| GRASSROOTS REFINERY PROJECT AT PARADIP (ORISSA) |
| Project Cost: Rs. 29,777.00 crore |
| Expected Commissioning: March-November, 2012 |
| Benefit: The project will help in partially meeting the deficit in distillates viz. LPG, Naphtha, MS, Jet/Kero, Diesel and other products, in the eastern part of the country. The complex will generate intermediate petrochemicals feedstock. |
| Brief Description: A 15 MMTPA refinery is being constructed at Paradip in Orissa. The refinery will have, apart from a Crude and Vacuum Distillation Unit, a Hydrocracking Unit, a Delayed Coker Unit and other secondary processing facilities. This will be the most modern refinery in India with a nil-residue production, and the products would meet stringent specifications. IndianOil has taken over 3344 acres of land for the project and necessary infrastructure development jobs prior to setting up of the main refinery are in progress. |
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| RESIDUE UPGRADATION AND MS/HSD QUALITY IMPROVEMENT PROJECT AT GUJARAT REFINERY |
| Project Cost: Rs. 5,882.00 crore |
| Expected Commissioning: March-June, 2010 |
| Benefit: The objectives of the project are multifold. It will ensure compliance to product quality requirement of MS/HSD to EURO-III/IV levels, enable processing of increased quantity of high sulphur crude, and improvement in distillate yield. |
| Brief Description: The project envisages setting up of a number of units like VGO-HDT, ATF-Merox, FCC-Merox, LPG-Merox, ISOM, Coker, DHDT, HGU (PDS) and SRU. |
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| IMPROVEMENT IN DIESEL QUALITY AND CAPACITY EXPANSION AT HALDIA REFINERY (WEST BENGAL) |
| Project Cost: Rs. 2,869.00 crore |
| Expected Commissioning: February 2010 |
| Benefit: Improvement in quality of HSD conforming to Euro-II/Euro-IV equivalent norms. In addition, it will improve the distillate yield and crude processing capacity of the refinery. |
| Brief Description: The project comprises installation of facilities for improvement in Diesel quality and Distillate yield (Hydrocracker) at Haldia, and capacity expansion of the Refinery from 6 MMTPA to 7.5 MMTPA. This involves Once-through Hydrocracking Unit (OHCU), Hydrogen Unit, Sulphur Recovery Units, revamp of Crude Distillation Units, related utilities and offsite facilities. |
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| NAPHTHA CRACKER AND POLYMER COMPLEX AT PANIPAT (HARYANA) |
| Project Cost: Rs. 14,439.00 crore |
| Expected Commissioning: March 2010 |
| Benefit: This project is the cornerstone for IndianOil's entry into petrochemicals thereby creating a new business line for growth. For the state of Haryana, this project shall lay the foundation for creation of a world-class petrochemicals hub, which will engender significant industrial activity in the coming years. |
| Brief Description: The project envisages setting up of a Naphtha Cracker based on captive utilisation of naphtha from Panipat, Mathura and Koyali refineries of IndianOil. With a capacity of 800,000 MT/year of ethylene production, the Cracker Complex will have associated units viz. hydrogenation, butadiene extraction, benzene extraction etc. besides downstream polymer units like Swing Unit (LLDPE/HDPE), a dedicated HDPE Unit, Polypropylene Unit and MEG Unit. |
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| FCC GASOLINE DESULPHURISATION UNIT AT MATHURA REFINERY (UTTAR PRADESH) |
| Project Cost: Rs. 348.00 crore |
| Expected Commissioning: February 2010 |
| Benefit: The implementation of this project will improve the quality of MS to conform to Euro-IV equivalent norms. |
| Brief Description: In this project a FCC Gasoline Desulpurisation Unit will be installed. |
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| MS QUALITY UPGRADATION PROJECT BARAUNI REFINERY (BIHAR) |
| Project Cost: Rs. 1,492.00 crore |
| Expected Commissioning: June 2010 |
| Benefit: The implementation of this project will improve the quality of MS to conform to Euro-III equivalent norms. |
| Brief Description: The major process units under this project are Isomerisation, Naphtha Hydrotreater, Reformate Splitter, FCC Gasoline Desulpurisation Unit and Hydrogen Generation Unit. |
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| MS QUALITY UPGRADATION PROJECT AT GUWAHATI REFINERY (ASSAM) |
| Project Cost: Rs. 372.00 crore |
| Expected Commissioning: June 2010 |
| Benefit: The implementation of this project will improve the quality of MS to conform to Euro-III equivalent norms. |
| Brief Description: The major process units under this project are Isomerisation, Light Naphtha Splitter, Naphtha Hydrotreater and Indmax Gasoline Splitter. |
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| MS QUALITY UPGRADATION PROJECT AT DIGBOI REFINERY (ASSAM) |
| Project Cost: Rs. 356.00 crore |
| Expected Commissioning: June 2010 |
| Benefit: The implementation of this project will improve the quality of MS to conform to Euro-III equivalent norms. |
| Brief Description: The major process units under this project are Isomerisation, Naphtha Splitter, Naphtha Hydrotreater and Reformate Splitter. |
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| DADRI-PANIPAT R-LNG SPUR PIPELINE |
| Project Cost: Rs. 298.00 crore |
| Expected Commissioning *: February 2010 |
| Benefit: The 132 km long 30 inch diameter spurline carrying regassified LNG (R-LNG) will stretch from GAIL India’s Dadri terminal in UP to Panipat. |
| Brief Description: The proposed R-LNG pipeline will provide for an economical means of feeding natural gas to Panipat refinery. |
| * Subject to availability of RoW |
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| PANIPAT REFINERY EXPANSION FROM 12 MMTPA TO 15 MMTPA |
| Project Cost: Rs. 1,007.83 crore |
| Expected Commissioning * : August 2010 |
| Benefit: To meet the growing deficit of petroleum products in the high demand Northwest region of India. |
| Brief Description: The project consists of capacity revamp of Crude and Vacuum Distillation Units (CDU / VDU), Once through Hydrocracking Unit (OHCU), Delayed Coking Unit, and installation of second stage reactors in Diesel Hydrotreating Unit (DHDT). |
| * Qaulity part completed in November, 2009 |
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| CHENNAI - BENGALURU PRODUCT PIPELINE |
| Project Cost: Rs. 273.00 crore |
| Expected Commissioning: February 2009 |
| Benefit: The pipeline will facilitate effective evacuation of products from CPCL refinery in Chennai and ensure uninterrupted, regular and economical transportation of petroleum products to Bengaluru-fed areas in a cost-effective manner. |
| Brief Description: Project consists of laying 14/12-inch diameter 290 km long product pipeline from CPCL refinery, Chennai to existing TOP at Devanagonthi (Bengaluru). |
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| BRANCH PIPELINE FROM KSPL, VIRAMGAM TO KANDLA |
| Project Cost: Rs. 349.00 crore |
| Expected Commissioning: August 2011 (30 months after receipt of environment & forest clearance) |
| Benefit: The pipeline would provide cost-effective link with the sea route ex-Kandla for coastal movement of surplus products of Koyali refinery and enhance flexibility in the system for ensuring sustained operation of the refinery. |
| Brief Description: Project consists of laying of 16-inch diameter 217 km long product pipeline from Viramgam to Churwa and use of 22” diameter 14 km existing KBPL pipeline between Churwa to Kandla. |
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| DIESEL HYDRO-TREATMENT (DHDT) PROJECT AT BONGAIGAON REFINERY (ASSAM) |
| Project Cost: Rs. 1646.39 crore |
| Expected Commissioning: June 2010 |
| Benefit: The implementation of this project will improve the quality of HSD to conform to Euro-III equivalent norms. The project would also improve smoke point of Raw Kerosene and enhance production of SKO and ATF. |
| Brief Description: The major process units under this project are DHDT Unit, Sulphur Recovery Block, Reformer, Power Plant, DM Plant and Hydrogen Generation Unit. |
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| MS QUALITY UPGRADATION PROJECT AT BONGAIGAON REFINERY (ASSAM) |
| Project Cost: Rs. 293.60 crore |
| Expected Commissioning: June 2010 |
| Benefit: The implementation of this project will improve the quality of MS to conform to Euro-III equivalent norms. |
| Brief Description: The major process unit under this project is Light Naphtha Isomerisation Unit. Existing Xylene Fractionation facilities would also be used. |
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| PARADIP-NEW SAMBALPUR-RAIPUR-RANCHI PIPELINES |
| Project Cost: Rs. 1793.60 crore |
| Expected Commissioning: September 2012 |
| Benefit: The proposed pipeline would ensure the evacuation of Paradip Refinery products and uninterrupted supply to major parts of Orissa, Chhattisgarh and Jharkhand. |
| Brief Description: Project consists of laying of 1108 km long product pipeline with intermediate pumping stations at Jatni and New Sambalpur and delivery stations at Jatni, Jharsuguda, Ranchi, Raipur and Korba. The pipeline will be having a telescopic diameter of 18”/14”/12”/10” OD. |
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| DE-BOTTLENECKING OF SALAYA-MATHURA CRUDE PIPLEINE |
| Project Cost: Rs. 1584.00 crore |
| Expected Commissioning: 30 months after receipt of statutory clearances |
| Benefit: With the proposed de-bottlenecking/augmentation of SMPL, the refineries would be in a position to process more crude oil. |
| Brief Description: The proposal is for enhancing the capacity of Salaya-Viramgam section from 21 MMTPA to 25.0 MMTPA, [Viramgam-Koyali section from 8.5 MMTPA to 9.0 MMTPA, Viramgam-Chaksu section from 13.5 MMTPA to 16.5 MMTPA, Chaksu-Mathura section from 7.5 MMTPA to 9.2 MMTPA and Chaksu-Panipat section from 6 MMTPA to 7.3 MMTPA]. |
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| INTEGRATED CRUDE OIL HANDLING FACILITIES AT PARADIP |
| Project Cost: Rs. 1492.33 crore |
| Expected Commissioning: June 2012 |
| Benefit: The proposed facilities would enhance crude handling capacity at Paradip port. |
| Brief Description: The proposal is for installation of 2nd SPM for Paradip Refinery and 3rd SPM & sub-sea crude oil transfer pipeline with associated facilities as a part of Integrated Offshore Crude Handling Facilities at Paradip. |
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| Updated on February 23, 2010 |