/A N/A

N/A N/A N/A

N/A N/A N/A 6.105574927 577.6783897 94.61490466 1 86.72821971 0.462466155

N/A N/A N/A 1.08553501 115.2466335 106.1657455 1 40.1149821 0.421345492

0.001886505 0.178289722 0.819823773

2.92686E-13 0.999882291 0.000117709

0.011518196 1.088561258 5.005495474 N/A N/A N/A N/A N/A

3.17721E-13 1.085407233 0.000127777 N/A N/A N/A N/A N/A

N/A N/A N/A

N/A N/A N/A



N/A N/A N/A

N/A N/A N/A



N/A N/A N/A

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Hla Summary Report

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