1. FEED-HT
PFR
NA-HEAT
COOL
RF-1
RF-2
RF-3
RF-4
RF-5
HX-DIK
C1-2
C2-3
C3-4
HX-IPA
COOL3-4
HX-ETH
HX-KET
HX-METH
HX-CO
VALAVE COL-6
25
1.62
8000
FEED
762
1.62
11781
PFR-IN
757
1.62
11781
PFR-OUT877
0.95
20000
NA-OUT
877
0.95
20000
NAIN
75
1.62
11781TO-COL1
109
1.62
87
DIK-OUT
25
1.62
87
DIKETENE
50
1.62
11694DIST1
126
5.00
11694
TO-COL2
64
5.00
9376DIST2 148
15.00
9376TO-COL3
120
5.00
2319
IPA-OUT
25
1.62
2319
IPA
-1
15.00
5595
DIST3
164
15.00
3781ACETONE
119
60.00
5595C3-4OUT
0
60.00
5595TOCOL4
-81
60.00
1948
DIST4
-123
60.00
894
CO-OUT
25
1.62
894
CO
-73
60.00
1054
METH-OUT
25
1.62
1054
METHANE
55
60.00
3646
BTMS4
25
60.00
941
ETH-OUT
25
1.62
941
ETHYLENE
100
60.00
2706
KET-OUT
25
1.62
2706
KETENE
71
1.62
3781RECYLCE
Temperature (C)
Pressure (bar)
Mass Flow Rate (kg/hr)
Fig: Base Model- started our journey.

2. RF-6
RF-4
RF-5RF-3
RF2
RF1
HX-ACE
HX-IPA
HX-KET
HX-DIK
HX-SC6
HX-ETH
HX-METH
HX-CO
C2-3
HX-SC4
COOL
NA-HEAT
PFRFEED-HT
PRE-HT
55
60.00
3314.56
TO-RF-6
13
10.00
2454.99
KET-OUT
-52
10.00
859.57
ETH-OUT
-82
60.00
1837.32
DIST3
-164
10.00
865.58
CO-OUT
-124
10.00
971.73
METH-OUT
50
1.62
2772.85
TO-SC6
71
1.62
973.82
ACE-OUT94
1.62
1799.03
IPA-OUT
25
1.62
2848.13
TO-SC4
142
1.62
75.28
DIK-OUT
86
1.62
2772.85
DIST2
241
60.00
5151.87
TO-COL3
75
1.62
8000.00
TO-COL1
-62
1.62
5151.87
DIST1
80
1.62
2848.13
BTMS1
25
1.62
973.82
ACETONE 25
1.62
1799.03
IPA
25
1.62
2454.99
KETENE
25
1.62
75.28
DIKETENE
25
1.62
859.57
ETHYLENE
25
1.62
971.73
METHANE
25
1.62
865.58
CO
784
1.62
8000.00
PFR-OUT
883
1.01
20000.00
883
1.01
20000.00NAIN
761
1.62
8000.00
PFR-IN
25
1.62
8000.00
FEED
S1
582
1.62
8000.00S2
Temperature (C)
Pressure (bar)
Mass Flow Rate (kg/hr)
Fig: Final Flow diagram of project design.