Coal Gassification Fm Korea

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    Day 2 Tuesday 16 October 2007

    Session 8: FBC/ USC/ IGCC/ CCS

    Speech 5 Korea

    Analysis of 3-TPD Coal Gasification System in Korea

    Dr. Hyung Taek Kim

    Professor

    Division of Energy System

    Ajou University

    Korea

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    Status of IGCC R&D Program in Korea< Operation Experiences of 3 TPD Gasifier Systemand Planning of 300 MW Demonstration Plant >

    October 2007Hyung-Taek Kim, Ph.D.

    Professor in Energy Engineering, Ajou UniversityExpert Advisor, Korea Energy Management Corporation

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    Introduction

    Pilot-scale 3 TPD Gasification System Plant Description

    Results of Continuous Run

    Criteria for the Candidate Coal Selection

    National Program of Demonstration IGCC Plant

    Background Present Status

    Summary

    Contents

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    IntroductionIntroduction

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    Why coal now? Remaining Ultimate Recoverable Fossil Fuel Resources

    Source : Shell Coal Gasification Process, Chhoa, 2003

    OilConventional Unconventional

    Natural Gas Coal

    551012 toe.71012 toe 4.41012 toe 1.71012 toe

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    International Utilization Sector of Coal

    Amount of Coal Utilization in Power Generation is steadily increase. Requirement of Low-Pollution, High-Efficiency CCT.

    69%

    12%16%

    3%

    2002

    Powergeneartion

    Other

    Industry

    Residential

    3%

    79%

    8%

    12%

    1%

    2030

    Power

    geneartion

    OtherIndustry

    Residential1%

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    Conceptual Process of IGCC

    Gasifier Systemasifier SystemGasifierasifier

    Coal

    Slag

    A S US UOxygen

    SyngasPurificationSystemSyngasPurificationSystem

    Combined Cycleombined CycleS/T PowerGenerationS/T PowerGeneration G/T PowerGenerationG/T PowerGeneration

    Steam

    Sulfur

    Air

    Electricity

    HeatExchangerHeatExchanger

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    Application Area of Gasification Technology

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    CO2 Reduction with Different Fuels in Power Plant

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    Comparison of Pollutant Emission IGCC Process emits minimal amounts of pollutant. IGCC recognized as future power plant option.

    SOx ( ppm ) NOx ( ppm ) Particulate( mg/Nm3 )Emission standards 100 250 40

    Boryung Power PlantP.C. 502 227 176

    P.C. + FGD 150 200 40

    Demkolec IGCC 15 63 1.5

    Wabash IGCC 7 32 6.6

    Vacuum Residue IGCC 84 ( * ) 33 4

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    Pilot-scale3 TPD Gasification SystemPilot-scale3 TPD Gasification System

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    Process & Flow Diagram of Gasification System

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    Initial Operation Condition of Gasifier

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    Operation Data of Gasification (Baiduri, 26 atm.)

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    Gasification of Baiduri (Gas Composition)

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    Gasification of Baiduri (Efficiency)

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    Carbon Conversion (Baiduri, 26 atm.)

    - P.C.(as-feed) : 585 kg(M : 3.58%)- P.C.(dry) : 564kg (C : 69.93%)- Input Carbon : 394kg (C : 100%)

    - Slag : 11.0 kg (C : 0.31%)- Carbon in Slag : 0.034 kg (C : 0.009%)

    - Fly ash 1(Cyclone 1, dry) : 0.23kg(C: 11.15%)- Carbon in Cyclone 1 : 0.026kg (C : 0.007%)

    - Fly ash 2(Cyclone 2, dry) : 0.49kg(C: 28.23%)- Carbon in Cyclone 2 : 0.138kg (C : 0.0035%)

    - Fly ash 3(Scrubber, dry) : 0.04kg(C: 34.34%)- Carbon in Scrubber : 0.0137kg (C : 0.003%)

    Carbon Conversion : 99.95%Carbon Conversion : 99.95%

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    Operation of 4 Day Period

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    Carbon Conversion, Cold Gas efficiency

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    Elemental Analysis of Coals Used

    54.4

    71.45 70.6172.96

    67.08 63.04 68.0870.77 74.15

    01020304050607080

    Usib

    ell

    Cyprus

    Dray

    ton

    Curra

    g

    Daton

    Kide

    co

    Adaro

    Baid

    ur

    Deniso

    vsk

    C H O N S Ash

    (53

    04kc

    al/kg)

    (60

    80kc

    al/kg)

    (65

    56kc

    al/kg)

    (66

    14kc

    al/kg)

    (66

    08kc

    al/kg)

    (5670

    kcal/kg)

    (67

    48kc

    al/kg)

    (6367k

    cal/k

    g)

    (71

    39kc

    al/kg)

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    Ash Fusion Temperature (Reducing State)

    100011001200130014001500160017001800

    Usib

    ell

    Cyprus

    Dray

    ton

    Curra

    g

    Datong

    Kide

    co

    Adaro

    Baid

    ur

    Deniso

    vsky

    AhFoempaue(C

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    Classification of Candidate Coal

    0.0

    0.5

    1.0

    1.5

    2.0

    2.5

    3.0

    1100 1200 1300 1400 1500 1600

    Zone A

    Zone B

    Zone C

    Zone D

    A : Australia

    CA : Canada

    CH : China

    IN : Indonesia

    J : Japan

    R : Russia

    S : South Africa

    U : USA

    : 3/ (/)

    : 2/ ()

    Ash Fusion Temp.

    FuelRat

    io

    (FC/VM)

    CH)

    Black Water (A)

    Kleinkopje (S)

    South Black Water (A)

    Blair Athol (A)

    Moura (A)

    Warkworth (A)

    Lemington (A)

    Ulan (A)

    Ermelo(S)

    Wambo (A)

    Pittsburgh (U)

    Plateau (U)Drayton(A)

    Denisovsky(R)

    Curragh(A)

    (J)

    Usibelli(U)

    Baiduri(IN)

    Cyprus(A)Obed (CA)

    Adaro(IN)

    Illinois #5 (U)

    Drayton (A)

    (CH)

    Coal Valley (CA)

    Kideco(IN)

    Datong (CH)

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    Characteristics of Zone A Coal

    Usibellicausingfoulingproblems inheatexchanger

    ref.

    Evaluation for Gasifier

    Cyprus (USA)

    Baiduri(Indonesia)

    Kideco(Indonesia)

    Usibelli (USA)

    Korea(3T/D)

    Coal

    smallasy

    smallasy

    smallasy

    smallasy

    CharFormation

    SlaggingPotential

    60~755~100O : 55~60H2 : 30~35

    60~703~100O : 60~67H2 : 22~33

    60~750~100O : 50~70H2 : 20~28

    60~700~100O : 60~65H2 : 20~28

    Cold GasEfficiency

    CarbonConversion

    GasComposition

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    Flyslag Fouling in the Exit section of Gasifier

    Coal : Alaska UsibelliOperating Pressure : 15 kg/cm2

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    Characteristics of Zone B Coal

    CO : 60~65H2 : 20~30

    GasCompositionref.

    Evaluation for Gasifier

    relativelysmallasyatong (China)orea

    (3T/D)

    CharFormationSlaggingPotential

    Coal

    60~700~100

    Cold GasEfficiencyCarbonConversion

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    Characteristics of Zone C Coal

    needflux

    ref.

    Evaluation for Gasifier

    CO : 60~70H2 : 30~35

    GasComposition

    relativelyhighifficultyrayton

    (Australia)Korea(3T/D)

    CharFormationSlaggingPotentialCoal

    63~700~100

    Cold GasEfficiencyCarbonConversion

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    Denisovsky (Russia)

    Characteristics of Zone D CoalEvaluation for Gasifier

    inadequatecoal forgasificationNeed char

    recycle

    ref.

    CO : 55~60H2 : 20~25

    CO : 60~65H2 : 18~22

    GasComposition

    40~605~80

    42~580~90

    Cold GasEfficiencyCarbonConversion

    Korea(3T/D)

    high

    highDifficult,Unburnedcharproblem

    Curragh (Austraiia)

    CharFormationSlaggingPotential

    Coal

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    Characteristics of Gasifier Operation

    13.24enisovsky (R)8.09atong (C)

    4.12daro (IN)5.32aiduri (IN)

    10.99rayton (A)

    1.68ideco (IN)17.37urragh (A)

    3.96yprus (U)10.86sibelli (U)

    Ash (%)oneoal CharProductionAshSlaggingGasific-ation

    O

    OO

    O

    O

    Compat-ibility

    Good Problem

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    Commercial IGCC PowerPlant

    Commercial IGCC PowerPlant

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    Background Korean Governments Plan to increase NRE utilization

    By the year 2012, 7% of total power generation will be covered by NRE

    Power sector planning to construct # 1 IGCC power plant Construction of 300MW CCT will be completed by 2012

    Strategy of acquiring the design and demonstration of IGCC plant License agreement with Gasifier Vender Detailed Design by Korean Engineering Company Manufacturing most of the equipment in Korea

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    ObjectiveFinal objective

    Design & Demonstration of 300MW class IGCC Plant Maximize the Korean Participation

    Thermal efficiency: over 42% (HHV, Net) CO2 : 10% reduction, NOx: below 20 ppm, SOx: below 15ppm Domestic portion of Design: over 90% Korean Manufacturing of Equipment : over 90%

    Target

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    schedule

    1phase 06.12~09.12(3yr)

    2phase 09.12~12.12(3yr)

    - Gasifier vendor contract

    - Design of IGCC Demo Plant

    - Construction of300MW IGCC Plant

    -Development ofOperation Technology

    of Demo Plant

    - Operation of 300MW

    Demo. Plant

    -Renovation of Designthrough OperationExperience, R&D

    Design of IGCC

    Construction of IGCC

    Schedule of the Project

    Demon. Operation

    3phase 12.12~15.12(3yr)

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    Project 1 : Develop Design Capability of Gasifier(Doosan, KAIST, Yonsei University) Acquisition of PDP through Liscence Agreement with Gasifier Vender PEP of Gasification/Purification Process is Digested by Doosan Manufacturing of Gasification/Purification Plant is Managed Domestically

    PDP (Process Design Package) PEP (Preliminary Engineering Package)

    PDPPDP

    G/T

    Combined

    Cycle

    G/T

    CombinedCycle

    Gasifier

    Purification

    Liscence

    Agreement

    (Foreign)

    Plant Engineering

    ASU

    Development of

    Unit Process

    (Domestic)

    IGCC Plan t Design

    Domestic PlantDesign Technology

    Research & Development & Demo. Program

    R h & D l & D P

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    Project 2 : Design & Construction of IGCC Plant(Western Power, KOPEC) Design of Entire IGCC Plant except Gasifier and ASU Managing Engineering Procedure (EPC) Evaluation of Environmental Effect

    /

    /

    300MW

    300MW IGCC PlantEngineering

    BasicFor

    Design

    300MW IGCC PlantProcurements & Construction

    Pre-Operation

    Demo Operation/

    LiscenceAgreement

    1st Stage (3 year) 2nd Stage (3 year) 3rd Stage (2 year)

    Construction Roadmap

    Research & Development & Demo. Program

    R h & D l t & D P

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    Project 3 : Operation & Maintenance of Demo Plant- KEPRI, Power Co, KEPCO, SNU, Inha, Korea, Kunsan Management Technology of Demo Plant Develop IGCC Plant Manpower Availability: Increase 78~82% 92% [PC Plant] Optimozation of Gas Turbine Combustion Develop Real-time Operation Watching System Develop Operation Simulator, Train Operator

    Operat ing Mal func t ion Watching Program Simulator

    23%

    56%

    14%

    7%

    Research & Development & Demo. Program

    R h & D l t & D P

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    Project : Pilot Test-Bed and Development of Unit Process- KEPRI, Power Co., KEPCO, Doosan, IAE, KIER, Ajou, Hongik, Suwon Develop Gasifier Parts with Pilot Gasifier Pilot Test-Bed [30TPD] Construction Coal Selection, Preliminary Operation, Trouble shooting, Reliability Test Develop Desulfurization & Dedusting Process

    IGCC HT Filterilot Gasifier (KEPRI, IAE, KIER)

    Research & Development & Demo. Program

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    Government supported National Project Government & KEPCO

    Project Management and financial support Doosan Heavy Industry / KOPEC

    300MW IGCC Design, manufacture and construction Western Power CO

    Plant site, construction and operation KEPRI

    Management & Technical support for whole project License Agreement with Gasifier Vendor

    candidate vendors Shell, GE Energy, ConocoPhillips, MHI

    PDP introduced from the vendor, PEP from Engineering Company Plant Design, manufacturing and construction of IGCC should be

    conducted by Doosan and KOPEC

    Strategy

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    SUMMARY The position of coal as power generation fuel sourceand coal-utilizing CCT technology is explained. Because of IGCCs high efficiency and cleanenvironment characteristics, IGCC is most advanced coalutilization technology in the future power generationmarket. Baseline methodology for selecting candidate coal forgasification is established with coal characteristics such

    as fuel ratio and ash fusion behavior Explain the Korean national project of fordesign/construction/operation of 300 MW demonstrationIGCC plant

    Members of Energy Process Laboratory

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    (Accredited Best Lab in NRE Area by MOCIE)Professor

    Ph. D candidates

    Young Shin, Jeon Li Hua, Xu Hyun Min,Shim

    Master candidates

    Joon Soo, Lee Su Young, Jung Young Hoon, Kim Hueon, Nam gung Na Hyung

    Hong yue, Wang

    Hyung-Taek, Kim

    Post Doc. Researcher