KRISTALISASI PADA PENGOLAHAN CPO
Yield olein from processing palm oil into cooking; oil depends on crystallization process. Two system fractionation palm oil is dry <br /> fractionation and detergent fractionation, where dry _ fractionation process is a cheaper than detergent fractionation. Dry fractionation at <br />...
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| Format: | Theses |
| Language: | Indonesia |
| Online Access: | https://digilib.itb.ac.id/gdl/view/1722 |
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| Institution: | Institut Teknologi Bandung |
| Language: | Indonesia |
| Summary: | Yield olein from processing palm oil into cooking; oil depends on crystallization process. Two system fractionation palm oil is dry <br />
fractionation and detergent fractionation, where dry _ fractionation process is a cheaper than detergent fractionation. Dry fractionation at <br />
i'ractionation as first step process in palm oil is a potential process to he developed. <br />
In this research, the effect of agitation (35, 70, 140 and 2150 rpm), variation of temperature cooling water (27 - 21 °C) and tine of <br />
crystallization process (2 and 3 hours) on growth and the increasing wei u ht of stearin crystal from fractionation palm oil were investigated. This research used CPO and RBDPO. <br />
The growth and the increasing weight of stearin crystal from fractionation CPO and RBDPO have two reginis is 27 - 25 °C (CPO), 30 - 25`C (RBDPO) as a regim 1 and 25 - 22 ° C as a regim It.The optimum agitation as a result of variation of agitation is 3 rpm;. In this research, maximal yield olein in the acceptable range standard cloud point (CP) cooking oil is 64 <br />
CP 10T from crystallization CPO and 64 °•'O', CP 9,5" C from crystallization RBDP0. |
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