Transesterification of croton megalocarpus oil to biodiesel over WO3 supported on silica mesoporous-macroparticles catalyst

被引:36
作者
Aziz, M. A. A. [1 ]
Puad, K. [2 ]
Triwahyono, S. [2 ]
Jalil, A. A. [1 ,3 ]
Khayoon, M. S. [2 ]
Atabani, A. E. [4 ]
Ramli, Z. [2 ]
Majid, Z. A. [2 ]
Prasetyoko, D. [5 ]
Hartanto, D. [5 ]
机构
[1] Univ Teknol Malaysia, Dept Chem Engn, Fac Chem & Energy Engn, Johor Baharu 81310, Johor, Malaysia
[2] Univ Teknol Malaysia, Dept Chem, Fac Sci, Johor Baharu 81310, Johor, Malaysia
[3] Univ Teknol Malaysia, Ctr Hydrogen Energy, Inst Future Energy, Johor Baharu 81310, Johor, Malaysia
[4] Erciyes Univ, Energy Div, Dept Mech Engn, Fac Engn, TR-38039 Kayseri, Turkey
[5] Inst Teknol Sepuluh Nopember, Dept Chem, Fac Math & Nat Sci, Sukolilo 60111, Surabaya, Indonesia
关键词
Silica mesoporous-macroparticles (SMP); WO3; catalyst; Transesterification; Croton megalocarpus oil; Response surface methodology; Lewis acid sites; RESPONSE-SURFACE METHODOLOGY; ACID; ESTERIFICATION; NANOPARTICLES; GLUTARALDEHYDE; OPTIMIZATION; CARBON;
D O I
10.1016/j.cej.2017.02.049
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The transesterification of croton megalocarpus oil with methanol to fatty acid methyl ester (FAME) was carried out using WO3 supported on silica mesoporous-macroparticles (WO3/SMP) as a heterogeneous acid catalyst. The silica mesoporous-macroparticles (SMP) and WO3/SMP were synthesized by sol-gel and impregnation method, respectively. The catalysts were characterized with XRD, FTIR, N2 adsorption-desorption, SEM and TEM. The presence of WO3 gave a negative effect on the crystallinity and surface area of the SMP as evidenced by XRD and N-2 adsorption-desorption studies, respectively. Pyridine adsorbed FTIR spectroscopy showed that the concentration of Bronsted and Lewis acid sites was dependent on the WO3 loading on SMP. 2 wt% of WO3 loading on SMP (2WO(3)/SMP) exhibited the highest intensity of Lewis acid sites which is vital in transesterification reaction. Under the optimum reaction condition determined through response surface methodology (RSM), 2 wt% WO3 loading, 4.5 wt% catalyst amount, 9:1 methanol to oil molar ratio, 45 min reaction time and 343 K reaction temperature yielded a 96% of biodiesel product. The highest catalytic activity of 2WO(3)/SMP may be attributed to the high Lewis acid sites content and the presence of both intra- and interparticle pores of the catalyst that facilitated and enhanced the transport of reactants and products during the reaction. (C) 2017 Elsevier B.V. All rights reserved.
引用
收藏
页码:882 / 892
页数:11
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