Приложение г. Результаты расчета реактора идеального вытеснения

$ Generated by PRO/II Keyword Generation System <version 8.3>

$ Generated on: Thu Dec 04 15:26:36 2014

TITLE

PRINT STREAM=ALL, RATE=M,WT, FRACTION=M,WT, PERCENT=M,WT

DIMENSION SI, TEMP=C, STDTEMP=0, STDPRES=101.325

SEQUENCE SIMSCI

CALCULATION RVPBASIS=APIN, TVP=37.778

COMPONENT DATA

LIBID 1,22PR/2,IPENTANE/3,PENTANE/4,22MB/5,23MB/6,2MP/7,3MP/ &

8,HEXANE, BANK=SIMSCI,PROCESS

ASSAY CONVERSION=API94, CURVEFIT=CURRENT, KVRECONCILE=TAILS

THERMODYNAMIC DATA

METHOD SYSTEM=SRKM, SET=SRKM01, DEFAULT

STREAM DATA

PROPERTY STREAM=S1, TEMPERATURE=170, PRESSURE=3100, PHASE=M, &

COMPOSITION(WT,KG/H)=1,6/2,450/3,6320/4,650/5,510/6,2200/ &

7,1300/8,7200

RXDATA

RXSET ID=ISOMER_C5-C6

REACTION ID=1

STOICHIOMETRY 6,1/8,-1

REACTION ID=2

STOICHIOMETRY 7,1/8,-1

REACTION ID=3

STOICHIOMETRY 4,1/8,-1

REACTION ID=4

STOICHIOMETRY 5,1/8,-1

REACTION ID=5

STOICHIOMETRY 2,1/3,-1

REACTION ID=6

STOICHIOMETRY 1,1/3,-1

UNIT OPERATIONS

PLUG UID=R1

FEED S1

PRODUCT M=S2

OPERATION LENGTH=4, DIAMETER=2000, DP=50, POINTS=10, &

ADIABATIC, DUTY=0

RXCALCULATION RUNGEKUTTA, NSTEPS=20

RXSTOIC RXSET=ISOMER_C5-C6

REACTION 1

REACTION 2

REACTION 3

REACTION 4

REACTION 5

REACTION 6

END

SIMULATION SCIENCES INC. R PAGE R-1

PROJECT PRO/II VERSION 8.3 ELEC V7.0

PROBLEM INPUT

THERMODYNAMIC DATA

==============================================================================

VLE K-VALUE DATA FOR SET 'SRKM01'

SRK SIMSCI PURE COMPONENT DATA

COMP CRITICAL CRITICAL ALPHA C1 C2 C3

TEMPERATURE PRESSURE TYPE

DEG C KPA

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

1 160.63 3199.00 6 0.0737 0.9045 5.2823

2 187.28 3381.00 6 0.1883 0.8677 2.9845

3 196.55 3370.00 6 0.5316 0.8700 1.4810

4 215.63 3081.00 6 0.3067 0.8562 2.1437

5 226.83 3127.00 6 0.2695 0.8545 2.3891

6 224.35 3010.00 6 0.2838 0.8475 2.3909

7 231.28 3124.00 6 0.3080 0.8508 2.2697

8 234.45 3025.00 6 0.1581 0.8728 3.8442

SRK SIMSCI INTERACTION PARAMETERS

KIJ = A(I,J) + B(I,J)/T + C(I,J)/T**2

ALL PAIRS HAVE BEEN DEFAULTED TO IDEAL

SIMULATION SCIENCES INC. R PAGE R-4

PROJECT PRO/II VERSION 8.3 ELEC V7.0

PROBLEM INPUT

THERMODYNAMIC DATA

==============================================================================

THERMODYNAMIC SETS USED FOR EACH UNIT OPERATION

DEFAULT METHOD IS SRKM01

THERMODYNAMIC SET UNIT OPERATIONS

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

SRKM01 R1

UNIT IDENTIFIER UNIT OPERATION THERMODYNAMIC SET

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

R1 PLUG FLOW REACTOR SRKM01

SIMULATION SCIENCES INC. R PAGE R-5

PROJECT PRO/II VERSION 8.3 ELEC V7.0

PROBLEM INPUT

THERMODYNAMIC DATA

==============================================================================

THERMODYNAMIC METHODS USED FOR EACH SET

THERMODYNAMIC SET SRKM01 (DEFAULT)

PROPERTY METHOD

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

KVALUE(VLE) SRK-MODIFIED-PANAGIOTOPOULOS-REID

KVALUE(LLE) UNSPECIFIED

KVALUE(SLE) UNSPECIFIED

LIQUID ENTHALPY SRK-MODIFIED-PANAGIOTOPOULOS-REID

VAPOR ENTHALPY SRK-MODIFIED-PANAGIOTOPOULOS-REID

LIQUID DENSITY API

VAPOR DENSITY SRK-MODIFIED-PANAGIOTOPOULOS-REID

LIQUID ENTROPY SRK-MODIFIED-PANAGIOTOPOULOS-REID

VAPOR ENTROPY SRK-MODIFIED-PANAGIOTOPOULOS-REID

LIQUID VISCOSITY IDEAL

VAPOR VISCOSITY IDEAL

LIQUID CONDUCTIVITY IDEAL

VAPOR CONDUCTIVITY IDEAL

SURFACE TENSION IDEAL

LIQUID DIFFUSIVITY UNSPECIFIED

SIMULATION SCIENCES INC. R PAGE H-1

PROJECT PRO/II VERSION 8.3 ELEC V7.0

PROBLEM CALCULATION

HISTORY 12/04/14

==============================================================================

*** PROBLEM SOLUTION BEGINS

FEED FLASH COMPLETE

** WARNING ** UNIT 1, 'R1' - Reaction phase is vapor, however, liquid phase

was detected within the reactor. The results may be in error.

UNIT 1 SOLVED - 'R1 '

*** PROBLEM SOLUTION REACHED

*** THIS RUN USED 6.41 PRO/II SIMULATION UNITS

*** RUN STATISTICS

STARTED 15:26:33 12/04/14 NO ERRORS

FINISHED 15:26:33 12/04/14 1 WARNING

RUN TIMES NO MESSAGES

INTERACTIVE 0 MIN, 0.00 SEC

CALCULATIONS 0 MIN, 0.07 SEC

TOTAL 0 MIN, 0.07 SEC

SIMULATION SCIENCES INC. R PAGE I-1

PROJECT PRO/II VERSION 8.3 ELEC V7.0

PROBLEM OUTPUT

INDEX 12/04/14

==============================================================================

PAGE CONTENTS

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

1 COMPONENT DATA

2 CALCULATION SEQUENCE AND RECYCLES

2 SEQUENCE MAP

3 PLANT MATERIAL BALANCE

PLUGFLOW REACTOR SUMMARY

4 UNIT 1, 'R1'

7 STREAM MOLAR COMPONENT RATES

8 STREAM MOLAR COMPONENT FRACTIONS

9 STREAM MOLAR COMPONENT PERCENTS

10 STREAM WEIGHT COMPONENT RATES

11 STREAM WEIGHT COMPONENT FRACTIONS

12 STREAM WEIGHT COMPONENT PERCENTS

13 STREAM SUMMARY

SIMULATION SCIENCES INC. R PAGE P-1

PROJECT PRO/II VERSION 8.3 ELEC V7.0

PROBLEM OUTPUT

COMPONENT DATA 12/04/14

==============================================================================

COMPONENT COMP. TYPE PHASE MOL. WEIGHT DENSITY

KG/M3

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

1 22PR LIBRARY VAP/LIQ/SOL 72.150 596.729

2 IPENTANE LIBRARY VAP/LIQ/SOL 72.150 625.850

3 PENTANE LIBRARY VAP/LIQ/SOL 72.150 631.126

4 22MB LIBRARY VAP/LIQ/SOL 86.177 653.234

5 23MB LIBRARY VAP/LIQ/SOL 86.177 665.521

6 2MP LIBRARY VAP/LIQ/SOL 86.177 657.054

7 3MP LIBRARY VAP/LIQ/SOL 86.177 668.608

8 HEXANE LIBRARY VAP/LIQ/SOL 86.177 664.452

COMPONENT NBP CRIT. TEMP. CRIT. PRES. CRIT. VOLM.

C C KPA M3/KG-MOL

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

1 22PR 9.500 160.630 3199.000 0.3036

2 IPENTANE 27.844 187.280 3381.000 0.3058

3 PENTANE 36.070 196.550 3370.000 0.3130

4 22MB 49.730 215.630 3081.000 0.3590

5 23MB 57.980 226.830 3127.000 0.3578

6 2MP 60.260 224.350 3010.000 0.3664

7 3MP 63.270 231.280 3124.000 0.3664

8 HEXANE 68.730 234.450 3025.000 0.3710

COMPONENT ACEN. FACT. HEAT FORM. G FORM. GLASS TEMP.

KJ/KG-MOL KJ/KG-MOL C

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

1 22PR 0.19636 -168070.00 -17140.00 MISSING

2 IPENTANE 0.22746 -153700.00 -14050.00 MISSING

3 PENTANE 0.25151 -146760.00 -8813.00 MISSING

4 22MB 0.23497 -184680.00 -8745.00 MISSING

5 23MB 0.24610 -176800.00 -3125.00 MISSING

6 2MP 0.27744 -174550.00 -5338.00 MISSING

7 3MP 0.27373 -172000.00 -3420.00 MISSING

8 HEXANE 0.30126 -166940.00 -66.34 MISSING

COMPONENT DATABANK(S) USED

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

1 22PR SIMSCI

2 IPENTANE SIMSCI

3 PENTANE SIMSCI

4 22MB

5 23MB

6 2MP SIMSCI

7 3MP

8 HEXANE SIMSCI

SIMULATION SCIENCES INC. R PAGE P-2

PROJECT PRO/II VERSION 8.3 ELEC V7.0

PROBLEM OUTPUT

CALCULATION SEQUENCE AND RECYCLES 12/04/14

==============================================================================

CALCULATION SEQUENCE

SEQ UNIT ID UNIT TYPE

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

1 R1 PLUGFLOW

SEQUENCE MAP

SEQ DESCRIPTION

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

1 PLUGFLOW 'R1'

SIMULATION SCIENCES INC. R PAGE P-3

PROJECT PRO/II VERSION 8.3 ELEC V7.0

PROBLEM OUTPUT

PLANT MATERIAL BALANCE 12/04/14

==============================================================================

FEED STREAMS: S1

PRODUCT STREAMS: S2

OVERALL PLANT MOLAR BALANCE

---------------- KG-MOL/HR ---------------- PERCENT

COMPONENT FEED +REACTION -PRODUCT =DEVIATION DEV

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

1 22PR 0.083 17.961 18.044 0.000 0.00

2 IPENTANE 6.237 17.961 24.198 0.000 0.00

3 PENTANE 87.595 -35.922 51.673 0.000 0.00

4 22MB 7.543 13.619 21.161 0.000 0.00

5 23MB 5.918 13.619 19.537 0.000 0.00

6 2MP 25.529 13.619 39.147 0.000 0.00

7 3MP 15.085 13.619 28.704 0.000 0.00

8 HEXANE 83.549 -54.475 29.074 0.000 0.00

TOTAL 231.539 0.000 231.539 0.000 0.00

OVERALL PLANT MASS BALANCE

------------------ KG/HR ------------------ PERCENT

COMPONENT FEED +REACTION -PRODUCT =DEVIATION DEV

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

1 22PR 6.00 1295.89 1301.89 0.00 0.00

2 IPENTANE 450.00 1295.89 1745.89 0.00 0.00

3 PENTANE 6320.00 -2591.79 3728.21 0.00 0.00

4 22MB 650.00 1173.62 1823.62 0.00 0.00

5 23MB 510.00 1173.62 1683.62 0.00 0.00

6 2MP 2200.00 1173.62 3373.62 0.00 0.00

7 3MP 1300.00 1173.62 2473.62 0.00 0.00

8 HEXANE 7200.00 -4694.47 2505.53 0.00 0.00

TOTAL 18636.00 0.00 18636.00 0.00 0.00

SIMULATION SCIENCES INC. R PAGE P-4

PROJECT PRO/II VERSION 8.3 ELEC V7.0

PROBLEM OUTPUT

PLUGFLOW REACTOR SUMMARY 12/04/14

==============================================================================

UNIT 1, 'R1'

OPERATING CONDITIONS

Reactor Flow Type Open Pipe

Thermal Specification Type Fixed Duty

Duty, M*KJ/HR 0.0000

Total Heat of Reaction at 25.00 C, M*KJ/HR -1.0558

Tubes 1

Diameter, MM 2.00E+03

Length, M 4.0000

Total Volume, M3 12.5664

Residence Time, sec 947.40

Maximum Velocity at 4.00 M from Inlet, M/sec 0.0044

Pressure Drop From Feed Stream, KPA 0.0000

REACTING SIDE Inlet Outlet

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

Feed S1

LIQUID Product S2

Temperature, C 170.00 182.63

Pressure, KPA 3100.0000 3050.0000

REACTION DATA

--------- Rates, KG-MOL/HR ---------- Fraction

Component Feed Change Product Converted

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

1 22PR 0.0832 17.9610 18.0442

2 IPENTANE 6.2370 17.9610 24.1980

3 PENTANE 87.5949 -35.9220 51.6729 0.4101

4 22MB 7.5426 13.6187 21.1613

5 23MB 5.9180 13.6187 19.5367

6 2MP 25.5288 13.6187 39.1475

7 3MP 15.0852 13.6187 28.7039

8 HEXANE 83.5488 -54.4746 29.0742 0.6520

Total 231.5386 0.0000 231.5386

KG-MOL/HR Fraction

Base Component Reaction Converted Converted

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

8 HEXANE 1 13.6187 0.1630

8 HEXANE 2 13.6187 0.1630

8 HEXANE 3 13.6187 0.1630

8 HEXANE 4 13.6187 0.1630

3 PENTANE 5 17.9610 0.2050

3 PENTANE 6 17.9610 0.2050

SIMULATION SCIENCES INC. R PAGE P-5

PROJECT PRO/II VERSION 8.3 ELEC V7.0

PROBLEM OUTPUT

PLUGFLOW REACTOR SUMMARY 12/04/14

==============================================================================

UNIT 1, 'R1' (Cont)

REACTOR MASS BALANCE

----------- Rates, KG/HR ------------ Fraction

Component Feed Change Product Converted

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

1 22PR 6.0000 1295.8927 1301.8927

2 IPENTANE 450.0000 1295.8927 1745.8927

3 PENTANE 6320.0000 -2591.7854 3728.2146 0.4101

4 22MB 650.0000 1173.6167 1823.6167

5 23MB 510.0000 1173.6167 1683.6167

6 2MP 2200.0000 1173.6167 3373.6167

7 3MP 1300.0000 1173.6167 2473.6167

8 HEXANE 7200.0000 -4694.4670 2505.5330 0.6520

TOTAL 18636.0000 0.0000 18636.0000

SIMULATION SCIENCES INC. R PAGE P-6

PROJECT PRO/II VERSION 8.3 ELEC V7.0

PROBLEM OUTPUT

PLUGFLOW REACTOR SUMMARY 12/04/14

==============================================================================

UNIT 1, 'R1' (Cont)

REACTOR PROFILES

Reactor

Distance Temp Pres

M C KPA

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

0 0.0000 170.00 3100.0000

1 0.4000 171.51 3095.0000

2 0.8000 173.34 3090.0000

3 1.2000 174.98 3085.0000

4 1.6000 176.44 3080.0000

5 2.0000 177.76 3075.0000

6 2.4000 178.94 3070.0000

7 2.8000 180.00 3065.0000

8 3.2000 180.97 3060.0000

9 3.6000 181.84 3055.0000

10 4.0000 182.63 3050.0000

-- Component Mole Fractions vs. Distance from Inlet

Distance 8 3 1 2 4

M HEXANE PENTANE 22PR IPENTANE 22MB

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

0 0.0000 0.36084195 0.37831684 0.00035916 0.02693712 0.03257601

1 0.4000 0.32302335 0.35794320 0.01054598 0.03712394 0.04203066

2 0.8000 0.28953720 0.33888266 0.02007625 0.04665421 0.05040220

3 1.2000 0.25985240 0.32104102 0.02899707 0.05557502 0.05782340

4 1.6000 0.23349040 0.30432083 0.03735717 0.06393512 0.06441390

5 2.0000 0.21003961 0.28863418 0.04520049 0.07177844 0.07027660

6 2.4000 0.18914510 0.27390169 0.05256674 0.07914469 0.07550022

7 2.8000 0.17049998 0.26005148 0.05949184 0.08606980 0.08016150

8 3.2000 0.15383819 0.24701837 0.06600840 0.09258635 0.08432695

9 3.6000 0.13892855 0.23474314 0.07214601 0.09872397 0.08805436

10 4.0000 0.12556964 0.22317189 0.07793164 0.10450959 0.09139409

Distance 5 6 7

M 23MB 2MP 3MP

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

0 0.0000 0.02555964 0.11025726 0.06515202

1 0.4000 0.03501429 0.11971191 0.07460667

2 0.8000 0.04338583 0.12808345 0.08297821

3 1.2000 0.05080703 0.13550465 0.09039941

4 1.6000 0.05739753 0.14209515 0.09698991

5 2.0000 0.06326022 0.14795785 0.10285260

6 2.4000 0.06848385 0.15318148 0.10807623

7 2.8000 0.07314513 0.15784276 0.11273751

8 3.2000 0.07731058 0.16200820 0.11690296

9 3.6000 0.08103799 0.16573561 0.12063037

10 4.0000 0.08437772 0.16907534 0.12397010

SIMULATION SCIENCES INC. R PAGE P-7

PROJECT PRO/II VERSION 8.3 ELEC V7.0

PROBLEM OUTPUT

STREAM MOLAR COMPONENT RATES 12/04/14

==============================================================================

STREAM ID S1 S2

NAME

PHASE LIQUID LIQUID

THERMO ID SRKM01 SRKM01

FLUID RATES, KG-MOL/HR

1 22PR 0.0832 18.0442

2 IPENTANE 6.2370 24.1980

3 PENTANE 87.5949 51.6729

4 22MB 7.5426 21.1613

5 23MB 5.9180 19.5367

6 2MP 25.5288 39.1475

7 3MP 15.0852 28.7039

8 HEXANE 83.5488 29.0742

TOTAL RATE, KG-MOL/HR 231.5386 231.5386

TEMPERATURE, C 170.0000 182.6260

PRESSURE, KPA 3100.0000 3050.0000

ENTHALPY, M*KJ/HR 8.2662 9.0900

MOLECULAR WEIGHT 80.4877 80.4877

MOLE FRAC VAPOR 0.0000 0.0000

MOLE FRAC LIQUID 1.0000 1.0000

SIMULATION SCIENCES INC. R PAGE P-8

PROJECT PRO/II VERSION 8.3 ELEC V7.0

PROBLEM OUTPUT

STREAM MOLAR COMPONENT FRACTIONS 12/04/14

==============================================================================

STREAM ID S1 S2

NAME

PHASE LIQUID LIQUID

THERMO ID SRKM01 SRKM01

FLUID MOLAR FRACTIONS

1 22PR 3.5916E-04 0.0779

2 IPENTANE 0.0269 0.1045

3 PENTANE 0.3783 0.2232

4 22MB 0.0326 0.0914

5 23MB 0.0256 0.0844

6 2MP 0.1103 0.1691

7 3MP 0.0652 0.1240

8 HEXANE 0.3608 0.1256

TOTAL RATE, KG-MOL/HR 231.5386 231.5386

TEMPERATURE, C 170.0000 182.6260

PRESSURE, KPA 3100.0000 3050.0000

ENTHALPY, M*KJ/HR 8.2662 9.0900

MOLECULAR WEIGHT 80.4877 80.4877

MOLE FRAC VAPOR 0.0000 0.0000

MOLE FRAC LIQUID 1.0000 1.0000

SIMULATION SCIENCES INC. R PAGE P-9

PROJECT PRO/II VERSION 8.3 ELEC V7.0

PROBLEM OUTPUT

STREAM MOLAR COMPONENT PERCENTS 12/04/14

==============================================================================

STREAM ID S1 S2

NAME

PHASE LIQUID LIQUID

THERMO ID SRKM01 SRKM01

FLUID MOLAR PERCENTS

1 22PR 0.0359 7.7932

2 IPENTANE 2.6937 10.4510

3 PENTANE 37.8317 22.3172

4 22MB 3.2576 9.1394

5 23MB 2.5560 8.4378

6 2MP 11.0257 16.9075

7 3MP 6.5152 12.3970

8 HEXANE 36.0842 12.5570

TOTAL RATE, KG-MOL/HR 231.5386 231.5386

TEMPERATURE, C 170.0000 182.6260

PRESSURE, KPA 3100.0000 3050.0000

ENTHALPY, M*KJ/HR 8.2662 9.0900

MOLECULAR WEIGHT 80.4877 80.4877

MOLE FRAC VAPOR 0.0000 0.0000

MOLE FRAC LIQUID 1.0000 1.0000

SIMULATION SCIENCES INC. R PAGE P-10

PROJECT PRO/II VERSION 8.3 ELEC V7.0

PROBLEM OUTPUT

STREAM WEIGHT COMPONENT RATES 12/04/14

==============================================================================

STREAM ID S1 S2

NAME

PHASE LIQUID LIQUID

THERMO ID SRKM01 SRKM01

FLUID RATES, KG/HR

1 22PR 6.0000 1301.8927

2 IPENTANE 450.0000 1745.8927

3 PENTANE 6320.0000 3728.2146

4 22MB 650.0000 1823.6167

5 23MB 510.0000 1683.6167

6 2MP 2200.0000 3373.6167

7 3MP 1300.0000 2473.6167

8 HEXANE 7200.0000 2505.5330

TOTAL RATE, KG/HR 18636.0000 18636.0000

TEMPERATURE, C 170.0000 182.6260

PRESSURE, KPA 3100.0000 3050.0000

ENTHALPY, M*KJ/HR 8.2662 9.0900

MOLECULAR WEIGHT 80.4877 80.4877

WEIGHT FRAC VAPOR 0.0000 0.0000

WEIGHT FRAC LIQUID 1.0000 1.0000

SIMULATION SCIENCES INC. R PAGE P-11

PROJECT PRO/II VERSION 8.3 ELEC V7.0

PROBLEM OUTPUT

STREAM WEIGHT COMPONENT FRACTIONS 12/04/14

==============================================================================

STREAM ID S1 S2

NAME

PHASE LIQUID LIQUID

THERMO ID SRKM01 SRKM01

FLUID WEIGHT FRACTIONS

1 22PR 3.2196E-04 0.0699

2 IPENTANE 0.0241 0.0937

3 PENTANE 0.3391 0.2001

4 22MB 0.0349 0.0979

5 23MB 0.0274 0.0903

6 2MP 0.1181 0.1810

7 3MP 0.0698 0.1327

8 HEXANE 0.3863 0.1344

TOTAL RATE, KG/HR 18636.0000 18636.0000

TEMPERATURE, C 170.0000 182.6260

PRESSURE, KPA 3100.0000 3050.0000

ENTHALPY, M*KJ/HR 8.2662 9.0900

MOLECULAR WEIGHT 80.4877 80.4877

WEIGHT FRAC VAPOR 0.0000 0.0000

WEIGHT FRAC LIQUID 1.0000 1.0000

SIMULATION SCIENCES INC. R PAGE P-12

PROJECT PRO/II VERSION 8.3 ELEC V7.0

PROBLEM OUTPUT

STREAM WEIGHT COMPONENT PERCENTS 12/04/14

==============================================================================

STREAM ID S1 S2

NAME

PHASE LIQUID LIQUID

THERMO ID SRKM01 SRKM01

FLUID WEIGHT PERCENTS

1 22PR 0.0322 6.9859

2 IPENTANE 2.4147 9.3684

3 PENTANE 33.9129 20.0054

4 22MB 3.4879 9.7855

5 23MB 2.7366 9.0342

6 2MP 11.8051 18.1027

7 3MP 6.9757 13.2733

8 HEXANE 38.6349 13.4446

TOTAL RATE, KG/HR 18636.0000 18636.0000

TEMPERATURE, C 170.0000 182.6260

PRESSURE, KPA 3100.0000 3050.0000

ENTHALPY, M*KJ/HR 8.2662 9.0900

MOLECULAR WEIGHT 80.4877 80.4877

WEIGHT FRAC VAPOR 0.0000 0.0000

WEIGHT FRAC LIQUID 1.0000 1.0000

SIMULATION SCIENCES INC. R PAGE P-13

PROJECT PRO/II VERSION 8.3 ELEC V7.0

PROBLEM OUTPUT

STREAM SUMMARY 12/04/14

==============================================================================

STREAM ID S1 S2

NAME

PHASE LIQUID LIQUID

THERMO ID SRKM01 SRKM01

----- TOTAL STREAM -----

RATE, KG-MOL/HR 231.539 231.539

K*KG/HR 18.636 18.636

STD LIQ RATE, M3/HR 28.633 28.805

TEMPERATURE, C 170.000 182.626

PRESSURE, KPA 3100.000 3050.000

MOLECULAR WEIGHT 80.488 80.488

ENTHALPY, M*KJ/HR 8.266 9.090

KJ/KG 443.559 487.768

MOLE FRACTION LIQUID 1.0000 1.0000

REDUCED TEMP (KAYS RULE) 0.9047 0.9417

PRES (KAYS RULE) 0.9766 0.9603

ACENTRIC FACTOR 0.2724 0.2561

WATSON K (UOPK) 12.862 12.867

STD LIQ DENSITY, KG/M3 650.859 646.972

SPECIFIC GRAVITY 0.6515 0.6476

API GRAVITY 85.690 86.996

-------- VAPOR ---------

RATE, KG-MOL/HR N/A N/A

K*KG/HR N/A N/A

K*M3/HR N/A N/A

NORM VAP RATE(1), K*M3/HR N/A N/A

SPECIFIC GRAVITY (AIR=1.0) N/A N/A

MOLECULAR WEIGHT N/A N/A

ENTHALPY, KJ/KG N/A N/A

CP, KJ/KG-C N/A N/A

DENSITY, KG/K*M3 N/A N/A

Z (FROM DENSITY) N/A N/A

TH COND, W/M-K N/A N/A

VISCOSITY, PAS N/A N/A

KVIS (VISC/DENS), CSTOKE N/A N/A

(1) NORMAL VAPOR VOLUME IS 22.414 M3/KG-MOLE (273.15 K AND 1 ATM)

SIMULATION SCIENCES INC. R PAGE P-14

PROJECT PRO/II VERSION 8.3 ELEC V7.0

PROBLEM OUTPUT

STREAM SUMMARY 12/04/14

==============================================================================

STREAM ID S1 S2

NAME

PHASE LIQUID LIQUID

THERMO ID SRKM01 SRKM01

-------- LIQUID --------

RATE, KG-MOL/HR 231.539 231.539

K*KG/HR 18.636 18.636

M3/HR 39.392 42.184

GAL/MIN 173.435 185.730

STD LIQ RATE, M3/HR 28.633 28.805

SPECIFIC GRAVITY (H2O=1.0) 0.6515 0.6476

MOLECULAR WEIGHT 80.488 80.488

ENTHALPY, KJ/KG 443.559 487.768

CP, KJ/KG-C 3.279 3.660

DENSITY, KG/M3 473.097 441.779

Z (FROM DENSITY) 0.1431 0.1466

SURFACE TENSION, N/M 2.9365E-03 1.7921E-03

THERMAL COND, W/M-K 0.07947 0.08262

VISCOSITY, PAS 1.00795E-04 8.71733E-05

KVIS (VISC/DENS), CSTOKE 0.2131 0.1973