Continuous biodiesel production from acidic oil using a combination of the acid-, alkali-catalyzed membrane and GO/PVDF separation membrane

被引:9
|
作者
Shi, Wenying [1 ]
Li, Tengfei [1 ]
Li, Hongbin [1 ]
Du, Qiyun [2 ]
Zhang, Haixia [1 ]
Qin, Xiaohong [1 ,3 ]
机构
[1] Henan Univ Engn, Sch Text Engn, 1 Xianghe Rd, Zhengzhou 450007, Henan, Peoples R China
[2] Tianjin Polytech Univ, State Key Lab Separat Membranes & Membrane Proc, Tianjin 300387, Peoples R China
[3] Donghua Univ, Sch Text Sci, Shanghai 201620, Peoples R China
关键词
Esterification; Transesterification; Continuous biodiesel production; Separation membrane; Catalytic membrane; SOYBEAN OIL; TRANSESTERIFICATION; OPTIMIZATION; REACTOR; FAT;
D O I
10.1016/j.jiec.2021.11.057
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
An integrated process of esterification with phosphotungstic acid/poly (ether sulfone) (PWA/PES) membrane, transesterification with alkalized polysulfone (APSF) membrane and Graphene Oxide/poly (vinylidene fluoride) (GO/PVDF) separation membrane was carried out to produce biodiesel from acidic oil. At the first step, the PWA/PES membrane was introduced to catalyze the esterification reaction. The morphology, maximum pore size, porosity and catalytic esterification performance of PWA/PES membrane were investigated. After the esterification, products and reactants without reaction were put into the GO/PVDF separation membrane to soybean oil and other substances. The permeation mixture flux and soybean oil rejection of the GO/PVDF separation membrane is 597.89 L/m(2).h and 98.02%, respectively. At the second step, the APSF membrane was added to catalyze the transesterification reaction in which the soybean oil reacted with methanol. The results showed that the esterification conversion was 98.6% and transesterification conversion was 91.2%. The main parameters of the biodiesel product obtained meet the Chinese Standard (GB/T 20828) and European Standard (EN 14214). (C) 2021 The Korean Society of Industrial and Engineering Chemistry. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:268 / 279
页数:12
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