Приложение б. Результаты расчета равновесного реактора

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

$ Generated on: Thu Dec 04 15:12:12 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

EQUREACTOR UID=R1

FEED S1

PRODUCT M=S2

OPERATION ADIABATIC, PHASE=L, DP=50

RXCALCULATION MODEL=STOIC

RXSTOIC RXSET=ISOMER_C5-C6

REACTION 1

EQUILIBRIUM(K,KG,M3,KPA) A=7.0578, D=-0.0133

REACTION 2

EQUILIBRIUM(K,KG,M3,KPA) A=2.1878, D=-0.0033

REACTION 3

EQUILIBRIUM(K,KG,M3,KPA) A=15.438, D=-0.0348

REACTION 4

EQUILIBRIUM(K,KG,M3,KPA) A=4.8835, D=-0.0105

REACTION 5

EQUILIBRIUM(K,KG,M3,KPA) A=13.736, D=-0.0273

REACTION 6

EQUILIBRIUM(K,KG,M3,KPA) A=45.355, D=-0.1058

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-1

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 EQUILIBRIUM REACTOR SRKM01

SIMULATION SCIENCES INC. R PAGE R-2

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

UNIT 1 SOLVED - 'R1 '

*** PROBLEM SOLUTION REACHED

*** THIS RUN USED 2.00 PRO/II SIMULATION UNITS

*** RUN STATISTICS

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

FINISHED 15:12:04 12/04/14 NO WARNINGS

RUN TIMES NO MESSAGES

INTERACTIVE 0 MIN, 0.00 SEC

CALCULATIONS 0 MIN, 0.03 SEC

TOTAL 0 MIN, 0.03 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

EQUILIBRIUM REACTOR SUMMARY

4 UNIT 1, 'R1'

6 STREAM MOLAR COMPONENT RATES

7 STREAM MOLAR COMPONENT FRACTIONS

8 STREAM MOLAR COMPONENT PERCENTS

9 STREAM WEIGHT COMPONENT RATES

10 STREAM WEIGHT COMPONENT FRACTIONS

11 STREAM WEIGHT COMPONENT PERCENTS

12 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 EQUIL REAC

SEQUENCE MAP

SEQ DESCRIPTION

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

1 EQUIL REAC '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 1.074 1.157 0.000 0.00

2 IPENTANE 6.237 66.641 72.878 0.000 0.00

3 PENTANE 87.595 -67.715 19.880 0.000 0.00

4 22MB 7.543 4.627 12.169 0.000 0.00

5 23MB 5.918 14.464 20.382 0.000 0.00

6 2MP 25.529 24.539 50.068 0.000 0.00

7 3MP 15.085 21.478 36.563 0.000 0.00

8 HEXANE 83.549 -65.107 18.442 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 77.48 83.48 0.00 0.00

2 IPENTANE 450.00 4808.14 5258.14 0.00 0.00

3 PENTANE 6320.00 -4885.62 1434.38 0.00 0.00

4 22MB 650.00 398.70 1048.70 0.00 0.00

5 23MB 510.00 1246.48 1756.48 0.00 0.00

6 2MP 2200.00 2114.69 4314.69 0.00 0.00

7 3MP 1300.00 1850.89 3150.89 0.00 0.00

8 HEXANE 7200.00 -5610.76 1589.24 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

EQUILIBRIUM REACTOR SUMMARY 12/04/14

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

UNIT 1, 'R1'

** WARNING ** UNIT 1, 'R1' - Activity BASIS has been changed to Molar

Fraction for the Liquid phase reaction.

OPERATING CONDITIONS

REACTOR TYPE ADIABATIC REACTOR

DUTY, M*KJ/HR -2.61682E-09

TOTAL HEAT OF REACTION AT 25.00 C, M*KJ/HR -1.0055

INLET OUTLET

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

FEED S1

LIQUID PRODUCT S2

TEMPERATURE, C 170.00 182.42

PRESSURE, KPA 3100.0000 3050.0000

REACTION DATA

--------- RATES, KG-MOL/HR ---------- FRACTION

COMPONENT FEED CHANGE PRODUCT CONVERTED

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

1 22PR 0.0832 1.0739 1.1570

2 IPENTANE 6.2370 66.6407 72.8777

3 PENTANE 87.5949 -67.7145 19.8804 0.7730

4 22MB 7.5426 4.6266 12.1692

5 23MB 5.9180 14.4641 20.3822

6 2MP 25.5288 24.5389 50.0677

7 3MP 15.0852 21.4778 36.5630

8 HEXANE 83.5488 -65.1073 18.4415 0.7793

TOTAL 231.5386 0.0000 231.5386

KG-MOL/HR FRACTION

BASE COMPONENT REACTION CONVERTED CONVERTED(1)

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

8 HEXANE 1 24.5389 0.2937

8 HEXANE 2 21.4778 0.2571

8 HEXANE 3 4.6266 0.0554

8 HEXANE 4 14.4641 0.1731

3 PENTANE 5 66.6407 0.7608

3 PENTANE 6 1.0739 0.0123

SIMULATION SCIENCES INC. R PAGE P-5

PROJECT PRO/II VERSION 8.3 ELEC V7.0

PROBLEM OUTPUT

EQUILIBRIUM 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 77.4792 83.4792

2 IPENTANE 450.0000 4808.1433 5258.1433

3 PENTANE 6320.0000 -4885.6225 1434.3775 0.7730

4 22MB 650.0000 398.7039 1048.7039

5 23MB 510.0000 1246.4777 1756.4777

6 2MP 2200.0000 2114.6893 4314.6893

7 3MP 1300.0000 1850.8925 3150.8925

8 HEXANE 7200.0000 -5610.7634 1589.2366 0.7793

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

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 1.1570

2 IPENTANE 6.2370 72.8777

3 PENTANE 87.5949 19.8804

4 22MB 7.5426 12.1692

5 23MB 5.9180 20.3822

6 2MP 25.5288 50.0677

7 3MP 15.0852 36.5630

8 HEXANE 83.5488 18.4415

TOTAL RATE, KG-MOL/HR 231.5386 231.5386

TEMPERATURE, C 170.0000 182.4160

PRESSURE, KPA 3100.0000 3050.0000

ENTHALPY, M*KJ/HR 8.2662 9.0592

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-7

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 4.9971E-03

2 IPENTANE 0.0269 0.3148

3 PENTANE 0.3783 0.0859

4 22MB 0.0326 0.0526

5 23MB 0.0256 0.0880

6 2MP 0.1103 0.2162

7 3MP 0.0652 0.1579

8 HEXANE 0.3608 0.0796

TOTAL RATE, KG-MOL/HR 231.5386 231.5386

TEMPERATURE, C 170.0000 182.4160

PRESSURE, KPA 3100.0000 3050.0000

ENTHALPY, M*KJ/HR 8.2662 9.0592

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 PERCENTS 12/04/14

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

STREAM ID S1 S2

NAME

PHASE LIQUID LIQUID

THERMO ID SRKM01 SRKM01

FLUID MOLAR PERCENTS

1 22PR 0.0359 0.4997

2 IPENTANE 2.6937 31.4754

3 PENTANE 37.8317 8.5862

4 22MB 3.2576 5.2558

5 23MB 2.5560 8.8029

6 2MP 11.0257 21.6239

7 3MP 6.5152 15.7913

8 HEXANE 36.0842 7.9648

TOTAL RATE, KG-MOL/HR 231.5386 231.5386

TEMPERATURE, C 170.0000 182.4160

PRESSURE, KPA 3100.0000 3050.0000

ENTHALPY, M*KJ/HR 8.2662 9.0592

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 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 83.4792

2 IPENTANE 450.0000 5258.1433

3 PENTANE 6320.0000 1434.3775

4 22MB 650.0000 1048.7039

5 23MB 510.0000 1756.4777

6 2MP 2200.0000 4314.6893

7 3MP 1300.0000 3150.8925

8 HEXANE 7200.0000 1589.2366

TOTAL RATE, KG/HR 18636.0000 18636.0000

TEMPERATURE, C 170.0000 182.4160

PRESSURE, KPA 3100.0000 3050.0000

ENTHALPY, M*KJ/HR 8.2662 9.0592

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-10

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 4.4795E-03

2 IPENTANE 0.0241 0.2821

3 PENTANE 0.3391 0.0770

4 22MB 0.0349 0.0563

5 23MB 0.0274 0.0943

6 2MP 0.1181 0.2315

7 3MP 0.0698 0.1691

8 HEXANE 0.3863 0.0853

TOTAL RATE, KG/HR 18636.0000 18636.0000

TEMPERATURE, C 170.0000 182.4160

PRESSURE, KPA 3100.0000 3050.0000

ENTHALPY, M*KJ/HR 8.2662 9.0592

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 PERCENTS 12/04/14

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

STREAM ID S1 S2

NAME

PHASE LIQUID LIQUID

THERMO ID SRKM01 SRKM01

FLUID WEIGHT PERCENTS

1 22PR 0.0322 0.4479

2 IPENTANE 2.4147 28.2150

3 PENTANE 33.9129 7.6968

4 22MB 3.4879 5.6273

5 23MB 2.7366 9.4252

6 2MP 11.8051 23.1524

7 3MP 6.9757 16.9076

8 HEXANE 38.6349 8.5278

TOTAL RATE, KG/HR 18636.0000 18636.0000

TEMPERATURE, C 170.0000 182.4160

PRESSURE, KPA 3100.0000 3050.0000

ENTHALPY, M*KJ/HR 8.2662 9.0592

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 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 28.730

TEMPERATURE, C 170.000 182.416

PRESSURE, KPA 3100.000 3050.000

MOLECULAR WEIGHT 80.488 80.488

ENTHALPY, M*KJ/HR 8.266 9.059

KJ/KG 443.559 486.112

MOLE FRACTION LIQUID 1.0000 1.0000

REDUCED TEMP (KAYS RULE) 0.9047 0.9397

PRES (KAYS RULE) 0.9766 0.9556

ACENTRIC FACTOR 0.2724 0.2554

WATSON K (UOPK) 12.862 12.840

STD LIQ DENSITY, KG/M3 650.859 648.659

SPECIFIC GRAVITY 0.6515 0.6493

API GRAVITY 85.690 86.427

-------- 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-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

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

RATE, KG-MOL/HR 231.539 231.539

K*KG/HR 18.636 18.636

M3/HR 39.392 41.954

GAL/MIN 173.435 184.716

STD LIQ RATE, M3/HR 28.633 28.730

SPECIFIC GRAVITY (H2O=1.0) 0.6515 0.6493

MOLECULAR WEIGHT 80.488 80.488

ENTHALPY, KJ/KG 443.559 486.112

CP, KJ/KG-C 3.279 3.638

DENSITY, KG/M3 473.097 444.205

Z (FROM DENSITY) 0.1431 0.1459

SURFACE TENSION, N/M 2.9365E-03 1.7585E-03

THERMAL COND, W/M-K 0.07947 0.08472

VISCOSITY, PAS 1.00795E-04 9.16054E-05

KVIS (VISC/DENS), CSTOKE 0.2131 0.2062