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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.

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