TM

MM MM AAAAAA X X

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M M M AAAAAA X PC PROCESS SIMULATOR

M M A A X X

M M A A X X

RUN ID : MAX3

DEST

RELEASE: 1.1 FEBRUARY 18, 1998

SERIAL NUMBER:20658 WEDNESDAY

4:56:08 P.M.

THIS COPY OF MAX LICENSED TO

LTH

FOR: Kemiteknik

MAX IS A TRADEMARK OF HOTLINE:

ASPEN TECHNOLOGY, INC. U.S.A. 617/577-0337

TEN CANAL PARK EUROPE (32) 2/732-6300

CAMBRIDGE, MASSACHUSETTS 02141, U.S.A.

617/577-0100

MAX REL: 1.1 RUN ID: MAX3 SER# 20658 02/18/98 PAGE I

DEST

TABLE OF CONTENTS

SIMULATION INFORMATION SECTION................. 1

BLOCK STATUS.............................. 1

FLOWSHEET SECTION.............................. 2

FLOWSHEET CONNECTIVITY BY STREAMS......... 2

FLOWSHEET CONNECTIVITY BY BLOCKS.......... 2

CONVERGENCE STATUS SUMMARY................ 2

DESIGN-SPEC: BOT......................... 2

DESIGN-SPEC: DES......................... 2

CONVERGENCE BLOCK: $OLVER01.............. 3

CONVERGENCE BLOCK: $OLVER02.............. 3

COMPUTATIONAL SEQUENCE.................... 4

OVERALL FLOWSHEET BALANCE................. 4

PHYSICAL PROPERTIES SECTION.................... 5

COMPONENTS................................ 5

U-O-S BLOCK SECTION............................ 6

BLOCK: BOTVVX MODEL: HEATER............ 6

BLOCK: FEEDVVX MODEL: HEATER............ 6

BLOCK: KOLONN MODEL: RADFRAC........... 7

BLOCK: PUMP MODEL: PUMP.............. 11

STREAM SECTION................................. 12

7 8 BOTTEN DEST DESTFEED.................. 12

FEED...................................... 13

MAX REL: 1.1 RUN ID: MAX3 SER# 20658 02/18/98 PAGE 1

DEST

SIMULATION INFORMATION SECTION

BLOCK STATUS

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

****************************************************************************

* *

* ALL UNIT OPERATION BLOCKS WERE COMPLETED NORMALLY *

* *

* ALL CONVERGENCE BLOCKS WERE COMPLETED NORMALLY *

* *

****************************************************************************

MAX REL: 1.1 RUN ID: MAX3 SER# 20658 02/18/98 PAGE 2

DEST

FLOWSHEET SECTION

FLOWSHEET CONNECTIVITY BY STREAMS

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

STREAM SOURCE DEST STREAM SOURCE DEST

FEED ---- PUMP DESTFEED FEEDVVX KOLONN

7 PUMP FEEDVVX DEST KOLONN ----

BOTTEN KOLONN BOTVVX 8 BOTVVX ----

FLOWSHEET CONNECTIVITY BY BLOCKS

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

BLOCK INLETS OUTLETS

FEEDVVX 7 DESTFEED

PUMP FEED 7

KOLONN DESTFEED DEST BOTTEN

BOTVVX BOTTEN 8

CONVERGENCE STATUS SUMMARY

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

DESIGN-SPEC SUMMARY

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

DESIGN CONV

SPEC ERROR TOLERANCE ERR/TOL VARIABLE STAT BLOCK

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

BOT -0.11934E-03 0.10000E-02 -0.11934 2.4478 # $OLVER01

DES -0.21217E-03 0.10000E-02 -0.21217 30.900 # $OLVER02

# = CONVERGED

* = NOT CONVERGED

LB = AT LOWER BOUNDS

UB = AT UPPER BOUNDS

DESIGN-SPEC: BOT

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

SAMPLED VARIABLES:

XC1 : SENTENCE=COMPS VARIABLE=X ID1=C1 ID2=14 IN UOS BLOCK KOLONN

XC2 : SENTENCE=COMPS VARIABLE=X ID1=C2 ID2=14 IN UOS BLOCK KOLONN

XC3 : SENTENCE=COMPS VARIABLE=X ID1=C3 ID2=14 IN UOS BLOCK KOLONN

SPECIFICATION:

MAKE XC1+XC2+XC3 APPROACH 0.10000

WITHIN 0.0010000

MANIPULATED VARIABLES:

VARY : SENTENCE=COL-SPECS VARIABLE=MOLE-RR IN UOS BLOCK KOLONN

LOWER LIMIT = 1.00000

UPPER LIMIT = 10.0000

FINAL VALUE = 2.44782

MAX REL: 1.1 RUN ID: MAX3 SER# 20658 02/18/98 PAGE 3

DEST

FLOWSHEET SECTION

DESIGN-SPEC: DES

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

SAMPLED VARIABLES:

XC1 : C1 MASSFRAC IN STREAM BOTTEN

XC2 : C2 MOLEFRAC IN STREAM BOTTEN

XC3 : C3 MOLEFRAC IN STREAM BOTTEN

XC4I : I-C4 MOLEFRAC IN STREAM DEST

XC4N : N-C4 MOLEFRAC IN STREAM DEST

XC5I : I-C5 MOLEFRAC IN STREAM DEST

XC5N : N-C5 MOLEFRAC IN STREAM DEST

SPECIFICATION:

MAKE XC4I+XC4N+XC5I+XC5N APPROACH 0.050000

WITHIN 0.0010000

MANIPULATED VARIABLES:

VARY : SENTENCE=PRODUCTS VARIABLE=MOLE-FLOW ID1=BOTTEN IN UOS BLOCK

KOLONN

LOWER LIMIT = 1.00000 KMOL/HR

UPPER LIMIT = 300.000 KMOL/HR

FINAL VALUE = 30.9000 KMOL/HR

CONVERGENCE BLOCK: $OLVER01

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

SPECS: BOT

MAXIT= 30 STEP-SIZE= 100.00 % OF RANGE

MAX-STEP= 100. % OF RANGE

XTOL= 1.000000E-08

THE NEW ALGORITHM WAS USED WITH BRACKETING=NO .

METHOD: SECANT STATUS: CONVERGED

TOTAL NUMBER OF ITERATIONS: 4

*** FINAL VALUES ***

VARIABLE VALUE PREV VALUE ERR/TOL

BLOCK-VAR 0.2447820D+01 0.2447820D+01 -.1193442D+00

*** ITERATION HISTORY ***

DESIGN-SPEC ID: BOT

ITERATION VARIABLE ERROR ERR/TOL

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

1 1.976 0.1511E-01 15.11

2 2.066 0.1169E-01 11.69

3 2.373 0.1930E-02 1.930

4 2.448 -0.1193E-03 -0.1193

MAX REL: 1.1 RUN ID: MAX3 SER# 20658 02/18/98 PAGE 4

DEST

FLOWSHEET SECTION

CONVERGENCE BLOCK: $OLVER02

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

SPECS: DES

MAXIT= 30 STEP-SIZE= 100.00 % OF RANGE

MAX-STEP= 100. % OF RANGE

XTOL= 1.000000E-08

THE NEW ALGORITHM WAS USED WITH BRACKETING=NO .

METHOD: SECANT STATUS: CONVERGED

TOTAL NUMBER OF ITERATIONS: 1

*** FINAL VALUES ***

VARIABLE VALUE PREV VALUE ERR/TOL

BLOCK-VAR KMOL/HR 0.3090000D+02 0.3090000D+02 -.2121675D+00

*** ITERATION HISTORY ***

DESIGN-SPEC ID: DES

ITERATION VARIABLE ERROR ERR/TOL

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

1 30.90 -0.2122E-03 -0.2122

COMPUTATIONAL SEQUENCE

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

SEQUENCE USED WAS:

PUMP FEEDVVX $OLVER02 $OLVER01 KOLONN $OLVER01<--- $OLVER02<--- BOTVVX

OVERALL FLOWSHEET BALANCE

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

*** MASS AND ENERGY BALANCE ***

IN OUT RELATIVE DIFF.

CONVENTIONAL COMPONENTS (KMOL/HR )

C1 4.31000 4.31000 -0.162273E-10

C2 38.7900 38.7900 -0.161315E-10

C3 131.886 131.886 -0.109596E-10

I-C4 65.0810 65.0810 0.731101E-11

N-C4 179.727 179.727 0.869618E-11

I-C5 9.48200 9.48200 0.912401E-11

N-C5 1.72400 1.72400 0.912624E-11

TOTAL BALANCE

MOLE(KMOL/HR ) 431.000 431.000 0.000000E+00

MASS(KG/HR ) 22088.8 22088.8 0.191049E-11

ENTHALPY(WATT ) -0.161030E+08 -0.163819E+08 0.170260E-01

MAX REL: 1.1 RUN ID: MAX3 SER# 20658 02/18/98 PAGE 5

DEST

PHYSICAL PROPERTIES SECTION

COMPONENTS

----------

ID FORMULA DATABANK NAME

C1 CH4 METHANE

C2 C2H6 ETHANE

C3 C3H8 PROPANE

I-C4 C4H10-2 ISOBUTANE

N-C4 C4H10-1 N-BUTANE

I-C5 C5H12-2 2-METHYL-BUTANE

N-C5 C5H12-1 N-PENTANE

MAX REL: 1.1 RUN ID: MAX3 SER# 20658 02/18/98 PAGE 6

DEST

U-O-S BLOCK SECTION

BLOCK: BOTVVX MODEL: HEATER

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

INLET STREAM: BOTTEN

OUTLET STREAM: 8

PROPERTY OPTION SET: RK-SOAVE REDLICH-KWONG-SOAVE EQUATION OF STATE

*** MASS AND ENERGY BALANCE ***

IN OUT RELATIVE DIFF.

TOTAL BALANCE

MOLE(KMOL/HR ) 275.840 275.840 0.000000E+00

MASS(KG/HR ) 15801.4 15801.4 0.000000E+00

ENTHALPY(WATT ) -0.103884E+08 -0.113915E+08 0.880588E-01

*** INPUT DATA ***

TWO PHASE TP FLASH

SPECIFIED TEMPERATURE C 18.0000

PRESSURE DROP BAR 0.0

MAXIMUM NO. ITERATIONS 30

CONVERGENCE TOLERANCE 0.00010000

*** RESULTS ***

OUTLET TEMPERATURE C 18.000

OUTLET PRESSURE BAR 18.000

HEAT DUTY WATT -0.10031E+07

VAPOR FRACTION 0.00000E+00

V-L PHASE EQUILIBRIUM :

COMP F(I) X(I) Y(I) K(I)

C1 0.20461E-06 0.20461E-06 0.53476E-05 5.2348

C2 0.53425E-03 0.53425E-03 0.33069E-02 1.2395

C3 0.99346E-01 0.99346E-01 0.21865 0.44063

I-C4 0.21903 0.21903 0.24145 0.22066

N-C4 0.64047 0.64047 0.52050 0.16268

I-C5 0.34370E-01 0.34370E-01 0.13841E-01 0.80605E-01

N-C5 0.62496E-02 0.62496E-02 0.22454E-02 0.71912E-01

BLOCK: FEEDVVX MODEL: HEATER

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

INLET STREAM: 7

OUTLET STREAM: DESTFEED

PROPERTY OPTION SET: RK-SOAVE REDLICH-KWONG-SOAVE EQUATION OF STATE

MAX REL: 1.1 RUN ID: MAX3 SER# 20658 02/18/98 PAGE 7

DEST

U-O-S BLOCK SECTION

BLOCK: FEEDVVX MODEL: HEATER (CONTINUED)

*** MASS AND ENERGY BALANCE ***

IN OUT RELATIVE DIFF.

TOTAL BALANCE

MOLE(KMOL/HR ) 431.000 431.000 0.000000E+00

MASS(KG/HR ) 22088.8 22088.8 0.000000E+00

ENTHALPY(WATT ) -0.160930E+08 -0.155430E+08 -0.341764E-01

*** INPUT DATA ***

TWO PHASE PQ FLASH

SPECIFIED PRESSURE BAR 18.0000

SPECIFIED HEAT DUTY WATT 550,000.

MAXIMUM NO. ITERATIONS 30

CONVERGENCE TOLERANCE 0.00010000

*** RESULTS ***

OUTLET TEMPERATURE C 64.583

OUTLET PRESSURE BAR 18.000

VAPOR FRACTION 0.24899E-01

V-L PHASE EQUILIBRIUM :

COMP F(I) X(I) Y(I) K(I)

C1 0.10000E-01 0.84273E-02 0.71591E-01 8.4953

C2 0.90000E-01 0.86212E-01 0.23835 2.7647

C3 0.30600 0.30454 0.36329 1.1929

I-C4 0.15100 0.15236 0.97675E-01 0.64106

N-C4 0.41700 0.42199 0.22157 0.52505

I-C5 0.22000E-01 0.22397E-01 0.64576E-02 0.28832

N-C5 0.40000E-02 0.40748E-02 0.10720E-02 0.26307

BLOCK: KOLONN MODEL: RADFRAC

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

INLETS - DESTFEED STAGE 9

OUTLETS - DEST STAGE 1

BOTTEN STAGE 14

PROPERTY OPTION SET: RK-SOAVE REDLICH-KWONG-SOAVE EQUATION OF STATE

*** MASS AND ENERGY BALANCE ***

IN OUT RELATIVE DIFF.

TOTAL BALANCE

MOLE(KMOL/HR ) 431.000 431.000 0.000000E+00

MASS(KG/HR ) 22088.8 22088.8 0.191049E-11

ENTHALPY(WATT ) -0.155430E+08 -0.153787E+08 -0.105657E-01

MAX REL: 1.1 RUN ID: MAX3 SER# 20658 02/18/98 PAGE 8

DEST

U-O-S BLOCK SECTION

BLOCK: KOLONN MODEL: RADFRAC (CONTINUED)

**********************

**** INPUT DATA ****

**********************

**** INPUT PARAMETERS ****

NUMBER OF STAGES 14

ALGORITHM OPTION STANDARD

ABSORBER OPTION NO

INITIALIZATION OPTION STANDARD

HYDRAULIC PARAMETER CALCULATIONS NO

INSIDE LOOP CONVERGENCE METHOD BROYDEN

DESIGN SPECIFICATION METHOD NESTED

MAXIMUM NO. OF OUTSIDE LOOP ITERATIONS 25

MAXIMUM NO. OF INSIDE LOOP ITERATIONS 10

MAXIMUM NUMBER OF FLASH ITERATIONS 50

FLASH TOLERANCE 0.00010000

OUTSIDE LOOP CONVERGENCE TOLERANCE 0.00010000

**** COL-SPECS ****

MOLAR VAPOR DIST / TOTAL DIST 0.0

MOLAR REFLUX RATIO 2.44782

DISTILLATE TO FEED RATIO 0.36000

**** PROFILES ****

P-SPEC STAGE 1 PRES, BAR 16.7000

MAX REL: 1.1 RUN ID: MAX3 SER# 20658 02/18/98 PAGE 9

DEST

U-O-S BLOCK SECTION

BLOCK: KOLONN MODEL: RADFRAC (CONTINUED)

*******************

**** RESULTS ****

*******************

TOP STAGE TEMPERATURE C 14.8280

BOTTOM STAGE TEMPERATURE C 98.7705

TOP STAGE LIQUID FLOW KMOL/HR 379.804

BOTTOM STAGE LIQUID FLOW KMOL/HR 275.840

TOP STAGE VAPOR FLOW KMOL/HR 0.0

BOTTOM STAGE VAPOR FLOW KMOL/HR 595.138

MOLAR REFLUX RATIO 2.44782

MOLAR BOILUP RATIO 2.15755

CONDENSER DUTY (W/O SUBCOOL) WATT -2,251,680.

REBOILER DUTY WATT 2,415,900.

**** MAXIMUM FINAL RELATIVE ERRORS ****

DEW POINT 0.54578E-04 STAGE= 6

BUBBLE POINT 0.25572E-04 STAGE= 1

COMPONENT MASS BALANCE 0.11288E-05 STAGE= 9 COMP=C1

ENERGY BALANCE 0.16365E-04 STAGE= 8

**** PROFILES ****

ENTHALPY

STAGE TEMPERATURE PRESSURE J/KMOL HEAT DUTY

C BAR LIQUID VAPOR WATT

1 14.828 16.700 -0.11579E+09 -0.91678E+08 -.22517+07

2 40.983 16.800 -0.11965E+09 -0.10063E+09

8 74.170 17.400 -0.13100E+09 -0.11067E+09

9 76.608 17.500 -0.13159E+09 -0.11115E+09

10 82.091 17.600 -0.13240E+09 -0.11361E+09

12 90.564 17.800 -0.13402E+09 -0.11701E+09

13 94.608 17.900 -0.13480E+09 -0.11847E+09

14 98.770 18.000 -0.13558E+09 -0.11982E+09 .24159+07

STAGE FLOW RATE FEED RATE PRODUCT RATE

KMOL/HR KMOL/HR KMOL/HR

LIQUID VAPOR LIQUID VAPOR MIXED LIQUID VAPOR

1 379.8 0.0000E+00 155.1600

2 402.2 535.0

8 372.2 529.7

9 820.6 527.3 431.0000

10 840.3 544.8

12 862.4 576.8

13 871.0 586.6

14 275.8 595.1 275.8400

MAX REL: 1.1 RUN ID: MAX3 SER# 20658 02/18/98 PAGE 10

DEST

U-O-S BLOCK SECTION

BLOCK: KOLONN MODEL: RADFRAC (CONTINUED)

**** X-PROFILE ****

STAGE C1 C2 C3 I-C4 N-C4 I-C5

1 .27777E-01 .24905 .67338 .30056E-01 .19722E-01 .87746E-05

2 .34213E-02 .11024 .75891 .71135E-01 .56249E-01 .47435E-04

8 .10494E-02 .32307E-01 .34565 .20350 .40724 .88195E-02

9 .10565E-02 .31735E-01 .31493 .19131 .44185 .16258E-01

10 .19209E-03 .15329E-01 .28625 .20571 .47289 .16688E-01

12 .63945E-05 .32151E-02 .19707 .22632 .55055 .19457E-01

13 .11668E-05 .13752E-02 .14728 .22768 .59559 .23888E-01

14 .20461E-06 .53425E-03 .99346E-01 .21903 .64047 .34370E-01

**** X-PROFILE ****

STAGE N-C5

1 .75459E-06

2 .45376E-05

8 .14340E-02

9 .28655E-02

10 .29284E-02

12 .33859E-02

13 .41909E-02

14 .62496E-02

**** Y-PROFILE ****

STAGE C1 C2 C3 I-C4 N-C4 I-C5

1 .21604 .41262 .36133 .65499E-02 .34646E-02 .71424E-06

2 .27777E-01 .24905 .67338 .30056E-01 .19722E-01 .87746E-05

8 .88735E-02 .96392E-01 .47312 .15681 .26107 .32457E-02

9 .89137E-02 .96080E-01 .44208 .15247 .29322 .62271E-02

10 .15913E-02 .47532E-01 .42408 .17727 .34129 .70883E-02

12 .51614E-04 .10309E-01 .31458 .21761 .44638 .95243E-02

13 .93053E-05 .44758E-02 .24303 .22974 .50826 .12444E-01

14 .16128E-05 .17650E-02 .16949 .23169 .57479 .19030E-01

**** Y-PROFILE ****

STAGE N-C5

1 .53346E-07

2 .75459E-06

8 .48603E-03

9 .10123E-02

10 .11521E-02

12 .15442E-02

13 .20392E-02

14 .32367E-02

**** K-VALUES ****

STAGE C1 C2 C3 I-C4 N-C4 I-C5

1 7.7786 1.6568 .53656 .21789 .17565 .81384E-01

2 8.1189 2.2592 .88731 .42254 .35062 .18499

8 8.4518 2.9830 1.3687 .77066 .64113 .36808

9 8.4352 3.0272 1.4037 .79700 .66366 .38304

10 8.2820 3.1003 1.4814 .86175 .72174 .42479

12 8.0699 3.2062 1.5962 .96155 .81081 .48954

13 7.9739 3.2543 1.6501 1.0091 .85339 .52095

14 7.8814 3.3036 1.7061 1.0578 .89745 .55369

MAX REL: 1.1 RUN ID: MAX3 SER# 20658 02/18/98 PAGE 11

DEST

U-O-S BLOCK SECTION

BLOCK: KOLONN MODEL: RADFRAC (CONTINUED)

**** K-VALUES ****

STAGE N-C5

1 .70683E-01

2 .16630

8 .33901

9 .35330

10 .39344

12 .45611

13 .48660

14 .51792

BLOCK: PUMP MODEL: PUMP

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

INLET STREAM: FEED

OUTLET STREAM: 7

PROPERTY OPTION SET: RK-SOAVE REDLICH-KWONG-SOAVE EQUATION OF STATE

*** MASS AND ENERGY BALANCE ***

IN OUT RELATIVE DIFF.

TOTAL BALANCE

MOLE(KMOL/HR ) 431.000 431.000 0.000000E+00

MASS(KG/HR ) 22088.8 22088.8 0.000000E+00

ENTHALPY(WATT ) -0.161030E+08 -0.160930E+08 -0.619987E-03

*** INPUT DATA ***

OUTLET PRESSURE (BAR ) 18.0000

DRIVER EFFICIENCY 1.00000

FLASH SPECIFICATIONS:

LIQUID PHASE CALCULATION

NO FLASH PERFORMED

MAXIMUM NUMBER OF ITERATIONS 30

TOLERANCE 0.00010000

*** RESULTS ***

VOLUMETRIC FLOW RATE (CUM/SEC ) 0.011738

PRESSURE CHANGE (BAR ) 5.20000

FLUID POWER (WATT ) 6,103.58

BRAKE POWER (WATT ) 9,983.62

ELECTRICITY (WATT ) 9,983.62

PUMP EFFICIENCY USED 0.61136

NET WORK (WATT ) -9,983.62

MAX REL: 1.1 RUN ID: MAX3 SER# 20658 02/18/98 PAGE 12

DEST

STREAM SECTION

7 8 BOTTEN DEST DESTFEED

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

STREAM ID 7 8 BOTTEN DEST DESTFEED

FROM : PUMP BOTVVX KOLONN KOLONN FEEDVVX

TO : FEEDVVX ---- BOTVVX ---- KOLONN

PHASE: LIQUID LIQUID LIQUID LIQUID MIXED

COMPONENTS: KMOL/HR

C1 4.3100 5.6441-05 5.6441-05 4.3099 4.3100

C2 38.7900 0.1473 0.1473 38.6426 38.7900

C3 131.8860 27.4036 27.4036 104.4823 131.8860

I-C4 65.0810 60.4174 60.4174 4.6635 65.0810

N-C4 179.7270 176.6669 176.6669 3.0600 179.7270

I-C5 9.4820 9.4806 9.4806 1.3615-03 9.4820

N-C5 1.7240 1.7238 1.7238 1.1708-04 1.7240

COMPONENTS: MOLE FRAC

C1 1.0000-02 2.0461-07 2.0461-07 2.7777-02 1.0000-02

C2 9.0000-02 5.3425-04 5.3425-04 0.2490 9.0000-02

C3 0.3060 9.9346-02 9.9346-02 0.6733 0.3060

I-C4 0.1510 0.2190 0.2190 3.0056-02 0.1510

N-C4 0.4170 0.6404 0.6404 1.9722-02 0.4170

I-C5 2.2000-02 3.4370-02 3.4370-02 8.7746-06 2.2000-02

N-C5 4.0000-03 6.2496-03 6.2496-03 7.5459-07 4.0000-03

TOTAL FLOW:

KMOL/HR 431.0000 275.8400 275.8400 155.1600 431.0000

KG/HR 2.2089+04 1.5801+04 1.5801+04 6287.4464 2.2089+04

CUM/SEC 1.1757-02 7.6547-03 9.6427-03 3.6274-03 1.6186-02

STATE VARIABLES:

TEMP C 35.6192 18.0000 98.7704 14.8279 64.5834

PRES BAR 18.0000 18.0000 18.0000 16.7000 18.0000

VFRAC 0.0 0.0 0.0 0.0 2.4899-02

LFRAC 1.0000 1.0000 1.0000 1.0000 0.9751

SFRAC 0.0 0.0 0.0 0.0 0.0

ENTHALPY:

J/KMOL -1.3442+08 -1.4867+08 -1.3558+08 -1.1579+08 -1.2983+08

J/KG -2.6228+06 -2.5953+06 -2.3668+06 -2.8573+06 -2.5332+06

WATT -1.6093+07 -1.1392+07 -1.0388+07 -4.9904+06 -1.5543+07

DENSITY:

KMOL/CUM 10.1830 10.0098 7.9461 11.8816 7.3968

KG/CUM 521.8814 573.4102 455.1894 481.4732 379.0902

AVG MW 51.2502 57.2846 57.2846 40.5223 51.2502

MAX REL: 1.1 RUN ID: MAX3 SER# 20658 02/18/98 PAGE 13

DEST

STREAM SECTION

FEED

----

STREAM ID FEED

FROM : ----

TO : PUMP

PHASE: LIQUID

COMPONENTS: KMOL/HR

C1 4.3100

C2 38.7900

C3 131.8860

I-C4 65.0810

N-C4 179.7270

I-C5 9.4820

N-C5 1.7240

COMPONENTS: MOLE FRAC

C1 1.0000-02

C2 9.0000-02

C3 0.3060

I-C4 0.1510

N-C4 0.4170

I-C5 2.2000-02

N-C5 4.0000-03

TOTAL FLOW:

KMOL/HR 431.0000

KG/HR 2.2089+04

CUM/SEC 1.1738-02

STATE VARIABLES:

TEMP C 35.0000

PRES BAR 12.8000

VFRAC 0.0

LFRAC 1.0000

SFRAC 0.0

ENTHALPY:

J/KMOL -1.3450+08

J/KG -2.6244+06

WATT -1.6103+07

DENSITY:

KMOL/CUM 10.1998

KG/CUM 522.7444

AVG MW 51.2502