8
7
6
5
4
3
2
1
GAS TO SRMGC 0,9
H
Gambar C.1
9,5
H
4-7/8 8-9
5-3/4/5/6/7,8-2C
152
114
610
14
G
CRUDEBUTANE
P-30/30A
258 13
8-7
8-8
KOLOM-V
KOLOM-I
G
P-46/47/48
63
405 10
F
118
P-42/43
255
9
EVAP 3-1
SR-TOPS
K O L O M II
E
K O L O M III
225 128
0,5 2,0
4-5/6
P-10/11
P-8/9
6-5/6,5-1,8-2B
NAPHTHA-II
0,9
1,8
E
215
1,2
92
F
279
P-36/37/38
LKD
D
4-9/10
P-1/2
D
P-34/ 35 DRAW DESCRIPTION
181 307
O
TEMPERATURE, C
C
256
P-44/45 138
2-1
KOLOM-IV
131
PRESSURE,kg/cm
368
2
C
FLOW, M.TON/Day REVISED
0,2
DRAWN BY
FURNACE I
B
344 8,1
6-1/2/ 3/4
2000
4-3/4
1230
A
8
932
RDP
B
TITLE
FURNACE II P-6/7
P-31/32/33 CRUDE OIL
8/12/2007
LCT
4-13/15
6-1/2/3/4
L.RES TO HVU SG
PFD CD-II / CD&GP
0,3
6-5/6
328
7
6
A 5
4
3
2
1
Gambar 10. Diagram Alir Proses CD-II Sumber : PT. Pertamina RU III Plaju, 2017
40
8
7
6
5
4
3
2
1 Gambar C.12
H
H cw
Diesel oil
E-5
G
E-4
G
Kerosine
cw
F
F
E-3 E-6
14
E-7
10
E-2
9
D-4
11
7
E
Naphta
12
8
D-2
9
D-3
E P-6
7
DRAWDESCRIPTION
P-2A/B
1 2 4 5 6 7 8
5 2 4
D
T - 1 PRIMARY TOWER 10'X30'
P-1A/B/C
1
: KOLOM : STRIPPER : COOLER : CONDENSER : HEAT EXCHANGER : REBOILER : ACCUMULATOR
T - 2
O
TEMPERATURE, C
SEC. TOWER 9'X40'2"
C
D
2
PRESSURE,kg/cm
C
FLOW, M.TON/Day REVISED
P 5A/B
B
8/12/2007 Long residue to HVU
DRAWN BY
HAR
P-3A/B
Long residue to tank
B
TITLE
PFD CD-VI / CD&GP
A
A
8
7
6
5
4
Gambar 14. Diagram Alir Proses CD-VI Sumber : PT. Pertamina RU III Plaju, 2017
3
2
1
44
8
7
6
5
4
3
2
1 Gambar C.14
H
H
G
G
F
F
E
E
D
D DRAWDESCRIPTION
C
C
REVISED
B
28/7/2003
B
DRAWNBY
TITLE
PFD FCCU PERTAMINA
A
A
8
7
6
5
4
Gambar 16. Diagram Alir Proses RFCCU Sumber : PT. Pertamina RU III Plaju, 2017
3
2
1
46
8
7
6
5
4
3
2
1
35.1
H
76.5 5-5/6/7/8/ 9/10
5-1/2/3/4 UNSTAB
5-11/12 80
DATA FLOW adalah rata-rata Flow bulan Agustus 2000
8 - 11
G
NOTE :
50
42
40
F
8 - 12
8 - 13
G
4 - 1
S A G S E R
4-2/3 P-11/12
29.6
P-9/10
P-7/8
F
72.7 31.4
E
Gambar C.7
RFG
9-4
H
E T A M I R P M O C
1 0 2 1 E T A S N E D N O C
D
ABSORBER COL 1-1
DEPROPAN COL 1-2
DEBUTAN COL 1-3
STAB. CR.TOP
STRIPPER COL 1-4
E
4-4/5 DRAW DESCRIPTION
9 - 2
20 7-1/2
110
1 4 5 7 8 9
7-3/4
7-5/6
: KOLOM : COOLER : CONDENSER : REBOILER : ACCUMULATOR : SURGE TANK
7 - 7 4 - 6
O
TEMPERATURE, C
C
120
9 - 1
D
120
17
PRESSURE,kg/cm
2
FLOW, M.TON/Day REVISED
P-3/4
8/12/2007 DRAWN BY
B FURNACE
JKP
23.4
HO. SURGE TK. 9 - 3
240
C
125 0.7
6
FBB C3
B
TITLE
PFD BBDISTILASI
6.3
A
8
PERTAMINA
P - 5/6
F. GAS
7
6
5
4
3
2
A
1
Gambar 17. Diagram Alir Proses BB Distiller Sumber : PT. Pertamina RU III Plaju, 2017
47
8
7
6
5
4
3
2
1 Gambar C.8
H
H
SETTLER - A
NC
NC
FBB ke Tk. 1252/53 & 1205/06
G FBB dari BBDIST
WATER SETTLER
CAUSTIC SETTLER
9 - 28
9 - 26 4
4
9 - 29 3.5
NC
F
NC
F
B
NC A
E
G
FINAL SETTLER
S - 20 NaOH FRESH
NC
E
sewer
P - 5/ 6
P - 3/ 4
NC
D
NC 4
CAUSTIC SETTLER
4
9 - 27
C
NC
WATER SETTLER
FINAL SETTLER
9 - 31
9 - 30 2.4
NC
A
NC
S - 19
D
NaOH SPENT DRAW DESCRIPTION
2
PRESSURE,kg/cm
NC
C
B REVISED
WATER
7/15/2006 DRAWN BY
B
JKP
B
TITLE
sewer
FBB dari S.Gerong
PFD BBTREATING
SETTLER - B
PERTAMINA
A
8
7
6
5
4
3
Gambar 18. Diagram Alir Proses BB Treating Sumber : PT. Pertamina RU III Plaju, 2017
2
A
1
48
8
7
6
5
4
3
2
1 Gambar C.6
to F.GAS
H
GAS From SRMGC + Reforming
4
H
NOTE :
DATA FLOW adalah rata-rata Flow bulan Agustus 2000
G
G
Steam 3 - 1
MGC-3
MGC-2
MGC-1
1201
F
61
F
22
4- 7
4- 8
4- 9
4 - 10
E
E DRAW DESCRIPTION
29.6
RES. GAS
D
3 : EVAPORATOR 4 : COOLER 8 : ACCUMULATOR
D
COMPRIMATE P-9/10/ 14
31.4
C
2
PRESSURE,kg/cm
8- 1
8-2
8-3
8- 4
8- 5
C
FLOW, M.TON/Day REVISED
7/15/2006 DRAWN BY
B
JKP PFD BBMGC CONDENSATE
A 8
7
B
TITLE
SEWER
6
5
4
Gambar 19. Diagram Alir Proses BBMGC Sumber : PT. Pertamina RU III Plaju, 2017
3
2
PERTAMINA
A
1
49
Gambar 20. Overview Kilang Polypropylene Sumber : Laboratorium Kilang Polypropylene PT.PERTAMINA.RU III-PLAJU 2017
50
8
7
6
5
4
3
E-203
H
2
1 Gambar C.15
FUEL HEADER
S-201
H E-303 A/B
V-205
V-204 FLARE
G
P-208 A/B
V-203
V-303
DRYER UNIT
G E-306 A/B E-307 A/B
V-207
P 305 A/B
P-204 A/B
F
C-201
C-203
C-202
C-204
C-205
C-320 C
C-206
C-320 A
F
C-320 B
T-102 T-103 1-104
P-301 A/B
E
E
PW E-208 V-204
E-204 E-205
D
REFINERY
E 201
E-202
D E-304
E-206 V-210
E-305 Ke V-600
C P 301 A/B
C DRAW DESCRIPTION REVISED
P-207 A/B
25/7/2003 DRAWN BY
B
DEA P-202 A/B
PUT/RUN
P-203
PFD Purifikasi PP PERTAMINA
A 8
7
6
5
4
3
Gambar 21. Diagram Alir Proses Unit Pu rifikasi Polypropylene Sumber : PT. Pertamina RU III Plaju, 2017
B
TITLE
T-101
2
A
1
51
Gambar C.17 Bahan Baku
UDARA from Atm
UNIT PROSES/UNIT OPERASI UTILITAS Compressed Air Plant
IA/SA (Plant Air)
Kap. Desain PL: (5x4350)+(1x1000) SG: (4x750) Nm3/J
Water Treating Plant (WTP)
Cooling Tower PL=12000 T/J + SG=4000 T/J
CAF Kap: PL:4x100 PS-1:150 SG:200
Injeksi Klorin
(Cl2) Kapasitas PL=3x100 T/J SG=35-40 T/J Kap:9,5 T/J
Gas Turbine GT 2015 UA/UB/UC
SOFTENER A/B/C/D kap: 4x75 T/J
PB & WHRU PB=2x50 T/J WHRU=3x60 T/J
Kap.Desain: 3x31 MWH = 93 MWH
CD & L/SG Kap. 25-30 T/J
EDG 2016 U Diesel Oil
kap. 0,75 MWH
Boiler PS-1 Boiler No.: 2/3/4/5/6/8=22 9/10/11=30 Tot=200 T/J
ST. 2017 U Fuel Gas (M.G/R.G)
CHEMICAL’s consumption sbg bahan pendukung
kap. 3 MWH
GUDANG UTL PL/SG/BK (Chemical’s handling )
Bising, Ceceran Lube Oil, Silika Gel
Nitrogen Gas & Cair
Perlite, Freon, Sil.Alumina Adsorber
Bising, Ceceran Lube Oil, Lumpur
Air Pendingin Sirkulasi (CT.CT)
Chemical’s Corr .inh, Scale inh, Biocide, Drain rutin, Gas Clorin
Air Bersih (Treated Wtr)
Chemical’s Alum, Caustic, PE, Kapur, Drain Lumpur, Lube Oil
Air Minum (Drink Water)
Injeksi Klorin, Carbon Active
Demin Water (DIW)
Chemical’s Caustic, A.Sulphate & Resin
Hidrogen (H2) Gas
Larutan KOH, H2 gas, Bising
Steam 42-K (HP-Steam)
Chemical’s Caustic & Tripho, Blowdown, Emisi Gas Buang, Bising
Demin Plant
Hidrogen Plant
Fuel Gas ex.EP
Udara Kempa
OT.CW (Once Through)
Coling Water Once Through, Fire Water
Kap.Disain: PS-2/PL=2x1100 T/J WTU/SG=400 T/J DWP/SG=150 T/J WTP/BK=50 T/J WTP PS-1/PL idle
Dampak Lingkungan
Nitrogen Plant Kap. Desain: LIN=336 Nm3/J GAN=1650 Nm3/J
RAW WATER ex.RPA Kap.total:15000 T/J PL:1/2/3/4 SG:5/6B BK:5
Produk
Distribusi
Steam 23-Kg/cm2 FGC-I/II/III RFCCU Steam 15-K (MP-Steam)
Chemical’s Caustic & Tripho, Blowdown, Emisi Gas Buang, Bising
LISTRIK Frek=50Hz
Bising, Lube Oil Drain, Emisi Gas Buang
Larutan Chemical
Ceceran, tumpahan selama transportasi dan Mixing sebelum di distribusikan ke unit
Gambar 23. Diagram Alir Sistem Utilitas Sumber : PT. Pertamina RU III Plaju, 2017
53
