optimalization of petrochemical feedstocks in ... - CMT Conferences

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IV. 3. Utilizing Sr. Kerosene as feed of N-Paraffin Plant RAW MATERIAL BALANCE ( SR. KEROSENE) CDU-DMI 19.40 16.10 20.60 NPP - DMI 3.20 N. PARAFFIN TANK 3.30 17.20 150,000 TPA 20.5 23.0 UPMS I 2.50 4.50 HCU-DMI CDU-SPK 6.60 2.10 DEPO-SIAK Source : PTM, 2007 PT PERTAMINA (PERSERO) 24
IV.3.a. ABS Process Flow Diagram (Benzene and N-Paraffin as feed) Refinery H2 Rich N - Paraffin Plants Benzene Sr. Kerosene N_Paraffin ABS Plant Returned Kero Alkyl Benzene Sulfonates Source : PTM, 2007 PT PERTAMINA (PERSERO) 25
Page 1 and 2: OPTIMALIZATION OF PETROCHEMICAL FEE
Page 3 and 4: III. NATIONAL OPTIMALIZATION FOR PE
Page 5 and 6: I.2.a. Indonesia Oil Reserves, 2005
Page 7 and 8: II.1. Petrochemical industry chain
Page 9 and 10: II.3 MAIN PETROCHEMICALS INDUSTRY P
Page 11 and 12: II. 3 MAIN PETROCHEMICALS INDUSTRY
Page 13 and 14: II.4. Domestic Petchem Feedstocks B
Page 15 and 16: II.5 OIL PRICE PREDICTION BY SOME I
Page 17 and 18: III. OPTIMALIZATION OF NATIONAL PET
Page 19 and 20: IV. 1. Utilizing Off gas ex RCC for
Page 21 and 22: IV. 2, Utilizing Natural Gas as fee
Page 23: Matindok GTL Technology (Continued)
Page 27: CONCLUSIONS • There is potential

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