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Biofuels in Perspective

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102 <strong>Biofuels</strong><br />

period of a decade. Therefore, it is questionable if the ambitious renewable energy targets<br />

can be met by follow<strong>in</strong>g this route.<br />

The second and perhaps to be preferred route comprises adapt<strong>in</strong>g today’s large-scale<br />

coal-based (entra<strong>in</strong>ed flow (EF)) gasification technology, <strong>in</strong>itially by co-fir<strong>in</strong>g biomass and<br />

later on construct biomass-based gasifiers. In this way the <strong>in</strong>stalled biosyngas capacity can<br />

be <strong>in</strong>creased rapidly, as basic technology is already proven on large scale.<br />

6.3.2 Biomass Feedstock<br />

Approximately 50 % of the biomass globally available for energy purposes (i.e. the technical<br />

potential) is wood or wood residues. A further 20 % is strawlike, which share will <strong>in</strong>crease<br />

to 40 % when strawlike crops are selected as energy crops. 12 Hence, for utilization of the<br />

large amounts of biomass for biosyngas production, it is important to develop technical<br />

routes that are able to utilize both wood and straw materials. Biomass materials like manure<br />

and waste streams will play only a m<strong>in</strong>or role <strong>in</strong> the biosyngas production, as the absolute<br />

amounts of these streams available for biosyngas production are very low compared to<br />

the required total amounts of biomass. Therefore, they are not of significance for largescale<br />

biosyngas production.<br />

Due to the distributed and global generation of the biomass, large transport distances are<br />

unavoidable. Transport by truck is the major cost driver <strong>in</strong> biomass transport; therefore,<br />

the transport over land should be m<strong>in</strong>imized. 2 Strawlike materials have a much lower bulk<br />

energy density, which would result <strong>in</strong> higher transport and transhipment costs. Therefore,<br />

energy densification of straw is desired to reduce transport costs and allow easier handl<strong>in</strong>g,<br />

viz. grasses and straw are converted <strong>in</strong>to a bioslurry via flash pyrolysis, 13 as will be discussed<br />

<strong>in</strong> Sections 6.3.4.4 and 6.3.4.5. Wood, although already relatively high-energy dense, will<br />

preferable also be densified (e.g. by torrefaction discussed <strong>in</strong> Section 6.3.4.2 or aga<strong>in</strong><br />

pyrolysis, result<strong>in</strong>g also <strong>in</strong> simplification of the biomass feed<strong>in</strong>g system of gasification)<br />

before be<strong>in</strong>g transported by ship to large centralized conversion facilities.<br />

The transition to green alternatives requires biomass, which should be available <strong>in</strong> large<br />

quantities. S<strong>in</strong>ce wood and grasslike material make up 70–90 % of the total technically<br />

available amount of biomass world-wide, it is reasonable to focus on these biomass fuels<br />

as ma<strong>in</strong> renewable energy sources for chemicals and fuels. 14<br />

6.3.3 Syngas Production Technology<br />

In order to produce biosyngas cost-effectively, high biomass-to-syngas yields are required.<br />

This implies that upon gasification of biomass the maximum share of energy conta<strong>in</strong>ed <strong>in</strong><br />

the biomass should be converted <strong>in</strong>to the syngas components H2 and CO.<br />

There are two thermo-chemical ways to produce synthesis gas (H2 and CO) from<br />

biomass: either by apply<strong>in</strong>g high temperatures or by us<strong>in</strong>g a catalyst at a much lower<br />

temperature Figure 6.4. 15 The first route <strong>in</strong>cludes a fluidized bed gasifier and a downstream<br />

catalytic reformer, both operat<strong>in</strong>g at approximately 900 ◦ C. In product gas from low<br />

temperature gasification the syngas components H2 and CO typically conta<strong>in</strong> only ∼50 %<br />

of the energy <strong>in</strong> the gas, while the rema<strong>in</strong>der is conta<strong>in</strong>ed <strong>in</strong> CH4 and higher (aromatic)

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