Panipat Refinery Capacity Expansion from 15 MMTPA to 25 MMTPA

Project Cost: Rs 34,627 Cr

Benefit:The project helps IndianOil to meet increase in demand of Petroleum and Petrochemical products in North India.

Brief Description:The project envisages capacity expansion of Panipat Refinery from the current 15 MMTPA to 25 MMTPA. The project will also involve the installation of a Polypropylene Unit and Catalytic Dewaxing Unit.

Petrochemical and Lube Integration Project at Gujarat Refinery

Project Cost: Rs 18,936 Cr

Benefit:The project helps IndianOil to meet increase in demand of Petroleum and Petrochemical products in West India.

Brief Description:The project envisages capacity expansion of Gujarat Refinery from current 13.7 MMTPA to 18 MMTPA along with its integration to Lube and Petrochemical Production Units. The project comprises a revamp of AVU-5, new VDU, INDMAX, PP unit, MS Block, CDW and HCU revamp along with LPG treater units and associated facilities.

Barauni Refinery Capacity Expansion from 6 MMTPA to 9 MMTPA

Project Cost: Rs 14,810 Cr

Benefit:The project helps IndianOil to meet increase in demand of Petroleum and Petrochemical products in East India.

Brief Description:The Project envisages capacity expansion of Barauni refinery capacity from current 6.0 MMTPA to 9.0 MMTPA. The expansion would enhance the flexibility in operations and would also improve the refining margin. It is also proposed to implement Polypropylene unit of 200 TMTPA capacity for processing propylene feed stock.

Integrated Para Xylene (PX) and Purified Terephthalic Acid (PTA) Project at Paradip Refinery

Project Cost: Rs 13,805 Cr

Benefit:The project helps IndianOil to meet captive and future demand of PX-PTA.

Brief Description:The Project envisaged configuration of 1.2 MMTPA Purified Terephthalic Acid (PTA) unit and 0.78 MMTPA Para Xylene (PX) unit along with associated Utilities, Offsite and dispatch facilities to cater the increasing demand growth of PX and PTA product in the near future.

Ethylene Glycol Project (MEG), Paradip Refinery

Project Cost: Rs 5,654 Cr.

Benefit:The project will help in consolidating the Polyester business of the corporation by way of producing Mono Ethylene Glycol (MEG) which is used to manufacture Polyester fibres, Bottle grade Chips & Polyester film grade chips. In non-Polyester applications, MEG is used to produce Antifreeze, Coolants, Paint formulations & Acrylic binders etc.

Brief Description:This Project envisages recovery of ethylene present in FCC off-gases and then upgrading it to Mono Ethylene Glycol (MEG), Di Ethylene Glycol (DEG) and Tri Ethylene Glycol (TEG) at Paradip Refinery.

Acrylics/ Oxo-Alcohol Project at Dumad, Gujarat

Project Cost: Rs 5,251‬ Cr

Benefit:The project helps IndianOil to meet increase in demand of Petrochemicals in North India and to reduce Indian import dependency.

Brief Description:Project envisages setting up of the Acrylic Acid (AA) Unit, Normal Butyl Alcohol (NBA) Unit, Syn-Gas Unit and Hydrogen, Butyl Acrylate (BA) Unit & Propylene Recovery Unit (PRU).

Fuel Quality Upgradation Project at Paradip Refinery

Project Cost: Rs 3361 Cr

Benefit:This project envisaged to improve the quality of Fuel.

Brief Description:Project envisaged for production of high-quality MS and HSD.

R&D-II Campus at Faridabad

Project Cost: Rs 3220‬ Cr

Benefit:To meet the future research and development plans of Indian Oil.

Brief Description:The complex is planned as an integrated campus combining the engineering/ technology offices, experimental research & development (R&D) laboratories, Pilot/ demonstration/ semi commercial scale-up units for development for processes and products for Alternative Energy, Petroleum, Nanotechnology, Biotechnology, Petrochemical, Catalyst and chemical industries.

Naphtha Cracker Expansion Project at Panipat Refinery

Project Cost: Rs 1,636 Cr.

Benefit:The project helps IndianOil to meet increase in demand of Petrochemical products in North India.

Brief Description:The project envisages Naphtha Cracker Unit (NCU) expansion (857 KTA to 947 KTA), Mono Ethylene Glycol (MEG) expansion (304 KTA to 425 KTA), Butadiene Extraction Unit (BEU) expansion (117 KTA to 204 KTA) and New Ethylene Recovery Unit (ERU) (227 KTA) at Panipat Refinery.

PX-PTA Expansion Project at Panipat Refinery and Petrochemical Complex

Project Cost:Rs 1,255‬ Cr

Benefit:The project helps Indian Oil to meet captive and future demand of PTA.

Brief Description:This Project envisaged for expansion of existing PX & PTA units at Panipat Refinery.

Installation of Second Catalytic Dewaxing Unit (CDW-II) at Haldia Refinery

Project Cost: Rs 1019 Cr

Benefit:The project helps in import substitution of Lube Oil Base Stock Grade -III.

Brief Description:Installation of 2nd CDW unit at Haldia Refinery for augmenting API Group-II & Group-III Lube oil base stock (LOBS) production.

Infrastructure facilities at JR & Dumad for KAhSPL

Project Cost: RS 906 Cr

Benefit:This Project is to create infrastructure facilities at Gujarat Refinery & Dumad for Koyali-Ahmednagar Solapur (KAhSPL) Pipeline.

Brief Description:Project envisaged construction of 4 HSD Tanks, 3 MS Tanks, 3 ATF Tanks, 2 PCK Tanks, 4 Fire water Tanks, 2 SKO Tanks & other operating facilities including QC lab, Fire station etc. at Dumad, a pumping facilities at Gujarat Refinery and cross-country pipeline between Gujarat Refinery & Dumad.

Capacity Expansion of Digboi Refinery from 0.65 MMTPA to 1 MMTPA

Project Cost: Rs 768 Cr

Benefit:Refinery Capacity Expansion project.

Brief Description:This project envisages capacity expansion of Digboi refinery from current 0.65 MMTPA to 1.0 MMTPA.

PSA Off-gas to Ethanol Project at Panipat Refinery

Project Cost: Rs 754 Cr

Benefit:The project helps IndianOil in meeting Government of India's policy on Ethanol blending to MS.

Brief Description:This project envisages conversion of HGU Off-gas to Ethanol using LanzaTech Technology.

Additional Storage Tankages at Paradip

Project Cost:RS 543 Cr

Benefit:The additional Tanks would increase the ullage and help in sustaining the refinery crude throughput during the outage of any secondary processing unit.

Brief Description:Project envisaged for construction of 10 new tanks along with the allied facilities at Paradip Refinery, which would comprise of feed Tanks for DHDT, NHT, VGO-HDT and Product Tanks for MS, Liquid Sulphur, Alkylate and PCK. The additional tanks are envisaged to increase ullage and help in sustaining the refinery crude throughput during outage of secondary processing unit.

Installation of SRU Train along with Incinerator at Paradip Refinery

Project Cost: Rs 427‬ Cr

Benefit:To meet the standby pollution control equipment condition specified by Odisha State pollution control board.

Brief Description:Presently the Paradip refinery is operating with 2 nos. of SRUs, and no standby SRU/ TGTU/ Incinerator is available. In the consent order of Odisha State Pollution Control Board (OSPCB) for Paradip Refinery, it is mentioned that Standby pollution control equipment or alternate arrangement should be kept ready for any eventuality. Also, Additional Sulphur recovery load from BS-VI units will be absorbed in the existing SRU plant of capacity 2 X 525 TPD. In view of this Standby SRU Train of 525 TPD along with Incinerator at Paradip Refinery is envisaged.

Guwahati Refinery Expansion (1.0 to 1.2 MMTPA) along with installation of CRU

Project Cost: Rs 412 Cr

Benefit:Installation of CRU Unit will provide savings towards GST and Freight cost to the Corporation on account of transportation of external reformate to GR. It provides perfect synergy to the refinery to achieve crude throughput of MMPTA.

Brief Description:The project envisages for expansion of Guwahati Refinery from 1.0 to 1.2 MMTPA along with the installation of Catalytic Reforming Unit.

Biturox Unit at Barauni Refinery

Project Cost: Rs 389 Cr

Benefit:The project helps to maintain supply-demand of Bitumen products in East India.

Brief Description:The project envisages installation of a new Bitumen unit of 300 KTPA capacity Installation of 300 KTA Bitumen Unit along with allied facilities at Barauni Refinery.

Catalyst Plant at Panipat Refinery

Project Cost: Rs 340.8 Cr.

Benefit:The project would help to ensure availability of catalyst for in house consumption.

Brief Description:The project envisages production of 500 MTPA FCC Catalyst additives and 1,000 MTPA DHDS/ DHDT Catalyst including the key raw materials for producing these catalysts i.e. Alumina and ZSM-5 Zeolite at 860 MTPA and 250 MTPA respectively using IOCL R&D technology.

Biturox Unit at Gujarat Refinery

Project Cost: Rs. 328.3 Cr

Benefit:The project helps to maintain supply-demand of Bitumen products in West India.

Brief Description:The project envisages installation of a new Bitumen unit of 500 KTPA capacity and 2 Bitumen storage tanks of 12 TKL capacity each.

Infrastructure Development to facilitate Grid power import at 220 KV, Panipat Refinery

Project Cost: Rs. 278.6 Cr

Infrastructure Development to facilitate Grid power import at 220 KV, Mathura Refinery

Project Cost: Rs. 255.4 Cr

Infrastructure Development to facilitate Grid power import at 220 KV, Barauni Refinery

Project Cost: Rs. 199.36 Cr

Benefit:IOCL has taken a strategic decision to develop infrastructure for importing bulk grid power @ 220KV voltage level at refineries to import grid power, whenever economic power is available. Further, power requirement for new projects is also envisaged from Grid power due to which capital investment also considerably reduced.

Brief Description:This consists of OSBL jobs covers installation & commissioning of 220 KV transmission line up-to refineries. And ISBL jobs of development of infrastructure at inside refineries for import of power at 220kV voltage level.

Infrastructure development for utilization of Natural gas at Paradip Refinery

Project Cost: Rs 202 Cr

Benefit:Strategic initiative for use of NG as an alternate fuel/Feed in HGU, TPS and Process unit Heaters. It is cost effective and better to control the emissions.

Brief Description:The project envisaged for development of infrastructure for utilizing Natural gas as a fuel in GT, HRSG, Existing HGU (Under BOO) and new HGU coming up in Fuel quality upgradation project, utility Boilers and as make-up fuel in Process unit Heaters at Paradip Refinery.

Bio-Fuel Complex at Gorakhpur

Project Cost: Rs 164.69‬ Cr

Benefit:To reduce GHG emissions and to create end use for agro - crop residue like rice straw which is presently being burnt in the fields of UP, Punjab, Haryana, Bihar causing severe environmental problems.

Brief Description:The compressed biogas plant planned at Gorakhpur aims to produce bio-gas from agri-crop residue like rice straw.

Indresid Demo plant at Panipat

Project Cost: Rs. 146 Cr

Benefit:This project helps Indian Oil to scale up, demonstration and commercialization of the Indresid process.

Brief Description:Indian Oil R&D had taken a strategic initiative to develop hydro conversion-based process for upgrading vacuum residue to value added products and establish a proof of concept for the same.

2G Ethanol Demo Plant at Panipat Refinery

Project Cost: Rs 115.6 Cr

Benefit:This project helps Indian Oil to scale up, demonstration and commercialization of conversion of Lignocellulosic Biomass to ethanol via enzymatic and Fermentation route.

Brief Description:Indian Oil is setting up an Integrated 10 Tons per day Demonstration plant for conversion of Lignocellulosic Biomass to ethanol via enzymatic and Fermentation route based on the technology developed by R&D center of lndianOil.

Development of Infrastructure facility for Utilizing Natural Gas at Haldia Refinery.

Project cost: 134.38 Cr.

Benefit:Strategic initiative for use of Natural Gas as an alternate fuel/ Feed for GT (Present fuel is Naphtha) and Process Heaters and Burners (present fuel is FO). It is very cost effective, environmentally friendly fuel and helps in better emissions control.

Brief Description:Haldia Refinery currently utilizes Naphtha as feed and fuel for Hydrogen generation in HGU and as fuel in Gas Turbines for power generation. Internal Fuel Oil is consumed as fuel in Boilers and process unit furnaces. Refinery Fuel gas is consumed in process unit heaters. The estimated Natural Gas consumption is 1.25 MMSCMD for process unit heaters, boiler-4 and Gas Turbines which is estimated to go up to 2.57 MMSCMD in the future considering HGU1 and HGU2.

Mundra Panipat Crude Oil Pipeline

Project Cost: Rs. 9,028 Cr

Brief Description:Project involves laying of 17.5 MMTPA capacity, new 36 Inch dia. 1033 km long Pipeline from Churwa in Gujarat to Panipat in Haryana. Pipeline traverses through the State of Gujarat, Rajasthan, and Haryana. The project objective is to meet the enhanced crude oil requirement of Panipat Refinery at its augmented capacity of 25 MMTPA post expansion of Panipat Refinery after completion of Panipat Refinery expansion project.

Ennore – Thiruvallur – Bengaluru – Puducherry – Nagapattinam – Madurai – Tuticorin

Natural Gas Pipeline

Project Cost: Rs. 6025 Cr

Brief Description:Project involves laying of 1,444 km pipeline from Ennore LNG Import Terminal for supply of natural gas to anchor customers and for city gas distribution in the states of Tamil Nadu, Andhra Pradesh and Karnataka. Capacity of pipeline will be 35 MMSCMD.

Paradip Hyderabad Pipeline Project

Project Cost: Rs. 3338 Cr

Brief Description:Project involves laying of 1,212 Km pipeline for transportation of petroleum products from Paradip to Hyderabad. Pipeline traverse through states of Odisha, Andhra Pradesh and Telangana. Pumping stations at Paradip & Berhampur (in Odisha); Vizag, Rajahmundry & Vijayawada (in Andhra Pradesh); Delivery facilities at Berhampur (in Odisha), Vizag, Achutapuram, & Vijayawada (in Andhra Pradesh) and Hyderabad (in Telangana) have been envisaged.

30” OD Crude Oil Pipeline in H-B section of PHBPL and Conversion of existing 18" twin Pipelines in H-B section from Crude to Product and Gas service

Project Cost: Rs. 3696 Cr

Brief Description:Project involves laying of 517 km long Crude pipeline from Haldia to Barauni. Pipeline traverses through states of West Bengal, Jharkhand and Bihar with modification in facilities at Paradip, Balasore, Bolpur and Haldia.

Augmentation of Paradip – Haldia – Durgapur LPG Pipeline and its extension up to Patna and Muzaffarpur

Project Cost: Rs. 3027.9 Cr

Brief Description:Project involves laying of 921 Km pipeline for transportation of LPG to consumption centre in Bihar. Pipeline traverses through state of West Bengal, Jharkhand and Bihar. Pumping facilities at Durgapur and Barauni and delivery facilities at LPG bottling plants at Banka, Patna and Muzaffarpur.

Koyali - Ahmednagar - Solapur Pipeline Project

Project Cost: Rs. 1945 Cr

Brief Description:Project involves laying of 747 Km pipeline for transportation of petroleum products from Koyali to Solapur. Pipeline traverses through state of Gujarat and Maharashtra. Pumping facilities at Dumad, Songarh and Manmad and delivery facilities at Manmad, Ahmednagar and Solapur have been envisaged.

Augmentation of Salaya-Mathura Crude Oil Pipeline System to meet additional crude oil requirement for Koyali Refinery project

Project Cost: Rs 1614 Crore

Brief Description:The project envisages capacity augmentation of Salaya-Mathura Crude Oil Pipeline System to meet additional crude oil requirement for Koyali Refinery project. The augmentation work involves augmenting pumping facilities at 5 locations (Vadinar, Jamnagar, Gauridad, Surendranagar and Bareja) storage facilities, and delivery facilities at Koyali refinery, all in Gujarat.

Replacement of existing Twin 42” Offshore Pipelines at Vadinar along with Existing PL Manifolds & 1 new Buoy

Project Cost: Rs. 1378 Cr

Brief Description:IOCL Owns and operates 2 SPM System along with offshore lines for meeting the crude requirement of IOCL refineries at Koyali, Panipat & Mathura. SPM System were installed in 1978 & 1997. This project involves replacement of existing offshore lines and abandon existing Pipeline End Manifold (PLEM), and relocate entire system (pipelines, the PLEMs and the interconnecting loop line) at a new location approximately 2 km away from existing location.

Paradip-Somnathpur-Haldia Pipeline

Project Cost: Rs. 1297.5 Cr

Brief Description:The pipeline is envisaged to meet the long term product requirements of Marketing terminals linked to Haldia – Barauni Pipeline and Barauni – Kanpur Pipeline through a 344 km long Product Pipeline with delivery staions at Somnathpur and Haldia.

POL Pipelines in Common Corridor Pipelines- Chennai

Project Cost: Rs. 829 Cr

Brief Description:The project involves laying of 2 Nos. 30” dia, 10.5 Km Bi-directional multiproduct pipelines from KPL jetty to Vallur terminal, and 3 Nos. 24” dia, 8.9 km dedicated pipelines for HSD, MS & SKO / ATF from CPCL Manali Refinery to upcoming Vallur terminal of IndianOil.

Product pipeline from CBR to Asanur

Project Cost: Rs. 564 Cr

Brief Description:The project involves laying 139 km long pipeline from Cauvery Basin Refinery (CBR) to Asanur and its linking with existing Chennai -Trichy-Madurai product pipeline for evacuation of the petroleum products from the CBR refinery of CPCL.

Muzaffarpur Motihari LPG-Pipeline

Project Cost: Rs. 403 Cr

Brief Description:Project involves laying of 108 Km long Pipeline from Muzaffarpur to Motihari to meet long-term projected throughput requirement at Motihari and Nepal Oil Corporation. Project is part of the scheme for connecting upcoming JV Project Kandla Gorakhpur Pipeline and Augmentation of Paradip Durgapur-Patna-Muzaffarpur Pipeline for developing an integrated East Coast -West Coast LPG pipeline grid. Pumping station at Barauni and delivery facilities at Motihari is envisaged.

Brief Description of all CGD projects:The project involves laying, building, operating or expanding city or local natural gas distribution networks which includes supply of Piped Natural Gas (PNG) and Compressed Natural Gas (CNG) to domestic, commercial, industrial and transport sector.

Aurangabad, Kaimur & Rohtas Districts GA (Bihar) – 9th Round

Project Cost: Rs. 176 Cr

Bokaro, Hazaribagh & Ramgarh Districts GA (Jharkhand) – 9th Round

Project Cost: Rs. 613 Cr

Rewa District GA (Madhya Pradesh) – 9th Round

Project Cost: Rs. 177 Cr

Coimbatore Districts (Tamil Nadu) – 9th Round

Project Cost: Rs. 2998 Cr

Salem District (Tamil Nadu) – 9th Round

Project Cost: Rs. 1304 Cr

Srikakulam, Visakhapatnam & Vizianagaram Districts (Andhra Pradesh) – 9th Round

Project Cost: Rs. 2880 Cr

Araria, Purnia, Katihar and Kishanganj Districts (Bihar) – 10th Round

Project Cost: Rs. 988 Cr

Arwal, Jehanabad, Bhojpur and Buxar Districts (Bihar) – 10th Round

Project Cost: Rs. 439 Cr

Khagaria, Saharsa and Madhepura (Bihar) – 10th Round

Project Cost: Rs. 163 Cr

Lakhisarai, Munger and Bhagalpur Districts (Bihar) – 10th Round

Project Cost: Rs. 347 Cr

Muzaffarpur, Vaishali, Saran and Samastipur Districts (Bihar) – 10th Round

Project Cost: Rs. 2996 Cr

Nawada and Koderma Districts (Bihar & Jharkhand) – 10th Round

Project Cost: Rs. 169 Cr

Sheikhpura, Jamui and Deoghar Districts (Bihar & Jharkhand) – 10th Round

Project Cost: Rs. 303 Cr

Kurnool, Guntur & Prakasam Districts (Andhra Pradesh) – 11th Round

Project Cost: Rs.1420 Cr

Jammu, Udhampur, Reasi, Samba & Kathua Districts (Jammu and Kashmir) – 11th Round

Project Cost: Rs. 538 Cr

Beed, Jalgaon & Jalna Districts (Maharashtra) – 11th Round

Project Cost: Rs. 864 Cr

Pathankot District (Punjab) – 11th Round

Project Cost: Rs. 151 Cr

Jhunjhunu, Sikar & Nagaur Districts (Rajasthan ) – 11th Round

Project Cost: Rs. 576 Cr

Dharmapuri & Krishnagiri Districts (Tamil Nadu) – 11th Round

Project Cost: Rs. 503 Cr

Madurai, Theni & Virudhnagar Districts (Tamil Nadu) – 11th Round

Project Cost: Rs. 1327Cr

Kanyakumari, Tuticorin, Tirunveli Kattabo and Tenkasi Districts (Tamil Nadu) – 11th Round

Project Cost: Rs. 1294 Cr

East Mednipore, West Medinipore & Jhargram Districts (West Bengal) – 11th Round

Project Cost: Rs. 609 Cr

(A): LPG

Augmentation of LPG Import facility at Kandla

Project Cost: Rs 730.20 Cr

Brief Description:Augmentation of LPG Import Terminal from 0.6 MMTPA to 2.5 MMTPA at Kandla, Gujarat.

Benefits:Facilities planned are:

• 2 No Refrigerated Propane & Liquid Butane tanks 15000 MTs each including 6 nos In-tank Pumps.
• Provision of 2 No Mounded Bullets (600 MT Capacity), Flash Gas Compressor, Boiler and other facilities.
• LPG facilities incl. marine unloading arms at Jetty and provision of Cross-Country Pipeline from Jetty to Terminal.

Benefits:Augmentation of LPG import infrastructure on west coast to 2.5 MMTPA, which can be further augmented to 5.0 MMTPA with suitable jetty infrastructure and pipeline connectivity with Kandla Gorakhpur pipeline. The product can be transported to northern India as well as western region through road, rail and pipeline network which shall ease the bulk distribution across India.

LPG Import facility at Cochin

Project Cost: Rs 1,236 Cr

Brief Description:Major Facilities are:

• Multi-User Liquid Terminal Jetty with 2 nos. LPG Marine Unloading Arms, Blending, Dosing, Pumping and ancillary facilities.
• LPG Terminal facilities at 3.5 kms from Jetty with Bulk storage of Mounded Storage Vessels of capacity 4x1800MT for Propane, 4x2050MT for Butane & other ancillary facilities along with 8 Bay Tank Truck Lorry filling Bay and provision for pipeline transfer of the product.
• 20” Cross Country Pipeline from Jetty to Terminal

Benefit:The terminal shall augment our import capacity in southern region and enable seamless supply distribution in Kerala and adjoining states. Since, the LPG can be transported by pipeline as well, the transportation of bulk LPG shall be eased. Propane and Butane may be supplied even to the bulk customers which can be beneficial for the industries in the state.

LPG Bottling Plant at Jodhpur

Project Cost: Rs. 229.8 Cr

Brief Description: Construction of 120 TMTPA Capacity LPG Bottling Plant at Jodhpur on 50 acre land with 3x600 MT Mounded Storage Vessels, 2 x 24 point Electronic Filling System and associated facilities.

Benefit:Being located close to high demand centers of Jodhpur, Jaisalmer and nearby areas, the plant shall be able to cater the demand generated due to increase in LPG penetration as well as strengthen the LPG distribution system in Rajasthan.

LPG Bottling Plant at Kharagpur

Project Cost: Rs. 207.36 Cr

Brief Description:Construction of 120 TMTPA Capacity LPG Bottling Plant at Vidya Sagar Industrial Park near Kharagpur, with Mounded Storage Vessels, Electronic Filling System and associated facilities.

Benefit:Being located close to the highest demand centre of West Bengal i.e. Paschim Medinipur the plant shall be able to cater to the demand generated due to increase in LPG penetration as well as strengthen the LPG distribution system in West Bengal.

LPG Bottling Plant at Chittoor

Project Cost: Rs. 167.0 Cr

Brief Description: Construction of 120 TMTPA Capacity LPG Bottling Plant at Chittoor, Andhra Pradesh on 38 acre land with 3x600 MT Mounded Storage Vessels, 2 x 24 point Electronic Filling System and associated facilities.

Benefit:Being located close to high demand centers of Vellore, Nellore, Tirupati and Chittoor the plant shall be able to cater the demand generated due to increase in LPG penetration as well as strengthen the LPG distribution system in Andhra Pradesh as well as neighboring states.

LPG Bottling Plant at Khordha

Project Cost: Rs. 161.59 Cr

Brief Description:Construction of 60 TMTPA Capacity LPG Bottling Plant at Village- Somnathpur, Tehsil-Khorda near Bhubaneswar, Odisha on approx 32 acre of land with 3 x 600 MT Mounded Storage Vessels, 2 x 24 point Electronic Filling System and associated facilities.

Benefit:Being located close to high demand centers of Odisha i.e. Bhubaneshwar, the plant shall be able to cater to the demand generated due to increase in LPG penetration as well as strengthen the LPG distribution system in Odisha.

LPG Bottling Plant at Sitarganj

Project Cost: Rs. 160.09 Cr (net of ITC)

Brief Description:Construction of 120 TMTPA Capacity LPG Bottling Plant at Sitarganj, Uttarakhand, with Mounded Storage Vessels, Electronic Filling System and associated facilities.

Benefit:The plant shall be able to cater the demand generated due to increase in LPG penetration as well as strengthen the LPG distribution system in the state of Uttarakhand.

(B): OPS

Construction of Captive POL/LPG Jetty at Kamarajar Port, Chennai

Project Cost: Rs. 921 Cr

Brief Description:Development of captive POL-LPG Jetty including loading & unloading facilities for a total handling capacity of 5 MMTPA and associated administrative facilities in the onshore area.

Benefit:Ensuring positioning of product at proposed Vallur terminal to account for continuous petroleum supplies in Chennai and adjoining areas.

Grass root POL Terminal at Vallur, Chennai

Project Cost: Rs. 827 Cr

Brief Description:Construction of new grass root POL Terminal at Vallur with 131 TKL tankage and 16 bay TLF.

Benefit:Construction of new grass root POL Terminal at Vallur with 131 TKL tankage and 16 bay TLF.

Grass Root Rail-fed Depot at Sekerkote, Agartala as resitement of existing Dharmanagar Depot

Project Cost: Rs. 656 Cr

Brief Description:Grass Root Rail-fed Depot at Sekerkote, Agartala as resitement of existing Dharmanagar Depot.

Benefit:Grass-root Depot at Sekerkote (Agartala), Tripura as re-sitement of existing Dharamnagar Depot, Tripura with 20.6 TKL Product tankage, 2.5TLK Fire Water Tank with Fire Fighting System, 1x8 Bays TLF Gantry and Tank Wagon receipt facility

New Petroleum Storage Grassroot Terminal at Atchutapuram, Andhra Pradesh (Resitement): is commissioned and dedicated to the Nation.

Augmentation of Additional Facilities at Baitalpur, Uttar Pradesh commissioned and dedicated to the Nation.