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Biofuels in Perspective

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Enzymatic Production of Biodiesel 147<br />

With cell-surface-displayed ProROL, substrate molecules could easily access ProROL<br />

and no treatment was needed to catalyze methanolysis reaction. S<strong>in</strong>ce the <strong>in</strong>itial reaction<br />

rate of FSProROL-display<strong>in</strong>g cells was as high as that of soluble ROL, the displayed<br />

FSProROL may have the same accessibility to substrates as free enzyme. For the <strong>in</strong>dustrial<br />

bioconversion process, lipases immobilized on the cell-surface are more cost effective and<br />

convenient, s<strong>in</strong>ce these whole-cell biocatalysts can be prepared simply by cultivation and<br />

recovered easily.<br />

8.6 Conclusions and Future Prospects<br />

In recent years, biodiesel has become more attractive as an alternative fuel for diesel eng<strong>in</strong>es<br />

because of its environmental benefits and the fact that it is made from renewable resources.<br />

Used oils can also be utilized for mak<strong>in</strong>g biodiesel fuel, thus help<strong>in</strong>g to reduce the cost<br />

of wastewater treatment <strong>in</strong> sewerage systems and generally assist<strong>in</strong>g <strong>in</strong> the recycl<strong>in</strong>g of<br />

resources. 80<br />

For the production of biodiesel fuel, an alkali-catalysis process has been established<br />

that gives high conversion levels of oils to MEs, and at present this is the method that<br />

is generally employed <strong>in</strong> actual biodiesel production. However, it has several drawbacks,<br />

<strong>in</strong>clud<strong>in</strong>g the difficulty of recycl<strong>in</strong>g glycerol and the need for either removal of the catalyst<br />

or wastewater treatment. In particular, several steps such as the evaporation of methanol,<br />

removal of saponified products, neutralization, and concentration, are needed to recover<br />

glycerol as a by-product.<br />

To overcome these drawbacks, which may limit the availability of biodiesel fuel, enzymatic<br />

processes us<strong>in</strong>g lipase have recently been developed. S<strong>in</strong>ce the cost of lipase<br />

production is the ma<strong>in</strong> hurdle to commercialization of the lipase-catalyzed process, the use<br />

of <strong>in</strong>tracellular lipase or cell-surface-displayed lipase as a whole-cell biocatalyst 47,48,75 is<br />

an effective way to lower the lipase production cost. Unlike <strong>in</strong> the case of extracellular<br />

lipase, these whole-cell biocatalysts can be prepared by simple cultivation and recovered<br />

easily.<br />

However, to utilize these whole-cell biocatalysts for <strong>in</strong>dustrial application, a high ME<br />

content of 90–95 % <strong>in</strong> many repeated methanolysis reaction cycles is required. One potential<br />

solution is the use of a whole-cell biocatalyst possess<strong>in</strong>g a non-specific lipase from a source<br />

such as C. antarctica 33 or P. cepacia 36 with<strong>in</strong> the cell or on the cell-surface, s<strong>in</strong>ce these<br />

lipases realize ME content of more than 95 %. Such a system could offer a promis<strong>in</strong>g<br />

prospect of realiz<strong>in</strong>g <strong>in</strong>dustrial biodiesel fuel production.<br />

References<br />

1. D. Bartholomew, Vegetable oil fuel, J. Am. Oil Chem. Soc., 58, 286A–288A (1981).<br />

2. E. H. Pryde, Vegetable oil as diesel fuel: overview, J. Am. Oil Chem. Soc., 60, 1557–1558 (1983).<br />

3. C. Adams, J. F. Peters, M. C. Rand, B. J. Schroer and M. C. Ziemke, Investigation of soybean<br />

oil as a diesel fuel extender: endurance tests, J. Am. Oil Chem. Soc., 60, 1574–1579 (1983).<br />

4. C. L. Peterson, D. L. Auld and R. A. Korus, W<strong>in</strong>ter rape oil fuel for diesel eng<strong>in</strong>es: recovery and<br />

utilization, J. Am. Oil Chem. Soc., 60, 1579–1587 (1983).

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