Page 71 - Process simulation and control using Aspen

64 PROCESS SIMULATION AND CONTROL USING ASPEN

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' lup I , IT _ LiiE| | |a|
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Mto SlAtM | Salami | HealEKclwgeij | Cokfwx naactan | pienueChange!i | Manpiaton | 5cM« [ UmModeb |
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STREAMS 1 BSinc BEoii HGMis RCSTB BPItg RBaM.
\ s FoWen JJswn Ru» H 1 HUM lfloAi Atfahie
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FIGURE 2.15

Viewing input summary
For input information, press Ctrl + Alt + I on the keyboard or select Input Summary
from the View pulldown menu (see Figure 2.16).

CBSES
Fie £* Forw* >Atw
input Sugary created by Aspen Plus K«1. 11.1 at 12:U:CM Thu jul 5, 300?
Oirecrory C: Proqr-5R Pi les'AspenTech .norfcing Pol ders'.Aspen Plus 11.1 Fllep e Ci Users-.akjana.AppMtaMocal Terep -ape906.tK}
'
.
title 'SlmUllon of the fiStolc Reactor"
IN-UNITS KET VOLU> E-FLOS<- cuB hr ENTM*LPV-Fl.O-'*»lkcal/hr' A
"
'
HCAT-TRAHS-C- kcal/hr-sqn-K" PRESSURE"bar TEMPERATURE-C &
'
VOLUHE-CUIT OELTA-T-C HEAD-neter httLE-DENSin'- fcisol/cuni' &
'
fASS-DENSITV- kg.'CUH" W)LE-£NTHALP- kcal,'noV t,
'
'
t-ASS-EWTM .P- kcal/kg' HE*T-MMkcal t'OLE-CONC-'mol . T &
POBOP-bar
OCF-STREAt'S COMVEN AIL
DESCRIPTIOH "
General SlHllailoi) mith Metric units :
C, bar, kg/hr, knclhr. MMKcal/hr, c\m/hr.
property Method: Mone
Flow basis for Input: Kole
Stream report cooposltlon: Kole flow
ROP-SOURCES PUBEll - AQUEOUS / SOLIDS f INORGANIC
COMPONENTS
ETHYL-01 C8H10-4 /
STVRENE C8H8 ,'
HVOiOGEN H2
f
PBOPERTIFS PENG-ROB
5THCAH F
SUBSTBEAf KIXEO TCHP-J60. PRE5-1.S MOLE-FLOW-100.
W>LE-FMC ETHYL-01 1.
t
t
B i I vjnwi-* |- la»«Jol | lo.»,-s || -WEME1 :« jpCitU
t
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FIGURE 2.16