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    IGCC for Power generation

    N.T.P.C GAS PLANT DADRI

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    Total installed capacity over 1,00,000 MW

    Thermal power generation has emerged as theprincipal source of electric power in Indiacontributing to about 70%

    Coal fired thermal stations are inpredominance and share about 84% of thetotal thermal installed capacity.

    It is prudent and economical to developmethods and process for efficient utilization oflow-grade Indian coals for power generation.

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    Gasification of coal is the cleanest way of utilizationof coal, while combined cycle power generation givesthe highest efficiency.

    Integration of these two technologies in IGCC power

    generation offers the benefits of very low emissionsand efficiencies of the order of 44-48%.

    The comparative indices show that in case of IGCC,

    emission of particulate, NOx and SOx are:7.1%, 20% and 16%, respectively, of thecorresponding emissions from PC plant.

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    Environmental performance of IGCC thusfar exceeds that of conventional and evensupercritical plants.

    Three major areas of technology that willcontribute to improvements in IGCC are :

    hot gas de-sulfurisation

    hot gas particulate removal advanced turbine systems

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    Commercialization of IGCC needs technologydemonstration at an intermediate scale of about

    100 MW to address the issues such as:hot gas clean ups and system optimization and

    to establish reliability and performance.

    This would also enable to design an optimummodule for air blown gasification, which inmultiples would constitute a commercial sizeplant in the range of 300-600 MW.

    The present study addresses these issues andsuggests suitable technologies for Indian Coals.

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    VISION 2020

    PROGRAM

    Post combustion Clean-up-Desulfurization

    (FGC systems) Supercritical

    In-combustion Clean-upFluidized bed

    combustion (CFBC,PFBC, AFBC)

    Gasification using +fluidized bed, moving bedor Entrant bed Gasifiers

    Pre combustion Clean-up beneficiation/washing

    Technologies for utilization of Coal for Power Generation with minimalpollutants discharged to the atmosphere (Reduced CO2, Sox, Nox,

    SPM) at high conversion efficiency.W.C.I.

    CLEAN COALTECHNOLOGIES

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    Gasifier Gas Cleanup Gas turbine

    HRSG Steam TurbineSteam

    Hot Gas

    Power

    BFW

    Steam Flue Gas to Stack

    Steam

    Coal

    Ash Sulfur Air

    Fuel gas

    Compressed Air

    Schematic Layout of the

    Integrated Gasification Combined Cycle

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    Comparison of various Power PlantsPower Plant

    ConceptsMajor Components Efficiency %

    Cost per

    MW (Rs.

    Crore/MWPC fired

    Thermal

    Boiler, Steam turbine, Coal

    handling and other BOP34-37 3.8-4.0

    CC PlantGas turbine, Steam turbine, Waste

    hear recovery boiler40 3.2-3.4

    IGCC (Coal)

    Coal preparation unit, gasifier,

    steam turbine, Gas cleaning GT,

    WHTSG

    46* (estimated) 4.86-4.95**

    IGCC (Pet

    Coke)

    Air separation unit GT, ST,

    WHRSG, Gas Clean up

    48* (with G/H

    class Gas

    turbines)

    4.25-4.30**

    Super CriticalAs for PC fired Thermal plus spiral

    tubes and high temp alloys37.5-39.5 3.95-4.10

    * High efficiency coupled with low emission (SPM: 7%,

    Sox:16%, Nox:21% of corresponding PC Plant)

    ** For Indigenous Units through systematic transfer of Technology

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    Identified R&D Areas are:

    Process optimization of selected gasificationprocess

    Improvement of design and reliability of plantcomponents & Resource Optimization

    Optimization of overall plant heat integration and

    layout

    Hot gas cleanup

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    COAL GASIFICATIONSELECTION OF

    GASIFICATION PROCESS

    The fluidised bed process has many technical and environmentaladvantages over the moving bed process, such as,

    The fluidised bed can use any amount of fines whereas inthe moving bed only 10% of fines can be used.

    In the fluidized bed process, hydrocarbon, liquid by-products such as tar, oil and gas-liquor are not producedand, hence, the pollution is reduced.

    High ash coals can also be successfully gasified in thefluidised bed.

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    BENEFITS EXPECTED FROM IGCC

    India endowed with large coal reserves over 200 billion

    tonnes.

    Environmental benefits due to higher efficiency ofconversion and reduced SPM, SOx, NOx levels can be

    achieved using coal based IGCC technology.

    Retrofit/Re-power options for gas based CCGT plantsby installing only coal based gasifiers are cost effective

    (opportunity cost low) and are environmentally benign.

    Adoption of IGCC technology in India has Global aswell as National benefits.

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    IGCC DEVELOPMENT PROGRAM IN INDIA

    Pioneering work on IGCC development in India taken upby BHEL in early eighties.

    Major Mile Stones

    Choice of gasification for high ash coals by BHEL

    6.2 MW IGCC demonstration plant established by BHELboth with moving Bed and Fluidized bed.

    Coal characterization by BHEL & IICT for gasificationapplication.

    Intensive data generated by IICT on oxygen-steamgasification in their moving bed gasifier.

    Task force CEA, CSIR, NTPC & BHEL constituted toassess technological maturity & financial requirement fora green field IGCC plant of 100 MW capacity at Dadri(NTPC).

    BHEL, CSIR & NTPC prepared proposal for setting up ofthis 100 MW IGCC demonstration plant.

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    Experience on the fluidized bed process is,very limited in the country.

    Internationally, the experience gained so far isonly for low ash coals.

    Thus there is a need for taking up extensiveR&D on IGCC Pilot Plant using high ash (40-50% Ash) Indian Coals.

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    Technology-related issues in IGCC

    Design of Advanced gasifiers (optimum gas

    composition, optimum scale-up etc.)

    Hot gas cleaning (de-sulphurisation and particulateremoval)

    Advanced gas turbines (blade design to sustain ash

    laden gas)

    CO2 emission abatement in IGCC Power Plants

    Operating conditions of IGCC plants in transient stage

    Configuration of an optimized system for IGCC

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    Fuelrelated issues

    In a Raw Pet-Coke and refinery residue based IGCC Plant

    System optimization, particularly the balance of plant

    Optimized Heat balance diagrams

    Scaling up of gasifiers to optimum size

    In a Coal/Lignite based IGCC Plant Process & Plant conceptual design

    De-sulfurization of syngas of high sulfur coal and lignite

    Optimized Heat balance diagrams

    Super critical Vs IGCC in Indian context

    Application of ASME PTC-47 code for IGCC for high ash coals and

    lignite

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    SOME IMPORTANT FINDINGS

    Reactive solid sorbent de-sulfurization combined with hot

    gas cleaning through ash and sorbent particle removal

    provides for higher energy efficiency to an extent of 4-7%.

    The current Capital cost of building an IGCC power plant is

    of the order of Rupees 6 crore/ MW.

    Improvements in hot gas cleaning coupled with Cycleoptimization shall bring down the cost drastically to a level

    of $ 1000/kW or about Rupees 4.5 crore/MW

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    The efficiency of refinery bottom based IGCC unit will be about2% higher than that of coal based IGCC unit.

    Refinery based IGCC plants - Advantages

    Co-generation of steam

    Co-production of hydrogen gas & recovery of sulfur element

    No use of limestone, as required for CFBC technology

    No requirement of extra land for disposal of solid waste

    In the long run the refinery based IGCC technology is equallyattractive to coal based IGCC from economic andenvironmental considerations.

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    SOME FINDINGS RELATED TO

    COMMERCIALIZATION OF TECHNOLGOY

    At present it may be prudent to implement the project in

    phased manner to absorb the risk of gasifier in the total

    project wrap-up guarantees fig. 1

    A Technology Transfer model for determination of velocity

    of Transfer of Technology (TOT) is an useful tool for TOTof a frontier technology from a developed economy to a

    developing economy fig. 2

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    Typical results of the velocity of TOT are : -

    (With year 2000 as base)

    IGCC (oxygen blown) - Pet cokeNormal pace ---- 5 years

    Accelerated ---- 2 years

    (Fig 3)

    IGCC (Air Blown) ---- Coal

    Normal pace ---- 7 years

    Accelerated ---- 5 years

    ( Fig 4)

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    Fig. 1

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    Fig. 2

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    Fig. 3

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    Fig. 4

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    Fig.5 EFFICIENCY IMPROVEMENT FORECAST

    CONVENTIONAL Vs IGCC

    60

    55

    50

    45

    40

    35

    301990 1995 2000 2005 2010

    Year of commercial use

    NetTherm

    alEfficiency(%)

    Ceramic gas

    turbine

    566 Co600 Co

    623 Co1300 Co 1500 C

    o

    540 Co

    650 Co1184 Co

    IGCC (15 C Amb)IGCC (Indian Condition)

    Super Critical PC Power Plant (15 C Amb.)o

    Super Critical PC Power Plant (Indian Condition)o

    Sub Critical PC Power Plant (Indian Condition)

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