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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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As the time required for one batch is generally between two and four days, the<br />

batch process will run through a number <strong>of</strong> days longer than the batch length<br />

before starting to record data, when a continuous feedstock supply is being used.<br />

This allows the batches to start working through so that the ethanol production<br />

and energy requirements will start from the beginning, for the different batches<br />

running simultaneously. This is also done in the transesterification process if<br />

the batch length is longer than 24 hours, but this is not generally the case. The<br />

outputs <strong>of</strong> the batch process simulation are the same as for the continuous<br />

process described in Section 6.4.2. This process is also shown in Figure 6.7.<br />

6.4.4 Use <strong>of</strong> Residues<br />

If energy crops are used, a certain amount <strong>of</strong> crop residue may be available.<br />

This may, again, be used as cattle feed, sent to an anaerobic digester or gasifier,<br />

or burned directly to produce heat and/or electricity, depending on the residue<br />

type, and other system requirements. The processes for dealing with this type <strong>of</strong><br />

residue are as described in Section 6.3.4. If these crop residues are used to meet<br />

some or all <strong>of</strong> the process energy needs, the input energy requirements and<br />

amount <strong>of</strong> residue produced are reduced accordingly.<br />

If a dry animal feed is produced, this can be used or processed in the same way<br />

as the energy crop residues. Determining the feedstock availability for this<br />

residue, however, is more difficult than for the crop residues, as it is produced<br />

more erratically. This is not a problem when gasification is being considered, as<br />

the feedstock is put into a store when available, and used from that store when<br />

possible. The gasification process characteristics are defined, and the outputs<br />

and energy use are calculated, in the same manner as described in Section 6.1,<br />

and the various options for processing the resulting gas are also available. If the<br />

dry animal feed is to be made available for use in boilers, engines or turbines, a<br />

temporal production rate graph for a specified “other” category <strong>of</strong> fuel is<br />

produced.<br />

If a wet animal feed is produced, this may be sent, if desired, to an anaerobic<br />

digester. This is also an option for the dry animal feed. The erratic nature <strong>of</strong><br />

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