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product partitioning incorporating multi-phase separation, probably including size grading, a degree<br />

<strong>of</strong> “gravity” separation and pneumatic separation. This equipment would be anticipated to be either<br />

fixed or re-locatable, but not mobile for “infield” use.<br />

Case by case evaluation <strong>of</strong> the economics <strong>of</strong> different strategies will be required, with factors such as<br />

eventual Industry size and distribution having a significant impact on future development paths.<br />

4.3 Mallee Products and Conversion Technologies.<br />

A range <strong>of</strong> products can potentially be derived from mallee trees, with three main processes being<br />

utilised:<br />

• Extraction <strong>of</strong> oils. Whilst a number <strong>of</strong> processes can be utilised for the extraction <strong>of</strong> oils from<br />

biomass, with mallee the main source <strong>of</strong> oils is in the leaf material and steam extraction is<br />

considered the most appropriate technology;<br />

• Thermal conversion. Thermal conversion ranges from combustion, where the aim is to<br />

maximise heat recovery for process heat or electricity generation, to a range <strong>of</strong> processes<br />

where the combustion process is controlled and targeted products are produced. The process<br />

can be manipulated to maximise output <strong>of</strong> a range <strong>of</strong> products from charcoal to combustible<br />

gasses. Gasses can then be further converted into liquid fuels (e.g “bio-crude”). Heat is also<br />

liberated. The process is well described by El Bassam (2010). Figure 4.5a illustrates the mass<br />

balance <strong>of</strong> the process <strong>of</strong> gasification and bio-oil production from a biomass crop, with the<br />

basis being 1000 kg <strong>of</strong> feedstock dry-material prior to the conversion process. Figure 4.5b<br />

gives the energy balance for material at 25% moisture content initial condition. The actual<br />

conversion efficiencies to the nominated end products can be manipulated by the temperature<br />

<strong>of</strong> the process, with higher temperatures favouring higher production <strong>of</strong> gasses and oil, and<br />

lower temperatures favouring the production <strong>of</strong> char.<br />

• Physical conversion. Physical conversion <strong>of</strong> biomass is in the context <strong>of</strong> a bioenergy crop is<br />

primarily by processes such as briquetting or pelleting. This strategy is primarily used to<br />

“standardise” the product and maximise density for transport.<br />

Whilst the oil extraction process and physical conversion require the addition <strong>of</strong> energy, thermal<br />

conversion is essentially exothermic. Whilst thermal conversion technology has been used on a large<br />

scale for many years (charcoal production, Fischer Tropsch for liquid fuel production and “producer<br />

gas” for stationary applications) technology is developing rapidly.<br />

Figure 4.5(a) Mass balance <strong>of</strong> biomass conversion using fast pyrolysis.(El Bassam 2010)<br />

109

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