Generated by PRO

$ Generated by PRO/II Keyword Generation System <version 9.2>

$ Generated on: Wed Dec 04 16:46:15 2013

TITLE PROJECT=APPBRIEF, PROBLEM=R7A, USER=SIMSCI, DATE=MAR92

PRINT INPUT=ALL, MBALANCE=OFF, SEQMAP=OFF

SEQUENCE SIMSCI

COMPONENT DATA

LIBID 1,C2/2,C3/3,IC4/4,NC4/5,IC5/6,NC5/7,NC6/8,NC7/9,NC8/ &

10,NC10, BANK=SIMSCI,PROCESS

ASSAY FIT=SPLINE, CONVERSION=API94, CURVEFIT=CURRENT, &

KVRECONCILE=TAILS, FORMATION=CURRENT

THERMODYNAMIC DATA

METHOD SYSTEM=GS, SET=GS01, DEFAULT

WATER PROPERTY=SATURATED

STREAM DATA

PROPERTY STREAM=FD, TEMPERATURE=100, PRESSURE=100, PHASE=M, &

RATE(M)=956.001, COMPOSITION(M)=1,1/2,5/3,100/4,100/5,150/ &

6,175/7,200/8,100/9,75/10,50, NORMALIZE

UNIT OPERATIONS

COLUMN UID=STAB, NAME=STABILIZER

PARAMETER TRAY=21,IO

FEED FD,17

PRODUCT OVHD(M)=OV,93.0001, BTMS(M)=BT, SUPERSEDE=ON

CONDENSER TYPE=BUBB, PRESSURE=65

DUTY 1,1,,CONDENSER

DUTY 2,21,,2

PRINT PROPTABLE=PART

ESTIMATE MODEL=CONVENTIONAL, RRATIO=3

PRESSURE 1,64.9999/2,70/21,75

SPEC ID=COL1SPEC1, STREAM=OV, RATE(LBM/H), COMP=5,6,WET, &

VALUE=0.3

SPEC ID=COL1SPEC2, STREAM=BT, RVP, VALUE=12

VARY DNAME=CONDENSER,2

OPTIMIZER UID=OPT1, NAME=OPTIMIZER

VARY ID=VARY_4, COLUMN=STAB, FTRAY(1), MINI=2, MAXI=20, &

STEPSIZE=1

OBJECTIVE COLUMN=STAB, DNAME(BTU/HR)=2, MINUS,8.5, MINIMIZE

OPTPARAMETER IPRINT=ALL

END

SIMULATION SCIENCES INC. R PAGE R-1

PROJECT APPBRIEF PRO/II VERSION 9.2 ELEC V9.0.6

PROBLEM R7A INPUT SIMSCI

THERMODYNAMIC DATA MAR92

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

DATA FOR SET 'GS01'

GRAYSON STREED PURE COMPONENT DATA

COMP CRITICAL CRITICAL ACENTRIC MOLAR SOLUBILITY

TEMPERATURE PRESSURE FACTOR VOLUME PARAMETER

DEG F PSIA FT3/LB-MOL

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

1 89.91 706.62 0.0995 0.8847 6.0614

2 206.02 616.12 0.1523 1.2126 6.4036

3 274.98 529.10 0.1808 1.6857 6.1445

4 305.55 550.56 0.2002 1.5455 6.6969

5 369.10 490.37 0.2275 1.8757 6.7751

6 385.79 488.78 0.2515 1.8589 7.0391

7 454.01 438.74 0.3013 2.1042 7.2835

8 512.69 397.40 0.3495 2.3551 7.4301

9 563.99 361.14 0.3996 2.6170 7.5279

10 652.19 306.03 0.4923 3.1368 7.6745





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

THERMODYNAMIC SETS USED FOR EACH UNIT OPERATION

DEFAULT METHOD IS GS01

THERMODYNAMIC SET UNIT OPERATIONS

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

GS01 STAB

UNIT IDENTIFIER UNIT OPERATION THERMODYNAMIC SET

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

STAB COLUMN GS01

OPT1 OPTIMIZER





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

THERMODYNAMIC METHODS USED FOR EACH SET

THERMODYNAMIC SET GS01 (DEFAULT)

PROPERTY METHOD

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

KVALUE(VLE) GRAYSON-STREED

KVALUE(LLE) UNSPECIFIED

KVALUE(SLE) UNSPECIFIED

LIQUID ENTHALPY CURL-PITZER

VAPOR ENTHALPY CURL-PITZER

LIQUID DENSITY API

VAPOR DENSITY SOAVE-REDLICH-KWONG

LIQUID ENTROPY CURL-PITZER

VAPOR ENTROPY CURL-PITZER

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


PROBLEM R7A CALCULATION SIMSCI

HISTORY MAR92

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

*** PROBLEM SOLUTION BEGINS

FEED FLASH COMPLETE

INNER 0 : E(ENTH+SPEC) = 2.861E-08

ITER 1 E(K) = 0.000E+00 E(ENTH+SPEC) = 2.861E-08 E(SUM) = 1.167E-07

DAMP = 1.000E+00


RETRIEVING PREVIOUS MATRIX

INNER 1 : E(ENTH+SPEC) = 1.428E-09 ALPHA = 1.0000


UNIT 1 SOLVED - 'STAB '

*** OPTIMIZER CYCLE 1 - END OF BASE CASE - OBJE = -9.02619E-03

UNIT 2 NOT SOLVED - 'OPT1 '


CALCULATING NEW MATRIX



ITER 1 E(K) = 7.526E-04 E(ENTH+SPEC) = 2.087E-06 E(SUM) = 1.312E-03


*** OPTIMIZER CYCLE 1 - END OF PERTURBATION 1

OPTIMIZER - END OF CYCLE 1 OBJECTIVE = -9.02619E-03

VARY CURRENT NEXT PERTURBATION

INDEX VARY VALUE VARY VALUE STEP SIZE

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

1 1.40271E+01 1.30271E+01 1.40271E-01

OPTIMIZER HISTORY AFTER CYCLE 1

---- VALUES ----

CYCLE BEST - 1

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

VARY 1 1.4027E+01

OBJECTIVE -9.0262E-03

*** END OPTIMIZER HISTORY













DAMP = 1.000E+00









HISTORY MAR92

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


DAMP = 1.000E+00






*** OPTIMIZER CYCLE 2 - END OF BASE CASE - OBJE = 3.37760E-02

*** OPTIMIZER LINE SEARCH BEGINS



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

1 1.30271E+01 1.38691E+01 1.30271E-01


---- VALUES ----

CYCLE BEST - 1 2

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

VARY 1 1.4027E+01 1.3027E+01

OBJECTIVE -9.0262E-03 3.3776E-02











DAMP = 1.000E+00




DAMP = 1.000E+00




*** OPTIMIZER CYCLE 2 - END OF BASE CASE - LINE SEARCH STEP 1

*** OPTIMIZER LINE SEARCH CONTINUES OBJE = 1.44547E-02



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

1 1.38691E+01 1.40113E+01 1.38691E-01


---- VALUES ----

CYCLE BEST - 1 2

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




HISTORY MAR92

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

VARY 1 1.4027E+01 1.3869E+01

OBJECTIVE -9.0262E-03 1.4455E-02









DAMP = 1.000E+00




DAMP = 1.000E+00





*** OPTIMIZER LINE SEARCH COMPLETE OBJE = -9.84835E-03








*** OPTIMIZER CYCLE 2 - END OF PERTURBATION 1

OPTIMIZER - END OF CYCLE 2 OBJECTIVE = -9.84835E-03



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

1 1.40113E+01 1.30113E+01 1.40113E-01


---- VALUES ----

CYCLE 1 BEST - 2

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

VARY 1 1.4027E+01 1.4011E+01

OBJECTIVE -9.0262E-03 -9.8484E-03













HISTORY MAR92

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





DAMP = 1.000E+00







DAMP = 1.000E+00






*** OPTIMIZER CYCLE 3 - END OF BASE CASE - OBJE = 3.37779E-02

*** OPTIMIZER LINE SEARCH BEGINS



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

1 1.30113E+01 1.38380E+01 1.30113E-01


---- VALUES ----

CYCLE 1 BEST - 2 3

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

VARY 1 1.4027E+01 1.4011E+01 1.3011E+01

OBJECTIVE -9.0262E-03 -9.8484E-03 3.3778E-02











DAMP = 1.000E+00




DAMP = 1.000E+00





*** OPTIMIZER LINE SEARCH CONTINUES OBJE = 1.71908E-02




HISTORY MAR92

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



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

1 1.38380E+01 1.39940E+01 1.38380E-01


---- VALUES ----

CYCLE 1 BEST - 2 3

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

VARY 1 1.4027E+01 1.4011E+01 1.3838E+01

OBJECTIVE -9.0262E-03 -9.8484E-03 1.7191E-02










DAMP = 1.000E+00




DAMP = 1.000E+00






*** OPTIMIZER LINE SEARCH CONTINUES OBJE = -9.29186E-03

*** OPTIMIZER LINE SEARCH COMPLETE OBJE = -9.29186E-03

*** RELATIVE CHANGES IN VARIABLES ARE ALL LESS THAN TOLERANCE **

*** BEST OBJECTIVE FUNCTION = -9.84835E-03 AT CYCLE NUMBER 2



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

1 1.39940E+01 1.40113E+01 1.39940E-01


---- VALUES ----

CYCLE 1 BEST - 2 3

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

VARY 1 1.4027E+01 1.4011E+01 1.3994E+01

OBJECTIVE -9.0262E-03 -9.8484E-03 -9.2919E-03








HISTORY MAR92

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

DAMP = 1.000E+00


RETRIEVING PREVIOUS MATRIX




UNIT 2 SOLVED - 'OPT1 '

*** PROBLEM SOLUTION REACHED

*** THIS RUN USED 154.16 PRO/II SIMULATION UNITS

*** RUN STATISTICS

STARTED 16:46:02 12/04/13 NO ERRORS

FINISHED 16:46:08 12/04/13 NO WARNINGS

RUN TIMES NO MESSAGES

INTERACTIVE 0 MIN, 0.00 SEC

CALCULATIONS 0 MIN, 5.65 SEC

TOTAL 0 MIN, 5.65 SEC

SIMULATION SCIENCES INC. R PAGE I-1


PROBLEM R7A OUTPUT SIMSCI

INDEX MAR92

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

PAGE CONTENTS

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

1 COMPONENT DATA

2 CALCULATION SEQUENCE AND RECYCLES

OPTIMIZER SUMMARY

3 UNIT 2, 'OPT1', 'OPTIMIZER'

COLUMN SUMMARY

4 UNIT 1, 'STAB', 'STABILIZER'

6 TRAY RATES AND DENSITIES

8 TRAY TRANSPORT PROPERTIES

9 STREAM MOLAR COMPONENT RATES

10 STREAM SUMMARY

SIMULATION SCIENCES INC. R PAGE P-1



COMPONENT DATA MAR92

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

COMPONENT COMP. TYPE PHASE MOL. WEIGHT API

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

1 C2 LIBRARY VAP/LIQ/SOL 30.070 266.652

2 C3 LIBRARY VAP/LIQ/SOL 44.097 147.986

3 IC4 LIBRARY VAP/LIQ/SOL 58.123 119.212

4 NC4 LIBRARY VAP/LIQ/SOL 58.123 110.417

5 IC5 LIBRARY VAP/LIQ/SOL 72.150 94.370






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

F F PSIA FT3/LB-MOL

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

1 C2 -127.480 89.906 706.624 2.3307

2 C3 -43.672 206.024 616.120 3.2037

3 IC4 10.904 274.982 529.097 4.2080

4 NC4 31.100 305.546 550.563 4.0847

5 IC5 82.119 369.104 490.372 4.8984

6 NC5 96.926 385.790 488.777 5.0138

7 NC6 155.714 454.010 438.739 5.9428

8 NC7 209.174 512.690 397.403 6.8559

9 NC8 258.224 563.990 361.144 7.7850

10 NC10 345.479 652.190 306.030 9.6111

COMPONENT ACEN. FACT. HEAT FORM. G FORM.

BTU/LB-MOL BTU/LB-MOL

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

1 C2 0.09949 -36036.11 -13723.13

2 C3 0.15229 -45004.30 -10485.81

3 IC4 0.18077 -57687.02 -8925.19

4 NC4 0.20016 -54079.97 -7179.71

5 IC5 0.22746 -66079.11 -6040.41

6 NC5 0.25151 -63095.44 -3788.91

7 NC6 0.30126 -71771.28 -28.52

8 NC7 0.34947 -80674.98 3510.32

9 NC8 0.39955 -89746.35 6878.76

10 NC10 0.49233 -107248.50 14264.83

COMPONENT DATABANK(S) USED

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

1 C2 SIMSCI

2 C3 SIMSCI

3 IC4 SIMSCI

4 NC4 SIMSCI

5 IC5 SIMSCI

6 NC5 SIMSCI

7 NC6 SIMSCI

8 NC7 SIMSCI

9 NC8 SIMSCI

10 NC10 SIMSCI




CALCULATION SEQUENCE AND RECYCLES MAR92

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

CALCULATION SEQUENCE

SEQ UNIT ID UNIT TYPE

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

1 STAB COLUMN

2 OPT1 OPTIMIZER




OPTIMIZER SUMMARY MAR92

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

UNIT 2, 'OPT1', 'OPTIMIZER'

BEST OBJECTIVE FUNCTION = -9.84835E-03 AT CYCLE NUMBER 2

*** LINE SEARCH BEGINS AT CYCLES 2 3

*** LINE SEARCH COMPLETE AT CYCLE 2

VARY --------- VARIABLE ----------

INDEX INITIAL VALUE OPTIMUM VALUE

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

1 1.40271E+01 1.40113E+01

OPTIMIZER HISTORY

---- VALUES ----

CYCLE 1 BEST - 2 3

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

VARY 1 1.4027E+01 1.4011E+01 1.3994E+01

OBJECTIVE -9.0262E-03 -9.8484E-03 -9.2919E-03




COLUMN SUMMARY MAR92

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

UNIT 1, 'STAB', 'STABILIZER'

TOTAL NUMBER OF ITERATIONS

IN/OUT METHOD 74

COLUMN SUMMARY

---------- NET FLOW RATES ----------- HEATER

TRAY TEMP PRESSURE LIQUID VAPOR FEED PRODUCT DUTIES

DEG F PSIA LB-MOL/HR MM BTU/HR

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

1C 95.3 65.00 244.2 149.3L -3.3082

2 106.7 70.00 250.9 393.4

3 109.1 70.26 249.9 400.1

4 110.7 70.53 248.5 399.2

5 112.2 70.79 246.7 397.8

6 113.9 71.05 244.2 396.0

7 116.2 71.32 240.7 393.4

8 119.2 71.58 236.1 389.9

9 123.2 71.84 230.7 385.3

10 128.0 72.11 224.8 379.9

11 133.4 72.37 218.5 374.1

12 139.4 72.63 209.6 367.8

13 147.6 72.89 187.4 358.9

14 166.9 73.16 1504.0 336.6 956.0L

15 169.8 73.42 1511.1 697.3

16 173.2 73.68 1517.3 704.4

17 177.6 73.95 1524.1 710.5

18 183.5 74.21 1532.3 717.4

19 191.5 74.47 1540.9 725.6

20 203.2 74.74 1528.7 734.2

21 228.3 75.00 722.0 806.7L 8.4910

FEED AND PRODUCT STREAMS

TYPE STREAM PHASE FROM TO LIQUID FLOW RATES HEAT RATES

TRAY TRAY FRAC LB-MOL/HR MM BTU/HR

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

FEED FD LIQUID 14 1.0000 956.00 3.0364

PROD OV LIQUID 1 149.27 0.3143

PROD BT LIQUID 21 806.73 7.9048

OVERALL MOLE BALANCE, (FEEDS - PRODUCTS) 3.3043E-13

OVERALL HEAT BALANCE, (H(IN) - H(OUT) ) 3.6035E-05





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

UNIT 1, 'STAB', 'STABILIZER' (Cont)

SPECIFICATIONS

SPECIFICATION PARAMETER TRAY COMP SPECIFICATION SPECIFIED CALCULATED

NUMBER TYPE NO NO TYPE VALUE VALUE

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

1 (ACTIVE) STRM OV 1 5- 6 MOL RATE 3.000E-01 3.000E-01

2 (ACTIVE) STRM BT 21 RVP 1.200E+01 1.200E+01

REFLUX RATIOS

-------- REFLUX RATIOS --------

MOLAR WEIGHT STD L VOL

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

REFLUX / FEED STREAM FD 0.2554 0.1794 0.2052

REFLUX / LIQUID DISTILLATE 1.6356 1.6356 1.6356





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


TRAY NET VAPOR RATES AND DENSITIES

--------------- RATES ---------------

TRAY MW ACTUAL DENS Z FROM STANDARD ACTUAL

LB/FT3 DENSITY M LB/HR M FT3/HR M FT3/HR

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

2 57.495 0.74381 0.89015 22.620 149.300 30.411

3 57.801 0.74795 0.88954 23.128 151.844 30.922

4 57.908 0.75022 0.88935 23.116 151.485 30.812

5 58.005 0.75242 0.88924 23.075 150.963 30.668

6 58.144 0.75477 0.88919 23.024 150.271 30.505

7 58.356 0.75731 0.88923 22.960 149.306 30.318

8 58.672 0.76008 0.88938 22.878 147.970 30.099

9 59.111 0.76319 0.88961 22.778 146.233 29.846

10 59.673 0.76673 0.88988 22.672 144.182 29.570

11 60.321 0.77059 0.89014 22.567 141.971 29.285

12 61.013 0.77405 0.89054 22.442 139.580 28.992

13 61.779 0.77491 0.89179 22.173 136.198 28.613

14 62.904 0.76247 0.89763 21.176 127.751 27.773

15 63.406 0.76851 0.89674 44.212 264.609 57.530

16 63.918 0.77393 0.89604 45.021 267.290 58.171

17 64.606 0.78033 0.89525 45.905 269.636 58.827

18 65.612 0.78896 0.89417 47.067 272.224 59.657

19 67.078 0.80091 0.89263 48.668 275.334 60.766

20 69.224 0.81645 0.89075 50.823 278.612 62.249

21 72.944 0.83221 0.89046 52.662 273.971 63.280





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


TRAY NET LIQUID RATES AND DENSITIES

--------------- RATES ---------------

TRAY MW ACTUAL DENS Z FROM STD LIQ ACTUAL

LB/FT3 DENSITY M LB/HR FT3/HR GAL/MIN

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

1 57.495 33.895 0.01851 14.038 395.659 51.633

2 57.984 33.609 0.01987 14.546 407.260 53.959

3 58.155 33.614 0.01991 14.534 405.714 53.906

4 58.312 33.630 0.01998 14.493 403.664 53.728

5 58.537 33.654 0.02006 14.442 401.318 53.502

6 58.883 33.690 0.02017 14.378 398.376 53.207

7 59.402 33.744 0.02031 14.295 394.548 52.816

8 60.134 33.820 0.02049 14.196 389.773 52.333

9 61.082 33.912 0.02069 14.090 384.339 51.800

10 62.197 34.011 0.02091 13.985 378.641 51.263

11 63.417 34.112 0.02114 13.859 372.288 50.654

12 64.830 34.234 0.02140 13.590 361.866 49.493

13 67.214 34.498 0.02179 12.594 330.807 45.514

14 75.725 35.571 0.02316 113.891 2876.490 399.188

15 75.906 35.516 0.02323 114.700 2892.848 402.636

16 76.179 35.464 0.02331 115.584 2909.851 406.344

17 76.601 35.401 0.02340 116.746 2931.912 411.152

18 77.236 35.321 0.02351 118.348 2962.343 417.737

19 78.202 35.221 0.02366 120.502 3002.657 426.547

20 80.030 35.137 0.02393 122.341 3025.427 434.100

21 86.373 35.331 0.02484 69.679 1686.245 245.883





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


TRAY TRANSPORT PROPERTIES

TRAY - THERMAL CONDUCTIVITY - ------ VISCOSITY ------- -- SURFACE --

BTU/HR-FT-F CP TENSION

LIQUID VAPOR LIQUID VAPOR DYNE/CM

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

1 5.4952E-02 0.0000E+00 1.4554E-01 0.0000E+00 9.2848E+00

2 5.4152E-02 1.0520E-02 1.3976E-01 8.0156E-03 8.8706E+00

3 5.4215E-02 1.0576E-02 1.3855E-01 8.0288E-03 8.8693E+00

4 5.4280E-02 1.0620E-02 1.3782E-01 8.0423E-03 8.8788E+00

5 5.4317E-02 1.0663E-02 1.3741E-01 8.0567E-03 8.8881E+00

6 5.4329E-02 1.0712E-02 1.3726E-01 8.0738E-03 8.8994E+00

7 5.4320E-02 1.0775E-02 1.3738E-01 8.0958E-03 8.9159E+00

8 5.4289E-02 1.0857E-02 1.3774E-01 8.1246E-03 8.9388E+00

9 5.4232E-02 1.0962E-02 1.3831E-01 8.1609E-03 8.9661E+00

10 5.4147E-02 1.1087E-02 1.3904E-01 8.2032E-03 8.9931E+00

11 5.4040E-02 1.1229E-02 1.3994E-01 8.2489E-03 9.0180E+00

12 5.3945E-02 1.1389E-02 1.4132E-01 8.2989E-03 9.0546E+00

13 5.3969E-02 1.1622E-02 1.4470E-01 8.3699E-03 9.1658E+00

14 5.4713E-02 1.2234E-02 1.5993E-01 8.5584E-03 9.6889E+00

15 5.4585E-02 1.2295E-02 1.5869E-01 8.5710E-03 9.6121E+00

16 5.4448E-02 1.2372E-02 1.5750E-01 8.5898E-03 9.5346E+00

17 5.4256E-02 1.2469E-02 1.5630E-01 8.6146E-03 9.4397E+00

18 5.3967E-02 1.2591E-02 1.5517E-01 8.6456E-03 9.3149E+00

19 5.3547E-02 1.2745E-02 1.5432E-01 8.6836E-03 9.1519E+00

20 5.2969E-02 1.2973E-02 1.5457E-01 8.7371E-03 8.9548E+00

21 5.3493E-02 1.3533E-02 1.6012E-01 8.8682E-03 8.7826E+00




STREAM MOLAR COMPONENT RATES MAR92

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

STREAM ID BT FD OV

NAME

PHASE LIQUID LIQUID LIQUID

THERMO ID GS01 GS01 GS01

FLUID RATES, LB-MOL/HR

1 C2 1.8918E-06 1.0000 1.0000

2 C3 7.3776E-03 5.0000 4.9926

3 IC4 10.2297 100.0001 89.7704

4 NC4 46.7900 100.0001 53.2101

5 IC5 149.7252 150.0002 0.2750

6 NC5 174.9752 175.0002 0.0250

7 NC6 200.0002 200.0002 1.9512E-07

8 NC7 100.0001 100.0001 1.1896E-12

9 NC8 75.0001 75.0001 1.4525E-17

10 NC10 50.0001 50.0001 0.0000

TOTAL RATE, LB-MOL/HR 806.7278 956.0010 149.2732

TEMPERATURE, F 228.2506 100.0000 95.3268

PRESSURE, PSIA 75.0000 100.0000 65.0000

ENTHALPY, MM BTU/HR 7.9048 3.0364 0.3143

MOLECULAR WEIGHT 86.3726 81.8634 57.4945

MOLE FRAC VAPOR 0.0000 0.0000 0.0000

MOLE FRAC LIQUID 1.0000 1.0000 1.0000




STREAM SUMMARY MAR92

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

STREAM ID BT FD OV

NAME



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

RATE, LB-MOL/HR 806.728 956.001 149.273

M LB/HR 69.679 78.262 8.582

STD LIQ RATE, FT3/HR 1686.245 1928.145 241.900

TEMPERATURE, F 228.251 100.000 95.327

PRESSURE, PSIA 75.000 100.000 65.000


ENTHALPY, MM BTU/HR 7.905 3.036 0.314

BTU/LB 113.446 38.798 36.626

MOLE FRACTION LIQUID 1.0000 1.0000 1.0000

REDUCED TEMP (KAYS RULE) 0.7626 0.6381 0.7478

PRES (KAYS RULE) 0.1681 0.2169 0.1202

ACENTRIC FACTOR 0.2963 0.2792 0.1863

WATSON K (UOPK) 12.856 12.951 13.718

STD LIQ DENSITY, LB/FT3 41.322 40.589 35.479

SPECIFIC GRAVITY 0.6626 0.6508 0.5689

API GRAVITY 82.063 85.920 117.234

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

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

M LB/HR N/A N/A N/A

M FT3/HR N/A N/A N/A

STD VAP RATE(1), M FT3/HR N/A N/A N/A

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

MOLECULAR WEIGHT N/A N/A N/A

ENTHALPY, BTU/LB N/A N/A N/A

CP, BTU/LB-F N/A N/A N/A

DENSITY, LB/M FT3 N/A N/A N/A

Z (FROM DENSITY) N/A N/A N/A

TH COND, BTU/HR-FT-F N/A N/A N/A

VISCOSITY, CP N/A N/A N/A

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

(1) STANDARD VAPOR VOLUME IS 379.48 FT3/LB-MOLE (60 F AND 14.696 PSIA)




STREAM SUMMARY MAR92

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

STREAM ID BT FD OV

NAME



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

RATE, LB-MOL/HR 806.728 956.001 149.273

M LB/HR 69.679 78.262 8.582

FT3/HR 1972.187 1989.693 253.200

GAL/MIN 245.883 248.066 31.568

STD LIQ RATE, FT3/HR 1686.245 1928.145 241.900

SPECIFIC GRAVITY (H2O=1.0) 0.6626 0.6508 0.5689


ENTHALPY, BTU/LB 113.446 38.798 36.626

CP, BTU/LB-F 0.711 0.542 0.567

DENSITY, LB/FT3 35.331 39.333 33.895

Z (FROM DENSITY) 0.0248 0.0347 0.0185

SURFACE TENSION, DYNE/CM 8.7826 14.7566 9.2848

THERMAL COND, BTU/HR-FT-F 0.05349 0.06422 0.05495

VISCOSITY, CP 0.16012 0.24469 0.14554

KVIS (VISC/DENS), CSTOKE 0.2829 0.3884 0.2681

Date post:	01-Jan-2016
Category:	Documents
Upload:	juliio-zalaz
View:	17 times
Download:	2 times

Generated by PRO

Documents