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ASPENTECH FLOWSHEET SIMULATION FOR
THE PROCESS INDUSTRIES
FOR HOTLINE SgRUICE, PLEASE CALL 617-L97-901C
ASPEN PLUS IS A TRADEMARK OF ASPEN TECHNOLOGY, INC, ESI UASSAR STREET CAMBRIDGE, MASSACHUSETTS CZl 3 9 617-L97-9310
uersion: IBM-CMS release: 8.1 INSTALLATION: RSCSLLC
OCTOBER 26, 1989 THURSDAY
l:l5:07 p.M.
SL 104524
ASPEN PLUS
UER : IBM-CMS
kEL: 8.1
INST: RSCSLKC
UOCM REACTOR BOTTOMS STRIPPER
10/^6/39 PAG
ASPEN PLUS(TM) is a proprietary product of aspen technology, INC, (ASPENTECH), CAMBRIDGE, MASSACHUSETTS, AND MAY BE USED ONLY UNDER AGREEMENT WITH ASPENTECH Ok THROUGH NETWORK" SERUICES LICENSED BY ASPENTECH. ASPEN PLUSITMl IS A TRADEMARK OF ASPENTECH, The ASPEN PLUS COMPUTER" SOFTWARE SYSTEM IS USED FOR FLOWSHEET SIMULATION.
t-iBle of contents
RUN
control section...................................................................... .. RUN CONTROL INFORMATION,,................ ............................... DESCRIPTION, ..........................................................
SLOCK STATUS................
1 1 I
I
INPUT SECTION................................................................. ................................,,, I -PuT r ILL' ( S I..,..,., .......................................... ...
L Z
FLOWSHEET SECTION.,,,...........................0
FLOWSHEET CONNECTIUITY BYSTREAMS.............................
FLOWSHEET CONNECTIUITY BYBLOCKS.,..........................
computational sequence ............... ....................... ................. juerall flowsheet balance....................................
9
8
8 s
PHYSICAL PROPERTIES SECTION................... .......................................... COMPONENTS.......................
9 9
U-O-S BLOCK SECT I ON. .
............................................... ID
block: udcstrip model: radfrac.......................
ic
ST=EAM SECTION.,...................... ............................................................... ... FEEOl LIJUID1 STEAM1 ................................................
15 IS
ASPEN plus
VER: I3M-CMS
PEL! 8,1
INST: RSCSLKC
vdcm reactor bottoms stripper
RUN CONTROL SECTION
RUN CONTROL INFORMATION
10/26/89 PAGE
THIS VERSION OF ASPEN PLUS LICENSEO TO PPG INDUSTRIES, INC, TYPE OF RUN: NS*
input file name: hi
output problem data file name: LOCATED in:
pi
GJI191
version no,
i
PDF SICE USEE FOP INPUT TRANSLATION:
number of file records (psize) =
NUMBER OF IN-C3R- SECONDS
=
PSIZE NEEDED FOP SIMULATION
=
20;
2" 32
CALLING PROGRAM NAME: LOCATED in:
PI
SIMULATION REOUESTtu FOR ENTIRE FLOWSHEET
description
THIS SIMULATION RILL Bfc USED TO DETERMINE The PACKING HEIGHT NElDlD FDR Nen U 0 CM REACTOR BOTTOMS STRIPPER
BLOCK STATUS
* * ALL UNIT OPERATION BLOCKS HERE COMPLETED NORMALLY
SL 104526
ASPEN PLUS INPUT FILE(S)
UcR:
{SH-C'S
ael: 8.1
INST: RSCSLKC
UDCM REACTOR 30TT0MS STRIPPER
INPUT SECTION
10/26/89 PAGE
>>ORIGINAL RUN 1 : l 3 : 3 l P. N ,
INPUT FILS: PHI output pdf: pi
VERSION;
OCTOBER 26, 1989 THURSDAY
located in: guii?i 1;
2 ;i
3 :o
*;
M C:\MMSYS R
M "Ml
.2,2
N S 27 13:26:59
5
6
7
d
9
I : SUMMARY MM
II
12 IN-UNITS ENG 13
14 OUT-UNITS t N G 15
1 6 TITLE "UDCM REACTOR BOTTOMS STRIPPER" 17
i a account-info accjunt = guillqry user-name="guilljry" 19
i
20 RUN-CONTROL MAX-TIMEilDODO 21
22 description "This simulation will 8S used to determine tme packing 23 HEIGHT NEEDED FOR NEW UDCM REACTOR BOTTOMS STRIPPER " 24
25 DATABANKS AQUEOUS / SOLIDS / DIPPRPCD 26
27 PROP-SOURCES AQUEOUS / SOLIOS / DIPPRPCD 28
29 COMPONENTS H 2 0 H2G H20 / NA3H NAOH NAOM / NA CL NACL NACL 6 3; / oh- oh- oh- / nay nay nay / cl- cl- cl- / per s 31 C2CL* PER 32
33 122
insert global caust h2q naoh nacl na2soy no
123 124
125
FLOWSHEET PERH20 BLOCK UDCSTRIP IN=FEED1 STEAN1 OUTpUAPORI LI0UI01
126 127
1iT2t89~
i3a
PROPERTIES SYSOP 15M / SYS0P12 / SYS0P15M PERH20 CHEMISTRYsCAUST TRUE-CGMPSO
PROP-DATA IN--UNITS SI
131 132_ 133
PROP-LIST BPUAL PER_ H20 BPUAL H20 PER
GNELCA -4,498
5,939
/GMELCB / GNELCM /3012,2 / ,2
/ 952,5 / .2
1
(
SL 104527
ASPEN PLUS
UER: I8M-C M 5
R-l: 8.1
INST: RSCSLKC
UDCrt REACTOR BOTTOMS STRIPPER
INPUT SECTION
10/26/69 PAGE
INPUT FIL(SI (CONTINUED)
13* 1 33
113376
139 139 1*0
1*1
1*2 1*3 1 **
1*5
1*6 1*7 1*6 1*9 150
151 15 2 153
1 5*
153 15 6
157
159
159 lei 16 1
162
163
16*
165 166
167 1 e8
169
17C
171 172
1 73 17* 175 176 177 178 179
180 181 182
183
PROP-LIST PPUAL PER (NAT CL- I PPUAL (NAT CL-) PER PPUAL D E R (NAT OH--1 PPUAL INAT ON-I PER
PPUAL (NAT C L-) PER PPUAL PER ( N A + CL-I PPUAL (NA + OH--) PER
PPUAL ER (NAT OH--)
GNELCC -*.*98
5,939 -*,*98 5.939
1.2*1 6,678 1.2*1 6.676
/ GMELCD / GMELCN
/ 3012,2 / .2 J SANE AS PER-H20
/ 952.5 / .2
/ 3012,2 / .2 (SANE AS PSR-H20
/ 952.5 / .2
/o
/ .2 ;same as egc-hcl
/J
/0
/ .2
/ .2
STREAM FEED1 5U3STREAM MIXsD PRlS=23,7 UFRACiO.vj MASS -- FL3WP35365
MASS-FRAC H2J ,611389 / P5R .000029 / NAOH . ,C86 / NACL .18
STREAM STEAM1 SJ3STRSAM TMP=350 1 SHASt=U mass-frac h2o i
PRES
16*.7 MASS-FL0N=135* NPHA SE =
SLOCK UDCSTR1P R A 0 F R A C PARAM N5TAGE-2 ABSORBERjNQ FEEDS FEED1 1 ON-STAGE / STEAM1 2 ON-STAGE PRODUCTS UAP0R1 1 U / LI9UID1 2 L P-SPEC l 23.7 / 2 2*.7 COL -SPECS 5N = U M0LE-RDU=1 (J1 = 0 T-EST 1 2*0 U-EST 1 39 L-EST 2 19o 9 UARY 1 FEED-FLON 5 200 STREANsSTEAHl SPEC 1 MASS-RATIO .025 STAGE=1 PHASE=U BASE-STREAHS=FED1
i UART 1 J;F ,w2 .0* : SPEC 1 MASS-FRAC 1E-C6 stream=liruidi CONPS=PER
PLOT 1 uASIS = MASS Y-SCALE*LOG PLOT-HEAO ING= 6 "LIGHT KEY / HEAUY FEY" S-OPTION=LOG HEAUY-KY=PER S-PL0T=H2O
TRaY-REPORT TRAY-OPTION=ALL-TRAYS FORMATsCOMBINED REPORT REPORT T0T3AL INPUT COMPBAL RESULTS
REPORT INPUT
BLOCK-REPORT COMPBAL
5TREAM-REP0R NOZEROFLOU NOLEFLOM HASSFLOW MOLEFRAC MASSFRAC
i PROPERTY--REP NOPARAMS NOPROP-DAtA
si>
ASPEN PLUS
UES: IBH-CNS
5EL: 8.1
INST: RSCSLKC
UOCM REACTOR BOTTOMS STRIPPER
INPUT SECTION
INPUT FILE(S) (CONTINUED 1
184 IBS
; ;
10/26/39 pace
Ci
104529 SI*
*# INSERT ECHO
II INSERT CAUST
FROM THE SYSTEM INSERT LIBRARY:
J #2 BY: TAKE date: 7-SEP-1909 OUT SALTS
; *1 by: cccdeu date; i-sep-1988 new
COPYRIGHT <C> 1988
ASPEN TECHNOLOGY, INC* CAMBRIDGE, M A
* # *#wwn
r*#****#ir*ftir*4
Insert name: cajst
PURPOSE
; PROVlDc PHYSICAL PROPERTY PARAMETERS FOR
hQUEOUS CAUSTIC SOLUTION WITH SUDIUM CHLORIDE
SODIUM SULFATE
data RANGE : TEMPERATURE FROM 0 TQ 2C0 C
PRESSURE UP TO 10 ATMOSPHERE
NAOH CONCENTRATION UP TO SO HTf PERCENT
NACL CONCENTRATION up TO SATURATION
N A 2 S 0 * CONCENTRATION UP TO SATURATION
AND
USAGE NOTE I l. apparent components are: H 2 0) NAOH, NACL f NA2SQY
ARGUMENT LIST ARGUMENT 1 : 'GLOBAL1 OR FLOWSHEET SECTION ID ARGUMENT 2 I COMPONENT ID FOR H20 ARGUMENT 3 : COMPONENT ID FOR NAOH ARGUMENT y : COMPONENT ID FOR NACL argument -5 : COMPONENT ID FOR NA2S0Y A n G U M E N T o : SIMULATION APPROACH
no : apparent component approach
YES : TRUE SPECIES APPROACH
calling example: INSERT GL03AL CAUST M20 NAOH NACL NA250Y NO
NOTE
: I. the INSERT CALL SHOULD APPEAR BEFORE ANY COMPONENTS PARAGRAPH
COMPONENTS *2 H 2 0 /
S3 NAOH A* NACL/%5
NAY NAY/ H3 03- OH-/ CLDATABANKS agueous/solids
CHEMISTRY CAUST
DISS %Y
NAY
1/ CL-
1
DISS %5 STOIC
NAY *3
2/ SOY-2 1
-1/ *2
2/
NA2S0Y/ CL-/ SOY-2 SOY-2
NAY 1/ HS03- 1
SL 104530
ASPEN PLUS
VER: IBM-CMS
Rl: B,1
INST: RSC5LKC
U DCM R EAC T 3ft BOTTOMS STRIPPER
INPUT SECTION
INPUT PILETS) (CONTINUED)
1C/26/89 pace
K-STOIC 1
1*2.30457 -1309,2795 -22.6825C9
PROPERTIES^VSQPl 5M 41 CHEM ISTRY = CAUST TRUE--CQMPS=46
; \3 -45 PROP-DATA
IN-UNITS sr
prop-list
PPUAL (NAT
PP UAL (NAT
PARAMETERS
H503-) (N A 7 SC 4-2 ) (NAT
S04-2I H533-I
GMELCC / GMELCD 2.L78676 / 84,29958 1* 168341 / 254.2* 15
: %3 -44
PARAMETERS
PROP-DATA
IN-UNITS SI
PROP-LIST
PPUAL (NAT M5Q3-) (NAT CL-)
PPUal (NAT CL - I (NAT rt 03-)
PPUAL S3
(NAT CL-)
PPUAL (NAT CL-I 43
GMELCC / CMELCD 0,3870701 / 326.3831 1.254995 /-525.4S5C
8 /n
2.096531 /-798.8S23
; 4* -ns PROP-DATA
parameters
IN-UNITS SI
PRQP-L1ST
GMELCC
/ GMELCD
/ GMELCE
PPUAL (NAT CL-) (NAT 504-2) 4,6984*1 / -969.465* / -1,891692
PPUAL (NAT S04-2) (NAT CL-) 0.3988628/ -278,8614 / -5.102501
; 45
-42 PARAMETERS
PROP-DATA
IN-UNITS 51
PROP-LIST
GMELCC
/ GMELCD
/
PPUAL 42 (NAT 504-2)
1.954500 / 1762.185 /
PPUAL INaT S04-2) 42 -2.033257 / -537.9684/
PROP-LIST UlCLR
BPUAL NAT SOa-2 3,86755270-2 0,1232671
GMELCE
7.552416 0.30691975
i 44 -42 PARAMETERS
PROP-DATA
IN-UNITS SI
PROP-LIST
GMELCC
/ GMELCD
/ GMELCE
PPUAL 42 (NAT CL-) 7,4586*9 / 430.0047 / -4,74*332
PPUAL (NAT CL-) 42
-4,334809 / -64.71828 / 3.4816IJ
PROP-LIST ULCLR
BPUAL NAT CL- G,1514218D--1 0,25287180-1
; 43 -42 PARAMETERS
FROP-DATA
IN-UNITS SI
PROP-LIST
GMELCC
/ GMELCD
/ GMELCE
PPUAL 42__ (NAT H503-) 2.1847974 / 2174.7390 / -3,0338148
SL 104531
ASPEN PLUS
yes: ibm-cms
sel: a,i
Inst: rscslkc
UDCM REACTOR BOTTOMS STRIPPER
INPUT SECTION
13/26/89 PAGE
INPUT FIlE(S) (CONTINUED)
PPUAL (NA+ H5Q3-) 62 -2.61*T815 / -579,26512/
PROP--LI ST-
GAEL C A / GMELCB
BP V A L 63 62
-0.7102*51 1 / -9.8710125D2
BPUAL 62 63
-9.999999 / 65.73599AD2
PROP-LIST
ULCLK
BPUAL NAT H503- j,26727988E-01 G,*B**1*66E-C1
*,S5*02C*
; pure component property constants for 63
PROP-DATA
IN-UNITS SI
PROP-LIST IRiR
/ TC
/PC
/ UC
PUAL 63 39,997 / 2920,3
/ 2.533107 / ,2
i QHFORM REGRESSEO TO INCLUDE DhuLWT
PROP-LIST
OHFORM
/ DCF OR M
PUAL 63
-C,*175*96*09 / -2,uC*6D8
PROP-LIST
DHULWT
PUAL 63 PROP-LIST
298,1 5 PLXANT
PUAL 63
-*J
/ ZC
/ RKTZRA
/ .2 20 / -`. 1 *2 9891 1
: pure component property constants for nat
PROP-DATA
IN-UNITS SI
PROP-LIST C PAQO
PUAL NAT
*6, *03
PROP-LIST RADIUS
PUAL NAT . 9 5 D -1 C*
i 3 j 0 Q 1 D CO
; PURE COMPONENT PROPERTY CONSTANTS FOR CL-
PROP-DATA
IN-UNITS SI
PROP-LIST RADIUS
PUAL CL-
i.eiD-i:
I PURE COMPONENT PROPERTY CONSTANTS FOR SO*- 2
PROP-DATA IN-UNITS SI PROP-LIST RADIUS PUAL SO*--2 3D--10
i PURE COMPONENT PROPERTY CONSTANTS FOR H503 " t
__ i
A COMPLEX WITH FORMULA OH-,262
PROP-DATA IN-UNITS SI
PROP--L I_ST
_ MU
/ CHARGE
SL 104532
aspen plus
uer:
ibm-cms VDCM
rel: a.i
Inst: rscslkc
REACTOR bottoms stripper
flowsheet section
FLOWSHEET CONNECTIVITY BY STREAMS
1C/26/89 PAGE
8
STREAM STEAM1
UAPOR1
SOURCE
DEST
---------
' VDCSTRIP
UDCSTRIP
----
FLOWSHfcET CONNECTIVITY BY BLOCKS
STREAM FEEDJ
LISUIOl
SOURCE ----
UOCSTRIP
OEST VDCSTRIP
block
UOCSTRIP
inlets
FEEDl STEAM1
COMPUTATIONAL SEQUENCE
outlets
VAPOR 1 LI3UID1
SEQUENCE USED MAS: VDCSTRIP
OVERALL FLOWSHEET BALANCE
* * * MASS AND ENERGY BALANCE # *
IN OUT
conventional components (LBMQL/HR)
H2Q
1603.36
1603,36
N AO H NACL OHNat
CLPER N a2 SQO H503-
7,63035 LOB.922 i. . }03030Et00
v.:03300E+00 3.33C 3C0E + 30
v.026513E-02 3.333303E+00 0.333300E+00
7.6OO0S 136.922
0.C OOOCIEf OC 0, COC.SOCEtOC 0. C-OOOCGEtOC 3. 026S13E-02 0. OOOOCOE-fOO 0. 30 OOOOE TOO
500-2 TOTAL BALANCE
3.3 3C030E+00
0. 3C OOOOE tOO
mole(lbmol/hri
1759.89
1759,89
massIlb/hr
i
36275.6
36275,6
ENTHALPY(BTU/hR )
-0,216792ETG9
-0.216793ET09
RELATIVE DIPF.
3.933925E-15 0.271568E-1O C , 273980E-10 0 , ">OOOCOETGO L.JV33COE+CC 3.3,,C OOCET30 -C , 068066E-13
c,oo*oooe+eo
13 .vCNOOCETOO C .OOuOOOEtOO
O, 1C658SE-10 0.U2923E-1O C.19310SE-3S
104534 sb
ASPEN PLUS COMPONENTS
UER: IBM-CM5
REL: 3.1
INST: RSCSLFC
UDCN REACTOR flOTTONS STRIPPER
PHYSICAL PROPERTIES SECTION
ID H
naqh
NACL OhNA + CL-
PR NA2S04
H503so*-a
TYPE c c c c c c c c c c
FORMULA H20 NAOH
N ACL OHNA + CLC2CL4 NA2504
OHS04-2
NAME OR ALIAS \ M20
NAOH
nacl
OH-
NA 4 CLC2CL4 NA2504 Oh504-2
13/i6/89 PAG*
9
REPORT NAME H20
NAQH
nacl
OHNA4
CLPER NA 2 S0 4
H 5 0 3SQ4-2
SL 104535
ASPEN PLUS
VER: IBM-CMS
REL: 8.1
INST: RSCSLKC
VOCM REACTOR BOTTOMS STRIPPER
U-O-S BLOCK SECTION
13/26/89 PAGE
1C
BLOCK: VDCSTRIP MODEL: RADFRAC
INLETS
- FEEDS
STAGE
1
STEANJL STAGE
2
OUTLETS - UAPQR1
STAGE
1
LIQUID1 stage
2
PROPERTY OPTION SET:
SYS0P15M
CHEMISTRY ID:
CAUST
APPARENT
FREE WATER OPTION SET! SYS0P12
SOLUBLE WATER OPTION: ORGANIC OPTION SET
components
*** MASS AND ENERGY balance ***
IN OUT
CONUENTIONAL COMPONENTS (LBM0L/MR)
h 20
1643.36
1643.36
naom
NaCL OH-
7.60435 108.922
ooodo oetco
7,6L435 108,922 0 .00C0CCE+03
NA + CL-
w, 330JOOE4S3 0.333O3OE TO G
0OCOOCC E400
c.ooococe+cc
PER NA2S04
0.426513E-02 0 3 3COE+ 0 3
0.426513E-32 3,00000 3 E 40 3
HS03-
O.OCOOOOE+OO
O.OOCOGCETOw
S04-2
-. 0 0 3 3 3 3 E + 0 0
COOOOOCE+CO
TOTAL BALANCE
MOLE(LBMOL/HR)
1759.89
1759.69
MASSILB/MR
)
3o275,6
36275,6
ENTHALPY(BTU/HR )
-0.216792E409
-0.216793E409
RELATIVE DIFF.
. .9339255-15 : .271568E-14
^ , 273984E-14 - . 'C * UC GE4-C0 3 , JOOJOCETOO l.SOCOCOETOO -0,48a'66E-13 C.2::c-3EY3; 3 , C0: 3335+30
J.^.J-IOCOE + OO
0, lf658SE-l 4 0.112823E--14 C.193145E-CS
Kir********************
**** INPUT OATA **** **********************
input parameters
****
NUMBER OF STAGES ALGORITHM OPTION ADSORBER OPTION INITIALIZATION OPTION INSIDE LOOP CONVERGENCE METHOD MAXIMUM NO. OF OUTSIDE LOOP ITERATIONS MAXIMUM NO. OF INSIOE LOOP ITERATIONS MAXIMUM NUMBER OF FLASH ITERATIONS FLASH TOLERANCE
OUTSIDE LOOP CONVERGENCE TOLERANCE
STANDARD NO STANOARD
BROYDEN 25 10 50
G.OOCtCOJCO C 0 OI 0 3 0 0 )
SL 104536
aspen plus
VER: I3M-CMS
pel: 9.1
INST: RSCSLKC
VDCM REACTOR BOTTOMS STRIPPER
U-Q-S 3LOCK SECTION
SLOCK: VDCSTRIP MODEL: RADFRAC (CONTINUED)
1C/26/8R
*+*+ COL-SPECS
****
MOLAR VAPOR DIST / TOTAL dist CONDENSER DUTY (W/O SU3CGJL) RcdOILER DUTY
6TU/MR OTU/HR
1 .J 0 CC C c.c
**** PROFILES
****
P-SPEC
STAGE
1 PRES, PSt 2
21.7000 2*.7GCG
TEMP-EST
STAGE I TEMP, F
24.,C OO
PAGE
**** RESULTS ****
TOP STmGE temperature
BOTTOM STAGE TEMPERATURE
TOP STAGE LIQUID FLOW BOTTOM STAGE LIQUID PLOW TOP STAGE VAPOR FLOW BOTTOM STAGE VhPOR FLOW
CONDENSER DUTY (w/0 SJBCOOL) RE30ILER DUTY
F
F lbmol/hr LBMOL/HR LBMOL/HR LBMOL/HR
BTU/HR BTU/HR
246.C 35
246,373 1,709.37 1 ,710.34
49,0422
49.5690 0.0
0.0
****
manipulated variables
****
FEED FLOW FOR STREAM STEAMl
LBMQL/HR
****
DESIGN SPECIFICATIONS ****
NO SPEC-TYPE 1 MASS-RATIO
UNIT
SPECIFIED VALUE ..251D;i-01
50.5464
CALCULATED VALUE
ABS. ERROR
0 25 000 E --01
-0,*4769E-0
****
MAXIMUM FINAL RELATIVE ERRORS
****
BUBBLE POINT COMPONENT MASS BALANCE ENERGY BALANCE
0,158166-03 0.A 97 77 E--10 0,29725 E --03
STAGES STAGE = STAGES
1 2 COMPsPER 1
1045^
SV
ASPEN PLUS
UER: IBM-CMS
REL! B.l
INST! RSCSLKC
UDCM REACTOR BOTTOMS STRIPPER
U-O-S BLOCK SECTION
block: udcstrip model: radfrac (continued)
PROFILES
10/26/09 PAGE
12
stage TCHPE* AT(j* f
PRESSURE PSI
enthalpy
BTU/LBMOL
LIQUID
UAPOR
HEAT DUTY BTU/hk
1 Z46 c 3 z 248,37
2 3.7.1: 24,70?
-7. 12382EF06 -0.1 "259EAT6 -i,12378EA06 -0,1D258EAQ6
stage
FLOW RATE
LBMOL/HR
liquid
1 17 l u ,
uapor
*?,;*
2 1711 ,
A9.57
liquid
FEED RATE lbmol/hr
uapor
mixed
1709,3383 SC,SABA
PRODUCT RATE LBMOL/HR
liquid
uapor
A9.CA22
1710,3AA9
STAGE 1
a
H20
,93 1 35 .93109
STAGE
1 2
H20 *99991 1 i v1 C 3 C
STAGE 1
Z
H20 i,:729
1 73 1
* ir * *
X-PRQFILE
NAOH 4*p472E-^2
N A CL ,63702E-C1
.63665E-C1
* * **
Y-PROFILE
NAOH
N ACL
, J " >; GC E 4 Z 1/ .00jjOEAOO
..uOGOE + OQ . QD3DOEOO
***
K-UALUES
NAOH 3 6 5 3 "25
NACL jocoE+oo
,37C:1E-2S . D53SOEAOO
* + ** PER .11262E-06 , 4859C E-98
It It it it PER 867995*34 ,37171E-G 5
it It It it PER 769,C9 7 6 A , 91
A***
STAGE =
***#
TEMP = 2 A 6,0 3
PRES i 23,700
PSI
DUTY = 0.0000 OE + OC BTU/HR
MIXED UAPOR LIQUID
H20 NAOH N AC L PER
enthalpy
BTU/LBMOL
flow rate
L3M0L/HR
FEED RATE LBMOL/HR
PRODUCT RATE LBMOL/HR
-0,10259EAC6 -0.12382ETJ6
AS,';a2 1709,9
1709,3388
A9.0A22
X Y K-UALUE5
0,93135 0,A4A72E-02
U,63702E-wl 0,1 1 262E-06
0,99991
0.OOOOOEASO
0,OOODOETOO 0.86799E-0A
1.0729
0.36S30E-2S 0,0 OOOOETOO
769,09
SL 104538
ASPEN PLUS
UER: IBrf-CMS
pel: S.l
INST: RSCSLKC
UDCM REACTOR BOTTOMS STRIPPER
U-O-5 BLOCK SECTION
10/26/89 PACE
13
SLOCK: UDCSTRIP MODEL: RADFRAC (CONTINUED)
****
STAGE :
J
****
TEMP i 2*3.37 F PRES = 24,700 PSI
DUTY = C.OOOCOE+OO BTU/mR
mixed
UAPQR LIQUID
M20 NAOM nacl ER
enthalpy
STU/L3M0L
flow rate
LBHOL/HR
FEED RATE lbmql/hr
PRODUCT RATE l a mol/hr
-0,1 j258E*06 "0.12379E+:6
*9* 5&9 1710.3
50.5484
1710,84*9
X V K-OALUES
'.93189
3,*4**8E-02 *,63o65E-jI U.48590E -33
1.CJ30
0.GU33CE403 0.:0000 + 00
, 3 7 1 7 1 E-C5
1.0731
3.37001E-25 0,DC 300E*00 764.91
SL 104539
-*o n w rtM 3 i-(M a i> c > o r
6SN PLUS
VER: IBM-C1S
RL : 8.1
INST: RSCSLKC
VOCM REACTOR 30TT0M5 STRIPPER
U-O-S BLOCK SECTION
1 0 f, , ? 4- -
i +
i 9. . . + -
I
*
I I Q , t O w 4* -
i i +
* LIGHT KEY / HEAVY KEY fr*#**lt*1
10/26/39 RAC'
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1
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- +--------------
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1.400
i.6:
TRAY NUMBER
***************************
*****a**: ***co**m*p*o*n*e*n*t****h*2*0*****
1 .SCO
" + '
2.000
^045^0
ASPEN PLUS
UER : IBN-CMS
REL: S.l
INST: R SC SLKC
VDCM REACT3R BOTTOMS STRIPPER
STREAM SECTION
MEEDl LIGUID1 STEAMI VAPOR 1
10/26/89 PACE
STREAM id from : TO :
FEED 1 ---VDCSTR IP
L IQUID1 VOCSTRIP --
STEAMI UDCSTRIP
VAPOR 1 VDCSTRIP "" --
SUQSTREAM; HXtO phase: COMPONENTS : LoMDL/Hh,
LI QUID
H20 NA0H
15 . 9:9 V 7#o^40
nacl
PER
1-9.9215 *,2Sl-'3
components: mole FR AC
hi j
NAOH
NACL PER
J ,9316
4,4*95-v 3 3721-j2 2,4952 -- t
components: lb/hr H 20
20694f!" *
NAOH
3 J4, 1 393
NACL
6705 , 7^v,
PER COMPONENTS: MASS FRAC
3,7373
H20 NAOH
-.3114 6 , b v v v .) 3
NACL
w, i6-:-
Pc*
2 . DC 3- js
total flom:
LBMOL/HR ls/hr CuFT/HR
STATE VARIABLES:
1 7 ,, 9 . J 3 8 B
3 . 6 16 5 + '* + 525,1016
TEMP
F
245.9432
PRES
PSI
23,7 >00
VFRAC
Lr RAC SFR AC
-1 * ' lH, . ' : o o
enthalpy: BTU/L3M0L
-1 .2382 + 05
STU/LB
-59d+,7163
BTU/HR
-2,1165+08
entropy:
BTU/LfiMQL-R
"34,t 804
BTU/LB-R
-1,6521
density:
LBMOL/CUFT
3.2553
LB/CUFT
67,3+89
AVG MM
20.6893
LIQUID
1594,3194 7,60+0
108.9215 3,3129-Cb
1.9319 +.4*46-03 6.3665-02 * . 359(1-09
VAPOR
5C , 5464 0* J
- -
1 . jO.jH n,D 0.0 0.0
2.9722+?+
30+,1390 6365,7CC? 1.3786-03
910.6269
:.t u .0 C,v
0.8115
l.OCOO
3.5936-03
0.0
, 6739H-oS>'
0.0 C.o
n--J
1710,8 + + 9
50.5+8+
3,5392+0*
910,6299
526.1606 2666.72+9
2+3.3731
2*.7000
0.0 1.occo 0,0
350.0000 16+.7000
1,OCUG 0,0 0,0
-1 .2378 + 05 -1.0X7++0S
-5983.+033 -56+7.5977 -2.U76 + C9 -5.1+29+06
-34,1234 *1.6495
-12.0539 -0.6691
3.2516
67,2637 20.6866
1,8955-02
0.3+15 18.0150
VAPOR
49,0390 2,34C3-26
:,: 4,2569-33
v .999? 4,772^-23
d. 67 99-C 5
983,4191 9,3606-25
- : , 70 5 9
D . 9992 1 ,J587-27
C .0 7,9844-04
+9.5+22 38*.125C 1.5671+0 +
2+6,03+9 23.7000 i,cc:v 3 ,u 0,0
-1.C259+05 -5690,52+1 -5.031l+u6
-9,3335 -0,5177
3.1295-03 5,6+17-C2
18.0278
SL 104541
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2277 27
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SL 104542
*#* # * * ** *
END END END
33CS314a RSCS3148
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