Essar Purchases Stanloiw

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    Essar EnergyExclusivity Agreement and offer for Stanlow refinery

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    Disclaimer

    This Document does not constitute or form part of and should not be construed as, any offer or invitation to sell or issue, or any solicitation of any offer to purchase or subscribefor, any securities, nor shall it (or any part of it), or the fact of its distribution, form the basis of, or be relied on in connection with or act as any inducement to enter into, anycontract, commitment or investment decision whatsoever.This Document and any information made available orally or in writing at any presentation or delivery of this Document is confidential and should not be distributed, published,copied or reproduced (in whole or in part) or disclosed by its recipients to any other person for any purpose, at any time or in any form other than with the prior written consentof the Company. By accepting receipt of this Document, you undertake not to forward this Document to any other person, or to reproduce, copy or publish this Document, inwhole or in part, for any purpose.The information contained in this Document has not been verified by the Company, its advisers or any other person and may be updated, completed, revised and amended inany way without liability or notice to any person. No reliance may be placed by any person for any purpose whatsoever on the information or opinions contained or expressedin this Document or on the completeness, accuracy or fairness of such information and opinions.No undertaking, representation or warranty or other assurance, express or implied, is made or given as to the accuracy, completeness, sufficiency or fairness of the informationor opinions contained or expressed in this Document or any information made available orally or in writing at any presentation or delivery of this Document and, to the extentpermitted by law and regulation, no responsibil ity or liability, howsoever arising, directly or indirectly, is accepted by any person for any loss, cost or damage suffered orincurred as a result of the reliance on such information or opinions or otherwise arising in connection with this Document. In addition, no duty of care or otherwise is owed byany person to recipients of this Document or any other person in relation to this Document or any information made available orally or in writing at any presentation or deliveryof this Document. Recipients of this Document should conduct their own investigation, evaluation and analysis of the business, data and property described in this Document.The information and opinions contained in this Document, unless otherwise specified, are provided as at the date of this Document. Distribution of this Document does notconstitute a representation, express or implied, by the Company, the Group, or their respective advisers, affiliates, officials, directors, employees or representatives that the

    information contained in this Document will be updated at any time after the date of this Document. The information contained herein or any information made available orallyor in writing at any presentation or delivery of this Document is subject to change without notice and past performance is not indicative of future results. The Company mayalter, modify or otherwise change in any manner the content of this Document, without obligation to notify any person of such revision or changes. The information contained inthis Document has not been independently verified.Certain statements, beliefs and opinions contained in this Document or any information made available orally or in writing at any presentation or delivery of this Document areor may be forward-looking statements. Forward-looking statements can be identif ied by the use of forward-looking terminology, including, without limitation, the termsbelieves, estimates, anticipates, expects, intends, plans, goal, target, aim, may, will, would, could or should or, in each case, their negat ive or othervariations or comparable terminology. These forward-looking statements include all matters that are not historical facts. By their nature, forward-looking statements involve risksand uncertainties because they relate to events and depend on circumstances that may or may not occur in the future and may be beyond the Groups ability to control orpredict. Forward-looking statements are not guarantees of future performance and are subject to a number of risks and uncertainties. No representation is made that any ofthesestatements or forecasts will come to pass or that any forecast result will be achieved.Neither the Company, nor any member of the Group, or any of their respective affiliates or directors, officers, employees, advisers or representatives, provides any warranty,representation, assurance or guarantee, express or implied, that the occurrence of the events expressed or implied in any forward-looking statements in this Document or any

    information made available orally or in writing at any presentation or delivery of this Document will actually occur. You are cautioned not to place any reliance on these forward-looking statements. None of the Company or any member of its Group is under any obligation and expressly disclaims any intention or obligation to update or revise anyforward-looking statements, whether as a result of new information, future events or otherwise.Certain information included in this Document and/or information made available orally or in writing at any presentation or delivery of this Document relates to reserves,resources, capacity and other technical measurements. Such information is sourced from technical expert reports where possible or Group data. Such information is basedon engineering, economic, geological and other technical data assembled and analysed by the Group's staff, including engineers and geologists, and that data in certain casesis reviewed by third parties. There are numerous uncertainties inherent in estimating quantities and qualities in respect of such information, including many factors beyond theGroups control. No assurance can be given that the indicated amount of reserves or resources will be recovered or that the Group's assets can continuously operate at thecapacities indicated.By accepting or accessing this Document or attending any presentation or delivery of this Document you agree to be bound by the foregoing limitations and conditions and, inparticular, will be taken to have represented, warranted and undertaken that you have read and agree to comply with the contents of this notice.

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    Summary

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    Summary

    Essar Energy signs exclusivity agreement with Shell

    Offers to buy Stanlow refinery for US$350m in cash

    High complexity, large scale refinery positioned to thrive in UKmarket

    Provides optionality for export of high quality products to the UKfrom Vadinar refinery in India

    Competitive acquisition price

    Enhances Essar Energys competitive position: focused on quality andgrowth

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    Key Transaction Details

    Essar Energy signs exclusivity agreement for Shells Stanlow refinery and associated assets

    Essar Energy to sign asset purchase agreement by 31 March 2011 or pay break fee of

    US$50 million

    Shell has 3 further business days to sign asset purchase agreement or pay break fee ofUS$10 million

    Consideration US$350m cash, with staged payments of US$175m on closure and US$175mplus interest at end of first year, following closure

    Shell to supply crude oil to the refinery for five years

    Stanlow Refinery to sell approximately 50%-60% of refined products to Shell for up to 10years, depending on product

    Separate payment for crude and refined products/inventory at time of closure (circa US$780million)

    Consideration from internal cash resources and potentially a new debt facilityInventory to be funded predominantly through a working capital facility to be put in place byEssar Oil UK, prior to completion.

    Expected to be earnings enhancing within the first year

    Transaction expected to close in the second half of 2011

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    Nothing in this announcement is or is intended to be a profit estimate for any period or a forecast of future profits and any statements relating to earningsaccretion should not be interpreted to mean that Essar Energys earnings per share for the current or future financial periods will necessarily match orexceed its historical published earnings per share

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    UK Refinery Landscape: Stanlow is a Quality Asset

    Stanlow is the 2nd largest UK refinery by capacity and with Nelson Complexity

    of 8.2

    UK total refining capacity of circa 90mmtpa, of which more than half currentlyfor sale, sold or closed

    Opportunity for Essar Energy to purchase a high quality asset

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    Refinery OperatorNameplateCapacity(MMTPA)

    Connectivity

    Fawley Exxonmobil 16 Pipeline, Water, Rail, Road

    Stanlow Shell 14 Water, Pipeline, Road, Rail

    Humber Conocophillips 11 Water, Pipeline, Road, Rail

    Pembroke Chevron 10 Water, Road, Rail

    Grangemouth Ineos 10 Pipeline, Road, Rail

    Coryton Petroplus 11 Water, Pipeline, Road, Rail

    Lindsey Total 11 Water, Pipeline, Road, Rail

    Milford Haven Murco 6 Water, Pipeline, Road, Rail

    Teeside Petroplus 5.8 Water, Pipeline, Road, Rail

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    0

    2

    4

    6

    8

    10

    12

    14

    (10,000) 40,000 90,000 140,000 190,000 240,000 290,000 340,000 390,000 440,000

    NC

    F

    Capacity (bbl/day)

    Stanlow: In Top Tier of EU Refineries by Capacity and Complexity

    Refinery capacity vs. Nelson Complexity Factor (Western Europe)

    Source: OGJ 2009

    Stanlow

    Suitable high volume product mix

    The talent of its employees and current managers

    Technical efficiency of the plant equipment

    Compliant with safety standards

    Proximity to high value product markets

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    8439

    8140

    33763307

    1987

    1182

    861

    678

    417

    322

    364

    144

    0

    200

    400

    600

    800

    1000

    0

    1,000

    2,000

    3,000

    4,000

    5,000

    6,000

    7,000

    8,000

    9,000

    Vlissingen from Totalto Lukoil, 2009:

    190,000 b/d

    Coryton to Petroplusfrom BP 2007:172,000 b/d

    Ruhr Oel to Rosneftfrom PDVSA, 2010:

    500,000 b/d

    Milford Haven toMurphy Oil from Total,

    2007: 108,000 b/d

    Petit Couronne andReichstett to Petroplusfrom Shell, 2007: total

    239,000 b/d

    Stanlow to Essar fromShell, 2011: 296,000

    b/d

    US$ per barrel complexity adjusted capacity (excluding inventory) (RHS)

    Stanlow mostcompetitively

    priced of recent

    transactions

    Competitive Acquisition Price vs. Comparator EU deals

    8

    US$ per barrel daily throughput capacity (excluding inventory) (LHS)

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    Leading Market Position in National Supply Envelope

    9

    Teesside - closed

    Humber

    Lindsey

    Coryton

    Stanlow

    Liverpool

    Mcr. Airport

    Newcastle upon Tyne

    NWNE

    CC

    South

    WestSE-WL

    SE-Thames

    Kingsbury

    Manchester

    HeathrowAvonmouth

    Buncefield

    Fawley

    Pembroke

    Milford Haven

    Main Line

    Government Pipeline

    Finaline

    UKOP North

    UKOP South

    ESSO Midline

    Manchester Jetline

    The UK Energy Corridor

    KEY

    The North West and Central Corridor

    100-250 kbpd

    >250 kbpd

    REFINING CAPACITY Advantaged location

    Positioned to serve the UKEnergy Corridor

    Natural supply envelope

    North West and Midlands

    Leading supply position

    Supported by integration intoextensive pipeline logistics andgood road links

    Birmingham

    UK Refining Overview

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    Refinery Overview

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    Stanlow Refinery Overview

    Located on south side of the Mersey estuary near Ellesmere

    Port Nameplate capacity 296,000b/d

    Currently operating at around 220,000b/d

    Nelson Complexity 8.2

    Accounts for circa one sixth of UK petrol other mainproducts diesel and kerosene for aircraft fuel

    Crude oil received at Tranmere oil terminal on the Merseyand transferred by pipeline to Stanlow

    Stanlows finished products are distributed as follows:

    20-25% by pipeline via the northern end of the United KingdomOil Pipeline (UKOP) running to Shell Haven on the Thames

    Circa 55% by road from the loading terminal at Stanlow

    Circa 20% by ship, via the Manchester Ship Canal

    650 hectare site11

    Stanlow is the UKs

    second largest refineryby capacity and has the

    complexity to thrive in UKmarket

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    Superior Assets

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    Complex site

    with deep

    conversion

    Largest residue

    cat crackerwithin the Shell

    group

    Integrated base

    oil plant

    Comprehensive

    petrochemical

    linkages

    CD3

    CD4

    Platformer

    HVI Lube OilUnit

    AromaticsExtraction

    GasolineBlender

    Merox

    Propylene

    Splitter

    Fuel Oil Blender

    Alkylation

    Ethyleneimport

    Crude Ethyl Benzene

    Shell HigherOlefins Process(SHOP)

    Alcohols (SHF)

    RefineryLubesChemicalsRetained by Shell

    KEY

    Fuel gas

    LPG

    Alpha OlefinsInternal Olefins

    Alcohols

    Gasoline

    Toluene

    Benzene

    Ethylbenzene

    Jet

    Gasoil

    Propylene

    Fuel Oil

    Base Oils

    Bitumen

    Cat Cracker

    Gas Oil HDS Gas Oil Blender

    PRODUCTS

    Process Overview

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    Site Configuration: Key Process Units

    13

    UNIT TECHNOLOGY BUILD YEARCAPACITY

    (KT/D(KB/D)

    T/A CYCLE(Years)

    T/ADURATION

    (Days)

    Crude Distillation(x2)

    CDU Shell 1965/1973 39 296 3.5/6 33/36

    CCR Platformer PF3 UOP 1984 4.1 35 6 14

    AromaticsExtraction

    U53 UOP 1974 2.6 19 7 30

    Ethyl Benzene Unit EBU Badger 1991 0.6 4.5 3 42

    Alkylation Alky UOP 1989 1.3 12 3.5 45PP Splitter PPS Shell 1989 0.8 10.4 3.5 35

    GasoilDesulphurisation

    HDS Shell 1968 8.0 60 1.5 34

    Residue CatalyticCracker

    FCC Shell 1988 11 76 3.5 35

    Luboil High VacuumUnit

    HVU Shell 1969 3.2 21.6 5 34

    DistillateHydrotreater

    HDT2 Shell 2001 (1) 2.5 19.1 3.5 30

    NaphthaHydrotreater

    HDT3 Shell 1984 4.1 35 3.5 34

    CD Hydro CD_H CD Tech 2004 3.4 23 3.5 35

    HD Select HD-Sel CD Tech 2004 1.9 13 3.5 35

    1 Revamp

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    Yield Profile

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    TYPICAL YIELD High Nelson complexity of 8.2 enableshigh black to white oil conversion

    Fuel oil production is significantlylower than industry norm

    Since early 2009, gas-to-liquidimports has supported increased jetand diesel production

    Speciality grades

    Production of lubricants base oils,differentiated fuels and bitumen is adifferentiator to marker margins

    Bitumen, although minimal to date,has been significantly expanded tocapture higher value product as wellas creating a sulphur sink formedium sulphur crudes

    Chemical grades offer significantupgrading

    Propylene sold via pipeline to anupgrading customer within the UK

    Ethylbenzene is sold to Shells

    Moerdijk Plant in the NetherlandsNote: Included within refinery fuel and loss is up to 0.8% of total yield that is

    consumed in units to be retained by Shell

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    Strong Personal Safety Performance

    15

    RECORDABLE INJURY FREQUENCY

    Accountability for personal safety

    at all levels in the organisation

    Comprehensive HSE Management

    Systems

    Embedded culture of learning from

    incidents and near misses

    Strong Contractor safety culture

    Joint ownership of the

    responsibility for safety on site

    Supporting processes developed

    in line with Global Shell learning

    Frequency per million man hours

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    Financials

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    Stanlow Financial Summary

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    US$000 FY 2008 FY 2009 H1 2010

    Refinery Intake Volumes (000bbl) 73,351 72,883 29,121

    Sales 9,688,747 5,365,232 2,520,843

    Gross Margin 615,755 244,847 144,140

    Operating Expenses (198,154) (184,120) (81,404)

    EBITDA 417,601 60,727 62,736

    Gross Refining Margin (US$/barrel) 8.4 3.4 4.9

    IEA benchmark GRM (US$/barrel) 4.9 1.3 2.7

    Headcount ~960 FTEs

    During the first six months of 2010 some of the units at the Stanlow Refinery were not operational for 50 days due to a planned refinery turnaround outage.

    The above results have been prepared to present the normalised and standalone operations of Stanlow. Historically, Stanlow did not exist as a separate legal entity and hencethe results of Stanlow were not available on a standalone basis. The above results have been prepared by extracting/ carving out financials from various entities afterconsidering various standalone and normalisation adjustments. These adjustments relate to transaction scoping and future structure of the business, accounting categorisationvs. that followed generally, transfer pricing arrangements proposed, changes to pension plan, planned and unplanned shutdowns, one off items, CSO income etc. Further,results as presented above are based on replacement cost basis (current cost of supply basis) and are on constant currency basis.

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    Stanlow Funding Plan

    Stanlow acquisition to be funded from internal sources andpotentially a new debt facility

    Working capital will be funded predominantly through a newworking capital facility to be put in place by Essar Oil UK, prior tocompletion.

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    Focus on Quality and Growth

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    Refining Capability

    20

    0

    200,000

    400,000

    600,000

    800,000

    1,000,000

    1,200,000

    Vadinar and KenyaPetroleum current

    throughput

    Vadinar phase I bymid-2011

    Stanlow by mid-2011 Vadinar optimisationby Sept 2012

    Vadinar phase II - inthe future

    Vadinar current Vadinar phase I Stanlow

    Vadinar optimisation Vadinar phase II Kenya Petroleum

    Barrels of crude daily throughput capacity

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    Summary

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    Summary

    Essar Energy signs exclusivity agreement with Shell

    Offers to buy Stanlow refinery for US$350m in cash

    High complexity, large scale refinery positioned to thrive in UKmarket

    Provides optionality for export of high quality products to the UKfrom Vadinar refinery in India

    Competitive acquisition price

    Enhances Essar Energys competitive position: focused on quality andgrowth

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