Lab Report Aspen Hysis UiTM
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Transcript of Lab Report Aspen Hysis UiTM
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1.0 PROCEDURE
1. The software, Aspen Hysys V8.6 was clicked and opened2. The File button was clicked on to select the ew !ase for the process.
". The !o#ponent $ist button was clicked to add the co#ponents as per instruct in the
%uestion.
!o#ponents
1 Hydrochloric Acid. H!l
2 &thylene
" &thyl !hloride
' itro(en
Fi(ure 1 ) *roperty *acka(e +indow
'. The Fluid *acka(es button was clicked to choose the desired Ther#odyna#ic #odel
in the fluid packa(e which is Adanced *en(-obinson.
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Fi(ure 2 ) Fluid *acka(e
/. Then, the reaction button was clicked to add the reaction which is the conersion.
Fi(ure " ) eaction6. &thylene was set as a base co#ponent with the conersion 0. The stoichio#etric
coefficients for each co#ponent was also added.
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Fi(ure ' ) eaction +indow
3. 4i#ulation was clicked to insert all the unit operations inoled in the reaction by
usin( the *alette bo5.
8. The #i5er icon was dra((ed fro# the palette bo5 to the worksheet. The inlet strea#
of the #i5er was na#ed as 4trea# 1 while the outlet strea# was na#ed as 4trea# 2.
Fi(ure / ) i5er
0. The #i5er icon was double-clicked to insert the properties of each co#ponents below.
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!o#ponents !o#positions
Hydrochloric Acid. H!l ./
&thylene .'8
&thyl !hloride .
itro(en .2
Fi(ure 6 ) i5er7s !o#positions
1. The followin( infor#ation were also included )
*ressure 1 at#
Te#perature 2/o!
Flow rate 1 k(#olh
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Fi(ure 3 ) i5er7s !onditions
11. !onersion reactor was added to the worksheet by dra((in( its icon fro# the palette
bo5. The strea# in for the reactor is 4trea# 2 while its apor outlet strea# was
known as 4trea# " and li%uid outlet strea# was 4trea# '.
Fi(ure 8 ) !onersion eactor12. The te#perature for the reactor re#ain constant because it is an isother#al reaction.
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Fi(ure 0 ) eactor7s !onditions
1". 4plitter was added. The inlet strea# for the splitter was strea# " while the oerhead
outlet known as 4trea# /,the botto# outlet is known as 4trea# 6.
Fi(ure 1 ) 4plitter
1'. Then, the T&& icon was dra((ed to the worksheet fro# the palette bo5 as a 9unction
for the pur(e strea#. The inlet strea# was 4trea# / while the outlet strea# was
chan(ed to 4trea# 3 and 4trea# 8.
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Fi(ure 11 ) *ur(e 4trea#
1/. Then the T&& icon was double-clicked to add the properties needed )
*ressure 1 at#
Te#perature 2/o!
Flow rate at strea# 3 1 k(#olh
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Fi(ure 12 ) !ondition for *ur(e
16. ecycle icon was dra((ed fro# the palette bo5 to the worksheet. The inlet for the
recycle strea# is 4trea# 8 and its outlet was known as 4trea# 0. The pressure was
contant at 1 at# and the te#perature at 2/!.
Fi(ure 1" ) ecycle 4trea#
13. :utlet of the recycle strea# which was 4trea# 0 was connected back to the #i5er.
2.0 PROCESS FLOW DIAGRAM ( PFD )
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3.0 WORKBOOKS
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4.0 QUESTIONS AND DISCUSSION
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1. Wha a!" h" #$%" &!a'$* &$! "a'h '$#+$" a h" "&&%," $& h"
!"a'$!-
Hydrochloric Acid ./2
&thylene ."2
&thyl !hloride .
itro(en .1030
2. Wha * h" &%$ !a" $& h" !"'/'%" *!"a#-
olar flow rate ;k#olh< 6.///
ass flow rate ;k(.h< 211.'
$i%uid olu#e flow ;barrelday< '0.'1
3. Wha * h" &%$ !a" $& h" &a% +!$,' a&"! !"'/'%-
The ob9ectie of this e5peri#ent is to install and coner(e a conersion reactor and to si#ulate a
process inolin( recycle. =y usin( Hysys software, all the ob9ecties were obsered. All the
e%uip#ent in the process is carried in isother#al and isobaric process. The te#perature is at 2/
! while the pressure is 1 at#.