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PhD Thesis - Energy Systems Research Unit - University of Strathclyde

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Where Biogas = Biogas production rate (kg/hr)<br />

GasLHV = Lower heating value <strong>of</strong> biogas (kJ/Nm 3 )<br />

GasDensity = Density <strong>of</strong> biogas (kg/Nm 3 )<br />

Pyr = Pyrolysis oil production rate (kg/hr)<br />

PyrDensity = Density <strong>of</strong> pyrolysis oil (kg/m 3 )<br />

1 kWh = 3610.3 kJ<br />

The charcoal production rate (kg/hour), and the production rates <strong>of</strong> any other<br />

specified outputs, are as provided for a specific process and feedstock, as are the<br />

requirements for electricity and heat (in kW).<br />

If the amount <strong>of</strong> feedstock available at a particular timestep is between the<br />

maximum and minimum feed rates, a linear relationship is assumed, and each <strong>of</strong><br />

the production rate figures is multiplied by the following partial production<br />

factor: -<br />

Partial Production Factor = Feed x Timesteps (6.6)<br />

FeedRate<br />

Where Feed = Amount <strong>of</strong> feedstock available (kg)<br />

Timesteps = Number <strong>of</strong> timesteps per hour<br />

FeedRate = Feedstock feed rate (kg/hr).<br />

The heat requirement is also multiplied by this factor, as this will vary with the<br />

amount <strong>of</strong> feedstock. The electricity requirement, however, is not reduced, as<br />

this will remain the same, despite the reduction in feedstock. When used, the<br />

amount <strong>of</strong> feedstock left in the store is reduced accordingly, and a tally is kept<br />

<strong>of</strong> the overall feed used (kg), outputs made and heat and electricity required<br />

(kWh). This information is displayed along with the final output graph.<br />

This procedure is shown graphically in Figure 6.3, where each timestep is<br />

considered in turn, in order to determine the fuel production rates for the<br />

different fuels being produced, and the related energy requirements.<br />

183

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