Document 7Rz6EpdBM0ReyoDMo6bg0ng48
LACSD1 ::MONROE
JOB 528
ARC696
Owner UIC: Account:
[MONROE] 355
Priority: Submit queue: Submitted: Printer queue: Printer node: Started:
100
LALP01_ANSI 18-MAY-1992 16:13 LPS20$LALP01 LALP01 18-MAY-1992 16:12
Digital Equipment Corporation
VAX/VMS Version V5.4-1
PrintServer 20
DO A 017242 CONFIDFNTTAI...
ASPEN PLUS IS A TRADEMARK OF ASPEN TECHNOLOGY, INC, 251 VASSAR STREET CAMBRIDGE, MASSACHUSETTS 02139 417/497-9010
VERSION: DEC-VAX RELEASE: 8,5-2 INSTALLATION: DON-VAX
HOTLINE: U.S.A. 417/497-9010 EUROPE (32) 2/732-4300
MAY 18, 1992 MONDAY 4:09:37 P.M.
C O N F ID F N T I
o o 3>
O
\)
DO A O 1 7 ? 4 4 CO NFIDENTIAL
ASPEN PLUS
VER: DEC-VAX PEL: 8.5-2
INST: DON-VAX
ETHANOLAMINES ARC INTERPRETATION
RUN CONTROL SECTION
RUN CONTROL INFORMATION
5/18/92 PAGE 1
THIS VERSION OF ASPEN PLUS LICENSED TO THE DON CHEMICAL COMPANY TYPE OF RUN: MEN
INPUT FILE NAME: DI8K8PE2:[MONROE.PRLAD.REACTIVE]ARC9.INP;4
OUTPUT PROBLEM DATA FILE NAME: ARG(9( VERSION NO. 1
LOCATED IN;
DISKIPE2:[MONROE.FRLAD.REACTIVE]
PDF SIZE USED FOR INPUT TRANSLATION: NUMBER OF FILE RECORDS (PSIZB) 99999
NUMBER OT IN-CORE RECORDS
- (00
PSIZE NEEDED FOR SIMULATION
- 2000
GALLING PROGRAM NAME: LOCATED IN:
GENERAL ASP$ROOt: [A8PD0N]
SIMULATION REQUESTED FOR ENTIRE FLOWSHEET DESCRIPTION
CALCULATIONS OT VLB, HEAT CAPACITY, AMD DENSITIES TO IMPROVE ACCURACY FOR ARC INTERPRETATION STUDIES. ETHANOLAMINES T-271 BOTTOMS 8AWLS ARC RCLi 92-0(96
BLOCK STATUS
ALL UNIT OPERATION BLOCKS WERE CCMPLBTED NORMALLY ALL CONVERGENCE BLOCKS HERE COMPLETED NORMALLY
ASPEN PLUS
VER: DEC-VAX REL: 8.5-2
INST: DOH-VAX
ETHANOLAMINES ARC INTERPRETATION
INPUT SECTION
INPUT FILE(S)
5/18/92 PAGE 2
ORIGXNAL RUN
MAY 18, 1992
4:08:37 P.M.
MONDAY
INPUT FILE: DISK8PE2: (MONROE.PRLAD.REACTIVE]ARC69C.IMP;4 OUTPUT PDF: ARC(9( VERSION: 1
LOCATED IN: DISK8PR2; [MONROE.PRLAD.REACTIVE)
1 2 TITLE 'ETHANOLAMINES ARC INTERPRETATION'
3
4 5
( DESCRIPTION "Calculations of VLB, boat capacity, and donaitioa to 7 laproTo accuracy for ARC interpretation atudloa.
8 EthanoXaBlnoa T-271 botto** aaaplo
9 10
11 ;
ARC RCL: 92-0(94"
12
13 IN-UNITS MET TEMPERATURES PRESSURE-P8I MASS-Oi
14 OUT-UNITS MET TEMPERATURES PRESSURB-F8I KAS5SM VOLUME-FUN^' L/HR'
15
1( RUN-CONTROL MAX-TIME-1000
17 18 ; SPECIFY THE PHYSICAL PROPERTY DATABANK
19
20 DATABANKS DON
21 22 ; SPECIFY NHAT PROPERTIES YOU MANT ON PRINTOUT
23
24 PROP-SET 8ET1 VMX
UNITS--"L/HR"
25 PROP-SET SET2 RHOMX UNITS--"GM/CC"
2( PROP-SET SBT3 CPMX UNITS--"CAL/CM-K*
27
PHASES PHASE-L PHASES
28 SPECIFY THE C0W0MBNT8
29
30
N2 NITROGEN
C02 002
/ MATER MATER /
31 MEA MONOETHANOLAMINE DBA DIETHANOLAMINE /
32
TEA TRIETHANOLAMINE
TEAGE 'TRIETHANOLAMINE GLYCOL ETHER
33
34
35 SPECIFY THE PHYSICAL PROPERTIES METHOD
3( IDEAL VAPOR LIQUID EQUILIBRIUM 37
38 PROPERTIES SYSOP0A HENRY-CCWS-LIST1 39
40 HENRY-COWS LIST1 N2 C02
41 ; 42 ;
43 / SPECIFY CCBIPOMENT DIPOLE MOMENT, SO ASPEN GAN PREDICT
44 ; VAPOR VISCOSITY FOR MIXTURE.
45
4( PROP-DATA 47 IN-UNITS MET
48 PROP-LIST
HUP
DO A 0 1 7 2 4 5
C O N F ID F N T T A L
ASPEN PLUS
VER: DEC-VAX NEL: 8.5-2
INST: DON-VAX
ETHANOLAMINES ARC INTERPRETATION
INPUT SECTION
5/18/92 PAGE 5
INPUT FILE(S) (CONTINUED)
155 158 157 158 159 180 181 182 183 184 185 188 187 188 189 170 171
172 173 174 175 178 177 178 179 180
181 182 183 184 185 188 187 188 189 190 191 192 193 194 195 198 197 198
SPEC VOL TO 10.0 TOL-SPEC .05 VARY STREAM-VAR 8TREAM-C02C VARIABLE-MASS -FLON ; VARY BLOCK-VAR BLOCK-C VARIABLE-PRES LIMITS .001 1.0
DESIGN-SPEC D
DEFINE VOL STREAM-PROP 8TREA1MESULT4 PROPERTY-SETl SPEC VOL TO 10,0
TOL-SPEC .05 VARY STREAM-VAR STREAM-STEAMD VARIABLE-MASS-FLON ; VARY BLOCK-VAR BLOCK-D VARIABLE-PRES LIMITS .001 3.0
DESIGN-SPEC E
DEFINE VOL STREAM-PROP STREAM-RESULTS PROPERTY-SETl SPEC VOL TO 10.0
TOL-SPEC .05 VARY STREAM-VAR STREAM-STEAMS VARXABIM(ASS-FLOW ; VARY BLOCK-VAR BLOCK-E VARIABLE--PRES LIMITS .001 3.0
DESIGN-SPEC P
DEFINE VOL STREAM-PROP STREAM-RESULTS PROPERTY-SETl SPEC VOL TO 10.0 TOL-SPEC .05
VARY STREAM-VAR STREAM-STEAMT VARIABLE-MASS-FLON ; VARY BLOCK-VAR BLOCK-F VARIABLE--PRES
LIMITS .001 3.0
DESIGN-SPEC END DEFINE VOL STREAM-PROP STREAM-FINAL PROPERTY-SETl SPEC VOL TO 10,0 TOL-SPEC .05 VARY BLOCK-VAR BLOCK-END VAR1ABLE-PRES LIMITS 25 300
REPORT INPUT
PROPERTY-REPORT WOCOWS
STREAM-REPORT MASSFRAC MASSPLOW MOLEFRAC MO&EFXON NOKEROFLOM S
PROPERTIES--SET1 SET2 SETS
A
1NCL-STREMIS-CCMF1 RZStJLTl RMULT2 RESULTS RESULT,,
RESULTS RESULTS FINAL PADGAS O02B
k
C02C STEAMD STEAMS STEAMF
SIMULATION STARTED
MODULE USED: GENERAL CREATION: ,5/ 8/92 18:03:08
LOCATED IN:ASP$R0OT;(ASPDOW)
>
SIMULATION COMPLETED FOR ENTIRE FLOWERET
ASPEN PLUS
VER: DEC-VAX REL: 8.5-2
INST: DON-VAX
ETHANOLAMINES ARC INTERPRETATION
FLOWSHEET SECTION
FLOWSHEET CONNECTIVITY BY STREAMS
5/18/92 PAGE 8
STREAM PADGAS C02B STEAMD STEAMF RESULT2 RESULTS RESULTS
SOURCE
-- -- --------**---
B D F
DEBT PAD
B D
F
C
E END
FLOWSHEET CONNECTIVITY BY BLOCKS
STREAM CCHP1 C02C STEAMS
RESULT1 RESULTS RESULTS FINAL
SOURCE
-- --------....
PAD C E END
DEBT PAD C E B D F
----
BLOCK PAD B C
D E F END
INLETS COMPl PADGAS RESULT1 002B RESULT2 C02C
RESULT3 8TEAMD RESULTS STEAMS RESULTS 8TEAMF RESULTS
OONVEMZNCR STATUS SOMARY
OUTLETS RE3ULT1 RESULT2 RESULT3 RESULT4 RESULTS RESULTS FINAL
DESIW-BPEC SUMARY
DESIQI SPEC
TOLERANCE
ERR/TOL
VARIABLE
CONV STAY BLOCK
A
0.3S038E-1Q 0.50000E-01 0.72077E-09 0.52387E-02 #
8OLVER01
B
-0.17S1SE-02 0.50000E-01 -0.3S232E-01 0.78089E-02
8OLVER02
C
0.SS217E-02 0.50000E-01 0,11243
0.34588K-01 #
8OLVER03
D
0.39S0SE-01 0.50000E-01 0*79212
0,31321
# 8OLVER04
E
-0.23660E-01 0.500001-01 -0.47320
0.38743
# 8OLVER05
F
-0.11S.71E-01 0.50000E-01 -0,23342
0,42138
# 8OLVER08
-0.31390E-01 0.500001-01 -0.82780
78.204
# IOLVERQ7
# - CONVERGED * - NOT CONVERGED LB AT LONER BOUNDS U - AT UPPER BOUNDS
DESIGN-SPEC: A
SAMPLED VARIABLES:
VOL
: PROPERTY 8TRNPR0P RETl IN STREAM RESULT1
SPECIFICATION:
MAKE VOL APPROACH 10.0000
WITHIN
0.050000
ASPEN PLUS
VER: DEC-VAX REL; 8.5-2
INST: DOW-VAX
ETHAB90LAMINES ARC INTERPRETATION
FLOWSHEET SECTION
5/16/92 PACT 9
DESIGN-SPEC: END (CONTINUED)
MANIPULATED VARIABLES:
VARY
: SENTENCEDARAM VARIABLB-PRES IN UOS BLOCK END
LOWER LIMIT *
25.0000
PSI
UPPER LIMIT -
300.000
PSI
FINAL VALUE -
78.2045
PSI
CONVERGENCE BLOCK: 9OLVER01
SPECS: A
MAXIT- 30 STEP-SIZE- XOO.OO
% OF RANGE
MAX-STEP-
100.
i OF RANGE
XTOL-
1.0000001-08
THE MEW ALGORITHM MAS USED WITH BRACKETING-NO
METHOD: SECANT
STATUS: CONVERGED
TOTAL NUMBER GT ITERATIONS:
3
.
*+* FINAL VALUES +*+
VARIABLE TOTAL MASSFL
KG/HR
VALUE 0.5238743D-02
PREV VALUE 0.5238743D02
ERR/TOL 0.7207457D-09
*** ITERATION HISfCftY ***
DESIGN-SPEC ID: A
ITERATION VARIABLE
ERROR
ERR/TOL
0.5275E-07 LB 0.5344E-07 LB
0.5195E-07 LB
0.7095E-01 0.1495 0.34041-10
1*419 2.990
0* 72081-09
CONVERGENCE BLOCK: 4OLVER02
SPECS: N
MAXIT- 30 STEF-SISE--
100.00
I OF RANGE
MAX-STEP--
100. % OF RANCT
XTOL-
1.QO0000E-O8
THE NEW ALGORITHM WAS USED WXTE BRACKETING-NO
METHOD: SECANT
STATUS: CONVERGED
TOTAL NUER OT ITERATIONS:
3
*** FINAL VALUES ***
VARIABLE TOTAL MASSFL
KG/HR
VALUE 0.780C871D-02
PREV VALUE 0.7604871D-02
ERR/TOL -.3523179D-01
m* ITERATION HISTORY **
o
o
ASPEN PLUS
VER: DEC-VAX REL: 8.5-2
INST: DOW-VAX
ETHANOLAMINES ARC INTERPRETATION
FLOWSHEET SECTION
5/18/92 PACT 10
CONVERGENCE BLOCK: 40LVER02 (CONTINUED)
DESIGN-SPEC ID: B
ITERATION VARIABLE
ERROR
ERR/TOL
0.3358E-07 LB
0.9C43E-07 LB 0.4927E-07 LB
-0,5859
1,748 -0.1762E-02
-11.72 35.35
-0.3523E-01
CONVERCTNCE BLOCK: 4OLVER03
SPECS * C
MAXIT- 30 STEP-SIZE- 100.00
OF RANGE
MAX-STEP-
100. 1 or RANGE
XTOL-
1.000000E-08
THE HEN ALGORITHM NAS USED WITH BRACKETING-NO
METHOD: SECANT
STATUS; CONVERGED
TOTAL NU1BER or ITERATIONS:
3
** FINAL VALDES ***
VARIABLE TOTAL MASSFL
RG/HR
VALUE 0.345S547D-01
PREV VALUE 0.345S547D-01
ERR/TOL 0.11243310*00
*** ITERATION HISTORY ***
DESIGN-SPEC ID: C
ITERATION VARIABLE
ERR/TOL
0.33SBE-07 IB
0.9443E-07 LB 0.21B3E-04 LB
-2.OBI -1.377
0.5C22E-02
-41.B2 -27. S3 0.1124
COHVERIXNCE BLOCK: 4OLVER04
SPECS: D
MAXIT- 30 STEP-SIZE- 100.00
* OF RANGE
MAX-STEP-
100.
4 OF RANGE
XTOL-
l.OOOOOOE-OB
THE HEN ALGORITHM NAS USED NITH BRACKETINO-MO
METHOD: SECANT
STATUS: CONVERGED
TOTAL NUMIER OF ITERATIONS:
4
** FINAL VALUES ***
VARIABLE TOTAL MASSFL
KG/HR
VALUE 0.31320420*00
PREV VALUE 0.31320420*00
ERR/TOL 0.73212150*00
* ITERATION HISTORY ***
Vi
> ' O'
ASPEN PLUS
VER: DEC-VAX REL: 8.5-2
INST: DON-VAX
ETHANOLAMINES ARC INTERPRETATION
FLOWSHEET SECTION
COMPUTATIONAL SEQUENCE
5/18/92 PAGE 13
SEQUENCE USED NAS: SOLVERDI PAD SOLVEROK----- SOLVER02 B SOLVER02<--------SOLVER03 C $OLVER03<----- SOLVER04 D $OLVER04<-------- SOLVER05 E $OLVER05<--------SOLVEROC F $OLVERO----- SOLVER07 END *OLVER07<--------
OVERALL FLOWSHEET BALANCE
+++ MASS AND ENERGY BALANCE
IN OUT
CONVENTIONAL COMPONENTS (RMUL/HR )
N2
0.187008E-03
0.187Q08E-03
002
0.94S252E-03
0.983252E-03
WATER
0.411749E-01
0.811789E-01
ICA
O.OOOOOOE+OO
O.OOOOOOE+OO
DBA
O.OOOOOOE+OO
o.ooooooE+oo
TEA
0.34184SE-01
0.341848E-01
0.4C5734E-02
0.485734E-02
TOTAL BALANCE
MOLE < KMOL/HR )
0.101189
0.101189
MASS(KG/HR )
7.14975
7.14975
ENTHALPY (CAL/SEC )
-2884.48
-2710.34
RELATIVE Dirr.
O.OOOOOOE+OO O.OOOOOOE+OO o.ooooooE+oo o.ooooooe+oo o.ooooooe+oo o.ooooooe+oo o.ooooooe+oo
O.OOOOOOE+OO O.OOOOOOE+OO 0.954794B-02
ASPEN PLUS
VER: DEC-VAX REL: 8.5-2
INST: DON-VAX
ETHANOLAMINES ARC INTERPRETATION
O-O-S BLOCK SECTION
5/18/92 PAGE 14
BLOCK: B
KJOEL: HEATER
INLET STREAMS:
OUTLET STREAM: PROPERTY OPTION SET HENRY-CCMPS ID:
RES0LT1 RESULT2 SYSOPOA LIST1
C02B IDEAL LIQUID / IDEAL GAS
***
TOTAL BALANCE MOLE (JCMOL/HR ) MASS(KG/RR ) ENTHALPY(CAL/SEC )
MASS AND ENERGY BALANCE *** IN OUT
0.392119E-01 4.01315
-1524.78
0.3821181-01
4.01315 -1307.50
RELATIVE DI1T.
O.OOOOOOE+OO 0.1844331-14 -0.143420
***
TWO
PHASE TP PLASH
SPECIFIED TD9ERATDRE SPECIFIED PRESSURE
MAXIMUM NO. ITERATIONS
CONVERGENCE TOLERANCE
INPUT DATA
C PSI
*++
244.230 41.0000 30
0.000100000
OUTLET TEMPERATURE OUTLET PRESSURE HEAT DUTY VAPOR FRACTION
*+ RESULTS C PSI CAL/SBC
+++
244.23 41.000 218.28 0.83393E-02
V-L PHASE EQUILIBRIUM :
COMP
N2 CQ2
MATER TEA
TEAGE
r(i) 0.47492E-02 0.45239E-02
0.141541-03 0,87179
0.11877
xm 0.19355E-04
0.89575E-04 0.131871-03
0.87988 0.11988
rti)
0.50860 0.47489
0.116941-02 0.143351-01
0.99988B-03
BLOCK: C
MODEL: HEATER
INLET STREAMS:
OUTLET STREAM: PROPERTY OPTION SET: HENRY-CCMPS ID:
RESULT2
RESULT3 SYSOPOA LISTl
002C IDEAL LIQUID / IDEAL GAS
K(I) 28278.
5301.8 8.8882
0.18292E-01 0.83404E-02
r>
oo
zn o
M I>
oT1 o z^
H si
M \)
I> *
r si
ASPEN PLUS BLOCK E
VER: DEC-VAX REL: 8.5-2
INST: DOW-VAX
STHANOLAMHVES ARC INTERPRETATION
U-O-S BLOCK SECTION
MODEL; HEATER (CONTINUED)
OUTLET TEMPERATURE OUTLET PRESSURE
HEAT DUTY VAPOR FRACTION
** RESULTS C PSI
CAL/SBC
***
5/18/92 PAGE 17
350.51 1408.5 121.25 0.72743E-01
V-L PHASE EQUILIBRIUM
COMP N2 C02
WATER
TEA TEAGE
p(D 0.24043E-02 0.12384B-01 0,48582 0.43951 0.S9879E-01
*<D 0,295911-04 0*259431-03
0.46175 0.47344
O.44520S-O1
Y(I)
0.32675E-01 0.16694
0*79274 0.70227E-02 0.621521-03
K(I> 1104.2 643.50
1.7168 0.14834E-01
0.96319E-02
boat: END
ICDELt HEATER
INLET STREAM: OUTLET STREAM: PROPERTY OPTION SET: HENRY-COMPS ID
RESULTS FINAL SYSOPOA LIST1
IDEAL LIQUID / IDEAL GAS
+++
TOTAL BALANCE HOLE (KMDL/HR ) MASS (KG/HR ) ENTHALPY(CAL/SBC )
MASS AND ENERGY IN
0.101169 7.14975
-2092.73
*** OUT
0.101169 7.14975
-2710.34
RELATIVE DIPT.
O.OOOOOOE+OO 0.0000008+00 0.227873
***
TWO
PHASE TP FLASH
SPECIFIED TtWERAYURE
SPECIFIED PRESSURE
MAXIMUM NO. ITERATIONS
CONVERGENCE TOLERANCE
INPUT DATA
C PSI
**
25.0000 78.2045 30
0.000100000
ASPEN PLUS
VER: DEC-VAX REL: 8.5-2
INST: DOW-VAX
ETHANOLAMINES 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 PJUX 18
25.000 78.204 ~617.fl 0.88455E-02
V-L PHASE EQUILIBRIUM
COMP N2 002
WATER TEA
TEAGE
pa) 0.18485E-02
0.95212E-02 0.60470
0.33790 0.46035B-01
*<n
O.1205CB-O4 0.2565SE-02
0.61006 0.34091
0.44444E-01
Y<I) 0.20752 0.78869
0.35834E-02 0.36965E-09
0.IB203E-U
K(I> 16018. 307.47
0.58738E-02 0.10843E-08 0.391926-10
BLOCK: F
MODEL: HEATER
INLET STREAMS: OUTLET STREAM: PROPERTY OPTION SET: HENRY-COMPS ID:
RESULTS RESULTS SYSOPOA
LXST1
STEAMF IDEAL LIQUID / IDEAL GAS
***
TOTAL BALANCE MOLE (KMOL/HR ) MASS(KG/HR ) ENTHALPY(CAL/SBC )
MASS AND ENERGY BALANCE IN OUT
0.101169
7.14975 -2250.03
0.101169
7.14975 -2092.73
RELATIVE DIPT.
0.000000E+00 0.000000E+00 -0.699114E-01
+*
TWO
PHASE TP FLASH
SPECIFIED TEWERATURE
SPECIFIED PRESSURE
MAXIMUM NO* ITERATIONS CONVERGENCE TOLERANCE
INPUT DATA
C PSI
**+
380.080 2*429.10
30 0.000100000
CONF TDFNT TAl
o o i> o
N)
CO
ASPEN PLUS
VEA: DEC-VAX REL: 8.5-2
INST: DOM-VAX
ETHANDLAMINBS ARC INTERPRETATION
STREAM SECTION
OOMP1 RESULT1 RESULT2 RESULTS RE8ULT4
5/18/92 PAGE 21
STREAM ID PROM : TO
C0W1 PAD
RE8ULT1 PAD
B
RESULT2 B
RESULTS c D
RE8ULT4
D E
SUBSTREAM: MIXED PRASE:
LIQUID
MIXED X MIXED
OOMPOMfiVTS: KMOL/HR N2 C02
0*0 fl.Bioi-tjp 1.8701-04
0*0
fl .T733-04
MATER
5.5508-0# 5.5508-04 5.55M-0*
TEA
3.4185-02 S.4185-02 3.4185-02
TEAGE
4.4573-03 4.(573-03 4.(573-03
COMPONENTS: MOLE FRAG
N2
002
0.0 0.0
4.7908-03 4.7492-03
0.0
(.5239-03
MATER
X.4289-04 1.4220-04 1.4154-04
TEA TEAGE
0.8799 0.1198
0.8757 0.1193
0.717 0.1187
OPPONENTS: KG/NR
N2 C02
0.0 0*0
5.2587-03 5.2387-03
0.0
7.80(*-03
MATER TEA
1.0000-04 1.0000-04 1.0000-04
5.1000
5.1000
5.1000
TEAGE
0.9000
0.9000
0.9000
CMPONEMTS: MASS PRAC
M2
0.0
8.7235-04 .7121-04
C02 MATER
0.0
0.0
1.2*83-03
1.4444-05 1.4452-05 1.(430-05
TEA
0.8499
0.8492
0.8481
TEAGE
0.1500
0.1498
0.14*4
TOTAL FlOt:
KMOL/HR
KG/HR
L/HR
STATE VARIABLES':
NIXED 1.(701-04 i.l. 8701-04
3.4185-02 3741S5-1 4.4573-03 4.4573-03
4.4755-03 2.4083-02 1.3878-04
0,8544 0.1144
3.2589-03 1.(784-02
0.3030
0.5*57 8.11(2-02
5.2387-03
4.2393-02
1.0000-04 5.1000 0.9000
5.2387-03 4.2393-02
0.3133 5.1000 0.9000
8.4423-04 7.0097-03
1.4535-05
0.8432 0.1488
8.2358-04 4.4445-03 4.9255-02
0.9017
0.1414
n oo
LFRAC SFRAC Enthalpy: CAL/MDL CAL/OI CAL/SEC ENTROPY: CAL/HOL-K CAL/GN-K DENSITY: HOL/OC GM/CC AVC MT
NIXED
0. *472 0.0
-1.4038.05 -1.2004+05 -1.15*9+05 -*.7700+04 -12.4741 -782.7844 -7(7.128* -*1.3704
-1522.1434 -1307.5024 -1288.71*3 -1557.3173
-433.**20 -431.1134 -3*1.*44* -3(*.04*S -25*.((*5
-2.80*2
-2.*0(7
-2.4*0*
-2.4342
-2.3425
7.1447-03 1.1035
154.4527
3.*034-03 0.(005
1S3.*((
3,21*-03 0.(014
153.3500
3***75-03 0.(044
151.2017
5.7157-03 0.(335
110.8(9*
:
ASPEN PLUS
VER: DEC-VAX REL: 8.5-2
INST: DOM-VAX
ETHAMOLAMINES ARC INTERPRETATION
STREAM SECTION
5/18/82 pact; 22
OOMP1 RES0LT1 RESULT2 RESOLT3 RESULTS (CONTINUED)
STREAM ID
COMP1
RESOLT1
RESULT2
RESULTS
RESULTS
++ + fcTT PHASES ++*
VMX
L/HR
CPXX
CAL/GM-K
*** LIQUID PHASE *** RHOMX GM/OC
5.4372 0.503(
10JP'00 5074
1.1035 i 1.1035
*.*982 8833
0.9(17
10.0054
10.03*4
8.7095" 3|7S7T>
035(
n nL>
"22. ro
Jiz/gS-SMoffis .sots''
n, /nwOsfr&vrr
=- r.U- 't'2-
/'*y
m >sS1i
fa'
tf/AW* Mb* l'
ATaac.^ *->`1
tyo fid*
350.5"/
3 fO.O? zl.S7
.>W
u`
A f sO
ASPEN PLUS
VER: DEC-VAX REL: 8.5-2
INST: DON-VAX
ETHANOLAMINES ARC INTERPRETATION
STREAM SECTION
O02C STEAMD STEAME STEAMP
5/10/92 PAGE 25
STREAM ID
FROM TO
C02C c
STEAMD D
STEAME E
STEAMF F
SUBSTREAM: MIXED PHASE:
VAPOR
LIQUID
LIQUID
LIQUID
COMPONENTS: KMOL/HR
C02 NATER
7*8580-04
0.0
0.0
o.o
0.0
1.7384-02 2.0390-02 2.3390-02
COMPONENTS: MOLE FRAC
C02 NATER
1.0000 0.0
0.0 1.0000
0.0 1.0000
0.0 1.0000
COMPONENTS: KG/HR
C02
3.4580-02
0.0
0.0
0.0
NATER
0.0
0.3132
0.3074
0.4213
COMPONENTS: MASS FRAC
C02 NATER
1.0000 0.0
0.0 1.0000
0.0 1.0000
0.0 1.0000
TOTAL FLOW: KMOL/HR
7.0580-04 1.7380-02 2.0390-02 2.3390-02
KG/HR L/HR
3.4580-02 19.2208
0.3132 0.3287
0.3074 0.3857
0.4213 0.4423
STATE VARIABLES: TQtP C PRES PSI
25.0000 14.7000
100.0000 14.7000
100.0000 14.7000
100.0000 14.7000
VFRAC LPRAC
1.0000 0.0
0.0 1.0000
0.0 1.0000
0.0 1.0000
8FRAC
0.0
0.0
0.0
0.0
ENTHALPY: CAL/MDL
-9.4054+04 -0.0923+04 -0.0923+04 -0.6923+04
CAL/Ot CAL/SEC
-2137.1149 -3714.7757 -3714.7757 -3714.7757 -20.5315 -323.1919 -379.1494 -434.8109
ENTROPY:
CAL/MOL-R CAL/GM-K
0.0943 X.5777-02
-34.8074 -1.9354
-34.0074 -1.9354
-34.8674 -1.9354
DENSITY:
MOL/OC 04/CC
4.0880-05 5.2879-02 5.2879-02 5.2879-02
1.7994-03
0.9520
0.9520
0.9526
AVG MN
44.0098
10.0152
18.0152
18.0152
MIXED
SUBSTREAM PROPERTIES:
... ALL PHASES **
VMX
L/HR
CPMX
CAL/GM-K
19.2208 0.2007
0.3287 1.1700
0.3857 1.1700
0.4423 1.1700
LIQUID PHASE +**
RHOMX
ai/oc
MISSING
0.9520
0.9520
0.9524
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3* 3s
^ M~ in
'o
S'*