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PhD Thesis - Energy Systems Research Unit - University of Strathclyde

PhD Thesis - Energy Systems Research Unit - University of Strathclyde

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Where Methane = Methane Production Rate (kg/hr)<br />

Percent = Reaction Completion Percentage<br />

Density = Density <strong>of</strong> Methanol (kg/litre)<br />

If there is not sufficient carbon dioxide present, and extra may not be utilised,<br />

the amount <strong>of</strong> methanol that can be made with the carbon dioxide present is<br />

calculated using,<br />

Methanol Production = 512 x CO2 x Percent (6.23)<br />

Rate (litres/hr) 176 x Density x 100<br />

Where CO2 = CO2 Production Rate (kg/hr),<br />

and the remaining, unused methane is calculated using,<br />

Remaining = Methane – (196 x CO2 x Percent) (6.24)<br />

Methane (kg/hr) (176 x 100)<br />

The methanol that can be made using the first chemical reaction is then<br />

determined in the same manner, by direct proportion using the first chemical<br />

equation, and added to the methanol production rate for that timestep. If<br />

desired, the remaining methane production rate may be calculated as described<br />

for hydrogen production, as can the process electricity and heat requirements<br />

and the electricity required for gas storage. The total amount <strong>of</strong> methanol<br />

produced (litres) throughout the simulation period, and any extra carbon dioxide<br />

required, is given along with the final production rate graphs.<br />

197

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