How to view phase envelope reports and curves

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$ Generated by PRO/II Keyword Generation System $ Generated on: Sun Jul 05 22:04:55 2009 TITLE PROJECT=APPBRIEFS, PROBLEM=G1, USER=SIMSCI, DATE=NOV91 PRINT INPUT=ALL TOLERANCE FLASH=3E-6 SEQUENCE PROCESS COMPONENT DATA LIBID 1,N2/2,C1/3,C2/4,C3/5,NC4/6,NC5/7,NC6, BANK=PROCESS,SIMSCI THERMODYNAMIC DATA METHOD SYSTEM=SRK, SET=SRK01 STREAM DATA PROPERTY STREAM=1, TEMPERATURE=1.0004, PRESSURE=1, PHASE=M, & COMPOSITION(M,LBM/H)=1,1.4/2,94.3/3,2.6/4,0.68/5,0.44/6,0.37/ & 7,0.21 UNIT OPERATIONS PHASE UID=PHS1 EVAL STREAM=1,IPLOT=ON EVAL STREAM=1, LFRAC=0.05,IPLOT=ON EVAL STREAM=1, LFRAC=0.01,IPLOT=ON END SIMULATION SCIENCES INC. R PAGE R-1 PROJECT APPBRIEFS PRO/II VERSION 7.0 ELEC V6.6 PROBLEM G1 INPUT SIMSCI THERMODYNAMIC DATA NOV91 ============================================================================== VLE K-VALUE DATA FOR SET 'SRK01' SRK PURE COMPONENT DATA COMP CRITICAL CRITICAL ALPHA C1 C2 C3 TEMPERATURE PRESSURE TYPE DEG F PSIA ---- ---------- ---------- ----- ---------- ---------- ---------- 1 -232.42 492.31 1 0.5505 N/AN/A 2 -116.68 667.20 1 0.4964 N/AN/A 3 90.14 708.34 1 0.6335 N/AN/A 4 206.01 616.35 1 0.7165 N/AN/A 5 305.60 551.10 1 0.7897 N/AN/A 6 385.70 488.64 1 0.8634 N/AN/A 7 453.56 430.59 1 0.9280 N/AN/A SRK INTERACTION PARAMETERS KIJ = A(I,J) + B(I,J)/T + C(I,J)/T* * 2 IJ KA(I,J) KB(I,J) KC(I,J) UNITS FROM --- --- ---------- ---------- ---------- ----- ---- 1 2 0.0300 0.00 0.00 DEG K SIMSCI BANK 1 3 0.0600 0.00 0.00 DEG K SIMSCI BANK 1 4 0.0900 0.00 0.00 DEG K SIMSCI BANK 1 5 0.1130 0.00 0.00 DEG K SIMSCI BANK 1 6 0.1400 0.00 0.00 DEG K SIMSCI BANK 1 7 0.1660 0.00 0.00 DEG K SIMSCI BANK 2 3 -7.800E-03 0.00 0.00 DEG K SIMSCI BANK 2 4 9.000E-03 0.00 0.00 DEG K SIMSCI BANK 2 5 5.600E-03 0.00 0.00 DEG K SIMSCI BANK 2 6 0.0190 0.00 0.00 DEG K SIMSCI BANK 2 7 0.0374 0.00 0.00 DEG K SIMSCI BANK 3 4 -2.200E-03 0.00 0.00 DEG K SIMSCI BANK 3 5 6.700E-03 0.00 0.00 DEG K SIMSCI BANK 3 6 5.600E-03 0.00 0.00 DEG K SIMSCI BANK 3 7 -0.0156 0.00 0.00 DEG K SIMSCI BANK 4 6 0.0233 0.00 0.00 DEG K SIMSCI BANK 4 7 -2.200E-03 0.00 0.00 DEG K SIMSCI BANK 5 6 0.0204 0.00 0.00 DEG K SIMSCI BANK 5 7 -0.0111 0.00 0.00 DEG K SIMSCI BANK ALL PAIRS NOT PRINTED ARE DEFAULTED TO IDEAL SIMULATION SCIENCES INC. R PAGE R-4 PROJECT APPBRIEFS PRO/II VERSION 7.0 ELEC V6.6 PROBLEM G1 INPUT SIMSCI THERMODYNAMIC DATA NOV91 ====================================================================================== THERMODYNAMIC SETS USED FOR EACH UNIT OPERATION DEFAULT METHOD IS SRK01 THERMODYNAMIC SET UNIT OPERATIONS --------------- --------------- SRK01 UNIT IDENTIFIER UNIT OPERATION THERMODYNAMIC SET ------------------ ----------------- ----------------- PHS1 PHASE ENVELOPE SRK01 SIMULATION SCIENCES INC. R PAGE R-5 PROJECT APPBRIEFS PRO/II VERSION 7.0 ELEC V6.6 PROBLEM G1 INPUT SIMSCI THERMODYNAMIC DATA NOV91 ============================================================================== THERMODYNAMIC METHODS USED FOR EACH SET THERMODYNAMIC SET SRK01 (DEFAULT) PROPERTY METHOD -------- ------ KVALUE(VLE) SOAVE-REDLICH-KWONG KVALUE(LLE) UNSPECIFIED KVALUE(SLE) UNSPECIFIED LIQUID ENTHALPY SOAVE-REDLICH-KWONG VAPOR ENTHALPY SOAVE-REDLICH-KWONG LIQUID DENSITY API VAPOR DENSITY SOAVE-REDLICH-KWONG LIQUID ENTROPY SOAVE-REDLICH-KWONG VAPOR ENTROPY SOAVE-REDLICH-KWONG LIQUID VISCOSITY UNSPECIFIED VAPOR VISCOSITY UNSPECIFIED LIQUID CONDUCTIVITY UNSPECIFIED VAPOR CONDUCTIVITY UNSPECIFIED SURFACE TENSION UNSPECIFIED LIQUID DIFFUSIVITY UNSPECIFIED SIMULATION SCIENCES INC. R PAGE H-1 PROJECT APPBRIEFS PRO/II VERSION 7.0 ELEC V6.6 PROBLEM G1 CALCULATION SIMSCI HISTORY NOV91 ============================================================================== * * * PROBLEM SOLUTION BEGINS FEED FLASH COMPLETE UNIT 1 SOLVED - 'PHS1 ' * * * PROBLEM SOLUTION REACHED * * * THIS RUN USED 77.65 PRO/II SIMULATION UNITS * * * RUN STATISTICS STARTED 22:02:25 07/05/09 NO ERRORS FINISHED 22:02:26 07/05/09 NO WARNINGS RUN TIMES NO MESSAGES INTERACTIVE 0 MIN, 0.00 SEC CALCULATIONS 0 MIN, 0.11 SEC TOTAL 0 MIN, 0.11 SEC SIMULATION SCIENCES INC. R PAGE I-1 PROJECT APPBRIEFS PRO/II VERSION 7.0 ELEC V6.6 PROBLEM G1 OUTPUT SIMSCI INDEX NOV91 ============================================================================== PAGE CONTENTS ------ ---------------------------------------------------------------- 1 COMPONENT DATA 2 CALCULATION SEQUENCE AND RECYCLES PHASE ENVELOPE SUMMARY UNIT 1, 'PHS1' 3 SET 1, STREAM '1' PHASE ENVELOPE SUMMARY UNIT 1, 'PHS1' 6 SET 2, STREAM '1', LIQUID FRACTION = 0.050 PHASE ENVELOPE SUMMARY UNIT 1, 'PHS1' 8 SET 3, STREAM '1', LIQUID FRACTION = 0.010 10 STREAM MOLAR COMPONENT RATES 11 STREAM SUMMARY SIMULATION SCIENCES INC. R PAGE P-1 PROJECT APPBRIEFS PRO/II VERSION 7.0 ELEC V6.6 PROBLEM G1 OUTPUT SIMSCI COMPONENT DATA NOV91 ================================================================================ COMPONENT COMP. TYPE PHASE MOL. WEIGHT API -------------------------- ----------- ----------- ----------- ----------- 1 N2 LIBRARY VAP/LIQ 28.013 43.600 2 C1 LIBRARY VAP/LIQ 16.043 340.167 3 C2 LIBRARY VAP/LIQ 30.070 265.526 4 C3 LIBRARY VAP/LIQ 44.097 147.208 5 NC4 LIBRARY VAP/LIQ 58.124 110.629 6 NC5 LIBRARY VAP/LIQ 72.151 92.747 7 NC6 LIBRARY VAP/LIQ 86.178 81.602 COMPONENT NBP CRIT. TEMP. CRIT. PRES. CRIT. VOLM. FF PSIA FT3/LB-MOL -------------------------- ----------- ----------- ----------- ----------- ----------- 1 N2 -320.440 -232.420 492.314 1.4433 2 C1 -258.682 -116.680 667.195 1.5858 3 C2 -127.534 90.140 708.344 2.3707 4 C3 -43.726 206.006 616.348 3.2518 5 NC4 31.100 305.600 551.098 4.0847 6 NC5 96.933 385.700 488.641 4.8696 7 NC6 155.732 453.560 430.591 5.9268 COMPONENT ACEN. FACT. HEAT FORM. G FORM. BTU/LB-MOL BTU/LB-MOL -------------------------- ----------- ----------- ----------- 1 N2 0.04500 0.00 0.00 2 C1 0.01040 -32066.21 -21726.14 3 C2 0.09860 -36120.21 -13810.45 4 C3 0.15290 -44650.04 -10139.64 5 NC4 0.20130 -54072.23 -7169.22 6 NC5 0.25060 -62968.62 -3672.87 7 NC6 0.29430 -71771.28 -34.39 SIMULATION SCIENCES INC. R PAGE P-2 PROJECT APPBRIEFS PRO/II VERSION 7.0 ELEC V6.6 PROBLEM G1 OUTPUT SIMSCI CALCULATION SEQUENCE AND RECYCLES NOV91 ==================================================================================== CALCULATION SEQUENCE SEQ UNIT ID UNIT TYPE --- ---------------- ---------- 1 PHS1 PHASE ENV SIMULATION SCIENCES INC. R PAGE P-3 PROJECT APPBRIEFS PRO/II VERSION 7.0 ELEC V6.6 PROBLEM G1 OUTPUT SIMSCI PHASE ENVELOPE SUMMARY NOV91 ================================================================================ UNIT 1, 'PHS1' SET 1, STREAM '1' F PSIA CRICONDENTHERM 28.45 606.9 CRICONDENBAR -27.42 1328.6 CRITICAL POINT -95.15 853.1 MAX. TEMP AND PRES 28.45 1328.6 TEMP PRES TEMP PRES F PSIA F PSIA -------- -------- -------- -------- -------- 1 DEW PT -51.30 14.7 41 DEW PT -77.30 1065.8 2 DEW PT -51.08 14.8 42 DEW PT -82.61 1008.9 3 DEW PT -39.91 24.2 43 DEW PT -83.39 1000.1 4 DEW PT -21.82 51.3 44 DEW PT -88.94 934.4 5 DEW PT -10.53 80.5 45 DEW PT -94.02 868.7 6 DEW PT -1.77 114.2 46 DEW PT -94.20 866.4 7 DEW PT 4.36 146.2 47 DEW PT -96.97 828.9 8 DEW PT 13.11 211.9 48 DEW PT -96.97 828.9 9 DEW PT 17.07 254.1 49 DEW PT -96.96 829.0 10 DEW PT 18.89 277.6 50 DEW PT -95.82 844.1 11 DEW PT 22.90 343.3 51 DEW PT -94.64 858.8 12 DEW PT 25.58 408.9 52 DEW PT -94.58 859.5 13 DEW PT 27.26 474.6 53 DEW PT -94.58 859.5 14 DEW PT 28.16 540.3 54 CRITICAL -95.15 853.1 15 DEW PT 28.34 565.4 55 BBL PT -95.74 846.6 16 DEW PT 28.45 606.0 56 BBL PT -97.36 829.5 17 MAX TEMP 28.45 606.9 57 BBL PT -99.91 803.2 18 DEW PT 28.17 671.7 58 BBL PT -99.92 803.0 19 DEW PT 27.32 737.4 59 BBL PT -104.59 756.0 20 DEW PT 25.92 803.0 60 BBL PT -106.48 737.4 21 DEW PT 24.80 843.5 61 BBL PT -112.99 674.2 22 DEW PT 24.02 868.7 62 BBL PT -113.25 671.7 23 DEW PT 21.61 934.4 63 BBL PT -120.31 606.0 24 DEW PT 18.52 1000.1 64 BBL PT -125.86 556.7 25 DEW PT 14.68 1065.8 65 BBL PT -127.76 540.3 26 DEW PT 14.25 1072.3 66 BBL PT -129.38 526.6 27 DEW PT 10.06 1131.5 67 BBL PT -130.05 521.0 28 DEW PT 3.94 1197.1 68 BBL PT -130.38 518.2 29 DEW PT -1.10 1238.4 69 BBL PT -130.55 516.8 30 DEW PT -4.72 1262.8 70 BBL PT -130.64 516.0 31 DEW PT -10.49 1293.1 71 BBL PT -135.74 474.6 32 DEW PT -22.13 1325.3 72 BBL PT -144.42 408.9 33 DEW PT -26.36 1328.5 73 BBL PT -144.74 406.6 34 MAX PRES -27.42 1328.6 74 BBL PT -154.04 343.3 35 DEW PT -28.49 1328.5 75 BBL PT -160.80 301.5 36 DEW PT -39.43 1312.4 76 BBL PT -164.97 277.6 37 DEW PT -51.89 1262.8 77 BBL PT -177.25 214.7 38 DEW PT -62.34 1197.1 78 BBL PT -177.84 211.9 39 DEW PT -62.63 1195.0 79 BBL PT -193.51 147.6 40 DEW PT -70.42 1131.5 80 BBL PT -193.91 146.2 SIMULATION SCIENCES INC. R PAGE P-4 PROJECT APPBRIEFS PRO/II VERSION 7.0 ELEC V6.6 PROBLEM G1 OUTPUT SIMSCI PHASE ENVELOPE SUMMARY NOV91 ============================================================================== UNIT 1, 'PHS1' (Cont) TEMP PRES TEMP PRES F PSIA F PSIA -------- -------- -------- -------- -------- 81 BBL PT -209.14 98.8 86 BBL PT -258.50 19.4 82 BBL PT -216.46 80.5 87 BBL PT -262.57 16.4 83 BBL PT -223.84 64.8 88 BBL PT -264.96 14.8 84 BBL PT -237.45 41.9 89 BBL PT -265.19 14.7 85 BBL PT -249.91 27.0 SIMULATION SCIENCES INC. R PAGE P-5 PROJECT APPBRIEFS PRO/II VERSION 7.0 ELEC V6.6 PROBLEM G1 OUTPUT SIMSCI PHASE ENVELOPE SUMMARY NOV91 ============================================================================ UNIT 1, 'PHS1' (Cont) PHASE ENVELOPE FOR SET 1, STREAM '1' 1500. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+ | | | | | | | | | | | | | | | | | | 1350. + | | | | + | | | | DDDDPDD | | | | | D | DD | | | | | D | D | 1200. +-----------+-----------+-----------+----DD-----+------D----+ | | | | D | D | | | | | D | D | | | | | D | D | 1050. + | | | DD | D+P | | | |D | D | R | | | D | D | E | | | D | D | S 900. +-----------+-----------+-----------D+-----------+----------D+ S | | | C| | D| U | | | * | | D| R | | | B | | D| E750. + | | B | | D+, | | | B | | D | | | B | | DP | | | B | | DS 600. +-----------+-----------+-----B-----+-----------+-----------TI | | | B | | DA | | | B | | D | | | B | | D| 450. + | | B | | D+ | | |B | | D| | | B | | D| | | B| | | D| 300. +-----------+----------B-+-----------+-----------+----------D-+ | | BB | | | DD | | | BB | | | D | | | BB | | | D | 150. + | BB | | | D + | BB | | | DD | | BBBB| | | | DD | | BBBBBB | | | DDDDDD | 0. +B----+-----+-----+-----+-----+-----+-----+-D---+-----+-----+ -270.0 -210.0 -150.0 -90.0 -30.0 30.0 TEMPERATURE, F KEY... D - DEW POINT B - BUBBLE POINT T - CRICONDENTHERM P - CRICONDENBAR C - CRITICAL POINT SIMULATION SCIENCES INC. R PAGE P-6 PROJECT APPBRIEFS PRO/II VERSION 7.0 ELEC V6.6 PROBLEM G1 OUTPUT SIMSCI PHASE ENVELOPE SUMMARY NOV91 ==================================================================================== UNIT 1, 'PHS1' SET 2, STREAM '1', LIQUID FRACTION = 0.050 F PSIA CRICONDENTHERM -80.63 880.4 CRICONDENBAR -83.66 924.2 CRITICAL POINT -95.15 853.0 MAX. TEMP AND PRES -80.63 924.2 TEMP PRES TEMP PRES F PSIA F PSIA -------- -------- -------- -------- 1 -227.92 14.7 25 -91.47 634.8 2 -227.68 14.8 26 -88.69 676.2 3 -224.05 17.2 27 -86.22 717.5 4 -218.03 21.9 28 -84.09 758.8 5 -205.14 35.3 29 -83.86 763.7 6 -191.26 56.2 30 -82.36 800.1 7 -186.21 65.8 31 -81.12 841.5 8 -172.81 97.5 32 MAX TEMP -80.63 880.4 9 -165.41 119.4 33 -80.64 882.8 10 -159.67 138.8 34 -82.22 920.8 11 -149.25 180.2 35 -83.39 924.1 12 -143.19 208.2 36 MAX PRES -83.66 924.2 13 -140.53 221.5 37 -83.94 924.1 14 -133.00 262.8 38 -88.08 908.2 15 -126.36 304.2 39 -91.48 882.8 16 -120.52 344.8 40 -94.22 858.1 17 -120.42 345.5 41 -94.84 853.4 18 -115.06 386.8 42 -94.86 853.6 19 -110.19 428.2 43 -94.66 857.6 20 -105.75 469.5 44 -94.55 859.4 21 -101.68 510.8 45 -94.56 859.4 22 -99.36 536.2 46 -94.68 858.2 23 -97.96 552.2 47 CRITICAL -95.15 853.0 24 -94.56 593.5 SIMULATION SCIENCES INC. R PAGE P-7 PROJECT APPBRIEFS PRO/II VERSION 7.0 ELEC V6.6 PROBLEM G1 OUTPUT SIMSCI PHASE ENVELOPE SUMMARY NOV91 ============================================================================ UNIT 1, 'PHS1' (Cont) PHASE ENVELOPE FOR SET 2, STREAM '1' 1000. +-------+-------+-------+-------+-------+-------+-------+-------+ | | | | | | | | | | | | | | LP| 900. + | | | LL L | | | | LT | | | | CL | | | | L| 800. +---------------+---------------+---------------+--------------L+ | | | | L | | | | | L | | | | | L | 700. + | | | L+P | | | | L | R | | | | L | E | | | | L | S 600. +---------------+---------------+---------------+---------L-----+ S | | | | L | U | | | | L | R | | | | L | E500. + | | | L + , | | | | L | | | | | L | P | | | | L | S 400. +---------------+---------------+---------------+--L----------------+ I | | | |LL | A | | | L | | | | LL| | 300. + | | LL | + | | | L | | | | | LL | | | | | L | | 200. +---------------+---------------+-----LL--------+---------------+ | | | LLLL | | | | LLL | | | | LL | | | 100. + | LLLL | | + | | LLLL | | | | |LLLL | | | | LLLLLLLLLLLL | | | 0. +-------+-------+-------+-------+-------+-------+--------+-------+ -240.0 -200.0 -160.0 -120.0 -80.0 TEMPERATURE, F KEY... L - LIQ FRAC = .0500 T - CRICONDENTHERM P - CRICONDENBAR C - CRITICAL POINT SIMULATION SCIENCES INC. R PAGE P-8 PROJECT APPBRIEFS PRO/II VERSION 7.0 ELEC V6.6 PROBLEM G1 OUTPUT SIMSCI PHASE ENVELOPE SUMMARY NOV91 ================================================================================ UNIT 1, 'PHS1' SET 3, STREAM '1', LIQUID FRACTION = 0.010 F PSIA F PSIA -------- -------- -------- -------- -------- 1 -130.14 14.7 27 -24.80 968.0 2 -129.92 14.8 28 -26.72 1021.0 3 -118.57 24.2 29 -29.53 1072.3 4 -99.32 51.3 30 -29.63 1073.9 5 -91.54 67.8 31 -34.34 1126.9 6 -76.12 114.2 32 -47.95 1179.8 7 -74.39 120.8 33 MAX PRES -48.69 1179.9 8 -62.96 173.7 34 -49.44 1179.8 9 -54.44 226.7 35 -51.91 1177.8 10 -50.78 254.1 36 -65.53 1126.9 11 -47.71 279.6 37 -73.42 1073.9 12 -42.21 332.6 38 -79.76 1021.0 13 -37.70 385.5 39 -83.86 981.2 14 -34.00 438.5 40 -85.14 968.0 15 -30.96 491.4 41 -89.97 915.1 16 -28.47 544.4 42 -94.34 862.1 17 -27.61 565.4 43 -96.03 839.9 18 -26.44 597.3 44 -96.30 836.7 19 -24.84 650.3 45 -96.30 836.7 20 -23.69 703.2 46 -96.11 839.6 21 -23.00 756.2 47 -95.10 852.9 22 -22.76 809.1 48 -94.57 859.5 23 MAX TEMP -22.75 813.6 49 -94.57 859.5 24 -22.82 843.5 50 -94.58 859.4 25 -22.93 862.1 51 CRITICAL -95.15 853.1 26 -23.59 915.1 SIMULATION SCIENCES INC. R PAGE P-9 PROJECT APPBRIEFS PRO/II VERSION 7.0 ELEC V6.6 PROBLEM G1 OUTPUT SIMSCI PHASE ENVELOPE SUMMARY NOV91 ============================================================================== UNIT 1, 'PHS1' (Cont) PHASE ENVELOPE FOR SET 3, STREAM '1' 1200. +-----+-----+-----+-----+-----+-----+-----+-----+-----+-----+ | | | |LLLLPLL | | | | | LLL LLL | | 1100. + | | LL | L| + | | | LL | L | | | | LL | |L | 1000. +-----------+-----------+--L--------+-----------+-L---------+ | | | L | | L | | | |L | | L | 900. + | LL | | L + | | C | | | L | P | | LL | | | L | R 800. +-----------+-----------+-----------+-----------+--T--------+ E | | | | | L | S | | | | | L | S700. + | | | | L+U | | | | | L | R | | | | |L | E 600. +-----------+-----------+-----------+-----------+L----------+ , | | | | |L | | | | | |L | P 500. + | | | L+S | | | | L| | I | | | | L | | A 400. +-----------+-----------+-----------+--------L--+-----------+ | | | | L | | | | | | L | | 300. + | | | L | + | | | | LLL | | | | | | L | | 200. +-----------+-----------+-----------LL----------+-----------+ | | | LLL| | | | | | LLL | | | 100. + | | LLLL | | + | | LLLLLLLLLL | | | | LLLLLL | | | | 0. +-----+-LLL-+-----+-----+-----+-----+-----+-----+-----+-----+ -150.0 -120.0 -90.0 -60.0 -30.0 0.0 TEMPERATURE, F KEY... L - LIQ FRAC = .0100 T - CRICONDENTHERM P - CRICONDENBAR C - CRITICAL POINT SIMULATION SCIENCES INC. R PAGE P-10 PROJECT APPBRIEFS PRO/II VERSION 7.0 ELEC V6.6 PROBLEM G1 OUTPUT SIMSCI STREAM MOLAR COMPONENT RATES NOV91 ================================================================================== STREAM ID 1 NAME PHASE TOTAL RATE, LB-MOL/HR 100.0000 TEMPERATURE, F 1.0004 PRESSURE, PSIA 1.0000 ENTHALPY, MM BTU/HR 0.1280 MOLECULAR WEIGHT 17.3061 MOLE FRAC VAPOR 1.0000 MOLE FRAC LIQUID 0.0000 SIMULATION SCIENCES INC. R PAGE P-11 PROJECT APPBRIEFS PRO/II VERSION 7.0 ELEC V6.6 PROBLEM G1 OUTPUT SIMSCI STREAM SUMMARY NOV91 ================================================================================ STREAM ID 1 NAME PHASE VAPOR ----- TOTAL STREAM ----- RATE, LB-MOL/HR 100.000 M LB/HR 1.731 STD LIQ RATE, FT3/HR 87.918 TEMPERATURE, F 1.000 PRESSURE, PSIA 1.000 MOLECULAR WEIGHT 17.306 ENTHALPY, MM BTU/HR 0.128 BTU/LB 73.960 MOLE FRACTION LIQUID 0.0000 REDUCED TEMP (KAYS RULE) 1.3019 PRES (KAYS RULE) 1.5065E-03 ACENTRIC FACTOR 0.0165 WATSON K (UOPK) 18.881 STD LIQ DENSITY, LB/FT3 19.684 SPECIFIC GRAVITY 0.3156 API GRAVITY 316.818 -------- VAPOR ---------- RATE, LB-MOL/HR 100.000 M LB/HR 1.731 M FT3/HR 494.256 STD VAP RATE(1), M FT3/HR 37.948 SPECIFIC GRAVITY (AIR=1.0) 0.598 MOLECULAR WEIGHT 17.306 ENTHALPY, BTU/LB 73.960 CP, BTU/LB-F 0.493 DENSITY, LB/M FT3 3.501 Z (FROM DENSITY) 0.9998 -------- LIQUID -------- RATE, LB-MOL/HR N/AM LB/HR N/A FT3/HR N/A GAL/MIN N/A STD LIQ RATE, FT3/HR N/A SPECIFIC GRAVITY (H2O=1.0) N/A MOLECULAR WEIGHT N/A ENTHALPY, BTU/LB N/A CP, BTU/LB-F N/A DENSITY, LB/FT3 N/AZ (FROM DENSITY) N/A (1) STANDARD VAPOR VOLUME IS 379.49 FT3/LB-MOLE (60 F AND 14.696 PSIA)