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Table 4.5 Value <strong>of</strong> feedstock components for Metallurgical Charcoal<br />
Product Value ($/t)<br />
Component Used<br />
Extraction cost ($/t)<br />
$198 high volume sales<br />
Woodchip / log and “extracted” leaf and twig<br />
$50/t charcoal<br />
Product Value ($/t) $148.00<br />
Product yield (% <strong>of</strong> freshweight) 20-30%<br />
Value/gt freshweight separated woodchip/log $ 36.00-$54.00<br />
Value/gt freshweight whole tree including extracted leaf $ 36.00-$54.00<br />
Residual and co-products<br />
Co-Product value<br />
Heat & syngas/ bio-crude.<br />
App 60% <strong>of</strong> initial energy content as heat and<br />
combustables/feedstock.<br />
As with the production <strong>of</strong> activated charcoal, the production <strong>of</strong> metallurgical charcoal results in<br />
significant heat production and production <strong>of</strong> syngas. Whilst a greater proportion <strong>of</strong> the initial energy<br />
is lost to the charcoal product stream, significant energy is still available for downstream use as heat<br />
or for the production <strong>of</strong> bio-crude.<br />
4.3.4 Bio-Char<br />
Bio-char is a relatively newly commercialised product, with a range <strong>of</strong> uses. Bio-char has high value<br />
use as a fertiliser component, whilst a lower value use is as a soil physical ameliorant. Biochar can<br />
also be used as a vehicle for carbon sequestration, and a value can be derived based on the value<br />
assumed for a carbon tax <strong>of</strong> nominally $50/tonne CO 2 .<br />
As with other thermal conversion processes, the recovery <strong>of</strong> bio-char is dependent on the time and<br />
temperature in the reactor, with low temperatures preferred for maximising char recoveries, with<br />
overall recoveries <strong>of</strong> approximately 30% (char : freshweight) being reported as typical. The process<br />
consumes the syngases and bio-crude, however the combustion <strong>of</strong> these products maximises the<br />
exothermic nature <strong>of</strong> the reaction.<br />
These lower temperature processes reduce the potential for efficient use <strong>of</strong> the liberated heat in<br />
“steam cycle” conversion processes, however the exhaust heat temperature matches some processes<br />
such as Organic Rankine Cycle units for electricity production.<br />
Bio-Char as an industrial feedstock for the fertiliser industry has a very significantly higher value than<br />
for its use for carbon sequestration, however the value as an industrial product will be dependent on<br />
supply. The current price is in the order <strong>of</strong> $500/tonne (J Joyce, Pers Com, 2011). For this application,<br />
pre-extraction <strong>of</strong> oil from leaf material would reduce its value because <strong>of</strong> the value <strong>of</strong> alkalis and<br />
other inorganics in the leaf material when used as a fertiliser component.<br />
Syngas and heat are by-products <strong>of</strong> the production <strong>of</strong> bio-char production, and these can be used<br />
directly in downstream processes, e.g thermal applications.<br />
Table 4.6 Value <strong>of</strong> feedstock components for Bio-Char for various uses.<br />
Bio Char Fertiliser Additive CO 2 Sequestration<br />
Product Value ($/t) $ 500 $50/t CO 2<br />
Component Used whole tree whole tree<br />
Extraction cost ($/t) $25 $25<br />
115