Esterification of Free Fatty Acids in Used Cooking Oil Using Ion-Exchange Resins as Catalysts: An Efficient Pretreatment Method for Biodiesel Feedstock

被引:55
作者
Abidin, Sumaiya Zainal [2 ,3 ]
Haigh, Kathleen F. [2 ]
Saha, Basudeb [1 ]
机构
[1] London S Bank Univ, Dept Appl Sci, Fac Engn Sci & Built Environm, London SE1 0AA, England
[2] Univ Loughborough, Dept Chem Engn, Loughborough LE11 3TU, Leics, England
[3] Univ Malaysia Pahang, Fac Chem & Nat Resources Engn, Kuantan 26300, Pahang Darul Ma, Malaysia
基金
英国工程与自然科学研究理事会;
关键词
VEGETABLE-OIL; ACETIC-ACID; FRYING OIL; SEED OIL; TRANSESTERIFICATION; ETHANOLYSIS; METHANOL;
D O I
10.1021/ie3007566
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The esterification of used cooking oil (UCO) with methanol was studied using different types of ion exchange resins, that is, Purolite D5081, Purolite D5082, and Amberlyst 36. Several catalyst characterization. analyses (elemental analysis, surface area measurement, particle size distribution analysis, scanning electron microscopy analysis, true density measurement, and acid capacity analysis) have been conducted in the screening stage. Of all of the catalysts investigated, Purolite D5081 resin showed the best catalytic performance and was selected for further experimental studies. The esterification process was carried out in a jacketed stirred batch reactor for 8 h. Elimination of mass transfer resistances and the effect of catalyst loading (0.5-1.5% w/w), reaction temperature (50-65 degrees C), and methanol to UCO feed mole ratio (4:1-12:1) on the conversion of FFAs were investigated. The highest FFAs conversion was found to be 92%, at a catalyst loading of 1.25% w/w, 60 degrees C reaction temperature, 6:1 methanol to UCO molar ratio, and stirring speed of 475 rpm. During the reusability study, the conversion of catalyst dropped by 8-10% after each reutilization cycle. Several experiments have been conducted through the homogeneous contribution study, and the results confirmed that both resin pore blockage and sulfur leaching are dominant factors that decrease the catalytic performance of Purolite D5081 ion exchange resin.
引用
收藏
页码:14653 / 14664
页数:12
相关论文
共 46 条
[1]  
[Anonymous], 2011, Reference number ISO, V13314, P1
[2]   Potential alternatives to edible oils for biodiesel production - A review of current work [J].
Balat, Mustafa .
ENERGY CONVERSION AND MANAGEMENT, 2011, 52 (02) :1479-1492
[3]   Review: examining the use of different feedstock for the production of biodiesel [J].
Behzadi, S. ;
Farid, M. M. .
ASIA-PACIFIC JOURNAL OF CHEMICAL ENGINEERING, 2007, 2 (05) :480-486
[4]   Low Temperature De-acidification Process of Animal Fat as a Pre-Step to Biodiesel Production [J].
Bianchi, C. L. ;
Boffito, D. C. ;
Pirola, C. ;
Ragaini, V. .
CATALYSIS LETTERS, 2010, 134 (1-2) :179-183
[5]   Foreword - Biodiesel production and processing [J].
Boehman, AL .
FUEL PROCESSING TECHNOLOGY, 2005, 86 (10) :1057-1058
[6]   The potential of restaurant waste lipids as biodiesel feedstocks [J].
Canakci, Mustafa .
BIORESOURCE TECHNOLOGY, 2007, 98 (01) :183-190
[7]   Transesterification of vegetable oil to biodiesel using a heteropolyacid solid catalyst [J].
Chai, Fang ;
Cao, Fenghua ;
Zhai, Fengying ;
Chen, Yang ;
Wang, Xiaohong ;
Su, Zhongmin .
ADVANCED SYNTHESIS & CATALYSIS, 2007, 349 (07) :1057-1065
[8]  
David F., 2005, Agilent Technologies, Column Selection for the Analysis of Fatty Acid Methyl Esters, P1
[9]   Gas chromatographic characterization of soapstocks from vegetable oil refining [J].
Dowd, MK .
JOURNAL OF CHROMATOGRAPHY A, 1998, 816 (02) :185-193
[10]   Ethanolysis of used frying oil.: Biodiesel preparation and characterization [J].
Encinar, J. M. ;
Gonzalez, J. F. ;
Rodriguez-Reinares, A. .
FUEL PROCESSING TECHNOLOGY, 2007, 88 (05) :513-522