Document g2YeE7pdj9JD4x4a7L20g0ebG
LACSD1 ::MONROE
JOB 429
ARC695
Owner UIC: Account:
[MONROE] 355
Priority: Submit queue: Submitted: Printer queue: Printer node: Started:
100
LALP01_ANS! 18-MAY-1992 15:53 LPS20$LALP01 LALP01 18-MAY-1992 15:51
Digital Equipment Corporation
VAX/VMS Version V5.4-1
00 a 017081 CONFIDENTIAL
PrintServer 20
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ASPEN PLUS IS A TRADEMARK OF ASPEN TECHNOLOGY, INC. 251 VASSAR STREET CAMBRIDGE, MASSACHUSETTS 02139 (17/497-9010
VERSION: Dec-VAX RELEASE: 8,5-2 INSTALLATION: DON-VAX
HOTLINE: U.S.A. *17/447-9010 EUROPE (32) 2/732-6300
MAY 18, 1992 MONDAY 8:35:22 A.M.
t
C O N F ID E N T IA L
ASPEN PLUS VER: DEC-VAX REL: 8.5-2
INST: DON-VAX
ARC INTERPRETATION
5/18/82 PAGE
I
ASPEN PLUS(TM) IS A PROPRIETARY PRODUCT OF ASPEN TECHNOLOGY, INC. (ASPENTECH) , AND KAY BE USED ONLY UNDER AGREEMENT WITH ASPENTECH. RESTRICTED RIGHTS LEGEND: USE, DUPLICATION, OR DISCLOSURE BY THE GOVERNMENT IS SUBJECT TO RESTRICTIONS AS SET FORTH IN DEAR AND DFAR 252-227-7013 <C)(1)(II) OF THE RIGHTS IN TECHNICAL DATA AND COMPUTER SOFTWARE CLAUSES OR OTHER SIMILAR REGULATIONS OF OTHER GOVERNMENTAL AGENCIES WHICH DESIGNATE SOFTWARE AND DOCUMENTATION AS PROPRIETARY,
TABLE OF CONTENTS
RUN CONTROL SECTION.................................................................... RUN CONTROL INFORMATION.............................................. DESCRIPTION............................................................................ BLOCK STATUS.........................................................................
1 1 1 1
INPUT SECTION................................................................................... 2 INPUT riLE<S)....................................................................... 2
FLOWSHEET SECTION......................................................................... FLOWSHEET CONNECTIVITY BY STREAMS..................... FLOWSHEET CONNECTIVITY BY BLOCKS....................... CONVERGENCE STATUS SC9MARY...................................... DESIGN-SPEC: A................................................................. DESIGN-SPEC; B................................................................. DESIGN-SPEC: C................................................................. DESIGN-SPEC: D.................................................................
DESIGN-SPEC: E................................................................. DESIGN-SPEC: F................................................................. DESIGN-SPEC: END............................................................ CONVERGENCE BLOCK: SOLVEROl.............................. CONVERGENCE BLOCK: 8OLVER02.............................. CONVERGENCE BLOCK: 80LVER03.............................. CONVERGENCE BLOCK; $OLVERQ4.............................. CONVERGENCE BLOCK: 8OLVER05.............................. CONVERGENCE BLOCK: $OLVEROC.............................. CONVERGENCE BLOCK: $OLVER07.............................. COMPUTATIONAL SEQUENCE................................................ OVERALL FLOWSHEET BALANCE.........................................
4 6 8 6 7 7 7
8 8 8 9 9 10 10 11 11 12 13 13
U-O-S BLOCK SECTION....................................................................
BLOCK: B
MODEL; HEATER............................
BLOCK: C
MODEL: HEATER............................
BLOCK; D
MODEL: HEATER............................
BLOCK: E
MODEL: HEATER............................
BLOCK; END
MODEL: HEATER............................
BLOCK: F
MODEL: HEATER............................
BLOCK: PAD
MODEL: HEATER............................
14 14 14 15 16 17 18 19
ASPEN PLUS
VER: DEC-VAX
REL: 8.5*2
INST: DON-VAX
ARC INTERPRETATION
TABLE OF CONTENTS
5/18/82 PA(* II
STREAM SECTION*.*...********* 21 C0MP1 RESULTl RESULT2'RESULTS*RE5ULT4!!!!! 21
RESULTS RESULTS FINAL PADGAS C02B.....................23 C02C STEAMD STEAMS STEAMF......................................... 25
* ---J
-
ASPEN PLUS VER: DEC-VAX RUN CONTROL INFORMATION
REL: 8.5-2
INST; DON-VAX
ARC INTERPRETATION
RUN CONTROL SECTION
5/18/82 PAGE 1
THIS VERSION OP ASPEN PLUS LICENSES TO THE DON CHEMICAL COMPANY TYPE OF RUN: HEN
INPUT FILE NAME: DISK5PK2:[MONROE.PRLAD.REACTIVE]ARC695.INP;9
OUTPUT PROBLEM DATA FILE NAME: ARC895 VERSION NO. 1
LOCATED IN:
DISK4PE2: [MONROE. PRLAD.REACTIVE]
PDF SIZE USED FOR INPUT TRANSLATION:
NUMBER OF FILE RECORDS (PSIZE) - 98989
NUMBER OF IN-CORE RECORDS
- 800
PSIZE NEEDED FOR SIMULATION
2000
CALLING PROGRAM NAME: LOCATED IN:
GENERAL ASP$R0OT; [ASPDOM]
SIMULATION REQUESTED FOR ENTIRE FLONSHEET DESCRIPTION
CALCULATIONS OF VLK, HEAT CAPACITY, AMD DENSITIES TO IMPROVE ACCURACY FOR ARC INTERPRETATION STUDIES. ETHANOLAMDIES T-250 BOTTOMS SAMPLE ARC RCL: 92-0895
BLOCK STATUS
*
* ALL UNIT OPERATION BLOCKS WERE COMPLETED NORMALLY * * ALL CONVERGENCE BLOCKS MERE COMPLETED NORMALLY
*
* *
* *
1
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ASPEN PLUS VER: DEC-VAX INPUT FILE(S)
REL: 8.5-2
INST: DON-VAX
ARC INTERPRETATION
INPUT SECTION
5/1S/92 PACE 2
ORIGIMAL RUN
MAY 1*. 1992
8:33:13 A.M*
MONDAY
INPUT riLE: DISKSPE2: [MONROE.PRLAD.REACTIVE]ARC*95.INP;9
OUTPUT PDF: ARC895 VERSION; 1
LOCATED IN: DISK$PE2: [MONROE.PRLAD.REACTIVE]
2 TITLE 'ARC INTERPRETATION' 3 *
< DESCRIPTION 'Calculation, of VLB, haat capacity, and danaitiaa to
7 inprova accuracy for ARC intarprotation atudina. 8 Ethnol*mln* T-250 bottom
9 ARC RCL: 92-0695' 10
11
12
13 IN-UNITS MET TEMPERATURE-C PRESSURE-MI MASS^M
14 OUT-UNITS MET TEMPERATURE-C PRESSURE--P81 MAS8-GM VOLUME-FLOW-' L/HR'
15
16 RUN-CONTROL MAX-TIME-1000
17
19 SPECIFY THE PHYSICAL PROPERTY DATABANK 19
20 DATABANKS DOW
21
22 t SPECIFY WHAT PROPERTIES YOU KENT ON PRINTOUT 23
24 PROP-SET SET1 VMX UNITS--'L/HR'
PHASE-T
25 PROP-SET SET2 RHCMX UMITS-'GM/CC*
PHASE-L
26 PROP-SET SETS CPMX UMITS-'CAL/OI-E'
PHASE-T
27
28 ;
SPECIFY THE COMMENTS
29 r 30 XMP0NENT8 N2 NITROGEN
/ C02 002
/ MATER MATER /
31 MEA MONOETHAMOLAMINE / DBA DIETHANOLAMINE / 32 TEA TRIETHANOLAMINE / TEJHQE ' TRIETHANOLAMINE GLYCOL ETHER
33
34
35 SPECIFY THE PHYSICAL PROPERTIES METHOD
36 IDEAL VAPOR LIQUID EQUILIBRIUM
37
38 I 'ROPERTIES SYSCPOA HEY-CCaN>S-LISTl
39
40 1 IENRY-C06VS LIST1 N2 002
41
42
43 SPECIFY COMPONENT DIPOLE MOMENT, SO ASPEN CAN PREDICT
44 VAPOR VISCOSITY FOR MIXTURE*
45
48 PROP-DATA
47 IN-UNITS MET
48 PROP-LIST
NOP
/
| f '
ASPEN PLUS VER: DEC-VAX INPUT FILE(S) (CONTINUED)
REL: 8.5-2
INST: DOW-VAX
ARC INTERPRETATION
INPUT SECTION
5/18/92 PJUX 3
49 50 51 52 53
54 55 56 57 58 59 <0 1
42 63 64 65 66 67 68 69 70 71 72 73 74 75 76 77 78 79 80 81 82
S3 84 85 86 87 88 89 90 91 92 93 94 95 96 97 98 99
100 101
PVAL PVAL
PVAL PVAL PVAL
WATER MELA
DEA TEA TEAGE
1.85 2.60
2,84 3.60 3.60
; ENTER THE ENTHALPY POLYNOMIAL VIA THE WATSON EQUATION
PROP-DATA
IN-UNITS ENG TEMPERATURB-C
PROP-LIST DHVLWT
PVAL TEAK 24670.291 150.0 0.38 0 0
/
SPECIFY FLOWSHEET CONNECTIONS
f FLOWSHEET
BLOCK PAD
IN^XTHPl PADGAS OUT-RESULT1
BLOCK B
IN-RESULT1 C02B
OUT-RESU1T2
BLOCK C
IN-RESULT2 C02C OUT--RESULTS
BLOCK D
IN-RESULT3 STSAMD 00T-RESULT4
BLOCK E
IN--RESULT4 STEAMS OUTHIESULT5
BLOCK F
IN--RESULTS 8TEAHF OUT-41ESULT6
BLOCK END
IN--RESULT6
OUT-^IMAL
; Dasign B..1.: A ihII wont of vitw 1* adM to th. durg* to ; uk ASPEN um Henry*a law for tha nitrogen solubility. The ; Henry' a law constants in water will be the default for ell ; components. Accuracy h.ra ia not critical .inc* nitrogen la ; aaaantially an lnort gas.
STREAM COMPl
TQ<P-25.0[C] PRES-14.7[PSI]
MASS-runt DEA 2.85 / TEA 2.85 / MATER .0001
STREAM PADGAS TEMP-25.0(C) PRES-14.7[PSI] MASS-FLOW M2 0.00532
STREAM C02B
TEMP-25.0(C) PRES-14.7[PSI]
MASS-FLOW C02 0.00^32
STREAM C02C
TDIP-25.0[C] PRES-14.7[PSI]
MASS-FLOW 002 0.00532
STREAM STEAMD TEMP-10Q PRES-14.7 MOLE-FLOW WATER .0388
STREAM STEAME TEMP-100 FREE--14.7 MOLE-FLOW WATER .0388
STREAM 5TEAMF TEMP-100 PRES-14.7 MOLE-FLOW WATER .0388
BLOCK PAD HEATER ;Thia block adds nitrogen to estimate the ARC boab loading under
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-- J> o rn o z --1 H NJ >--{ o
00
---
ASPEN PLUS
VER: DEC-VAX
REL: 8.5-2
IMST: DOW-VAX
ARC INTERPRETATION
INPUT SECTION
5/18/92 FACE 4
INPUT FILE(S) (CONTINUED)
102 103 104 105 106 107 108 109 110 111 112 113 114 115 116 117 118 119 120 121 122 123 124 125 126 127
128 129 130 131
132 133 134 135
136 137 138 139 140
141 142 143 144 145 146 147 148 149 150 151 152
153 154
/nitrogen pad. FARAM PRES-14.7 TEW--25.
BLOCK B HEATER ;Computa tha molaa of C02 required to Match ARC pressure data. ;Includea pad gas and vapor pressure of charge Materials.
PARAM PRES--87.4 TEW-25(.03
BLOCK C HEATER ;Coapute tha aolaa of 002 required to Metch ARC pressure date. .`Includes pad gas and vapor pressure of charge neteriala.
PARAM PRES--127.3 TDIP-276.91
BLOCK D HEATER ;Coapute the nolea of H20 required to Metch ARC pressure dete. .'Includes 002 from previous blocks, pad gas and vapor pressure ;of charge Materials.
PARAM PRES--357.5 TEMP-301.il
BLOCK E HEATER /Coaputa tha molaa of H20 raquirad to match ARC prauurm data. .`Includes CQ2 from previous blocks, pad gas and vapor pressure ;of charga matariala.
FARAM PRES--759.4 TEW-325.08
BLOCK F NEATER .'Compute the Moles of H20 raquirad to Match ARC pressure data. /Includes 002 fro* previous blocks, pad gas and vapor pressure ;of charga matariala.
PARAM PRES--2707.9 TEW-386.97
BLOOC END HEATER /Estimate pressure after cool down.
PARAM PRES--100.0 TEMP-25.0
DESIGN-SPEC A DEFINE VOl STREAM-PROP 8TREAM-RESULT1 PROPERTY--SET1 SPEC VOL TO 10.0 T0X.-SPEC .05 VARY STREAM-VAR STREAM-PADGAS VARIAELE-NASS-flCW LIMITS .001 .01
DESIGN-SPEC B DEFINE VOL STREAM-PROP 8TREAIME8ULT2 PROPERTY--SET1 SPEC VOL TO 10.0 TOL-SPEC .05 VARY STREAM-VAR STREAIM302B VARlABLE^tAAS-FLON VARY BLOCK-VAR BLOOM VARIABLE--PRES LIMITS .001 1.0
DESIGN-SPEC C DEFINE VOL STREAM-PROP STREAM-RESULTS PROPERTY--SETl
, !
ASPEN PLUS
VER: DEC-VAX
REL: 8.5-2
INST: DOW-VAX
ARC INTERPRETATION
INPUT SECTION
5/18/92 PACE 5
INPUT FILE(S) (CONTINUED)
15S 156 157 158 159 160 161 162 163 164 165 166 167 168 169 170 171 172 173 174 175 176 177 178 179 180 181 182 183 184 185 186 187 188 189 190 191 192 193
194 195 196 197
198
SPEC VOL TO 10.0 TOL-SPEC .05 VARY STREAM-VAR STREAIM02C VARlABLE^fASS-FLOW ; VARY BLOCK-VAR BLOOM VARXABLE-FRES LIMITS .001 1.0
DESIGN-SPEC D
DEFINE VOL STREAM-PROP STREAM-RESULT! PROPERTY-SET1 SPEC VOL TO 10.0 TOL-SPEC .05
VARY STREAM-VAR STREAtHSTEAMD VARIABLE-MASS-FLOW ; VARY BLOCK-VAR BLOOM VARIABLE-PRE3
LIMITS .001 3.0
DESIGN-SPEC E DEFINE VOL STREAM-PROP STREAM-RESULT5 PROPERTY--SET1 SPEC VOL TO 10.0
TOL-SPEC .05 VARY STREAM-VAR STREAM-STEAME VARIABIMOSS-FLON ; VARY BLOCR-VAR BLOCK-K VARIABLE--PREB LIMITS .001 3.0
DESIGN-SPEC F
DEFINE VOL STREAM-PROP STREAM-RESULTS PROPERTY--SET1 SPEC VOL TO 10.0 TOL-SPEC .05
VARY STREAM-VAR STREAM-STEAMF VARIABl-MASS-FLOW ; VARY BLOCK-VAR BLOCK--F VARIABLE--PRES
LIMITS .001 3.0
DESIGN-SPEC END DEFINE VOL STREAM-PROP STREAM-FINAL PR0PERTY-6ET1 SPEC VOL TO 10.0
TOL-SPEC .05 VARY BLOCK-VAR BLOCK-END VARIABLE-FREE LIMITS 25 300
REPORT INPUT
.
PROPERTY-REPORT NOCOMPS
STREAM-REPORT MASSFRAC MA5SFL0W HOLEFRAC MOLEFLOW NOZEROFLOW 6
PROPERTIES--SET1 SET2 SET3
6
IKCL-STREAMS-CCMP1 RESULT1 RESULT2 RBSULT3 RESULTS6
RESULTS RESULTS FINAL PADGAS 0O2B
6
C02C STE8MD STEAME STEAMF
SIMULATION STARTED
MODULE USED; GENERAL CREATION;
LOCATED IN:ASP$ROOT:[ASPDOW]
SIMULATION COMPLETED FOR ENTIRE FLOWSHEET
5/ 8/92 18:03:08
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ASPEN PLUS
VER: DEC-VAX
REL; 8,5-2
INST: DON-VAX
ARC INTERPRETATION
FLOWSHEET SECTION
FLOWSHEET CONNECTIVITY BY STREAMS
5/18/92 pac
STREAM PADGAS C02B STEAMD STEAMF RESULT2 RESULTS RESULTS
SOURCE
-_______
-,
--
--
B D F
BEST PAD B
D F C E END
FLOWSHEET CONNECTIVITY BY BLOCKS
STREAM CCMPl C02C
STEAMS RESULTl RESULT3 RESULTS PINAL
SOOROS ---------------
-------PAD C E END
DEST PAD C
E B D F --------
BLOCK
PAD
B C
D
E r BHD
INLETS
COMP1 PADGAS
RESULTl C02B RESULT2 C02C
RESULT3 STEAMD RESULTS STEAME RESULT5 STEAMF RESULTS
CONVERGENCE STATUS SfBMARY
___
DESIGM-SPEC SUtMARY
OUTLETS RESULT1
RESULT2 RESULT3
RESULTS RESULTS RESULTS FINAL
DESIGN SPEC
ERROR
TOLERANCE
ERR/TQL
VARIABLE
GONV STAT BLOCK
A B
C D E F
END
-0.10014E-10 -0.61740E-03 -0.23733E-03 -0.30190E-01
0.30914E-01 -0.16803E-02
0.24016E-01
0.50000E-01 -0.20020E-09 0,50000E-01 -0.12346E-01
0.50000E-01 -0,4745CB-02
0.5OO00E-01 -0.40380 0.50000E-01 0.61828 0.50000E-01 -0.33407E-01 0.50000E-01 0.48032
0.56401E-02 #
0.14338E-01
0.78421E-02 *
0.18924
*
0.28907
8
0.93811
*
48.756
#
8OLVER01 4OLVER02 8OLVER03
6OLVER04 4OLVER05
8OLVER04 6OLVER07
# - CONVERGED
* - NOT CONVERGED LB - AT LOWER BOUNDS UB - AT UPPER BOUNDS
DESIGN-SPEC: A
SAMPLED VARIABLES:
VOL
: PROPERTY STRMPROP SET1 IN 8TRKAM RESULTl
SPECIFICATION:
MAKE VOL APPROACH 10.0000
NITfllN
0.050000
ASPEN PLUS
VER: DEC-VAX
PEL: 8.5-2
INST: DOW-VAX
ARC INTERPRETATION
FLOWSHEET SECTION
5/18/92 PAGE 7
DESIGN-SPEC: A (CONTINUED)
MANIPULATED VARIABLES:
VARY
: TOTAL MASSFLOW IN STREAM RADGES SUBSTREAM MIXED
LOWER LIMIT -
0.00100000
KG/HR
UPPER LIMIT -
0.0100000
KG/HR
FINAL VALUE -
0.005C401
KG/HR
DESIGN-SPEC: B
SAMPLED VARIABLES:
VOL
: PROPERTY STRMPR0P SETl IN STREAM RESULT2
SPECIFICATION:
MAKE VOL APPROACH 10.0000
WITHIN
0.050000
MANIPULATED VARIABLES:
VARY
: TOTAL MASSFLOW IN STREAM O02B SUBSTREAM MIXED
LONER LIMIT *
0.00100000
KG/HR
UPPER LIMIT -
1.00000
KG/HR
FINAL VALUE *
0.014338
KG/HR
DESIGN-SPEC: C
eilitlfVh triBT&BT T6*
VOL
: PROPERTY STRMPROP SETl IV STREAM RESULT3
SPECIFICATION: MAKE VOL APPROACH 10.0000
NITHIN
0,050000
MANIPULATED VARIABLES:
VARY
: TOTAL MASSFLOW IN STREAM C02C SUBSTREAM MIXED
LOWER LIMIT *
0.00100000
KG/HR
UPPER LIMIT -
1.00000
KG/HR
FINAL VALUE *
0.0078421
RG/HR
DESIGN-SPEC: D
1
SAMPLED VARIABLES:
VOL
: PROPERTY STRMPROP SETl IN STREAM RESULT4
SPECIFICATION:
MAKE VOL APPROACH 10.0000
NITHIN
0.050000
ASPEN PLUS
VER: DEC-VAX
REL: 8.5-2
INST: DOW-VAX
ARC INTERPRETATION
FLOWSHEET SECTION
5/18/92 pia a
DESIGN-SPEC: D (CONTINUED)
MANIPULATED VARIABLES:
VARY
: TOTAL MASSFLOW IN STREAM 3TEAMD SUBSTREAM MIXED
LOWER LIMIT -
0.00100000
KG/HR
UPPER LIMIT -
3.00000
RG/HR
FINAL VALUE -
0.18924
KG/HR
DESIGN-SPEC: E
SAMPLED VARIABLES:
VOL
: PROPERTY STRMPR0P SETl IN STREAM RESULTS
SPECIFICATION:
MAKE VOL APPROACH 10.0000
WITHIN
0.050000
MANIPULATED VARIABLES:
VARY
: TOTAL MASSFLOW IN STREAM STEAMS SUBSTREAM MIXED
LOWER LIMIT
0.00100000
KG/HR
UPPER LIMIT -
3.00000
RG/HR
FINAL VALUE -
0.28907
KG/HR
DESIGN-SPEC: F
SAMPLED VARIABLES:
.VOL
: PROPERTY STRMPROP SETl IN STREAM RESULT<
SPECIFICATION:
HARE VOL APPROACH 10.0000
NITHIN
0.050000
MANIPULATED VARIABLES:
VARY
: TOTAL MASSFLOW IN STREAM STEAMF SUBSTREAM MIXED
LOWER LIMIT -
0.00100000
KG/HR
UPPER LIMIT -
3.00000
RG/HR
FINAL VALUE -
0.93811
RG/HR
DESIGN-SPEC: END
SAMPLED VARIABLES:
VOL
; PROPERTY STRMPROP SETl IN STREAM FINAL
SPECIFICATION:
MAKE VOL APPROACH 10.0000
WITHIN
0.050000
C O N F ID E N T
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MO ]> CD
'4.
ASPEN PLUS
VER: DEC-VAX
REL: B.5-2
INST: DCW-VAX
ARC INTERPRETATION
FLOWSHEET SECTION
5/18/92 PAGE 9
DESIGN-SPEC: END (CONTINUED)
MANIPULATED VARIABLES:
VARY
: SENTENCE-?ARAM VARIABLE-PRES IN DOS BLOCK END
LONER LIMIT -
25.0000
PSI
UPPER LIMIT -
300.000
PSI
FINAL VALUE -
48.7550
PSI
CONVERGENCE BLOCK: SOLVEROl
SPECS: A
MAXIT- 3D STEP-SIZE-
100.00
4 OP RANGE
MAX-STEP-
100.
t or RANGE
XTOL--
1.000000E-08
THE HEN ALGORITHM NAS OSED WITH BRACKETING-NO
METHOD: SECANT
STATUS: CONVERGED
TOTAL NUMBER OF ITERATIONS:
3
*** FINAL VALDES ***
VARIABLE TOTAL MASSFL
KG/HR
VALUE 0.54+0144D-02
PREV VALUE 0.5440144D-02
BRR/TGL -.2002842D-09
*** ITERATION HISTORY ***
DESIGN-SPEC ID: A
ITERATION VARIABLE
ERROR
ERR/TOL
1 0.5275E-07 LB -0.2795
-S.590
2 0.53S4E-07 LB -0.2009
-4.019
3
0.5593E-07 LB -0.1001B-10
-0.2003E-09
CONVERGENCE BLOCK: SOLVER02
SPECS: B
MAXIT- 30 STEP-SIZE-
100.00
4 OP RANGE
MAX-STEP-
100.
1 or RANGE
XTOL-
1.QOOOOOK-08
THE NEN ALGORITHM MAS OSED NITH BRACKETING-NO
METHOD: SECANT
STATUS: CONVERXXD
TOTAL NUMBER OF ITERATIONS:
3
.
*** FINAL VALDES ***
VARIABLE TOTAL MASSFL
KG/HR
VALUE 0.14338020-01
PREV VALUE 0.1433802D-01
ERR/TOL -.12347900-01
*** ITERATION HISTORY ***
n oD zD "n T-1 ]>
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--1 %i
MO 3> 00
CO
ASPEN PLOS
VER: DEC-VAX
REL: 8.5-2
INST: DOW-VAX
ARC INTERPRETATION
FLOWSHEET SECTION
5/18/92 PAGE 10
CONVERGENCE BLOCK: SQLVER02 {CONTINUED)
DESIGN-SPEC ID: B
iteration variable
error
ERR/TOL
I
0.3358E-07 LB
-1.804
-32.08
2
0.9443E-07 LB
0.1729
3.457
3
0.9050E-07 LB -0.S174E-03
-0.1235E-01
CONVERGENCE BLOCK: SOLVER03
SPECS: C
MAXIT- 30 STEP-SIZE-
100.00
t OF RANGE
MAX-STEP-
100.
% Or RANGE
XTOL-
1.000000E-08
THE NEN ALGORITHM NAS USED NITH BRACKETING-NO
METHOD: SECANT
STATUS: OONVERCZD
TOTAL M0MER 0P ITERATIONS:
3
.
*** PINAL VALDES *
VARIABLE TOTAL MASSFL
KG/HR
VALOS 0.78421280-02
PREV VALUE 0.78421280-02
ERR/TOL -.47444030-02
ITERATION HISTORY **
DESIGN-SPEC ID: C
ITERATION VARIABLE
ERROR
ERR/TOL
1 0.335SE-07 LB -0.3281
-4.542
2
0.9443E-07 LB
0.9715
19.43
3
0.4950E-07 LB -0.2373E-03
-0.4747K-02
OOMVERIZ1KX BLOCK: SOLVER04
SPECS: D
MAXIT- 30 STEP-SIZE-
100.00
4 OP RANGE
MAX-STEP-
100.
4 OP RANGE
XTOL-
1.OOOOQOE-OS
THE HEN ALGORITHM MAS OSED NITH BRACKETING-NO
METHOD: SECANT
STATUS: CONVERGED
TOTAL HOMER OP ITERATIONS:
4
.
*** FINAL VALDES ***
VARIABLE TOTAL MASSFL
KB/HR
VALUE
PREV VALUE
0.1892409D+00 0.18924090+00
ERR/TOL -.40379900+00
** ITERATION HISTORY +++
'
1
!
' ,
'
ASPEN PLUS
VER: DEC-VAX
REL: 8.5-2
INST: DOW-VAX
ARC INTERPRETATION
FLOWSHEET SECTION
CONVERGENCE BLOCK; $0LVERQ4 (CONTINUED)
5/18/92 PAGE 11
DESIGN-SPEC ID; D
ITERATION VARIABLE
ERROR
ERR/TOL
1 0.1078E-04 2 0.1124E-04
3 0.4689E-05 4 0.3822E-05 5 0.3132E-05 4 0.2918E-05
43.84 47.17 4.828 1.890 0.3398 -0.3019E-01
876.8 943.4 95.56 37.80 6.796 -0.6038
|
a 1
BLOCK: SOLVER05
SPECS: :
MAXIT- 30 STEP-SIZE*
100.00
t OF RA1KZ
MAX-STEP*
ioo.
% or RANGE
XTOL-
3 .0000001-08
THE NEW ALGORITHM WAS USED WITH BRACKETING-MO
METHOD: SECANT
STATUS: CONVERGED
TOTAL NUMBER OF ITERATIONS:
5
.
FINAL VALUES **
VARIABLE TOTAL HASSFL
KG/HR
VALUE
PREV VALUE
0.28908C4D+00 0.2890884D+00
ERR/TOL 0.6182818D+00
*** ITERATION HISTORY **
DESIGN-SPEC ID; E
ITERATION VARIABLE
ERROR
ERR/TOL
1 Q,1078E-04 2 0.1124E-04 3 0.6143E-05 4 0.4958E-05 5 0.4457E-05
15.09 15.59 2.492 0.8284 ( 0.3091E-01
301.8 331.9 49*83 12.57 0.6183
CONVERGENCE BLOCK: 8OLVER0C
SPECS: F
MAXIT* 30 STEP-SIZE*
ioo.oo or RANGE
MAX-STEP*
100.
% OF RANGE
XTOL-
1 .OOOOQOE-08
THE NEW ALGORITHM WAS USED WITH BRACKETING-MO
ASPEN PLUS
VER: DEC-VAX
REL; -3-2
IMST: DOW-VAX
ARC INTERPRETATION
FLOWSHEET SECTION
3/18/92 PACE 12
CONVERGENCE BLOCK: $OLVEROC (CONTINUED)
METHOD: SECANT
STATUS: CONVERGED
TOTAL NUMBER OF ITERATIONS:
4
*** FINAL VALDES ***
VARIABLE TOTAL HASSFL
KG/HR
VALUE 0.9381078D+00
PREV VALUE 0.9381078D+00
ERR/TOL -.33COC78D-01
*** ITERATION HISTORY *#*
DESIGN-SPEC ID: F
ERROR
ERR/TOL
1 0.1078E-04
2 0.1124E-04 3 0.1489E-04 4 0.1446E-04
-0.8268 -0.7338
0.1072 -0.1680E-02
-16.54 -14.66
2,143 -0.33411-01
CONVERGENCE BLOCK: 8OLVER07
SPECS: 1END
MAXIT- 30 STEP-SIEE-
100.00
% OF RANGE
MAX-STEP-
100.
i OF RAMOS
XTOL-
L*OOOOOOE-08
THE HEN ALGORITHM MAS USED WITH BRACKETING-NO
METHOD: SECANT
STATUS: CONVERGED
TOTAL NtMER OF ITERATIONS:
5
.
** FINAL VALDES **
VARIABLE BLOCK-VAR
PSI
VALUE 0.48753SSD+02
PREV VALUE
ERR/TOL 0.4603238D+00
ITERATION HISTORY ***
DESIGN-SPEC ID: END
ITERATION VARIABLE
ERROR
ERR/TOL
1 0.4895E+06
-2.4S1
-49.43
2 0.7094E+04
-2.340
-50.80
3 0.1724E+0C IE 4*974
99.49
4 0.4196E+06
-0.9784
-19.57
5 0.3362E>06
0.2402E-01
0.4803
7 J
1>
mo z^
A ''l v-t O
3> r^
DO A 0 1 7 0 9 0
CO NFTDFNTIAI
ASPEN PLUS VER: DBC-VAX COMPUTATIONAL SEQUENCE
REL: 8.5*2
INST: DOM-VAX
ARC INTERPRETATION
PLONSHEET SECTION
5/18/82 PAGE 13
SEQUENCE USED MAS: $QLVER01 PAD $OLVER01<------$OLVER02 B 8OLVER02<-------- $OLVER03 C $OLVER03<------8OLVER04 D $OLVER04<--* 8QLVER05 E $GLVER05<--------80LVER06 P $QLVR06<------5OLVER07 END 8OLVER07<--------
OVERALL PLONSHEET BALANCE
** MASS AMD ENERGY
IN
CONVENTIONAL COMPONENTS (1QOL/HR )
N2 0.201337B-03
002
0.503982E-03
HATER
0.786286E-01
MEA
O.OOOOOOE+OO
DBA
0.271075B-01
TEA
0.191032E-01
TEAGB
O.OOOOOOE+OO
TOTAL BALANCE
MOLE (KMOL/HR )
0.125545
MASS(KG/HR )
7*14434
ENTHALPY(CAL/SEC )
-3152.18
*** OUT
0.201337E-03 0.503982E-03 0.786286E-01 O.OOOOOOE+OO 0.271075E-01 0.191032E-01 O.OOOOOOE+OO
0.12554S 7.14434
-3185.22
RELATIVE DIPP.
O.OOOOOOE+OO O.OOOOOOE+OO O.OOOOOOE+OO O.OOOOOOE+OO O.OOOOOOE+OO O.OOOOOOE+OO O.OOOOOOE+OO
O.OOOOOOE+OO -0.310798E-16
0.103727E-01
ASPEN PLUS
VER; DEC-VAX
REL: 8.5-2
INST; DOM-VAX
ARC INTERPRETATION
U-O-S BLOCK SECTION
5/18/82 PA 14
BLOCK;
MODEL: HEATER
INLET STREAMS: OUTLET STREAM: PROPERTY OPTION SET: HENRY-COMPS ID;
RESULT1 RESULT2 8YSOPOA LIST1
G02B IDEAL LIQUID / IDEAL GAS
TOTAL BALANCE MOLE (KMOL/HR )
MASS(KG/HR ) ENTHALPY(CAL/SEC )
MASS AMD ENERGY BALANCE ZN OUT
0.447433E-01 5.72008
-1485.95
0.447433E-01 5.72008
-1444.48
RELATIVE DIPT.
0.0000001+00 0.194092R-14 -0.130185
*+*
TNO
PHASE TP FLASH
SPECIFIED TEWERATURE
SPECIFIED PRESSURE MAXIMUM NO. ITERATIONS
CONVERGENCE TOLERANCE
INPUT DATA
C PSI
*+*
OUTLET TEMPERATURE OUTLET PRESSURE HEAT DUTY VAPOR FRACTION
*** RESULTS C PSI CAL/SEC
254.030 87.4000 30 0.000100000
254.03 87.400 219.49 0.12048K-01
V-L PHASE EQUILIBRIUM
COMP N2 CQ2 MATER DEA
TEA
Til) 0.43073B-02 0.5949SE-02 0.1197SE-03
0.57992 0.40868
0.19444E-04 0.13913E-03 0.1103SE-03 0.58615
0.41358
T(I) 0.35592 0.54710 0.80550E-03 0.49490E-01
0.46844E-02
XXX.: C
MODEL: HEATER
INLET STREAMS;
OUTLET STREAM: PROPERTY OPTION SET: HENRY-COMPS ID:
RBSULT2 RESULTS 8YS0P0A LISTl
C02C IDEAL LIQUID / IDEAL CUE
E(I)
18284, 4075.9 7.2977 0.11S55 0.16162E*
ASPEN PLUS
VER: DEC-VAX
REX.: 8.5-2
INST: DON-VAX
ARC INTERPRETATION
O-O-S BLOCK SECTION
5/18/92 PAGE 15
BLOCK: C
MODEL: HEATER (CONTINUED)
***
TOTAL BALANCE MOLE (KMOL/HR ) MASS (KG/HR ) ENTHALPY(CAL/SEC )
MASS AND ENERGY BALANCE *** IN OUT
0.469215E-01 5.72792
-1971.12
0.469215E-01 5.72792
-1448.97
RELATIVE DIET
O.OQOOOOE+OO 0.000000E+00 -0.184184E-01
***
TNO
PHASE TP FLASH
SPECIFIED TEMPERATURE SPECIFIED PRESSURE
MAXIMUM NO. ITERATIONS CONVERGENCE TOLERANCE
INPUT DATA **
C PSI
276.910 127.300
30 0.000100000
OUTLET TEMPERATURE OUTLET PRESSURE HEAT DUTY VAPOR FRACTION
*** RESULTS C PSI
CAL/SEC
+*+
276.91 127.30 24.150 0.16380E-01
V-L PHASE EQUILIBRIUM :
COMP N2
C02 WATER DEA TEA
P(I> 0.42909E-02
0.10741E-01 0.11830E-03
0.57772 0.40713
X(I) 0.20898E-04 0.18742E-03 0.10775E-03 0.58593 0.41376
Y (I) 0.26071 0.64449 0.75173E-03 0.84835E-01 0.92141E-02
1^1(3.
3438.8 6.9765 0.14479 0.22269E-01
BLOCK: D
MODEL: HEATER
INLET STREAMS:
OUTLET STREAM: PROPERTY OPTION SET: HENRY-COMPS ID:
RESULTS
RESULT4 SYSOPOA LISTl
STEAND IDEAL LIQUID / IDEAL GAS
***
TOTAL BALANCE MOLE (KMOL/HR ) MASS(KG/HR ) ENTHALPY (CAL/SEC )
HASS ANll ENERGY BALANCE *** IN OUT
0.574260B-01 5.91716
-1642.24
0.574280E-01 5.91716
-1595.73
RELATIVE DIFF
O.QOQGDOE+OO O.OOOOOOE+OO -0.283219E-01
ASPEN PLUS
VER: DEC-VAX
REL: 8.5-2
INST: DON-VAX
ARC INTERPRETATION
O-O-S BLOCK SECTION
5/18/92 PAGE 18
BLOCK: D
MODEL: HEATER (CONTINUED)
***
TNO
PHASE TP PLASH
SPECIFIED TEMPERATURE
SPECIFIED PRESSURE
MAXIMUM NO. ITERATIONS
CONVERGENCE TOLERANCE
INPUT DATA
C PSI
301.110 357.500
30 0.000100000
OUTLET TEMPERATURE
OUTLET PRESSURE HEAT DUTY VAPOR FRACTION
*+* RESULTS C
PSI CAL/SEC
***
301.11
357.50 46.511 0.34335E-01
V-L PHASE EQUILIBRIUM :
CCMP N2 C02 WATER DBA TEA
BLOCK
F(I) 0.35060E-02 0.87762E-02 0.18302 0.47204 0.33266
MODEL: HEATER
X(I) 0.23008E-04 0.16147E-03 0,16834 0.48719
0.34428
Y(I> 0.1014* 0.2510*
0.59580 0.45943E-01
0.5C530E-02
K(I) 4409.8 1554.8 3.5398 0.94302E* 0.1642OE'
INLET STREAMS: OUTLET STREAM:
PROPERTY OPTION SET: HENRY-COMPS ID:
RESULT4 RESULTS
SYSOPOA LISTl
STEAMS IDEAL LIQUID / IDEAL GAS
**
TOTAL BALANCE tCLE (KMOL/HR ) MASS (KG/HR ) ENTHALPY (CAL/SEC )
MASS AND ENERGY BALANCE **+ IN OUT
0.734716E-01
6.20623 -1894.01
0.73471CR-01 6.20623
-1830.59
RELATIVE Dirr.
0.000000S+00 -0.178889B-18 -0,334870E-01
TNO
PHASE TP FLASH
SPECIFIED TEI9BRATURE
SPECIFIED PRESSURE
MAXIMUM NO. ITERATIONS
CONVERGENCE TOLERANCE
INPUT DATA *+*
C PSI
325.080 759.400
30 0.000100000
oz ao
T1 M 3>
am o z
mO >&
ASPEN PLUS
VER: DEC-VAX
REL; 8.5-2
INST: DOH-VAX
ARC INTERPRETATION
U-O-S BLOCK SECTION
BLOCK: E
MODEL: HEATER (CONTINUED)
OUTLET TEMPERATURE OUTLET PRESSURE HEAT DUTY
VAPOR FRACTION
*** RESULTS C P5I CAL/SEC
+++
5/18/92 PAfX 17
325.08 759.40 3.425 0.50982E-01
V-L PHASE EQUILIBRIUM :
COMP M2 C02
WATER DEA TEA
r<i> Q.27403E-02 0.88S95B-02
0.38144
0.38895
0.26001
X(I) 0.25847E-04 0*14224E-03 0.33889 0.38719 0.27378
Y(I) 0.53270E-01 0.13190 0.78129 0.29498E-01 0.40484E-02
mi) 2081.0 927.31 2.3054 0.78188E-01 0.14781E-01
LOCK: END
MODEL: HEATER
INLET STREAM:
OUTLET STREAM: PROPERTY OPTION BET; HENRY-COMPS ID:
RESULT* FINAL 8YSOPOA LIST1
IDEAL LIQUID / IDEAL GAS
***
TOTAL BALANCE MOLE (KMOL/HR ) MASS(KG/HR ) ENTHALPY(CAL/SEC )
MASS AMD ENERGY BALANCE IN OUT
0.125545
7.14434 -2502.59
0.125545
7.14434 -3185.22
TNO
PRASE TP FLASH
SPECIFIED TEMPERATURE SPECIFIED PRESSURE
MAXIMUM NO. ITERATIONS
CONVERGENCE TOLERANCE
INPUT DATA *** C PSI
I
RELATIVE DIFT*
0.000000E+00 0.000000E+00 0.214312
25.0000 48.7559 30
0.000100000
ASPEN PLUS
VER: DEC-VAX
RELl $.5-2
INST: DOW-VAX
ARC INTERPRETATION
U-O-S BLOCK SECTION
BLOCK: END
MODEL: HEATER (CONTINUED)
OUTLET TEMPERATURE OUTLET PRESSURE HEAT DUTY VAPOR FRACTION
** RESULTS C PSI CAL/SEC
***
5/18/92 PA 18
25.000 48.758 -882.83 0.43591E-02
V-L PHASE EQUILIBRIUM :
COMP N2 C02
MATER DEA TEA
r<i>
0.16037E-02 0.40144E-02 0.82830 0.21592 0.15218
X(I)
0.14193E-04 0.12782E-02
0.82902 0.21888 0.15243
TU) 0.38488 0.62942
O.S9263E-02 0.42297B-07 0.24560E-O9
K(I) 25892. 493.16 0.94216E-02 0.19504E-08
0.17392E-0S
BLOCK: F
MODEL: HEATER
INLET STREAMS: OUTLET STREAM: PROPERTY OPTId HENRY-COMPS ID:
SET:
RESULTS RESULTS SYSOPOA LIST1
STEAMF IDEAL LIQUID /
...
TOTAL BALANCE MOLE (KMOL/HR ) MASS(KG/HR ) ENTHALPY(CAL/SEC
NABS ABD ENERGY BALANCE *# IN OUT
0.125545
7.14434 -2798.80
0.125545 7.14434
-2502.59
i1
H
RELATIVE DIPT.
O.OOOOOOE+OO -0.310798E-1* -0.105774
***
TWO
PHASE TP FLASH
SPECIFIED TEMPERATURE
SPECIFIED PRESSURE
MAXIMUM NO. ITERATIONS
CONVERGENCE TOLERANCE
INPUT DATA
C PSI
***
388.970 2,707.90
30 0.000100000
r>
oo
ZQ
a ho z^
h ni
--11 o 3> vD r- \)
DO A 0 1 7 0 9 3
CO NFIDENTIAL.
ASPEN PLUS
VER: DEC-VAX
REL: 8.5-2
INST: DOW-VAX
ARC INTERPRETATION
0-O-S BLOCK SECTION
MODEL; HEATER (CONTINUED)
OUTLET TEMPERATURE
OUTLET PRESSURE HEAT DUTY VAPOR FRACTION
*## RESULTS C
PSI CAL/SEC
5/18/92 PA: 19
386.97 2707.9 296.02 0.40704E-Q1
V-L PHASE EQUILIBRIUM
COMP
N2 C02 HATER
DEA TEA
F(I) 0.16037E-02
0,40144E-02 0.62630
0.21592 0.15216
X(I) 0.666868-04 0.19624E-03
0.61681 0*22442
0.15850
Y(I) 0.37828E-01
Q ,93999E-01 0*84986
0.15633E-01 0.26815E-02
K(I) 567,25 478.99 1,3778 0.69662E-01 0.16918E-01
LOCK: PAD
MODEL: HEATER
INLET STREAMS: OUTLET STREAM; PROPERTY OPTION SET:
HENRY-COMPS ID
CCMP1 RESULT1
8YSOPOA LIST1
PADGAS IDEAL LIQUID / IDEAL GAS
**
TOTAL BALANCE MOLE (KMOL/HR ) MASS (KG/HR ) ENTHALPY (CAL/SEC )
MASS AMD ENERGY BALANCE IN OUT
0.464176E-01 5.70574
-1477.44
0.464176E-01 5.70574
-1677.44
RELATIVE DIFF.
O.OOOOOOE+OO O.OOOOOOE+OO 0.22227 6E-04
**
TMO
PHASE TP FLASH
SPECIFIED TEMPERATURE
SPECIFIED PRESSURE
MAXIMUM NO. ITERATIONS
CONVERGENCE TOLERANCE
INPUT DATA C PSI
I
***
25.0000
14.7000 30
0.000100000
ASPEN PLUS
VER: DEC-VAX
REL: 8.5-2
INST: DOW-VAX
ARC INTERPRETATION
0-O-S BLOCK SECTION
BLOCK: PAD
MODEL: HEATER (CONTINUED)
OUTLET TEMPERATURE OUTLET PRESSURE HEAT DUTY VAPOR FRACTION
+** RESULTS C
PSI
CAL/SEC
***
5/1S/92 PJUX 20
25.000 14.700 -0.37285E-03 0.43258E-02
V-L PHASE EQUILIBRIUM
COMP N2
HATER DEA TEA
F(I> 0.43375E-02
0.11959E-03
0.58399 0.41155
XU) 0.11735E-04 0.12009E-03
0.58453 0.41334
Y(I) 1.0000 0.37526B-05
0.37942E-06 0.23843E-08
Ml) 85215.
0.31249E-01 0.64689E-04
0,574851-08
ASPEN PLUS
VER: DEC-VAX
REL: 8.5-2
INST: DOM-VAX
ARC INTERPRETATION
STREAM SECTION
CQMP1 RESULT1 RESULT2 RESULTS RESULT4
S/18/92 PACT! 21
STREAM ID FROM :
TO :
COMPl ------PAD
RESULT1
PAD B
RESOLT2 B
RESULT3 C
RESULT4 D E
SUBSTREAM: MIXED
PHASE: COMPONENTS: KMOL/HR
LIQUID
N2 0.0
C02
0.0
MATER
5.5508-0*
DBA TEA
2.7108-02 1.9103-02
COMPONENTS: MOLE FRAC
N2 0.0
C02
0.0
MATER
1.2011-04
DEA TEA
0.5845 0.4133
COMPONENTS: KG/HR
N2 0.0
C02
0.0
MATER
1.0000-04
DEA
2.8500
TEA COMPONENTS: MASS FRAC
2.8500
N2 C02
0.0 0.0
HATER
1.7544-05
DEA
0.4999
TEA
0.4999
MIXED / MIXED
<f.0134-O4') 2.0134-04
oTo------ 3.2574=04 5.5508-04 S.HAS-O* 2.7108-02 2.7108-02 1.9103-02 1.9103-02
4.3375-03 0.0
1.1959-04 0.5839 0.4115
4.3073-03 4.9496-03 1.1875-04
0.5799 0.4084
5.*401-03 0.0
1.0000-04 2.8500 2.8500
5.*401-03 1.4338-02
1.0OOO-O4 2.8500 2.8500
9.8850-04 0.0
1.7524-05 0.4995 0.4995
9.8403-04 2.5044-03
1.7482-05 0.4982
0.4982
MIXED
2.0134-04 5.6348=015 5.5500-06 2.7108-02 1.9103-02
4.2909-03 1.0741-02 1.1830-04
0.5777 0.4071
5.4401-03 2*2180-02 1.0000-04
2,8500 2.8500
9.84*8-04 3.8723-03 1.7458*05
0.4975 0.4975
MIXED i.0134-04
KG/HR L/HR STATE VARIABLES:
(S 1 PRES PSI
LFRAC SFRAC ENTHALPY: CAL/M31 CAL/GM CAL/SEC ENTROPY: CAL/MOL-K CAL/OI-R DENSITY: MCJL/CC GH/CC AVG MM
---"T. 6214^77'\ 4.4410-02
v-
/ 5.7057
570800
10.0000
4.4743-02 5.7200 9.9993
4*4922-02 5.7279
9.9997
" 3b.6666 -------75". 0000 35*.0300 274.9100 301 Tnoo \
14.7000
14.7000 4.3258-03
, Shp991.36*8-02
127.3000 i.ft3uu-09
357 .s. ooqy TT4J335S-ur
1.0000
0.9954
0.9879
0.9834
0.9454
0.0
0.0
0.0
0.0
0.0
-1.30M+05 -1.3010405 -1.1294+05 -1.1102+05 -1.0004405
-1059.4144 -1056.3474 -922.9357 *909.4195 -970.8420 -1*77.4354 -1477.4340 -1444.4424 -1444.9473 -1595.7302
-309.3932 -306.0513 -244.7934 -2*0.3883 *212.9139
-2.5085
-2.5040
-2.1*38
-2.1330
-2.0443
9.0818-03 1.1201
123.3354
4.4418-03 0.5705
122.9220
4.474C-03 0.5720
122.3720
4.4923-03 0.5728
122.0744
5.7400*03 0.5935
103.0397
a
o
i
T>
} 1O 7
A -< O I> ^0
r
MIXED
SUBSTREAM PROPERTIES:
ASPEN PLUS
VER: DEC-VAX
REL: 8.5-2
INST: DOW-VAX
ARC INTERPRETATION
STREAM SECTION
5/18/92 PAGE 22
COMP! RESULT1 RESULT2 RESULTS RESULT4 (CONTINUED)
STREAM ID
COMPl
RESULT1
RESULT2
RESULTS
RESULT4
1T.T- PHASES
VMX
L/HR
CPMX
CAL/GM-R
*** LIQUID PHASE ***
RH0MX
Qt/CC
5.0688 0.4898
1.1201
10.0000 {7T7IEN6
1201
9.9993 IT. 709?
0.9474
9.9997 u./jD
9.9496 1 u!fllr
0.9495
0.952?>
$-
fM*
0j
DO A 0 1 7 0 9 5
C O N F ID F N T T Al.
ASPEN PLUS
VER: DEC-VAX
REL: 8.S-2
INST: DOW-VAX
ARC INTERPRETATION
STREAM SECTION
RESOLT5 RESULTS FINAL PADGAS C02B
S/18/92 PAGE 23
STREAM ID FROM : TO :
RESULTS E r
RESULT6 r END
FINAL END
--
PADGAS
--
PAD
C02B B
SUBSTREAM: !MIXED
PHASE:
MIXED
MIXED
MIXED
VAPOR
COMPONENTS: KMOL/HR
N2 2.0134-04 2.0134-04 2.0134-04 2.0134-04
C02
5.0398-04 5*0396-04
0.0
MATER
/T.555|-D2_ 7.6429-02.:\ 7.6629-02
0.0
DEA
2.7108-02 "2T7IOT=UT 2.7108-02
0.0
TEA
1.9103-02 1.9103-02 1,9103-02
0*0
COMPONENTS: MOLE PRAC
N2
2.7403-03 1.4037-03 1.6037-03
1.0000
C02
6.8595^03 4.0144-03 4.0144-03
0.0
MATER
0.3614
0.6263
0.4243
0.0
DEA
0.3689
0.2159
0*2159
0.0
TEA
0.2600
0.1521
0.1521
0.0
COMPONENTS: KG/HR
N2 5.<401-03 5,4401-03 5.6401-03 5.4401-03
C02
2.2180-02 2.2180-02 2.2180-02
0.0
MATER
0.4784
1.4165
1.4145
0.0
DEA
2.8500
2*8500
2.8500
0.0
TEA
2.8500
2.6500
2.8500
0*0
COMPONENTS: MASS PRAC
N2
9.0879-04 7.8944-04 7.8944-04
1.0000
C02
3.5739-03 3*1046-03 3.1046-03
0.0
MATER
7.7065-02
0.1982
0*1982
0.0
DEA
0.4592
0.3989
0.3989
0.0
TEA
0.4592
0.3989
0.3989
0.0
TOTAL FLOW:
KM3L/HR
7.3472-02
0.1255
0.1255 2.0134-04
KG/HR
6.2062
7.1443
7.1443 .5*6401-03
L/HR
10*0309
9.9983
10.0240
4.9243
STATE VARIABLES:
TEMP C
325.0800 384.9700
25.0000
25.0000
PRES PSI VFRAC
759.4000 . 2707.9000
M 14.7000
5.0982-02 ' 4.0704-02 473511-01 ~------ -
VAPOR
0.0 3.2579-04
0.0 0.0 0.0
0.0 1.0000 0.0 0.0 0.0
0.0 1.4338-02
0.0 0.0 0.0
0.0 1.0000 0.0 0.0 0.0
3,2579-04 1.4338-02
7.9683
25.0000 14.7000
1.0000
SFRAC ENTHALPY:
CAL/MOL
CAL/GM CAL/SEC ENTROPY: CAL/M0L-1C CAL/GM-K DENSITY: MOL/OC GM/CC AVG MM
0.6
0.0
0.0
0.0
o.o
-8.9696404 -7.1742+04 -9.1334+04 -1061.8553 -1241.0424 -1405.0143 -1830.5878 -2502.5842 -3185.2153
0.0 0.0 0.0
-9.4054+04
-2137.1149 -8.5114
-168.0670 -1.9896
-98.90X2 -137.2710 -1.0509-03
0.6943
-1.7379
-2.4122 -3.7514-05 1.5777-02
7.3245-03 0.6187
84.4710
1.2557-02 0.7145
56.9047
1.2524-02 0.7127
56.9067
4.0866-05 1.1454-03
28.0134
4.0886-05 1.7994-03
44.0098
1XED
SUBSTREAM PROPERTIES:
ASPEN PLUS
VER: DEC-VAX
REL: 8.5-2
INST: DOM-VAX
ARC INTERPRETATION
STREAM SECTION
5/18/92 PAGE 24
RESULTS RESULTS FINAL PADGAS 0028 (CONTINUED)
STREAM ID
RESULTS
RESULTS
FINAL
PADGAS
C02B
+** all phases +
VMX
L/HR
CPMX
CAL/GM-K
*** LIQUID phase ***
RHOMX
GM/OC
0.9115 0.9443
10.0240 0,6102 7 0.6027
0.6273
1.1695
4.9243 0.2486
MISSING
7.9683 0.2007
MISSING
<s-7)cr*<"
/.$L
ASPEN PLUS VER: DEC-VAX C02C STEAMD STEAME STEAMF
REL: 8.5-2
INST: DOW-VAX
ARC INTERPRETATION
STREAM SECTION
5/18/92 PAGE 25
STREAM ID
PROM : TO :
C02C
c
STEAMD D
S--T--E--A--ME
E
S--TEAMP
F
SUBSTREAM: MIXED
PHASE:
VAPOR
LIQUID
LIQUID
LIQUID
COMPONENTS: KMOL/RR
C02
1.7819-04
0.0
0.0
0.0
MATER
0.0
1.0504-02 1.8048-02 5.2073-02
COMPONENTS: HUB PRAC C02
MATER
1.0000
0.0
0.0 1.0000
0.0
1.0000
0.0 1.0000
COMPONENTS: KG/HR
C02
7.8421-03
0.0
0.0
0.0
MATER
0.0
0.1892
0.2890
0.9381
COMPONENTS: MASS PRAC C02 WATER
1.0000
0.0
0.0
1.0000
0.0
1.0000
0.0 1.0000
TOTAL FLOW:
KMOL/HR
1.7819-04 1.0504-02 1.8048-02 5.2073-02
KG/HR
7.8421-03
0.1892
0.2890
0.9381
L/HR
4.3582
Q.19BC
0.3034
0.9847
STATE VARIABLES: TEMP C
25.0000 100.0000 100.0000 loo.oooo
PRES PSI
VFRAC LFRAC
14.7000
1.0000
0.0
14.7000 0.0
1.0000
14.7000 0.0
1.0000
14.7000 0.0 1.0000
SFRAC
0.0
0.0
0*0
0.0
ENTHALPY:
CAL/MOL
->.4054+04 -8.8923404 -8.8923404 -8.8923404
CAL/04
-2137.1149 -3714.7757 -3714.7757 -3714.7757
CAL/SEC
-4*8554 -195.2743 -298.2824 -948.0144
ENTROPY:
CAL/MOL-K
0.8943 -34.8874 -34.8874 -34.8474
CAL/GM-K
1,5777-02
-1.9354
-1.9354
-1.9354
DENSITY:
HOL/OC
4.0884-05 5.2879-02 5.2879-02 $.2879-02
OM/CC
1.7994-03
0.9528
0.9528
0.9528
AVG MM
44.0098
18.0152
18.0152
18.0152
MIXED
SUBSTREAM PROPERTIES:
+++ ALL PHASES **
VMX
L/HR
CPMX
CAL/GM-E
4.3582 0.2007
0.1988 1.1700
0.3034 1.1700
0.9847 1.1700
*** LIQUID PHASE ***
RHOMX
/ 0
MISSING
0.9528
0.9528
0.9528
C O N FID EN TIAL