Glycerolysis of palm fatty acid distillate for biodiesel feedstock under different reactor conditions

被引:23
作者
Islam, Aminul [1 ]
Masoumi, Hamid Reza Fard [3 ]
Teo, Siow Hwa [3 ]
Abdollahi, Yadollah [4 ]
Janaun, Jidon [1 ]
Taufiq-Yap, Yun Hin [2 ,3 ]
机构
[1] Univ Malaysia Sabah, Fac Engn, Kota Kinabalu 88400, Sabah, Malaysia
[2] Univ Putra Malaysia, Fac Sci, Catalysis Sci & Technol Res Ctr, Upm Serdang 43400, Selangor, Malaysia
[3] Univ Putra Malaysia, Fac Sci, Dept Chem, Upm Serdang 43400, Selangor, Malaysia
[4] Univ Malaya, Dept Chem, Fac Sci, Kuala Lumpur 50603, Malaysia
关键词
Glycerolysis; Free fatty acids; Palm fatty acid distillate; Acidity; OIL;
D O I
10.1016/j.fuel.2016.01.088
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
This paper deals with the comparative study on glycerolysis of palm fatty acid distillate (PFAD) in a solvent free system at different reaction conditions in an attempt to get maximum degree of FFA% reduction for biodiesel feedstock. Initially, optimization of varied reaction parameters was performed under all the different reaction conditions using artificial neural network (ANN) based on the genetic algorithm (GA). It has been found that the reduction of acidity varies with varying reaction conditions with maximum reaction rate observed in case of reaction carried-out in open reactor system with inert gas flow, followed by the reaction in open reactor system without inert gas flow and then in case of reaction under the close reactor system. In the most favorable case, 1.5 mgKOH/gPFAD of FFA (free fatty acid) was achieved after 90 min of reaction time with an excess glycerol of 4% at 220 degrees C. The results from the ANN model show good agreement with experimental results. Thus, the glycerolysis in open reactor system with inert gas flow (N-2) option is much-preferred option compared to acid esterification for the same biodiesel plant capacity, particularly for high-FFA feedstocks. (c) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:133 / 139
页数:7
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