T-101
T-102
E-101
R-101
P-101 A/B
E-102
R-102
C-103
Refinery
Steam
Cracker
Cooler
1
Reactor
1
Pump
Heater
1
Reactor
2
Compressor Heater Reactor 3 Cooler
2
3
2
C-101
C-102
E-103
R-102
Reactor
2
C-103
E-103
Compressor Heater
R-103
E-104
Reactor 3 Cooler
2
E-102
Heater
1
C-104
V-101
Expander 3-Phase
Separator
T-103
Distillation
Column 1
E-104
C-105
V-101
C-104
Compressor
4
T-104
Expander 3-Phase
Separator
T-103
C-105
Compressor
4
T-104
Distillation
Column 2
6
2
R-101
P-101 A/B
Reactor Pump
1
2
C-102
Compressor
3
T-102
E-101
Steam
Cooler
Cracker
C-101
Compressor
1
1
T-101
Refinery
R-103
Propylene
Methane
Ethylene
Hydrogen
21
T-102
5
E-102
cw
9
7
C-102
14
E-103
bfw
Water
V-101
Ethylbenzene (v)
Styrene (v)
27
R-101
R-102
R-103
16
Steam
Benzene
Toluene
24
cw
10
E-101
17
C-101
Benzene
13
T-103
22
20
25
26
T-104
11
C-104
C-105
18
2
12
15
19
28
E-104
P-101 A/B
C-103
23
Betadine
Kerosene
Diesel
I
3
4
Fuel oil
Lubricating oil
C-104
Expander
2
R-103
E-104
Reactor 3 Cooler
3
R-102
C-103
E-103
Reactor Compressor Heater
2
2
1
P-101 A/B E-102
Pump
Heater
1
21
E-102
cw
9
14
E-103
bfw
Water
24
C-102
7
5
17
cw
C-105
Compressor
T-104
Distillation
Column 2
Distillation
Column 1
V-101
10
R-101
R-102
27
E-101
V-101
3-Phase
Separator
T-103
Distillation
Column 1
Propylene
Ethylene
Methane
Hydrogen
Benzene
Toluene
6
1
2
R-101
Reactor
1
T-102
C-101
Ethylbenzene (I)
Styrene (I)
Water (v)
cw
8
T-102
E-101
Steam
Cooler
Cracker
C-101
C-102
Compressor Compressor
4
T-101
Crude Oil
T-101
Refinery
R-103
Steam
Ethylbenzene (v)
Styrene (v)
T-103
22
Benzene
16
20
11
13
T-104
2
C-104
15
25
26
C-105
18
12
C-103
Compressor
1
28
cw E-104
8
T-101
Ethylbenzene (I)
Styrene (I)
Water (v)
Betadine
3
Kerosene
Diesel
4
I
23
19
P-101 A/B
Crude Oil
Fuel oil
Lubricating oil
Compressor
2
Propylene
6
T-102
Ethylene
Methane
Hydrogen
21
C-102
C-101
E-103
bfw
E-102
cw
7
9
5
Water
14
V-101
10
Benzene
22
T-103
20
16
13
T-104
11
25
C-104
2
26
C-105
18
15
12
19
P-101 A/B
Crude Oil
C-103
T-101
28
E-104
Betadine
8
Kerosene
Diesel
3
Fuel oil
Lubricating oil
4
GENERAL NOTES
PROCESS FLOW DIAGRAM IS NOT DRAWN TO SCALE
PLEASE REFER ADDITIONAL DOCUMENTATION FOR INFORMATION NOT LISTED HERE
BASIC CONTROL LOOP IS INCLUDED AFTER REVISION 1
PROJECT NAME & PROJCT NUMBER
STYRENE PRODUCTION PLANT (PROJ-HMSAY-012)
DRAWING TITLE
Ethylbenzene (I)
Styrene (I)
Water (v)
23
cw
I
1.
2.
3.
Ethylbenzene (v)
Styrene (v)
27
R-103
R-102
R-101
Steam
Benzene
Toluene
24
17
cw
E-101
Distillation
Column 2
CLIENT NAME AND ADDRESS
FIRM NAME
JOHNSON MATTHEY SDN BHD
PT 3349, JALAN PERMATA 1/2, ARAB- MALAYSIAN
INDUSTRIAL PARK, 71800 NILAI, NEGERI SEMBILAN.
PHONE NO:+603-2214133. FAX NO: +603-2214122.
johnson.matthey@corp.com
BASF (M) SDN BHD
POWERHOUSE, LOT 19.02, LEVEL 19, 1, NO. 1,
PERSIARAN BANDAR UTAMA, BANDAR UTAMA, 47800
PETALING JAYA, SELANGOR
03-7612 1888 MARILYN.LEE@BASF.COM
PROJECT NO
AO-HJ0220
SCALE
1:1
SHEET NO
1 OF 1
DRAWING NO
ECH3708-01
REVISION
SHEET
A4
N
DATE
PROCESS FLOW DIAGRAM OF ISOTHERMAL DEHYDROGENATION OF STYRENE
DRAWN BY
HAQEEM
25/3/2024
CHECKED BY
KAH YAN
27/3/2024
APPROVED BY
DR.MOHAMAD REZI
28/3/2024
ISSUED
31/3/2024
REV 01
25/3/24
REV 02
26/3/24
W
E
S