Academic
Publications
PROSES GLISEROLISIS MINYAK KELAPA SAWIT MENJADI MONO DAN DIACYL GLISEROL DENGAN PELARUT N- BUTANOL DAN KATALIS MgO

PROSES GLISEROLISIS MINYAK KELAPA SAWIT MENJADI MONO DAN DIACYL GLISEROL DENGAN PELARUT N- BUTANOL DAN KATALIS MgO,Didi Dwi Anggoro,Setia Budi

PROSES GLISEROLISIS MINYAK KELAPA SAWIT MENJADI MONO DAN DIACYL GLISEROL DENGAN PELARUT N- BUTANOL DAN KATALIS MgO  
BibTex | RIS | RefWorks Download
Indonesia is one of the biggest palm oil producing countries in the world. More than a half of its production is to fulfill internal necessity and the rest is exported. Derivative product from palm oil, such as Mono-Di-acyl Glyceride has high economic value and during this time, Indonesia gets it by importing. MAG-DAG can be formed chemically from glyceride which exist in fat or oil, such as CPO, with glycerol. The aim of this research are produced MAG-DAG from CPO at lower temperature (under 200 0 C) in laboratory batch reactor, and knowing the effect of the variables.. The dependent variables are temperature (low level=70 o C, medium level=90 o C, dan high level=110 o C), gyiserol/CPO ratio (low leve= 3, medium level=4, dan high level=5), dan catalyst concentration (low level=2, medium level=3, dan high level=4). And the independent variables are total weight basis 300 grams, speed of stirring 400 rpm, reaction time 4 hours and amount of solvent 20 ml/10 grams CPO. From processing data using STATISTICA version 6.0, optimum conditions are reached at 70-100 0 C, glyserol/CPO ratio at 3,5-4,5 and catalyst concentration at 2,5-4%. By adding n-butanol as a solvent, reaction can be held at lower temperature without decrease final concentration. ANOVA data processing and effect analyst result mathematical model of MAG-DAG production process.
Published in 2008.
Cumulative Annual
View Publication
The following links allow you to view full publications. These links are maintained by other sources not affiliated with Microsoft Academic Search.