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Amonia


Total equipment of pabrik amonia 1a is
29
⁠
with total detail equipment is
138
⁠
items |
18
⁠
items of detail equipment already build and there are
120
⁠
items need to be build in 3D model.
Total interaction in working interactions is
3021
⁠
that consist of
2077
⁠
interaction in startup scenarios,
932
⁠
shutdown scenarios, and
12
⁠
normal operation from Working instruction. The total number of interaction from operating window amonia 1a document is
209
⁠
⁠
A: 3 aset
Total Interactions :
3230
⁠
Interactions (
2077
⁠
startup +
932
⁠
shutdown +
221
⁠
normal operation)
Total Unique Equipment Items :
120
⁠
items
Pabrik 1A Amonia
category
Proses
Equipment
Detail Equipment
3D Done ?
Asset Image
Kesulitan 2
Mandays
A
81
Frontend Process Ammonia
1.1 NG Compressor
NG KO Drum (V-0101)
image.png
1
1
Frontend Process Ammonia
1.1 NG Compressor
NG Compressor Suction Separator (V-0411)
image.png
2
2
Frontend Process Ammonia
1.1 NG Compressor
Fuel NG Preheater (E-0101)
image.png
2
2
Frontend Process Ammonia
1.1 NG Compressor
NG Recycle Cooler (E-0411)
image.png
2
2
Frontend Process Ammonia
1.2 Air Compressor
Air Compresssor First Intercooler (E-0421)
image.png
1
1
Frontend Process Ammonia
1.2 Air Compressor
Air Compresssor Second Intercooler (E-0422)
image.png
1
1
Frontend Process Ammonia
1.2 Air Compressor
Air Compresssor Third Intercooler (E-0423)
image.png
1
1
Frontend Process Ammonia
1.2 Air Compressor
Air Compressor First Separator (V-0421)
image.png
1
1
Frontend Process Ammonia
1.2 Air Compressor
Air Compressor Second Separator (V-0422)
image.png
1
1
Frontend Process Ammonia
1.2 Air Compressor
Air Compressor Third Separator (V-0423)
image.png
1
1
Frontend Process Ammonia
1.3 Desulphurizer
Air Compressor Dry Gas Seal System
1
1
Frontend Process Ammonia
1.3 Desulphurizer
Desul Temp in CV, TV-0209
image.png
1
1
Frontend Process Ammonia
1.4 Process Steam
Line steam to Gas + Control Valve FV-0204/6
image.png
2
2
Frontend Process Ammonia
1.6 Primary Reformer
ID Fan/Fuel Gas Blower (K-0201 A/B)
image.png
3
3
Frontend Process Ammonia
1.6 Primary Reformer
NG Fuel System (CV FV-0215/6 + Line to burner)
image.png
1
1
Frontend Process Ammonia
1.6 Primary Reformer
Fuel off gas System (CV FV-0214 + Line to burner)
image.png
2
2
Frontend Process Ammonia
1.6 Primary Reformer
Feed Gas & Steam Preheater (E-0201)
image.png
1
1
Frontend Process Ammonia
1.6 Primary Reformer
Process Air Preheater (E-0202 AB)
image.png
1
1
Frontend Process Ammonia
1.6 Primary Reformer
Steam Superheater (E-0203)
image.png
1
1
Frontend Process Ammonia
1.6 Primary Reformer
NG Preheater (E-0204 ABC)
image.png
1
1
Frontend Process Ammonia
1.6 Primary Reformer
Catalyst tube + lantai top tube
image.png
2
2
Frontend Process Ammonia
1.7 Process Air
Line + CV FV-0209/211/212
image.png
1
1
Frontend Process Ammonia
1.8 Secondary Reformer
Check valve udara to SR
image.png
1
1
Frontend Process Ammonia
1.9 Reformed Gas Waste Heat Boiler
E-0208
image.png
1
1
Frontend Process Ammonia
1.11 CG Steam Superheater (E-0209)
E-0209
image.png
1
1
Frontend Process Ammonia
1.12 Methanator Trim Heater (E-0211)
E-0211
image.png
2
2
Frontend Process Ammonia
1.13 BFW Preheater No. 1 (E-0212)
E-0212 A/B
image.png
2
2
Frontend Process Ammonia
1.16 Startup N2 Circulation System
N2 Blower (K-0203)
image.png
1
1
Frontend Process Ammonia
1.16 Startup N2 Circulation System
Start up N2 Cooler (E-0214)
image.png
1
1
Frontend Process Ammonia
1.16 Startup N2 Circulation System
Start up N2 separatot (V-0202)
image.png
1
1
Frontend Process Ammonia
1.16 Startup N2 Circulation System
Start up N2 Heater (E-0216)
image.png
1
1
Steam System
2.2 Chemical System Deaerator
Hydrazine Injection Z-2501
image.png
2
2
Steam System
2.2 Chemical System Deaerator
ammonia injection (Z-2502)
image.png
1
1
Steam System
2.3 BFW Pump
pump (P-2501 A dan P-2501 B)
image.png
3
3
Steam System
2.4 Steam Drum
HP Steam Drum V-0201
image.png
2
2
Steam System
2.4 Steam Drum
Blowdown Drum (V-0211)
image.png
2
2
Steam System
2.4 Steam Drum
Blowdown Cooler (E-1101)
image.png
1
1
Steam System
2.6 Turbine Condenser
E-0401 + E-0401 P1A/B
image.png
1
1
Middle End Process
3.1 CO2 Removal
MDEA Filter (F-0301)
image.png
2
1
Middle End Process
3.1 CO2 Removal
MDEA Solution Storage Tank (T-0301)
3.1 T-0301 MDEA Solution Storage Tank.jpeg
1
1
Middle End Process
3.1 CO2 Removal
MDEA Solution Sump Tank (T-0303)
3.1 T-0303 MDEA Solution Sump Tank.jpeg
1
1
Middle End Process
3.1 CO2 Removal
CO2 product cooelr (E-0308)
image.png
1
1
Middle End Process
3.1 CO2 Removal
Solution Heat Exchanger (E-0301AB)
image.png
2
2
Middle End Process
3.1 CO2 Removal
Lean Solution Cooler (E-0303)
image.png
1
1
Middle End Process
3.1 CO2 Removal
DFW Preheater No. 1 (E-0304)
image.png
1
1
Middle End Process
3.1 CO2 Removal
DFW Preheater No. 2 (E-0305)
image.png
1
1
Middle End Process
3.1 CO2 Removal
Overhead Condensate Pump (P-0304)
3.1 P-0304 OH Condesate Pump (untuk E-0308).jpeg
2
2
Middle End Process
3.1 CO2 Removal
Process Gas Separator (V-0304)
3.1 V-0304 Process Gas Separator.jpeg
2
2
Middle End Process
3.1 CO2 Removal
MDEA Recycle Separator (V-0306)
image.png
1
1
Middle End Process
3.2 Process Condensate Treatment
Process Condensate Stripper (C-0701)
3.2 C-0701 Process Condensate Stripper.jpeg
2
2
Middle End Process
3.2 Process Condensate Treatment
Process Condensate KO Drum (V-0701)
3.2 V-0701 Process Condensate KO drum.jpeg
2
2
Middle End Process
3.2 Process Condensate Treatment
Process Condensate Exchanger (E-0701 ABC)
3.2 E-0701 ABC Process Condensate Exchanger.jpeg
1
1
Middle End Process
3.2 Process Condensate Treatment
Stripped Condensate Cooler (E-0703)
3.2 E-0703 Stripped Condensate Cooler.jpeg
1
1
Middle End Process
3.3 Methanator
Methanator (R-0301)
3.3 R-0301 Methanator.jpeg
2
2
Middle End Process
3.3 Methanator
Methanator Heat Exchnager (E-0311)
3.3 E-0311 Methanator Heat Exchanger.jpeg
2
2
Middle End Process
3.3 Methanator
Final Cooler (E-0312)
3.3 E-0312 Final Cooler.jpeg
1
1
Middle End Process
3.3 Methanator
Final Gas Separator (V-0311)
3.3 V-0311 Final Gas Separator.jpeg
1
1
Back End Process
4.1 Syngas Compressor
Syngas First Intercooler (E-0431)
4.1 E-0431 Syngas Compressor 1st Intercooler.jpeg
1
1
Back End Process
4.1 Syngas Compressor
Syngas Second Intercooler (E-0432)
4.1 E-0432 Syngas Compressor 2nd Intercooler.jpeg
1
1
Back End Process
4.1 Syngas Compressor
Syngas Aftercooler (E-0433)
4.3 E-0433 Syngas Aftercooler.jpeg
1
1
Back End Process
4.1 Syngas Compressor
Circulator Recycle Cooler (E-0434)
4.1 E-0434 Circulator Recycle Cooler.jpeg
1
1
Back End Process
4.1 Syngas Compressor
Syngas Compressor First Separator (V-0431)
4.1 V-0431 Syngas Compressor 1st Separator.jpeg
1
1
Back End Process
4.1 Syngas Compressor
Syngas Compressor Second Separator (V-0432)
4.1 V-0432 Syngas Compressor 2nd Separator.jpeg
1
1
Back End Process
4.1 Syngas Compressor
Syngas Compressor After Separator (V-0433)
4.1 V-0433 Syngas Compressor After Separator.jpeg
1
1
Back End Process
4.2 Ammonia Synthesis Loop
Start Up Heater (H-0501)
image.png
2
2
Back End Process
4.2 Ammonia Synthesis Loop
Syngas Steam Superheater (E-0500)
4.2 E-0500 SG Steam Superheater.jpeg
1
1
Back End Process
4.2 Ammonia Synthesis Loop
SG Waste Heat Boiler (E-0501)
4.2 E-0501 SG Waste Heat Boiler.jpeg
2
2
Back End Process
4.2 Ammonia Synthesis Loop
SG BFW Preheater (E-0502)
4.2 E-0502 SG BFW Preheater.jpeg
1
1
Back End Process
4.2 Ammonia Synthesis Loop
Water Cooler (E-0504)
4.2 E-0504 Water Cooler.jpeg
1
1
Back End Process
4.2 Ammonia Synthesis Loop
First Cold Exchanger (E-0505)
4.2 E-0505 1st Cold Exchanger.jpeg
2
2
Back End Process
4.2 Ammonia Synthesis Loop
First Ammonia Chiller (E-0506)
4.2 E-0506 1st Ammonia Chiller.jpeg
1
1
Back End Process
4.2 Ammonia Synthesis Loop
Second Cold Exchanger (E-0507)
4.2 E-0507 2nd cold Exchanger.jpeg
1
1
Back End Process
4.2 Ammonia Synthesis Loop
Second Ammonia Chiller (E-0508)
4.2 E-0508 2nd Ammonia Chiller.jpeg
1
1
Back End Process
4.2 Ammonia Synthesis Loop
PG Chiller (E-0514)
4.2 E-0514 PG Chiller.jpeg
2
2
Back End Process
4.3 Refrigerant Compressor
Ammonia Intercooler (E-0441)
4.3 E-0441 Ammonia Intercooler.jpeg
1
1
Back End Process
4.3 Refrigerant Compressor
Ammonia Compressor 2nd Stage KO Drum (V-0442)
4.3 V-0442 Ammonia compressor 2nd stage KO drum.jpeg
1
1
Back End Process
4.3 Refrigerant Compressor
Ammonia Compressort 3rd Stage KO Drum (V-0443)
4.3 V-0443 Ammonia Compressor 3rd Stage KO Drum.jpeg
1
1
Back End Process
4.4 Refrigerant System
Ammonia Condenser (E-0510)
4.4 E-0510 Ammonia Condenser.jpeg
1
1
Back End Process
4.4 Refrigerant System
Inert Gas Chiller (E-0511)
4.4 E-0511 Inert Gas Chiller.jpeg
1
1
Back End Process
4.4 Refrigerant System
Ammonia Product Heater (E-0512)
4.4 E-0512 AB Ammonia Product Heater.jpeg
1
1
Back End Process
4.4 Refrigerant System
Ammonia Accumulator (V-0504)
4.4 V-0504 Ammonia Accumulator.jpeg
1
1
C
13
Frontend Process Ammonia
1.1 NG Compressor
NG Comp Lube Oil System (reservoir, pump, filter, cooler)
2
​
Frontend Process Ammonia
1.2 Air Compressor
Air Compresor turbine (TS-0421)
3
3
Frontend Process Ammonia
1.2 Air Compressor
Air Compressor Lube Oil System (reservoir, pump, filter, cooler)
image.png
3
3
Steam System
2.6 Turbine Condenser
E-2302 + E-2302 P1A/B
image.png
3
3
Middle End Process
3.1 CO2 Removal
Lube oil System P-0301A
image.png
3
3
Middle End Process
3.1 CO2 Removal
Lube oil System P-0301B
image.png
3
3
Middle End Process
3.1 CO2 Removal
Semilean Pump C (P-0301 C + motor)
image.png
3
3
Middle End Process
3.1 CO2 Removal
Lube oil System P-0301C
image.png
3
3
Middle End Process
3.1 CO2 Removal
MDEA Lean pump (P-0302 A dan B)
image.png
3
3
Middle End Process
3.1 CO2 Removal
Hydraulic turbine (TX-0301)
3.1 TX-0301 Hidraulic Turbin for P-0301A.jpeg
3
3
Back End Process
4.1 Syngas Compressor
Syngas Compressor Lube Oil System (reservoir, pump, cooler, filter)
image.png
3
3
Back End Process
4.1 Syngas Compressor
Syngas Compressor Dry Gas Seal System
4.1 Dry Gas Seal for Syngas Compressor HP dan LP.jpeg
3
3
Back End Process
4.3 Refrigerant Compressor
Refrigerant Compressor Dry Gas Seal System
4.3 Drygas Seal Refrigeran Comp HP.jpeg
3
3
B
26
Frontend Process Ammonia
1.1 NG Compressor
NG Comp Dry Gas Seal System
image.png
3
3
Frontend Process Ammonia
1.2 Air Compressor
Air Compressor Suction Filter (F-0421)
image.png
1
1
Frontend Process Ammonia
1.2 Air Compressor
Air Compressor (K-0421)
image.png
1
1
Frontend Process Ammonia
1.5 Process Gas
CV FV-0201, 0201A, 0203
image.png
2
2
Frontend Process Ammonia
1.6 Primary Reformer
E-0205 BFW Preheater
2
2
Frontend Process Ammonia
1.15 BFW Preheater No. 2 (E-0213)
E-0213 A/B
2
2
Steam System
2.1 Deaerator
Deaerator Steam Stripping Line
image.png
2
2
Steam System
2.3 BFW Pump
turbine (TS-2501)
image.png
2
2
Steam System
2.5 Steam Header
Letdown HP to MP (line + CV : PV11021&2)
2
2
Steam System
2.5 Steam Header
MP Steam Vent (PV-11034&2)
2
2
Middle End Process
3.1 CO2 Removal
HP Flash Drum (V-0302)
3.1 V-0302 HP Flash Drum.jpeg
3
3
Middle End Process
3.1 CO2 Removal
Semilean Pump A (P-0301 A + motor + TX)
image.png
2
2
Middle End Process
3.1 CO2 Removal
Semilean Pump B (P-0301 B + TS)
image.png
3
3
Middle End Process
3.1 CO2 Removal
Reboiler (E-0302)
image.png
2
2
Middle End Process
3.1 CO2 Removal
Split stream pump (P-0303 A/B))
image.png
3
3
Middle End Process
3.1 CO2 Removal
Antifoam Injection System (Z-0301)
3.1 Z-0301 Antifoam Injection.jpeg
2
2
Middle End Process
3.1 CO2 Removal
Solution Transfer Pump (P-0305)
image.png
2
2
Middle End Process
3.2 Process Condensate Treatment
Condensate Pump (P-0704 AB)
3.2 P-0704 A&B Condensate Pump.jpeg
1
1
Back End Process
4.2 Ammonia Synthesis Loop
Hot Heat Exchanger (E-0503)
2
2
Back End Process
4.2 Ammonia Synthesis Loop
PG Separator (V-0514)
4.2 V-0514 PG Separator.jpeg
2
2
Back End Process
4.3 Refrigerant Compressor
Refrigerant Compressor (K-0441)
image.png
2
2
Back End Process
4.3 Refrigerant Compressor
Refrigerant Compressor Turbine (TS-0441)
2
2
Back End Process
4.4 Refrigerant System
Inert Gas Separator (V-0505)
4.4 V-0505 Inert Gas Separator.jpeg
2
2
Back End Process
4.4 Refrigerant System
Ammonia Product Pump (P-0501 A/B)
4.4 P-0501 B Ammonia Product Pump B.jpeg
2
2
Back End Process
4.4 Refrigerant System
Let Down Vessel (V-0502)
4.4 V-0502 Let Down Vessel.jpeg
2
2
Steam System
2.1 Deaerator
Deaerator (V-2501)
image.png
1
1
⁠
Total equipment
29
⁠
⁠
Total detail equipment
138
⁠
| detail equipment yang sudah dimodelkan
18
⁠
| detail equipment yang belum dimodelkan
120
⁠
⁠

3 ORANG
A: 81 → 1 orang 27 → 9 hari
B : 26 → 1 orang 8.5 item → 10 hari
C : 13 → 1 orang 4 item → 12 hari
Total : 31 hari
sep okt novemver → pertengahan oktober selesai
List Working Instructions 3
Nama Dokumen
Startup
Shutdown
Normal Operation
Total
WI-AM1A-SMT-OPS-05-007 (BFW SYSTEM _ FILL UP STEAM DRUM)
41
20
​
61
WI-AM1A-SMT-OPS-05-029 (AKTIFKAN STEAM SH SM SML SL HEADER)
99
20
​
119
WI-AM1A-SMT-OPS-05-030 (P-2501 AB BFW PUMP )
85
15
​
100
WI-AM1A-SMT-OPS-05-032 (AKTIFKAN GAS DARI SKG KE V - 0101)
30
0
​
30
WI-AM1A-SMT-OPS-05-033 (KM-0201 AB (ID FAN REFORMER)
18
17
​
35
WI-AM1A-SMT-OPS-05-034 (K-0203 (N2 BLOWER)
19
5
​
24
WI-AM1A-SMT-OPS-05-035 (AKTIFKAN FUEL SYSTEM REFORMER)
20
0
​
20
WI-AM1A-SMT-OPS-05-036 (AKTIFKAN NG COND RECOVERY KE FUEL SYSTEM)
19
0
​
19
WI-AM1A-SMT-OPS-05-037 (HEATING UP REFORMER _ HTS DGN SIRKULASI N2)
69
0
​
69
WI-AM1A-SMT-OPS-05-038 (IMPORT HYDROGEN DARI INTEGRASI)
15
0
​
15
WI-AM1A-SMT-OPS-05-039 (DESULPHURISER R-0201 _ R-0202)
12
0
​
12
WI-AM1A-SMT-OPS-05-040 (REFORMER)
112
0
​
112
WI-AM1A-SMT-OPS-05-041 (MASUKAN _ CABUT UDARA PROSES R-0203)
42
0
​
42
WI-AM1A-SMT-OPS-05-043 (AKTIFKAN _ NON AKTIFKAN LTS)
15
8
​
23
WI-AM1A-SMT-OPS-05-044 (PEMBUATAN DAN SIRKULASI MDEA)
48
0
​
48
WI-AM1A-SMT-OPS-05-045 (P 0302 AB (MDEA LEAN SOLUTION PUMP)
89
59
​
148
WI-AM1A-SMT-OPS-05-046 (P-0301 ABC (MDEA SEMI LEANSOLUTION PUMP)
236
35
​
271
WI-AM1A-SMT-OPS-05-047 (AKTIFKAN _ NON AKTIFKAN TX-0301)
18
6
​
24
WI-AM1A-SMT-OPS-05-049 (P-0303 AB (SPLIT STREAM PUMP)
37
9
​
46
WI-AM1A-SMT-OPS-05-050 (P-0304 AB (O.H CONDENSATE PUMP)
30
8
​
38
WI-AM1A-SMT-OPS-05-051 (PMP-0704 AB (PC PUMP)
35
9
​
44
WI-AM1A-SMT-OPS-05-052 (C-0701 PC STRIPER)
24
59
​
83
WI-AM1A-SMT-OPS-05-053 (EXTRA COOLER E-0308A)
9
0
​
9
WI-AM1A-SMT-OPS-05-054 (MASUKAN GAS KE CO2 REMOVAL)
34
0
​
34
WI-AM1A-SMT-OPS-05-055 (LOADING ANTIFOAM DI CO2 REMOVAL)
18
0
​
18
WI-AM1A-SMT-OPS-05-056 (F-0301 _ F-0302 (MDEA FILTER)
33
33
​
66
WI-AM1A-SMT-OPS-05-057 (EXPORT CO2 KE INTEGRASI)
13
0
​
13
WI-AM1A-SMT-OPS-05-059 (P-0308 (CONDENSATE RECOVERY PUMP)
25
0
​
25
WI-AM1A-SMT-OPS-05-060 (R-0301 (METHANATOR)
18
20
​
38
WI-AM1A-SMT-OPS-05-061 (TS K-0411 ( NG COMP)
77
0
​
77
WI-AM1A-SMT-OPS-05-062 (TSK-0421 (AIR COMP)
21
105
​
126
WI-AM1A-SMT-OPS-05-063 (TSK-0431 (SYN GAS COMP)
191
15
​
206
WI-AM1A-SMT-OPS-05-064 (TSK-0441 (REFRIGERANT COMP)
150
20
​
170
WI-AM1A-SMT-OPS-05-065 (E-0401-P1 AB (CONDENSATE PUMP)
15
0
​
15
WI-AM1A-SMT-OPS-05-066 (K-0421-P1 AB (LUBE OIL PUMP)
60
0
​
60
WI-AM1A-SMT-OPS-05-067 (SWITCHING K-0421-E1 AB)
25
0
​
25
WI-AM1A-SMT-OPS-05-074 (REDUKSI, START _ SHUTDOWN R-0501)
106
25
​
131
WI-AM1A-SMT-OPS-05-076 (AKTIFKAN STEAM SUPERHEATER E-0500)
18
0
​
18
WI-AM1A-SMT-OPS-05-078 (P-0501 AB (NH3 PUMP)
70
0
​
70
WI-AM1A-SMT-OPS-05-081 (REFRIGERANT SYSTEM)
18
0
​
18
WI-AM1A-SMT-OPS-05-083 (PENGENDALIAN OPERASI)
0
0
12
12
WI-AM1A-SMT-OPS-05-094 (SUPLAI GAS FAILURE)
63
0
​
63
WI-AM1A-SMT-OPS-05-095 ( I-81 AKTIF (ARU INTERNAL TRIP)
0
16
​
16
WI-AM1A-SMT-OPS-05-096 ( IS-51 AKTIF (SYNLOOP INTERNAL TRIP)
0
28
​
28
WI-AM1A-SMT-OPS-05-097 ( IS-44 AKTIF (K-0431 TRIP)
0
50
​
50
WI-AM1A-SMT-OPS-05-098 ( IS-45 AKTIF (K-0441 TRIP)
0
34
​
34
WI-AM1A-SMT-OPS-05-099 ( IS-33 AKTIF (METHANATOR R-0301 TRIP)
0
37
​
37
WI-AM1A-SMT-OPS-05-100 ( IS-42 AKTIF (K-0421 TRIP)
0
66
​
66
WI-AM1A-SMT-OPS-05-101 (IS-41 AKTIF (K-0411 TRIP)
0
71
​
71
WI-AM1A-SMT-OPS-05-102 (IS-31 AKTIF (MDEA PUMP TRIP)
0
43
​
43
WI-AM1A-SMT-OPS-05-103 (IS-32 AKTIF (CO2 REMOVAL INTERNAL TRIP)
0
44
​
44
WI-AM1A-SMT-OPS-05-104 (TRIP POMPA BFW P-2501 AB (I-251-1 AB)
0
55
​
55
There are no rows in this table
⁠
Total interaction in working interactions is
3021
⁠
that consist of
2077
⁠
interaction in startup scenarios,
932
⁠
shutdown scenarios, and
12
⁠
normal operation

Operating Window Amonia 1A
Tag No
P & ID
Description
Unit
Low Normal R III
High Normal R III
L (Alarm)
LL (TRIP)
H (ALARM)
HH (TRIP)
Low
High
LC-0101
P1
NG KO Drum Level
%
10
20
5
-
25
-
-
-
PAL-0102
P1
NG KO Drum Outlet
kg/cm²G
23
26
19
15
33
PC-0201
P1
Sulphur Adsorber ( R-0202 ) Outlet NG
kg/cm²G
41,5
42,5
35
-
43,5
46,5
AI-02062
P1
Sulphur Outlet R-0202
ppb
0
50
FC-0201
P2
Feed Gas & Steam Preheater ( E-0201 ) Inlet NG
Nm³/hr
48800
54000
41000
56000
FAL-0201
P2
Feed Gas & Steam Preheater ( E-0201 ) Inlet NG
Nm³/hr
48800
54000
41000
21000
FFI-0201
P2
E-0201 Gas / Air Ratio
Nm³/hr
0,63
0,65
0,58
0,51
FFI-0202
P2
E-0201 Gas / Air Ratio
Nm³/hr
0,63
0,65
0,58
0,51
FC-0204
P2
Feed Gas & Steam Preheater ( E-0201 ) Inlet NG
TPH
132
135
85
FFI-0204
P2
E-0201 Steam / Gas Ratio
kg/cm²G
2,59
2,79
2,1
FAL-0205
P2
Feed Gas & Steam Preheater ( E-0201 )Inlet NG
TPH
132
135
85
63,3
FFI-0205
P2
E-0201 Steam Gas / Air Ratio
kg/cm²G
2,59
2,79
2,1
1,81
FC-0206
P2
E-0201 Inlet SM Bypass
TPH
40
40
36
FC-0207
P2
Feed Gas & Steam Preheater
( E-0201 )Inlet NG
Nm³/hr
2960
2500
FC-0209
P2
PA Preheater - B E-0202 B inlet PA
Nm³/hr
76870
77000
65000
FAL-0210
P2
PA Preheater - B E-0202 B inlet PA
Nm³/hr
76870
77000
65000
38000
PAL-0203
P3
Primary Reformer ( H-0201 ) Inlet FG
kg/cm²G
2,5
2,8
0,1
7
PAH-0205
P3
Primary Reformer ( H-0201 )
mmH2O
-5
-3
3
PC-0206
P3
Primary Reformer ( H-0201 )
mmH2O
-5
-3
-15
0
PC-0212
P3
Primary Reformer ( H-0201 ) Inlet FG
kg/cm²G
5
5
4
6
7
PC-0218
P3
Primary Reformer ( H-0201 ) Inlet Off Gas
kg/cm²G
1,2
1,4
0,2
6,5
7
TI-0208
P2
Steam Preheater ( E-0201 ) Outlet NG
°C
535
535
545
TC-0209
P2
NG Preheater ( E-0204 A ) Outlet NG
°C
400
400
380
420
425
TI-0210
P2
Proces Air Preheater ( E-0202 A ) Outlet PA
°C
540
550
570
580
TC-0212
P2
Steam Superheter ( E-0203 ) Outlet SH
°C
515
517
505
525
530
TI-0252
P3
Primary Reformer ( H-0201 )
°C
970
985
1060
TI-0253
P3
Primary Reformer ( H-0201 )
°C
970
985
1060
TI-0254
P3
Primary Reformer ( H-0201 )
°C
970
985
1060
TI-0255
P3
Primary Reformer ( H-0201 )
°C
760
794
804
Tubes Skin Temperature
°C
888
LC-0201
P4
Steam Drum ( V-0201 ) Level
%
40
50
30
70
LAL-0203
P4
Steam Drum ( V-0201 ) Level
%
40
50
30
10
-
PI-0210
P4
Steam Drum ( V-0201 ) Level
kg/cm²G
116
120
125
133,5
AI-0202
P4
Steam Drum ( V-0201 ) Outlet BD
8,8
9,5
8,5
10
AI-0203
P4
Steam Drum ( V-0201 ) Outlet BD
µs/cm
3
10
Chloride
ppm
3
PH
9,4
9,6
Eliminox
ppb
100
150
Hydrazine
ppb
7
Conductivity
µs/cm
10
LC-0205
P4
Blowdown Drum ( V-0211 ) Level
%
40
50
18,3
51,7
LAH-0221
U3
Start Up N2 Separator ( V-0202 ) Level
%
0
0
75
TI-0257
U3
Start Up N2 Separator ( V-0202 ) Outlet N2
°C
40
50
60
65
-
65
PD-0222
U3
Start Up N2 Blower ( K-0203 ) Suction N2
kg/cm²G
0,8
1
1,1
1,4
TI-0222
P4
RG WHB ( E-028 ) Inlet RG
°C
950
960
612
1000
TAH-0223
P4
RG WHB ( E-028 ) Inlet RG
°C
950
960
612
1000
1010
TC-0224
P4
RG WHB ( E-028 ) Outlet RG
°C
340
350
320
360
410
TI-0232
P5
HT CO Converter ( R-0204 ) Outlet RG
°C
417
417
450
470
TI-0234
P5
CG Steam Superheater ( E-0209 ) Outlet SH
°C
380
380
400
410
TC-0239
P5
BFW Preheater -B ( E-0212-B ) Outlet CG
°C
194
196
170
210
250
TI-0250
P5
LT CO Converter ( R-0205 ) Outlet CG
°C
211
211
185
235
250
PC-0213
P6
BFW Preheater No. 2 ( E-0213A ) Inlet CG
kg/cm²G
32,7
32,7
35,5
37,5
TI-0256
P6
BFW Preheater No. 2 ( E-0213A ) Inlet CG
°C
177
183
165
220
FC-0301
P7A
OH Condensate Pump A/B ( P-0304 A/B ) Discharge MAS
TPH
580
650
500
300
LC-0304
P7A
LP Flash Drum ( V-0301 ) Level
%
35
40
32,8
83,8
LAL-0305
P7A
LP Flash Drum ( V-0301 ) Level
%
35
40
5
LI-0306
P7A
LP Flash Drum ( V-0301 ) Level
%
35
40
5,6
87,7
TI-0305
P7A
LP Flash Drum ( V-0301 ) Outlet CO2
°C
40
43
45
60
FC-0302
P7A
Solution Heat Exchanger-B ( E-0301B ) Inlet MAS
TPH
480
510
345
230
LC-0302
P7A
CO2 Stripper ( C-0301 ) Level
%
60
60
38,9
61,1
LAH-0303
P7A
CO2 Stripper ( C-0301 ) Level
%
60
60
38,9
5,6
61,1
94,4
FI-0303
P7A
BFW Preheater No. 1 ( E-0304 ) Inlet BFW
TPH
330
340
140
120
FC-0304
P9
CO2 Absorber ( C-0302 ) inlet MAS
TPH
427
450
320
220
FC-0306
P9
CO2 Absorber ( C-0302 ) inlet MAS
TPH
2713
2850
2035
1350
LC-0310
P9
CO2 Absorber ( C-0302 ) Level
%
50
65
38,9
63
LAL-0311
P9
CO2 Absorber ( C-0302 ) Level
%
50
65
38,9
5
AI-0301
P9
CO2 Absorber ( C-0302 ) Outlet CG
% Vol
0,05
55
0,06
LC-0301
P9
Process Gas Separator ( V-0304 ) Level
%
50
60
41,7
8,3
64,6
LC-0307
P7B
HP Flash Drum ( V-0302 ) Level
%
40
45
37,5
61,5
LAH-0308
P7B
HP Flash Drum ( V-0302 ) Level
%
40
45
37,5
61,5
80
LC-0309
P7B
MDEA Recycle Separator ( V-0306 ) Level
%
40
45
22
74
92
PC-0306
P7B
MDEA Recycle Separator ( V-0306 )
kg/cm²G
7
8
9
12
TI-0324
P7B
MDEA Recycle Separator
( V-0306 ) Outlet HG
°C
30
40
45
LC-0312
P10
Final Gas Separator ( V-0311 ) Level
%
40
45
18,3
68,3
LAH-0313
P10
Final Gas Separator ( V-0311 ) Level
%
40
45
68,3
50
LI-0321
U4
MDEA Solution Sump Tank ( T-0303 ) Level
%
20
70
20,8
62,5
66,7
LI-0322
U4
MDEA Solution Storage Tank ( T-0303 ) Level
%
0
80
91,8
PAL-0307
P8
Hydraulic Turbine for P-0301-A Suction MAS
kg/cm²G
30,8
30,3
35,5
PAL-0308A
P8
Semi Lean Solution Pump A P-0301A Suction MAS
kg/cm²G
3,5
4,6
2,8
-0,5
8
PAL-0308B
P8
Semi Lean Solution Pump B P-0301B Suction MAS
kg/cm²G
3,5
4,6
2,8
-0,5
8
PAL-0308C
P8
Semi Lean Solution Pump C P-0301C Suction MAS
kg/cm²G
3,5
4,6
2,8
-0,5
8
PAL-0310A
P8
Lean Solution Pump A ( P-0302A ) Suction MAS
kg/cm²G
1,7
1,7
1
-0,5
8
PAL-0310B
P8
Lean Solution Pump B ( P-0302B ) Suction MAS
kg/cm²G
1,7
1,7
1
-0,5
8
PAL-0309A
P8
Split Steam Pump A ( P-0303A ) Suction MAS
kg/cm²G
3,5
4,7
2,8
-0,5
8
PAL-0309B
P8
Split Steam Pump B ( P-0303B ) Suction MAS
kg/cm²G
3,5
4,7
2,8
-0,5
8
PAL-0311
P8
P-0301 A/B/C & P-0303 A/B Seal Water
kg/cm²G
12
11,5
PC-0322
P8
P-0301 A/B/C & P-0303 A/B Seal Water
kg/cm²G
12
11,5
11
TC-0313
P10
Methanator ( R-0301 ) Inlet CG
°C
275
290
250
310
470
TI-0314
P10
Methanator ( R-0301 )
°C
290
290
310
TA-0315
P10
Methanator ( R-0301 )
°C
290
290
250
430
TI-0316
P10
Methanator ( R-0301 )
°C
300
300
320
TA-0317
P10
Methanator ( R-0301 )
°C
308
308
270
330
450
450
LI-0401
C1
NG Compressor Suction ( V-0411 ) Level
%
0
LAH-0421
C2
PA Compressor 1st ( V-0421 ) Level
%
0
50
LAH-0422
C2
PA Compressor 1st ( V-0421 ) Level
%
0
50
75
LAH-0423
C2
PA Compressor 2nd ( V-0422 ) Level
%
0
50
LAH-0424
C2
PA Compressor 2nd ( V-0422 ) Level
%
0
50
75
LAH-0425
C2
PA Compressor 3st ( V-0423 ) Level
%
0
50
LAH-0426
C2
PA Compressor 3st ( V-0423 ) Level
%
0
50
66,7
LC-0441
C3
SG Compressor 1st Separator ( V-0431 ) Level
%
0
2,5
77,5
LAH-0442
C3
SG Compressor 1st Separator ( V-0431 ) Level
%
0
77,5
90
LIC-0443
C3
SG Compressor 2nd Separator ( V-0432 ) Level
%
0
25
50
LAH-0444
C3
SG Compressor 2nd Separator ( V-0432 ) Level
%
0
50
75
LC-0445
C3
SG Compressor 3rd Separator ( V-0433 ) Level
%
0
25
75
LI-0481
C4
NH3 Compressor 2nd Stage KO Drum ( V-0442 )
%
0
51,7
LAH-0482
C4
NH3 Compressor 2nd Stage KO Drum ( V-0442 )
%
0
51,7
85
LIC-0483
C4
NH3 Compressor 3rd Stage KO Drum ( V-0443 )
%
0
20
50
LAH-0484
C4
NH3 Compressor 3rd Stage KO Drum ( V-0443 )
%
0
20
62,5
TI-0402
C1
NG Booster Compressor ( K-0411 ) Discharge NG
°C
65
115
180
TAH-0403
C1
NG Booster Compressor ( K-0411 ) Discharge NG
°C
104
4
115
180
180
ZAH-04102
C1
NG Booster Compressor ( K-0411 ) Thrust Position ( Vibrastion )
mm
-0,2
0,2
-0,6
0,6
0,8
XAH-04103 /
04104
C1
NG Booster Compressor ( K-0411 ) Journal Vibrastion
µm
< 42
42
78
TAH-04108 -
04111
C1
NG Booster Compressor ( K-0411 ) Journal Bearing Temperature
°C
< 110
110
TAH-04112
- 04114
C1
NG Booster Compressor ( K-0411 ) Thrust Bearing Temperature
°C
< 110
110
PI-0421
C2
PA Compressor ( K-0421 ) 1st Suction PA
kg/cm²G
-5
-15
1,8
TI-0421
C2
PA Compressor ( K-0421 )
1st Discharge PA
°C
195
195
205
220
TAH-0422
C2
PA Compressor ( K-0421 )
1st Discharge PA
°C
195
195
8
205
220
220
TI-0423
C2
PA Compressor ( K-0421 )
2nd Discharge PA
°C
210
215
225
230
TAH-0424
C2
PA Compressor ( K-0421 )
2nd Discharge PA
°C
210
215
8
225
230
230
TI-0425
C2
PA Compressor ( K-0421 )
3rd Discharge PA
°C
130
139
150
160
TAH-0426
C2
PA Compressor ( K-0421 )
3rd Discharge PA
°C
130
139
4
150
160
160
TI-0427
C2
PA Compressor ( K-0421 )
4th Discharge PA
°C
145
184
195
200
ZAH-04202
C1
PA Compressor ( K-0421 )
Thrust Position Vibration
mm
-0,2
0,2
-0,6
0,6
0,8
XAH 04203 /
04204
C1
PA Compressor ( K-0421 )
Journal Vibration
µm
< 55
55
104
TAH 04208 -
04211
C1
PA Compressor ( K-0421 )
Journal Bearing Temperature
°C
< 110
110
TAH 04213 -
04215
C1
PA Compressor ( K-0421 )
Thrust Bearing Temperature
°C
< 110
110
ZAH-04203
C1
PA Compressor ( K-0421 )
Thrust Position Vibration
mm
-0,2
0,2
0,6
0,8
XAH 04205 /
04206
C1
PA Compressor ( K-0421 )
Journal Vibration
µm
< 55
55
104
TAH 04209 /
04212
C1
PA Compressor ( K-0421 )
Journal Bearing Temperature
°C
< 110
110
TAH 04213 -
04215
C1
PA Compressor ( K-0421 )
Thrust Bearing Temperature
°C
< 110
110
PC-0441
C3
SG Compressor ( K-0431 )
1st Suction
kg/cm²G
29
29
28
39
TI-0442
C3
SG Compressor ( K-0431 )
1st Discharge SG
°C
95
98
110
120
TI-0443
C3
SG Compressor ( K-0431 )
2nd Discharge SG
°C
95
98
110
130
114
TALH
C3
SG Compressor ( K-0431 )
2nd Discharge SG
°C
95
98
4
110
130
114
TI-0445
C3
SG Compressor ( K-0431 )
Recycle Discharge SG
°C
40
44
50
60
TI-0446
C3
SG Compressor ( K-0431 )
3rd Discharge SG
°C
119
124
145
150
TALH-0447
C3
SG Compressor ( K-0431 )
3rd Discharge SG
°C
119
124
4
145
150
150
ZAH-04401
C3
SG Compressor ( K-0431 )
Thrust Position ( Vibration )
mm
-0,2
0,2
-0,75
0,75
0,8
XAH-04401 /
04202
C3
SG Compressor ( K-0431 )
Journal Vibration
µm
-
< 40.5
40,5
62,4
TAH -04405 -
04408
C3
SG Compressor ( K-0431 )
Journal Bearing Temperature
°C
< 120
120
TAH-04402 -
04404
C3
SG Compressor ( K-0431 )
Thrust Bearing Temperature
°C
< 120
120
ZAH-04203
C3
SG Compressor ( K-0431 )
Thrust Position ( Vibration )
mm
-0,2
0,2
-
-
0,6
0,8
ZAH-04201 /
04206
C3
SG Compressor ( K-0431 )
Journal Vibration
µm
< 55
55
104
TAH-04209 -
04212
C3
SG Compressor ( K-0431 )
Journal Bearing Temperature
°C
< 110
110
TAH-04213 -
04215
C3
SG Compressor ( K-0431 )
Thrust Bearing Temperature
°C
< 110
110
PI-0481
C4
NH3 Compressor ( K-0441 )
1st Suction AG
kg/cm²G
0
-0,02
20
TI-0483
C4
NH3 Compressor ( K-0441 )
2nd Suction AG
°C
80
87
100
110
TALH-0484
C4
NH3 Compressor ( K-0441 )
2nd Suction AG
°C
80
87
4
100
110
110
TI-0486
C4
NH3 Compressor ( K-0441 )
3rd Suction AG
°C
90
108
120
125
TALH-0487
C4
NH3 Compressor ( K-0441 )
3rd Suction AG
°C
90
108
4
120
125
125
ZAH-04802
C4
NH3 Compressor ( K-0441 )
Thrust Position ( Vibration )
mm
-0,5
0,5
-0,75
0,75
0,8
XAH-04803 -
04804
C4
NH3 Compressor ( K-0441 )
Journal Vibration
µm
< 40.5
40,5
62,4
TAH-04808 -
04811
C4
NH3 Compressor ( K-0441 )
Journal Bearing Temperature
°C
< 120
120
TAH-04812 -
04814
C4
NH3 Compressor ( K-0441 )
Thrust Bearing Temperature
°C
< 120
120
ZAH-04803
C4
NH3 Compressor ( K-0441 )
Thrust Position ( Vibration
mm
-0,5
0,5
-0,75
0,75
0,8
XAH-04805 -
04806
C4
NH3 Compressor ( K-0441 )
Journal Vibration
µm
< 40.5
40,5
62,4
TAH-04815 -
04818
C4
NH3 Compressor ( K-0441 )
Journal Bearing Temperature
°C
< 120
120
TAH-04819 -
04821
C4
NH3 Compressor ( K-0441 )
Thrust Bearing Temperature
°C
< 120
120
LIC-0501
P12
1st Chiller ( E-0506 ) Level
%
65
65
61,1
77,8
LIC-0502
P12
Inert Gas Chiller ( E-0511 ) Level
%
60
65
44
64
LIC-0504
P13
Purge Gas Chiller ( E-0514 ) Level
%
60
65
54
70
LIC-0505
P13
2nd Chiller ( E-0508 ) Level
%
65
65
61,1
77,8
LIC-0506
P13
NH3 Separator ( V-0501 ) Level
%
50
50
31
69
LAH-0507
P13
NH3 Separator ( V-0501 ) Level
%
50
50
31
69
70
LIC-0508
P14
Let Down Vessel ( V-0502 ) Level
%
20
25
54,7
85
LAL-0509
P14
Let Down Vessel ( V-0502 ) Level
%
20
25
< 20
LIC-0510
P14
Flash Vessel ( V-0503 ) Level
%
50
60
37,5
62,5
LAH-0511
P14
Flash Vessel ( V-0503 ) Level
%
55
60
37,5
6,8
62,5
93,2
LIC-0512
P15
Inert Gas Separator ( V-0505 ) Level
%
45
50
31
61
LIC-0513
P15
NH3 Accumulator ( V-0504 ) Level
%
35
40
17,8
82,1
PIC-0501
P11
Start Up Heater ( H-0501 ) Inlet FG
kg/cm²G
1,5
0,1
1,7
PALH-0502
P11
Start Up Heater ( H-0501 ) Inlet FG
kg/cm²G
1,5
0,1
0,05
1,7
2
PDI-0503
P11
1st NH3 Converter ( R-0501 ) Inlet SG
kg/cm²G
0,2
0,1
PDAL-0504
P11
1st NH3 Converter ( R-0501 ) Inlet SG
kg/cm²G
0,2
0,05
PIC-0507
P13
2nd Chiller ( E-0508 )
kg/cm²G
1,86
2,1
1,6
2,6
20
PIC-0508
P14
Let Down Vessel ( V-0502 )
kg/cm²G
25
22,5
27,5
27,5
PI-0511
P15
NH3 Accumulator ( V-0504 )
kg/cm²G
15,8
18,2
20
PIC-0516
P14
Flash Vessel ( V-0503 )
kg/cm²G
mmH2o
0.05
( 500 )
0.01
( 100 )
0.09
( 900 )
20
PAHH-0517
P14
Flash Vessel ( V-0503 )
kg/cm²G
0.05
( 500 )
0.01
( 100 )
0.09
( 900 )
1
20
TI-0501
P11
Start Up Heater ( H-0501 )
°C
833
880
900
TIC-0514
P11
1st NH3 Converter ( R-0501 )
°C
360
362
340
380
450
TI-0522
P11
1st NH3 Converter ( R-0501 ) Outlet SG
°C
439
460
470
TIC-0523
P11
SG Steam Superheater ( E-0500 )
Outlet SG
°C
376
360
400
450
TI-0536
P11
2nd NH3 Converter ( R-0502 )
Outlet SG
°C
418
440
470
TI-0539
P11
Hot Heat Exchanger ( E-0503 ) Inlet SG
°C
274
281
300
300
TIC-0542
P11
Hot Heat Exchanger ( E-0503 ) Outlet SG
°C
236
248
230
265
355
TI-0544
P11
SG BFW Preheater ( E-0502 ) Outlet BFW
°C
304
325
340
TIC-0560
P15
NH3 Product Heater-A ( E-0512A )
Outlet AL
°C
25
15
35
60
TI-0562
P11
Start Up Heater ( H-0501 ) Outlet SG
°C
510
520
PI-0448
U32
Steam Turbine for K-0431
( TS-0431 ) Outlet
kg/cm²G
43
44
TI-0429
U31
Steam Turbine for K-0421
( TS-021 ) Outlet
°C
55
60
TI-0449
U32
Steam Turbine for K-0431
( TS-0431 ) Outlet
°C
54,9
60
LIC-0701
U2
Process Condensate Stripper
( C-0701 ) Level
%
40
50
39,1
6,2
60,9
93,8
LI-0702
U2
Process Condensate KO Drum
( C-0701 ) Level
%
0
80
90
PI-0701
U2
Process Condensate Stripper
( C-0701 ) Outlet SM
kg/cm²G
39
40,4
38,5
42,5
46
TI-0701
U2
Process Condensate Stripper
( C-0701 ) Outlet SM
°C
245
250
260
410
AI-0701
U2
Process Condensate Cooler
( E-0703 ) Outlet CP
µs/cm
10
30
PA-1116-1
U10
Turbine Bypass Valve
( PV-1102-1 ) Supply Air
kg/cm²G
7
2
PA-1116-2
U10
Turbine Bypass Valve
( PV-1102-2 ) Supply Air
kg/cm²G
7
2
TI-1102
U10
HP Steam Header
°C
510
515
500
530
TI-1104
U10
Medium Steam Header
°C
384
387
375
410
TI-1105
U10
Medium Low Steam Header
°C
249
249
230
270
TI-1106
U10
Low Steam Header
°C
217
226
205
280
LIC-2501
U1
Deaerator ( V-2501 ) Level
%
65
70
60
75
LALH-2502
U1
Deaerator ( V-2501 ) Level
%
65
70
60
8,3
75
87,5
PIC-2501
U1
Deaerator ( V-2501 )
kg/cm²G
1,5
1,5
2
4
PA-2502A/B
U1
BFW Pump A/B
( P-2501A/B ) Suction BFW
kg/cm²G
3
2,6
6
PI-2503
U1
BFW Pump A/B
( P-2501A/B ) Discharge BFW
kg/cm²G
130
130
125
123
170
LI-2901
U19
MDEA Collection Sump Tank ( T-0304 )
%
20
80
35,7
21,4
78,6
92,9
There are no rows in this table
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