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Oil and gas production handbook An introduction to oil ... - ABB Group

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after well completion <strong>and</strong> fracturing, the coal seam (layer of coal) must be<br />

dewatered. A common solution is <strong>to</strong> extract water through the well tubing.<br />

Generally, the water needs <strong>to</strong> be pumped out <strong>and</strong> therefore control is<br />

needed <strong>to</strong> prevent the <strong>gas</strong> from entering the water in the tubing (the well<br />

becomes <strong>gas</strong>sy). This reduces the pressure <strong>and</strong> allows methane <strong>to</strong> desorb<br />

from the matrix <strong>and</strong> be produced through the casing.<br />

9.1.5 Coal, <strong>gas</strong> <strong>to</strong> liquids <strong>and</strong> synthetic fuel<br />

Coal is similar in origin <strong>to</strong> <strong>oil</strong> shales, but typically formed from the anaerobic<br />

decay of peat swamps <strong>and</strong> relatively free from non-organic sediment<br />

deposits, reformed by heat <strong>and</strong> pressure. To form a 1-meter thick coal layer,<br />

as much as 30 meters of peat was originally required. Coal can vary from<br />

relatively pure carbon <strong>to</strong> carbon soaked with hydrocarbons, sulfur, etc.<br />

(For synthesis <strong>gas</strong>, see also chapter 7.3.)<br />

It has been known for decades that synthetic diesel could be created from<br />

coal. This is done, first by creating water <strong>gas</strong> as synthesis <strong>gas</strong> by passing<br />

steam over red-hot coke. The reaction is endothermic <strong>and</strong> requires heating:<br />

C + H 2 O → H 2 + CO<br />

More hydrogen is produced in the water <strong>gas</strong> shift reaction:<br />

CO + H 2 O → H 2 + CO 2<br />

Often two stages are used: a high temperature shift (HTS) at 350 °C with<br />

catalyst iron oxide promoted with chromium oxide, <strong>and</strong> a low temperature<br />

shift (LTS) at 190–210 °C with catalyst copper on a mixed support composed<br />

of zinc oxide <strong>and</strong> aluminum oxide.<br />

These synthesis <strong>gas</strong>es are then used in the Fischer–Tropsch process:<br />

(2n+1)H 2 + nCO → C n H (2n+2) + nH 2 O<br />

This process runs at a pressure of 2-4 MPa. With iron catalyst a high<br />

temperature process at 350 °C will yield a diesel fuel quite similar <strong>to</strong> normal<br />

diesel with an average carbon number of 12, <strong>and</strong> a certain content of<br />

unwanted aromatics. The low temperature process uses a cobalt catalyst<br />

<strong>and</strong> a temperature of 200 °C <strong>and</strong> yields a pure synthetic diesel composed of<br />

alkanes with a carbon number of 10-15 <strong>and</strong> an average carbon number of<br />

12.<br />

131

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