Biofuels in Perspective
Biofuels in Perspective
Biofuels in Perspective
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90 <strong>Biofuels</strong><br />
KOH<br />
Methano<br />
Oil/Fat<br />
Acid<br />
Catalyst<br />
Preparation<br />
Oil Pretreatment<br />
Fully automatic<br />
Transesterification<br />
Methylester<br />
Methanol-Recovery<br />
Methylester<br />
Purification –<br />
Distillation<br />
Qlitt Cl<br />
Glycer<strong>in</strong>e phase<br />
After- treatment<br />
Fertilizer<br />
Separation<br />
Free Fatty Acid<br />
Recovery<br />
Crude Glycer<strong>in</strong>e<br />
Methanol-Recovery<br />
Pharmaceutical<br />
Glycer<strong>in</strong>e Production<br />
Figure 5.6 Multifeedstock production scheme accord<strong>in</strong>g to BioDiesel International. 39<br />
Fertilizer<br />
Crude Glycer<strong>in</strong>e<br />
Pharmaglycer<strong>in</strong>e<br />
BioDiesel<br />
Distillation side-product<br />
technologies is the use of additional reaction steps, like pre-esterification of free fatty acids.<br />
So <strong>in</strong> a first step free fatty acids are pre-esterified with the use of acidic catalysts, followed<br />
by one or two alkal<strong>in</strong>e catalyzed transesterification steps. The raw fatty acid methyl esters<br />
are purified by water wash<strong>in</strong>g steps and additionally can be further ref<strong>in</strong>ed by vacuum<br />
distillation. The ma<strong>in</strong> advantage of this technology is the fact that the yield of conversion<br />
of fatty acid material <strong>in</strong>to fatty acid methyl esters is almost 100 %. The highest yield can<br />
be obta<strong>in</strong>ed, when rema<strong>in</strong><strong>in</strong>g soaps <strong>in</strong> the glycerol layer are recycled by acidification of<br />
the glycerol and separation of free fatty acids, which can be re<strong>in</strong>troduced <strong>in</strong>to the preesterification<br />
step or first step of transesterification. 39 Another approach for convert<strong>in</strong>g<br />
high acidic oils <strong>in</strong>to fatty acid methyl esters is the conversion of fatty acids <strong>in</strong>to glycerides,<br />
followed by traditional transesterification. 40<br />
5.8.3 Small Scale Production Units<br />
A lot of production plants have a production capacity of up to 5000 t/a, us<strong>in</strong>g different<br />
feedstocks and different production technologies. Mostly these plants have not been built by<br />
big biodiesel technology companies, but the technology has been developed by <strong>in</strong>dividual<br />
groups and organizations based on own experience and development. The glycerol layer<br />
must be used directly without any purification, e.g. as substrate for biogas plants, or will be<br />
purified to be sold as raw glycerol. The catalyst for transesterifications is ma<strong>in</strong>ly potassium<br />
hydroxide, because it gives the highest conversion rates. Several of these production plants<br />
are organized as co-operatives, us<strong>in</strong>g vegetable oils produced locally, and also the biodiesel<br />
will be used by the members directly. Most of the very small production units don’t have<br />
their own facilities for quality control, so the quality of the product might vary and is not<br />
guaranteed to meet EN 14214.