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gas hydrate - CCOP

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where R POC is the POC degradation rate, C (DIC) is the concentration of dissolved inorganic<br />

carbon (CO 3 + HCO 3 + CO 2 ) in the considered depth interval, C (CH 4 ) is the ambient<br />

methane concentration in pore waters, k x is an age-dependent kinetic constant, POC is the<br />

POC concentration and KC is a Monod constant describing the inhibition of POC degradation<br />

by DIC and CH 4 . The age effects on POC degradation are considered using the approach<br />

introduced by (Middelburg, 1989). Ages were calculated from sediment depth and burial rate<br />

assuming an initial age of 1000 years. The rate law predicts that the microbial degradation of<br />

organic matter is inhibited by metabolites accumulating in adjacent pore fluids since the<br />

Gibb’s free energy available for the microbial metabolism is reduced in the presence of high<br />

concentrations of reaction products.<br />

Dissolved methane is produced via microbial organic matter degradation after sulfate has<br />

been depleted by microbial sulfate reduction (Wallmann et. al., 2006). Gas <strong>hydrate</strong> is<br />

precipitated from the pore solution when the concentration of dissolved methane calculated in<br />

the model surpasses the solubility of <strong>gas</strong> <strong>hydrate</strong>s (C SAT ).<br />

R<br />

GH<br />

⎛ C(CH ⎞<br />

4<br />

)<br />

= k ⋅<br />

⎜ −1<br />

⎟<br />

GH<br />

⎝ CSAT<br />

⎠<br />

We use a kinetic approach to simulate <strong>hydrate</strong> precipitation and dissolution (Hensen and<br />

Wallmann, 2005; Torres et al., 2004) and a modified Pitzer-approach for the calculation of<br />

<strong>hydrate</strong> solubility (Tishchenko et al., 2005). The kinetic constant for <strong>hydrate</strong> precipitation is<br />

set to a large value (k GH = 2 x 10 -2 wt-% yr -1 ) to prevent over-saturation with respect to <strong>gas</strong><br />

<strong>hydrate</strong>. Hydrates are allowed to dissolve in under-saturated pore solutions applying a<br />

corresponding kinetic constant of k GHD = 2 x 10 -2 wt-% yr -1 :<br />

R<br />

GHD<br />

= k<br />

GHD<br />

⎛ C(CH ⋅<br />

⎜1<br />

−<br />

⎝ CSAT<br />

4<br />

) ⎞<br />

⎟ ⋅ G GH<br />

⎠<br />

( )<br />

Hydrate concentrations (G(GH)) are initially calculated in wt-% and are subsequently<br />

converted into percent of pore volume filled by <strong>hydrate</strong> considering the density of dry<br />

sediments (d S = 2.5 g cm -3 ) and <strong>gas</strong> <strong>hydrate</strong>s (d GH = 0.916 g cm -3 ).<br />

Boundary conditions for dissolved species applied at the base of the model column have a<br />

strong effect on the amount of <strong>hydrate</strong> formed in the model sediments. We apply constant<br />

gradient conditions for SO 4 , DIC, and CH 4 :<br />

δC<br />

δx<br />

δC<br />

δx<br />

( n) = ( n −1)<br />

where the concentration gradient in the last interval of the model column (n) is assumed to<br />

have the same value as the gradient in the overlying depth interval (n-1). With this approach,<br />

methane and DIC continuously produced in deeper sediment sections situated below the base<br />

of the model column (410 m) are allowed to enter the model domain via molecular diffusion.<br />

New Energy Resources in the <strong>CCOP</strong> Region - Gas Hydrates and Coalbed Methane 13

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