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INTERDISCIPLINARY JOURNAL OF CONTEMPORARY RESEARCH IN BUSINESS<br />

oil is dissolved <strong>in</strong> a solvent, to separate it from the <strong>in</strong>soluble meal that is primarily<br />

composed <strong>of</strong> prote<strong>in</strong> and carbohydrate.<br />

Various liquids has been <strong>in</strong> use as solvents for commercial oil extraction by the vegetable<br />

oil <strong>in</strong>dustries and others has been proposed based upon encourag<strong>in</strong>g laboratory results.<br />

However, mixture <strong>of</strong> hexane rich <strong>in</strong> n-hexane, have been the solvent <strong>of</strong> choice by the oil<br />

seed process<strong>in</strong>g <strong>in</strong>dustries for the past 50years. Due to the toxicological, environmental<br />

and economic reasons, other solvents have been proposed as an alternative to hexane.<br />

Palm kernels are usually prepared for solvent extraction by crack<strong>in</strong>g, heat<strong>in</strong>g and flak<strong>in</strong>g<br />

or by condition<strong>in</strong>g, screw-press<strong>in</strong>g, gr<strong>in</strong>d<strong>in</strong>g and flak<strong>in</strong>g.<br />

In a (cont<strong>in</strong>uous) solvent extraction process, the seeds are contacted with a solvent,<br />

generally hexane. The oil conta<strong>in</strong>ed <strong>in</strong> the seeds is dissolved <strong>in</strong> the solvent after which<br />

solvent and solids are separated. The solvent/oil mixture (usually 20-33 wt% oil)<br />

(Technology and solvents for extract<strong>in</strong>g oilseeds and nonpetroleum oils; Wan, P. J.;<br />

Wakelyn, P. J., Eds.; AOCS Press: Champaign,2004) is sent to the solvent recovery<br />

operation, where solvent is removed by evaporation. The residual cake is sent to a desolventiser<br />

/ toaster, which also removes the solvent by evaporation. Both oil and solids<br />

therefore undergo a heat treatment, which is detrimental for the oil and cake quality. The<br />

co-extraction <strong>of</strong> undesired components further reduces the quality <strong>of</strong> the oil. However,<br />

with this method it is possible to recover almost all <strong>of</strong> the oil from the seeds. Generally,<br />

this method is used <strong>in</strong> the high(est) capacity plants. To further improve the efficiency <strong>of</strong><br />

the process, the extraction can be preceded by a pre-press<strong>in</strong>g step. Here part <strong>of</strong> the oil is<br />

recovered by a screw press, which reduces the size <strong>of</strong> the extractor and improves the<br />

permeability <strong>of</strong> the solids.<br />

Figure 4: Hexane solvent extraction flow diagram.<br />

Source; Wan, P. J.; Wakelyn, P. J., Eds.; (2004)<br />

COPY RIGHT © 2011 Institute <strong>of</strong> <strong>Interdiscipl<strong>in</strong>ary</strong> Bus<strong>in</strong>ess <strong>Research</strong> 68<br />

JANUARY 2011<br />

VOL 2, NO 9

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