Pengenalan CBM

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Pengenalan CoalBed Methane

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  • PENGENALAN SIMULASI RESERVOIR CBMKULIAH MINGGU XIII PEMODELAN & SIMULASI RESERVOIR

    Joko PamungkasReservoir Simulation Specialist

  • Minggu XIiIBab V Pengenalan Siimulasi Reservoir CBM 2

    PENGENALAN SIMULASI RESERVOIR CBM

    Pertemuanke-

    Pokok bahasan atausubpokok bahasan

    13 V. PENGENALAN SIMULASI RESERVOIR CBM1. Latar Belakang2. Metodologi3. Pemodelan Reservoir4. Hasil5. Kesimpulan

  • Minggu XIiIBab V Pengenalan Siimulasi Reservoir CBM 3

    1. LATAR BELAKANG Reservoir gas konvensianal cadangannyasemakin menipis dan kebutuhan semakinmeningkat

    CBM merupakan alternatif cadangan gas yangperlu dikembangkan saat ini

    Perlunya diketahui kinerja masing-masingreservoir yaitu : gas konvensional dan CBM

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  • Minggu XIiIBab V Pengenalan Siimulasi Reservoir CBM 4

    2. MetodologiPerbandingan kinerja, meliputi : Perhitungan cadangan Laju produksi gas Penurunan tekanan reservoir Metode perhitungan dengan simulasi reservoir Nama simulator : CMG (computer ModellingGroup)

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  • Minggu XIiIBab V Pengenalan Siimulasi Reservoir CBM 5

    Classification of Unconventional gas

    Natural gas from Coal NGC : Natural Gas from Coal CBM: Coal Bed Methane CSG: Coal Seam Gas

    Shale Gas Tight Gas Gas hydrates or Methane hydrates.

  • Minggu XIiIBab V Pengenalan Siimulasi Reservoir CBM 6

    Structure of Coal & Gas FlowPhysics

    Primary Porosity: CoalMatrix

    Secondary Porosity:Cleats (Fractures)

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    CO2CH4

    N2

    Flow Regimes in Coal

    Primary CBMrecovery

    CO2 enhancedrecovery (CO2-ECBM) N2 enhancedrecovery (N2-ECBM) Flue gas enhancedrecovery

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    CH4

    CH4CH4 CH4

    CH4Coal Matrix

    CH4H2O

    Coal Cleats/fractures

    Primary CBM Recovery Mechanisms Reduce cleat pressure by producing water Methane desorbs from matrix, diffuses to cleats/fractures Methane and water flow to wellbore

    Darcy Flow through fractures Face and Butt Cleats Vertical connection of Face & Butt cleats

    Darcy or Pipe Flow in large fractures Large Cleats Induced Fracture(s)

    Pipe Flow in production tubing/wellbore Cleat permeability affected by matrix responses

  • Minggu XIiIBab V Pengenalan Siimulasi Reservoir CBM 9

    Enhanced Coalbed Methane (ECBM) Recovery Green House Gas (GHG) Sequestration

    ECBM Mechanisms

    CO2Deep Coalbed CH4 CH4CH4

    CH4 toSales

    N2

    Coal

    Flue Gas CO2 N2

    Injection

    Green PowerPlant

    Separation

  • Minggu XIiIBab V Pengenalan Siimulasi Reservoir CBM 10

    Properties of Coal: Multiple porositysystem Primary porosity system (coal matrix) Microporosity (< 2 nm) Mesoporosity (2 50 nm)+ Very low flow capacity: perms in microDarcy range Only Diffusive flow

    Secondary porosity system (coal cleats) Macroporosity (> 50 nm) Natural fractures Much greater flow capacity: perms in milliDarcy range Darcy Flow

  • Minggu XIiIBab V Pengenalan Siimulasi Reservoir CBM 11

  • Minggu XIiIBab V Pengenalan Siimulasi Reservoir CBM 12

    Volume Gas Storage (CBM)G = 1359.7 .A .h .B. Gc

    A = Drainage Area, Acreh = Ketebalan, ftB = average Coal Bulk Density, g/ccGc = Average Gas Constant, scf/ton

  • Minggu XIiIBab V Pengenalan Siimulasi Reservoir CBM 13

  • Minggu XIiIBab V Pengenalan Siimulasi Reservoir CBM 14

    Calculating Gas In Place (gas convensional)

    G = (43560 .Vb. . (1-Sw))/BgG = Gas in Place, SCFVb = Bulk Volum, Acre-ft= PorositySw = Water saturationBg = Gas volume factor, cu ft/scf

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    3. Pemodelan reservoir gas konvensionaldan CBM

    Uraian Reservoir gas konvensional Reservoir CBMJenis Grid Orthogonal OrthogonalJumlah Grid 36x32 x 4 = 4608 buah 36x32 x 4 = 4608 buahGrid Aktif 4608 buah 4608 buahUkuran 1 grid 50x 50 x 10 ft 50x 50 x 10 ftSistim Porositas Dual porositas Dual porositasJumlah Sektor 1 buah 1 buahBatas Gas Minyak (GOC) 1640 ft -Tekanan Awal 600 Psi 600 PsiSumur Produksi 5 Sumur 5 SumurPorositas fracture 0.10 (fraksi) 0.10 (fraksi)Permeabilitas fracture 10 mD 10 mD

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    Uraian Reservoir gas konvensional Reservoir CBMPorositas matriks 0.02 0.02Permeabilitas matriks 2 mD 2 mDFracture Spacing 0.2 0.2Coal desorbtion time (Ch4) day - 50Coal desorbtion time (CO2) day - 50Global Composition (CH4) - 0.8Global Composition (CO2) - 0.2Langmuir Adsorbtion Constant (CH4) - 3E-4 1/psiMaximum Adsorbed Mass (CH4) gmol/lb - 0.357Maximum Adsorbed Mass (CO2) gmol/lb 0.538Water Saturation 0.3 0.9

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    Parameter Satuan CBM Gas KonvensionalOriginal Gas in Place, OGIP STD FT3 1.14E+09 1.32E+09Original Water in Place, OWIP STD BBL 6.00E+06 3.34E+05

  • Minggu XIiIBab V Pengenalan Siimulasi Reservoir CBM 18

    SkenarioModel Gas Konvensional CBM

    Base Case (1) K = 10 mD K = 10 mD2 K = 15 mD K = 15 mD3 K = 5 mD K = 5 mD4 1 Sumur Produksi, q = 0.3 MMCF/day 1 Sumur produksi, q max5 1 Sumur Produksi, q = 1.5 MMCF/day -

    Catatan : Semua skenario menggunakan Tekanan alirdasar sumur (Pwf) = 50 psi

  • Minggu XIiIBab V Pengenalan Siimulasi Reservoir CBM 19

    CBMDefault-Field-PRO

    Time (Date)

    Gas

    Rat

    e SC

    (MM

    SCF/

    day)

    2011-1 2011-7 2012-1 2012-7 2013-1 2013-7 2014-1 2014-7 2015-10.00

    0.10

    0.20

    0.30

    0.40

    0.50

    Base CaseK = 15 mDK = 5 mDsingle well qmaxPerbandingan Laju Produksi

    gas Skenario Base case, 2 ,3dan 4

    Conventional Gas Reservoir performance

    Time (Date)

    Gas

    Rat

    e SC

    (MM

    SCF/

    day)

    2011 2012 2013 2014 2015 2016 2017 20180.00

    0.50

    1.00

    1.50

    2.00

    Base CaseK = 5 mDK = 15 mDSingle Well, Q = 0.3 MMSCF/DSingle Well, Q = 1.5 MMSCF/D

    4. Hasil

  • Minggu XIiIBab V Pengenalan Siimulasi Reservoir CBM 20

    Perbandingan ProduksiKumulatif Gas Skenario Basecase, 2 ,3 dan 4

    Default-Field-PRO CBM_2b.irf

    Time (Date)

    Cum

    ulat

    ive

    Gas

    SC

    (MM

    SCF)

    2011-1 2011-7 2012-1 2012-7 2013-1 2013-7 2014-1 2014-7 2015-10

    200

    400

    600

    800

    CBM_2b.irfCBM_2b1.irfCBM_2b2.irfCBM_2b3b.irf

    Conventional Gas Reservoir performance

    Time (Date)

    Cum

    ulat

    ive

    Gas

    SC

    (MM

    SCF)

    2011 2012 2013 2014 2015 2016 2017 20180

    200

    400

    600

    800

    1,000

    1,200

    1,400

    Base CaseK = 5 mDK = 15 mDSingle Well, Q = 0.3 MMSCF/DSingle Well, Q =1.5 MMSCF/D

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    Perbandingan Tekananrata-rata LapanganSkenario Base case, 2 ,3dan 4

    CBM

    FIELD

    Time (Date)

    Ever

    age

    Pres

    sure

    (psi

    )

    2011-1 2011-7 2012-1 2012-7 2013-1 2013-7 2014-1 2014-7 2015-1100

    200

    300

    400

    500

    600

    Base CaseK = 15 mDK = 5 mDSingle Well qmax

    Conventional Gas Reservoir performance

    Time (Date)

    Res

    ervo

    ir pr

    essu

    re (p

    si)

    2011 2012 2013 2014 2015 2016 2017 20180

    100

    200

    300

    400

    500

    600

    Base CaseK = 5 mDK = 15 mDSingle Well and Q = 0.3 MMSCF/DSingle Well and Q = 1.5 MMSCF/D

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    Recovery Factor Diawal Tahun 2015Skenario Model Kumulatif Produksi gas Kumulatif Porduksi gas Recovery Factor Recovery Factor

    Gas Konvensional (MMSCF) CBM (MMSCF) Gas Konvensional (%) CBM (%)Base Case (1) 1188.95 405.35 89.74 35.48

    2 1209.23 525.36 91.27 45.993 1128.24 195.97 85.16 17.164 493.50 72.23 37.25 6.325 959.73 - 72.44 -

  • Minggu XIiIBab V Pengenalan Siimulasi Reservoir CBM 23

    5. Kesimpulan1. Dengan nilai permeabilitas yang sama, ternyata laju

    produksi Gas reservoir CBM lebih rendah dari reservoir gaskonvensional.

    2. Tingkat pengurasan reservoir lebih jauh reservoir gaskonvensional bila dibandingkan dengan reservoir CBM,sehingga reservoir CBM perlu sumur yang lebih banyak.

    3. Pengaturan laju produksi di reservoir gas konvensional lebihmudah bila dibandingkan dengan reservoir CBM.

    4. Recovery factor yang didapat dalam kurun waktu yang sama,reservoir CBM lebih rendah bila dibandingkan denganreservoir gas konvensional.