1.1 4 RFCC 10 1.2 1.2.1 20 1
RFCC 1 2 1.2.1 1 2
1.2.1 New Unit UNIT : MBD (TPD) BPSD (TPD) Off Gas & LPG from CDU-IV Arab Heavy Crude API=27.8 224.3 LPG to Storage CDU LPG Sweetening 5MBD INDONESIAN MIX CRUDE API=38.6 OFF GAS/LPG 1.0 LN 2.8 CDU-V HN 12.2 Kero 13.8 60.0 60MBD GO 11.6 GAS Treatment LVGO LVGO to Fuel Oil AR 18.6 HVU-III 2.0 414 25MBD HVGO HVGO TO HCR 4.5 LPG 8.1 GO Kero LN VR 11.6 13.8 1.1 To RFCC & 8.5 Fuel Oil LN Export LN 16,621 13.3 Crude Flasher HN Export HN 37,370 225MBD 20.7 L-Kero to CDUIV 1,034 LN to Export LN to Mogas Blend 117.2 Off Gas LPG 7.2-1.7 LPG Recovery Fuel GAS LPG 20,805 Naph Cut Crude LN LN to Mogas Blend 5.3 7.0 HySCOP HN HN LPG 1.1 185.8 186MBD 14.3 12.2 CDU-IV HN HN NHT REFORMER Reformate MOGAS 44,492 22.2 20.0 20MBD 20MBD 15.7 Tr- Crude 200MBD Kero Jet/Kero 200.0 53.7 77,981 Gas Oil Diesel 39.4 69,489 AR 5.5 72.3 LVGO VGO from Dumai (Option) 5.5 (29) LPG 0.7 AR to HVU-II HVU-II LN 2.2 HCU 48.3 81MBD HVGO HCU Feed HN 2.3 A:27.5MBD 17.6 25.7 B:27.5MBD Kero 10.4 GO 13.0 AR To RFCC 8.1 24.0 VR HVGO from UCO - 25.1 HVU-III VR from VDU III LPG Sweetening & LPG 10.5 LPG PRU 6.3 5.5 9.3 10MBD Propylene Propylene 2,999 RFCC Feed RFCC 3.0 40.0 40MBD Gasoline Gasoline Gasoline HDS Gaso 21.8 22MBD 21.8 LCO 4.9 14.6 - DCO 6.2 4.8 Fuel Oil 25,603 25.6 3.1 LVGO from HVU-III 0.2 2.0 Home Fuel (LSFO) 5.2 5,150 Natural Gas Existing H2 A:34MMSCFD B34MMSCFD New H2 200 MMSCFD (100MBD x 2Train) H2 Acid Gas ARU & SRU 900 TPD (450TPD x 2Train) Sulfur (809) 3
2 1.2.1 1 2008 1 30 1.2.1 1 Cost (US$ Million) Onsite New Units 2,215 Onsite Revamp Units 10 Utility Facilities 365 Tankage & Loading Facilities 35 Offsite & Common Facilities 120 Total 2,745 1.2.1 2 1.2.1 2 Items Cost (US$ Million) Initial Cat. & Chem. Inventory 73 Licensor Cost 20 FEED Cost 50 Pre-operation Cost Total 143 4
1.2.1 3 1.2.1 3 Items Cost (US$ Million) Cat. & Chem. Make-up 79 Natural Gas Cost for New H2 Plant 103 Maintenance Cost 58 Insurance Cost 15 Employee Cost (Direct Expense) 10 General Administration Cost (Indirect Expense) 10 OPEX Total 275 3 FEED EPC FEED FEED EPC DCE FEED EPC 12 15 18 60 63 5
1.2.2 1.2.2 ABC Pertamina JVC EPC EPC ABC ABC JVC JVC EPC EPC JVC 1.2.1 Utility Facilities Tankage & Loading facilities Offsite & Common Facilities JVC ABC JVC Crude Upgrading Section Bottom Upgrading Section JVC 6
JVC 1.2.3 Project IRR NPV 1 1.2.2 JVC JVC 1.2.1 ( 1.2.1 1 Onsite New Units Utility Facilities Tankage & Loading Facilities) 19 3 16 16 330 9,200 / 100% 100% 100% 3,199 7
16 +/-30% 1.2.3 (1) 2,879.47 90% 1,439.74 45% 959.82 30% 479.91 15% 319.94 10% 3,199.41 100% 2,615.00 81.7% 314.84 9.8% 59.81 1.9% 209.76 6.6% 3,199.41 100% Process Fee Margin 20% OPEX 2% 2 2007 7 15 9.50% 8
1.2.3 2 Base case 2,615.00 Process Fee Margin 20.00% 9.50% Project IRR 10.23% NPV 110.90 Equity IRR 30.11% Process Fee Margin 1.2.3 2 Project IRR 10.23% 2007 7 15 9.50% NPV 2007 7 15 9.50% Project IRR 3,199 NPV 110.90 1.2.4 1 EIA Environment Impact Assessment EIA EIA EIA EIA 2 9
5 3 4 Euro III NOx SOx PM 5 1.3 1.3.1 1.3.2 10
5 5 1.3.3 1.3.4 420 bbl 3 2006 12 bbl 6 7 bbl 5 10 bbl 10 bbl 11
1.3.4 ( bbl/ ) 2003 2004 2005 2006 4,175 4,250 4,280 4,247 4,238 144.3 136.0 109.5 104.5 123.6 / 3.5% 3.2% 2.6% 2.5% 2.9% 116.4 150.3 135.8 167.7 142.6 / 2.8% 3.5% 3.2% 3.9% 3.4% 79.6 77.2 67.2 72.0 74.0 / 68.4% 51.4% 49.5% 42.9% 51.9 12
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