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Coal Flaring

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    September 2007

    Harworth Power Ltd

    CMM Flaring

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    Harworth Power

    Part of UK Coal PLC -Ex Nationalised British Coal

    UK Coal 4000 employees, 14Mt capacity, surface and deep mines

    VAM oxidation technology trialled on an operating coal mine

    CMM utilised in boilers since the 1960s

    CMM utilised in gas turbines and gas engines since 1991

    CMM utilised in high efficiency gas engines since 2000 (30MWe installed)

    CMM destructed in enclosed flares since 2004 (7 flares installed)

    Part of the UK ETS since 2001, 2.3Mt CO2e verified (3.9Mt total)

    Separate unit specialising in assisting mines maximise capture, qualityand utilisation engineers deployable to assist in design and

    implementation

    Typical capture rates 40% - 60% of coal face district gas

    Typical gas quality 30% to 50% methane

    All gas is utilised in generators, boilers or flared

    2

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    Key Issues in Flaring of CMM

    Gas is NOT utilised but destroyed

    Safety

    Capital Cost

    Operating Cost

    Equipment Delivery Will the Government allow gas to be flared rather than

    utilised?

    Ideal scenario in the US distributed remote gas sourceswithout realistic or economic means us using heat,electricity or low quality gas near the well head.

    3

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    Coal to CMM Flaring

    4

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    Coal Mining General Data

    KellingleyColliery

    ThoresbyColliery

    WelbeckColliery

    HarworthColliery

    StillingfleetMine

    Depth (m) 900 750 700 850 700

    Tonnage (Mt) 1.455 Mt 0.829 Mt 0.868 Mt Mothballed Mine Closed Mine

    Seam Thickness 2.1 1.85 1.85 2 3

    Gas M3/tonne 5.3 5.2 5.0 6.2

    Gas Typical FlowRate (l/s)

    400 600 250 - 350 350 - 450 650 850 950

    Gas TypicalConcentration

    40 50% 30 40% 35 45% 45 55% 80%

    Utilization /destruction

    2x 20,000 lb/hrdry sat steam

    boilers

    3x 1.4MWe gasengine generators

    1x 2,000 Nm3/hrenclosed flare

    2x 1.4MWe gasengine generators

    1x 2,000 Nm3/hrenclosed flare

    2x 20,000 lb/hrdry sat steam

    boilers

    2x 1.4MWe gasengine generators

    2 x 2,000 Nm3/hrenclosed flare

    2x 20,000 lb/hrdry sat steam

    boilers

    5x 1.4MWe gasengine generators

    1x 2,000 Nm3/hrenclosed flare

    18MWe CCGT

    4x 3MWe gasengine generators

    5

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    Overview

    Gas Flaring.Technology:Destruction of drained methane gas through combustion in

    a gas flare. 2000 Nm3

    /hr destruction capacity per flare.

    Benefits:A low capex cost technology with a short manufacture and installation lead time.Simple, low cost and reliable to operate, gas flaring offers a very high potential for significant GHG reduction.Low maintenance requirements.Installation Requirements:80 litres/s pure methane flow at 20% purity or above,Methane drainage infrastructure already in place, Suitable flame arrestor technology installed to prevent flame propagation into the mine.Mine Suitability:A disciplined drainage approach ensuring that methane isonly drained above 20% purity.

    6

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    Flare P&I Diagram

    2000 Nm3/hr methane destruction capacity

    >27% CH4 for reliable flare start

    Flare will operate down to 20% CH4

    Automatic control

    Internet Remote Monitoring and Control

    Skid mounted for ease of installation

    7

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    Importance of Gas Purity

    Gas will not burn or explode outside of the flammablerange

    Gas will not allow an existing flame to propagate into themine outside of the flammable range

    Multiple failsafe concentration transducers automatically

    stop supply of gas to extraction pumps and flare Careful consideration of system T90 reaction period

    Only effective means of protection against lightning as an

    ignition source

    8

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    Flammability of Methane / Air at Atmospheric Pressureand Temperature

    The flammability of mixtures of Methane and Air

    C

    Capable of formingflammable

    mixtures with airper se.

    FlammableRegion

    Coward Diagram

    20

    15

    10

    5

    0

    B

    E

    F

    D

    Not capable offorming

    flammable

    mixtures with air

    Oxygen

    Concentration

    255 10 15 20Methane Concentration

    9

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    Hierarchy of Explosion Prevention and Mitigation

    1. Prevent formation of flammable atmosphere measureconcentration and stop flow

    2. Prevent exposure of ignition source to flammableatmosphere necessary for destruction / combustion

    3. Prevent propagation through flammable mixture use ofequipment/burner design, flame arresters and valves

    4. Dissipate energy bursting discs / relief valves / vents

    5. Prevent of release of explosion energy vessel and

    pipework design

    10

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    Flame Propagation in Pipework

    Flame Speed

    Point ofIgnition

    50 x Pipe Diameters

    Direction of flame propagation

    Deflagration

    Detonation

    Overdriven DetonationChoked flame speed (Mach 1)

    M = 1

    x

    11

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    Specific Flare Safety Features

    Safety risk assessments carried out fordesign and operation to prevent flashback

    HAZOP Hazardous Area Classification Flame Arrester suitability assessment Multiple redundancy and safety features Gas quality monitoring and oxygen inter-

    trip PLC controlled with certain high integrity

    functions duplicate hard wired

    Burner velocity design to preventflashback

    Temperature sensing to prevent flamearrester burn through

    Purge for start-up

    12

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    September 2007

    Thank you

    Neil ButlerTechnical Director

    44-7798-571612

    [email protected]

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    USA Coal Mine Methane Conference

    The modern high temperature flareSt Louis, 26thSeptember 2007

    www.clarke-energy.com

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    Cla rk e Ener gy supp l i es, i nst a l ls and m a in t a ins HAASE f lar es

    15www.clarke-energy.com

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    Cheap and d i r t y v e rsus st a te -o f - t he -a r t

    60% CH4destruction

    99.9% CH4destruction

    16www.clarke-energy.com

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    HAASE f l a re t yp es h i gh t em pe ra tu re con t i nuou s du t y an d l o w t e m p er a t u r e e m er g e n cy

    0.3s retention

    99.9% CH4 destruction

    CH4 down to 25% or lowerwith propane assist atignition

    Turn down 5:1 or greater

    HT type LT type 2 LT type 1

    www.clarke-energy.com17

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    HAASE l i n i ng 1 0 y ear gu a ran t ee

    18www.clarke-energy.com

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    Cold s ide l i n in g f i x ing

    19www.clarke-energy.com

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    Germ an and UK regu la t i ons

    TA-Luft UK

    NOX 200 mg/m3 150 mg/m3

    CO 100 mg/m3 50 mg/m3

    Temperature 1,200oC (1830oF) 1,000oC (2200oF)

    (Reference 3% O2by vol. in exhaust gas)

    www.clarke-energy.com20

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    21www.clarke-energy.com

    Natu r a l l y ven t i l at ed and f an ven t i l at ed

    20MW

    27MW

    10:1 turndownfan assisted

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    4 x 4 5 0 0 m 3/ h + 2 x 15 00 m 3/ h ( 1 @ 1 0 : 1 t u r n d ow n )

    10:1turndown

    Total

    105MW

    22www.clarke-energy.com

    l fl ( l ) d

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    HAASE lean gas flare (pilot) down to 10%methane

    23www.clarke-energy.com

    T l l d l f

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    Telecontrol system can record values forcarbon credits

    On-site-control Remote control

    24www.clarke-energy.com

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    Hat f ie ld Co l l i e ry 4 x Roots blower delivering

    880Nm3/h (each) at -500mbarg to

    -100mbarg delivery

    2 x Roots blower delivering1660Nm3/h (each) at -100mbarg to

    +200mbarg delivery

    25www.clarke-energy.com

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    The HAASE st a te o f t he a r t h i gh t em pe ra tu re f l a re in su m m ar y ;

    99.9% CH4 destruction Down to 25% CH4 , or lower with propane

    assistance at ignition

    Turn down ratio 5:1 standard, 10:1 or greateroptional

    10 year lining guarantee Exceeds German TA Luft requirements

    www.clarke-energy.com26

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    Thank you!Clarke Energy distributes GE Energy Jenbacher and HAASE best in class products supplying, installing and maintaining

    www.clarke-energy.com


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