Baselinebofgaselectgeneration Sharma&Shrestha

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    Case Study 1: Basic Oxygen

    Furnace (BOF) Gas based

    Electricity Generation

    S. Kumar, S. Sharma and R.M. Shrestha

    Asian Institute of Technology

    4 April 2005

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    To provide the background of Case study 1

    Project description Baseline Methodology description

    The project details Baseline Methodology

    Methodology: Applicability conditions

    Identification of Baseline scenario

    Additionality

    Project Boundary Baseline formulae

    Leakage

    Emission reductions

    Data Sources and Vintage

    Presentation

    Objective

    Presentation

    Outline

    Presentation Objective and Outline

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    INTRODUCTION

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    World steel production 965 million metric tonnes (mmt)((63.3% by BOF)

    China (1st) 220.1 mmt; Japan 110.5 mmt; USA 90.4 mmt

    India (8th) 31.8 mmt (48.7% by BOF process)

    Total production for the Asian region was 41.4 mmt, a rise of

    10.3% on February 2004.

    China produced 24.8 mmt of crude steel in February, up21.2% on the same month in 2004.

    Source: http://www.worldsteel.org/media/wsif/wsif2004.pdf

    SOME STEEL DATA

    2003

    Feb.

    2005

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    The Jindal Vijayanagar Steel Plant (JVSL) is the mostmodern, technologically efficient and eco-friendly

    integrated steel plant of its kind, and uses therevolutionary Corex technology.

    The Plant has a hot rolling capacity of 2.5 million tpa.

    During the production of steel using BOF process, CO is produced.

    This has a calorific value of about 2,000 kcal/Nm3

    . This gas is currently flared.

    It is proposed to collect and use this gas

    as a fuel in a power plant to produce electricity. The electricity to

    be supplied to the state grid (about 95 GWh per year). The

    power plant currently uses coal.

    as a fuel for internal heating requirements of the plant

    It is estimated that the primary emission reductions would amount

    to 575,967 tonnes of CO2 during the 10 year crediting period.

    Source: http://www.jvsl.com/; Project Document

    SOME PROJECT DATA

    http://www.jvsl.com/http://www.jvsl.com/
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    BOF gas, 2000

    Kcal/NM3

    Used as fuel for heat

    Power Plant(i) Supply to existing power plant (sister concern)

    no capacity increase (BASE: only coal); &

    (ii) Few New proposed power plant supplying to grid

    PROJECT:Gas Collection,cleaning, storage

    and distribution systemBase Case: Flared

    PROJECT DESCRIPTION - SCHEMATIC

    STEEL

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    7Source: http://www.energymanagertraining.com/iron_steel/Iron_Steel_process.htm

    BOF GAS

    BASIC OXYGEN FURNACE (BOF) OPERATION

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    8http://www.mapsofindia.com/states/index.html

    .VSNL Plant

    540 km

    460 km

    PROJECT LOCATION

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    BASELINE

    METHODOLOGY

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    Methodology: Applicability conditions Part of waste gas used for internal heating requirements within the

    steel manufacturing industry, and remaining waste gases wouldnormally have been flared in the absence of the project activity;

    Project activity does not induce diversion of waste gases required forinternal usage, to project activity;

    No change in process except changes due to collection, stabilizationand transportation of waste gases to electricity generators;

    No local regulations/ programmes to constrain use of GHG intensivefuels (like coal), nor any regulation making use of waste gasesmandatory; and

    Project activity results in supply of electricity to local grid, excludinggrids with surplus power, unless cost of generation and supply isfavourable for inter-grid transfers.

    Though not stated methodology applicable to project that supplies gas to Existing power plant with no expansion of capacity, or

    Existing power plant with gas meeting requirement of capacity expansion, or New power plant supplying to grid.

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    Identification of Baseline Scenario

    Approach 48(a) existing actual or historical.

    The baseline scenario (ie. in the absence of the

    proposed project activity) has the following

    components: Flaring of excess BOF gas

    In absence of use of BOF gas for electricity generation

    use of more GHG intensive fuels for generation of additional

    electricity at the existing power plants leading to emission ofGHG (Case I); and

    need to establish new power plants to meet any shortfall in

    supply, with possibility of further GHG emission (Case II).

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    Identification of Baseline Scenario

    Case I: Partial replacement of existing GHG intensive fuel in anexisting power plant (no generation increase).

    The baseline scenario is therefore continued use of theGHG intensive fuel.

    Baseline: GHG intensity of existing power plant.

    Case II: Use of waste gas to generate additional power in existing

    power plant and/ or generate power in new powerplant(s).

    The baseline scenario in this case is electricity wouldhave otherwise been generated by the operation of grid-connected power plants and by addition of newgeneration sources.

    Baseline: Combined Margin grid intensity based onACM0002 methodology.

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    Additionality

    Use of Tool for assessment anddemonstration of Additionality Investment analysis

    investment comparison analysis using a financialindicator (such as IRR, NPV,cost benefit ratio,levelized cost of electricity generation or Rs./kWhvalues), and checking whether there is at least oneidentified alternative which is better for investment thanthe project activity.

    The chosen alternative to the project is flaring of thewaste gases, and purchasing power from the grid. Thecost of power in the alternative scenario in comparisonto the project activity is Rs 1.94/kWh.

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    Project Boundary

    Source: Project Document

    This includes points of generation of waste gases in steel mfg operation,

    stabilisation, cleaning and transportation of these gases to the power plant

    through a gas handling network, delivery of power to grid, and all associated

    equipment for such project activity, under the control of the projectproponents.

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    Baseline Case I: Formulae usedPartial replacement of existing GHG intensive fuel in an existing

    power plant (no generation increase).

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    Baseline Case 2: Formulae Used

    Operating Margin

    Build Margin

    The sample group m consists of either: five power plants that have been built most recently [including plants under

    construction], or

    power plants capacity additions in the electricity system that comprise 20%

    of the system generation (in GWh) and that have been built mostrecently [including plants under construction].

    Use of waste gas to generate additional power in existing powerplant and/ or generate power in new power plant(s).

    L k

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    Leakage Due to use of displaced hydrocarbon fuel by other smaller power

    generators who currently use renewables. However, in cases where there could be demand for power, such

    possibilities are ruled out since this would necessitate replacementand use of alternate power generating technology, which may not befeasible for a smaller generator.

    Diversion of waste gas use to producing electricity rate of waste gas generation fixed a priori, and the waste gas utilisation for internal heating and steam generation

    cannot be less than the sectoral average in the country or region

    CF: Correction Factor for gas quantity eligible for emissionreduction = Minimum[(X-Z), Y, W] / W Y : minimum quantity of waste gases flared in the steel manufacturing

    industry (average of sector during the last 3 years)

    Z: average amount of waste gases used for internal requirements ofall waste gas generators (in similar steel manufacturing sector) in theregion or country during the last 3 years

    X: the minimum quantity of waste gases generated in the steelmanufacturing industry sector during the last 3 years, and

    W: waste gas supplied to power plants

    If the steel industry sector values for X,Y and Z are not available, thenCF = 1

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    Emissions Reductions

    In existing power plant where only fuel replacementoccurs ERy(1) = Baseline I * CF PEy

    In existing power plant where fuel replacementoccurs along with additional power generation ERy(2) = (Baseline I + Baseline II)* CF PEy

    In a Greenfield power plant connected to the grid orapproximate emission reduction ERy(3) = Baseline II* CF PEy

    If more than one of the above occurs, thenERy(4) = (Baselinei * CF) - PEy

    Note: PEy = 0

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    Data Sources and Vintage

    Fuel

    Consumption, Calorific value, heat rate: Proprietary data Emission factor : IPCC

    Heat Rate : Proprietary data

    Electricity delivered: Regional Electricity Board

    Waste Gas: Proprietary data

    Local level data: 3 years old or of lesser vintage

    Regional level data: 5 years vintage

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    Next .

    Basic information regarding the project has beenpresented

    Whether the Methodology has been completelydefined

    Transparency and Conservativeness has been taken

    into account

    Is the Methodology correctly applied

    Thank You