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    2011 S nthesis Gas Seminar Mar arita

    MethanatorNovember 24, 2011

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    Methanator

    Function: Remove CO/CO2 to trace levels (< 5 ppmv)

    Hydrogen in RefineriesSome H2 applications involve catalysts sensitive to CO

    yp ca arge < ppm + 2,

    Sometimes

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    Methanator Reactions

    Steam

    2 4 2

    H = - 88,700 BTU / lb-moleHTS

    - - - uen

    2 4 2

    H = - 71,000 BTU / lb-mole

    = - 165 k-joules / g-mol

    Sd-Chemie Syngas Seminar | Margarita | Nov 2-4, 2011 Page 3

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    MethanatorT

    300 F

    360 F

    2 C

    240 F

    300 F

    O2 CO

    180 F

    1 C

    CO2

    60 F

    120 F

    0 F

    0.0 0.5 1.0 1.5 2.0 2.5 3.0

    C

    Sd-Chemie Syngas Seminar | Margarita | Nov 2-4, 2011 Page 4

    Mole of Component In Feed Gas

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    Catalyst Activity

    1.2

    1.4

    NH3

    0.8

    1.0

    ctivity H2

    0.6

    lative

    0.2

    0.4R

    0.0

    400 450 500 550 600 650 700 750 800 850

    Sd-Chemie Syngas Seminar | Margarita | Nov 2-4, 2011 Page 5

    Temperature F (C)

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    Methanator Design

    1.20

    1.30

    CO=0.10 CO=0.20 CO=0.30

    22

    1.00

    1.10

    olume

    0.90

    atalyst

    TEMP=600 F (316 C)

    0.70

    .

    Relative

    0.50

    .

    0.00 0.05 0.10 0.15 0.20 0.25 0.30

    Sd-Chemie Syngas Seminar | Margarita | Nov 2-4, 2011 Page 6

    Mole Percent CO2

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    Methanator Temp Profile

    300

    290ure,

    280p

    era

    Te

    9 Mos.

    15 Mos.

    22 Mos.

    270

    0 20 40 60 80 100

    Sd-Chemie Syngas Seminar | Margarita | Nov 2-4, 2011 Page 7

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    Methanator Operation

    4000

    100%

    ise

    3000

    +CO2

    60% ature

    2000

    PM

    CO

    40% empe

    100020% %

    of

    0

    0% 20% 40% 60% 80% 100%

    0%

    Sd-Chemie Syngas Seminar | Margarita | Nov 2-4, 2011 Page 8

    % of Bed

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    Operating Conditions

    an s: n ..

    T ... 20-35F (10-20C)

    .. - -

    T ... 20-35F (10-20C)

    - -..

    =

    Ni(CO)4 Forms at T < 350F (175C)

    Sd-Chemie Syngas Seminar | Margarita | Nov 2-4, 2011 Page 9

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    Nickel Carbonyl Ni(CO)4

    7.00E-07

    8.00E-07 3.00E-04

    ppm@900 K

    ppm@1000 K

    m 1200 K

    6.00E-07

    2.00E-04

    2.50E-04

    ppm@700 K

    4.00E-07

    . -

    1.50E-04

    2.00E-07

    3.00E-07

    1.00E-04

    0.00E+00

    1.00E-07

    0.00E+00

    5.00E-05

    Sd-Chemie Syngas Seminar | Margarita | Nov 2-4, 2011 Page 10

    0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 0.8 0.9

    CO partial pressure, bar

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    Nickel Carbonyl

    Ni(CO)Ni(CO)44 Formation:Formation: ppm at 200 psigppm at 200 psig

    Mole % COTem erature 0.2% 1.0% 3.2%

    150F (65C) 0.3 190 20,000

    200F (93C) 0.0 3 320300F (149C) 0.0 0 0.5

    400F (204C) 0.0 0 0.0

    Note: Toxic Threshold for Ni(CO)4 is 1 ppb

    Sd-Chemie Syngas Seminar | Margarita | Nov 2-4, 2011 Page 11

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    Catalyst Reduction

    e uce at > or est act v ty

    Dry gas (

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    Pre-Reduced Catalyst

    Pre-Reduced Catalyst An Advantage

    Temperatures

    oOperating Temperature is < 500F (260C)

    oMETH 134RS 3-6 mm

    Sd-Chemie Syngas Seminar | Margarita | Nov 2-4, 2011 Page 13

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    Methanator Deactivation

    oss o c v y ue o o sons

    Most Common Source

    oArsenic (Vetro Coke)oSulfur (Sulfinol)

    Hydrotreat to Break Ring

    Adsorb in Layer of ZnOoPhysical Masking (Potassium Carbonate)

    oMEA - No effect

    o e ec

    Sd-Chemie Syngas Seminar | Margarita | Nov 2-4, 2011 Page 14

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    Methanation Catalyst

    METH 134 Sph. 3-6 mmMETH 130 Ext. 5.5 mm

    Sd-Chemie Syngas Seminar | Margarita | Nov 2-4, 2011 Page 15

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    Q&A

    Sd-Chemie Syngas Seminar | Margarita | Nov 2-4, 2011 Page 16