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INTERDISCIPLINARY JOURNAL OF CONTEMPORARY RESEARCH IN BUSINESS<br />

8.1 KERNEL PRE-TREATMENT<br />

Proper kernel pre-treatment is necessary to efficiently extract oil from the kernels. the<br />

feed kernels must undergo such pre-treatment as dehaull<strong>in</strong>g, clean<strong>in</strong>g, dest<strong>in</strong><strong>in</strong>g, cook<strong>in</strong>g<br />

/ heat<strong>in</strong>g , dry<strong>in</strong>g to optimum moisture/temperature levels and flak<strong>in</strong>g. foreign materials<br />

are removed dur<strong>in</strong>g the process <strong>of</strong> clean<strong>in</strong>g to avoid damag<strong>in</strong>g <strong>of</strong> the screw presses,<br />

<strong>in</strong>creas<strong>in</strong>g cost and downtime and contam<strong>in</strong>ation <strong>of</strong> the products.<br />

A sw<strong>in</strong>g<strong>in</strong>g hammer gr<strong>in</strong>der, breaker rolls or the comb<strong>in</strong>ation <strong>of</strong> both breaks the kernels<br />

<strong>in</strong>to small fragments. This process <strong>in</strong>crease the surface area <strong>of</strong> the kernels, thus<br />

facilitat<strong>in</strong>g flak<strong>in</strong>g. The kernel fragments subsequently are subjected to flak<strong>in</strong>g <strong>in</strong> the<br />

roller mill. The thickness <strong>of</strong> the kernel cake is progressively reduced as it travels from top<br />

roller to the bottom roller. This progressive roll<strong>in</strong>g <strong>in</strong>itiates ruptur<strong>in</strong>g <strong>of</strong> the cell walls.<br />

The flakes at the bottom nip are from 0.25mm to 0.4mm thick(Golden oil,2002). The<br />

kernel flakes are then conveyed to a stack cooker for steam condition<strong>in</strong>g; the purpose <strong>of</strong><br />

which is to:<br />

� Adjust the moisture content <strong>of</strong> the meal to an optimum level<br />

� Rupture the cell wall <strong>of</strong> the palm kernel, <strong>in</strong>itiated by roll<strong>in</strong>g.<br />

� Reduce viscosity <strong>of</strong> the oil.<br />

� Coagulate the prote<strong>in</strong> <strong>in</strong> the meal to facilitate oil separation from prote<strong>in</strong> material.<br />

The meals are normally cooked to a moisture content <strong>of</strong> 3 % at 104-1100C.<br />

8.3 SREW-PRESSING<br />

The properly cooked meal is fed to the screw press, which consist <strong>of</strong> an <strong>in</strong>terrupted<br />

helical thread (worm); which revolves with<strong>in</strong> a stationary perforated cyl<strong>in</strong>der called the<br />

cage or barrel. The meal is forced through the barrel by the action <strong>of</strong> the revolv<strong>in</strong>g<br />

worms. The volume axially displaced by the worms dim<strong>in</strong>ishes from the feed<strong>in</strong>g end to<br />

the discharge end, thus compress<strong>in</strong>g the meal as it passes through the barrel.<br />

The expelled oil dra<strong>in</strong>s through the perforation <strong>of</strong> the l<strong>in</strong><strong>in</strong>g bars <strong>of</strong> the barrel while the<br />

de-oiled cake is discharged through annular orifice. In order to prevent extreme<br />

temperatures that could damage the oil and cake quality, the worm- shaft is always<br />

cooled with circulat<strong>in</strong>g water while the barrel is cooled by recycl<strong>in</strong>g some cooled oil. The<br />

follow<strong>in</strong>g facts can be drawn from the concept <strong>of</strong> screw press<strong>in</strong>g:<br />

� With <strong>in</strong>creas<strong>in</strong>g pressure the yield <strong>in</strong>creases reach<strong>in</strong>g a limit at higher pressures. This<br />

limit is dependent on the type <strong>of</strong> seed, seasonal variations, pre-treatment <strong>of</strong> the seed<br />

and the equipment used. Most data available <strong>in</strong> literature are limited to pressures<br />

below 35 MPa, with a few exceptions(.; Ford, R. J.; Wulfsohn, D.; Bargale, P. C<br />

Irudayaraj, J.; Sosulski, F. W.<strong>Journal</strong> <strong>of</strong> Agricultural Eng<strong>in</strong>eer<strong>in</strong>g <strong>Research</strong> 2000.)<br />

� Quality requirements for the oil or the meal may restrict the maximum allowable<br />

temperature to prevent undesired cell wall components pollut<strong>in</strong>g the oil. It is therefore<br />

desirable to reach high yields at lower temperatures.<br />

� Start<strong>in</strong>g from dry seeds, <strong>in</strong>creas<strong>in</strong>g the moisture content (MC) <strong>of</strong> the seeds <strong>in</strong>creases<br />

the yield until a seed-specific maximum. Increas<strong>in</strong>g the moisture content beyond this<br />

optimum decreases the yield aga<strong>in</strong>. This is due to two counteract<strong>in</strong>g phenomena.<br />

Increas<strong>in</strong>g the moisture content <strong>of</strong> the seeds is reported to make the cell walls more<br />

permeable (Bargale, P. C.; S<strong>in</strong>gh, J. <strong>Journal</strong> <strong>of</strong> food science and technology 2000),(<br />

which <strong>in</strong>creases the yield), but also, to cause a plasticization <strong>of</strong> the seed material<br />

COPY RIGHT © 2011 Institute <strong>of</strong> <strong>Interdiscipl<strong>in</strong>ary</strong> Bus<strong>in</strong>ess <strong>Research</strong> 66<br />

JANUARY 2011<br />

VOL 2, NO 9

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