Glycerol valorization through production of di-glyceryl butyl ether with sulfonic acid functionalized KIT-6 catalyst

被引:10
|
作者
Tran, Thi Tuong Vi [1 ]
Obpirompoo, Maytinee [1 ,2 ]
Kongparakul, Suwadee [1 ,2 ]
Karnjanakom, Surachai [3 ]
Reubroycharoen, Prasert [4 ]
Guan, Guoqing [5 ]
Chanlek, Narong [6 ]
Samart, Chanatip [1 ,2 ]
机构
[1] Thammasat Univ, Fac Sci & Technol, Dept Chem, Pathum Thani 12120, Thailand
[2] Thammasat Univ, Res Unit Bioenergy & Catalysis BCRU, Pathum Thani 12120, Thailand
[3] Rangsit Univ, Fac Sci, Dept Chem, Pathum Thani 12000, Thailand
[4] Chulalongkorn Univ, Fac Sci, Dept Chem Technol, Bangkok 10330, Thailand
[5] Hirosaki Univ, Inst Reg Innovat, Aomori 0300813, Japan
[6] Synchrotron Light Res Inst SLRI, 111 Univ Ave, Muang 30000, Nakhon Ratchasi, Thailand
关键词
Etherification; Glycerol; SO3H-KIT-6; catalyst; Valuable fuel additive; di-GNBEs; OXYGENATED ADDITIVES; HIGHLY EFFICIENT; ETHERIFICATION; FUEL; BUTANOL; COMBUSTION; CONVERSION; IMPACT;
D O I
10.1016/j.crcon.2020.12.003
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
In this work, the etherification of glycerol with n-butanol catalyzed by sulfonic acid functionalized on KIT-6 mesoporous silica (SO3H-KIT-6) was investigated for the production of valuable fuel additives. The SO3H-KIT6 catalyst was synthesized by co-condensation with different molar ratios of tetraethoxysilane and 3-mercaptopropyl(methyl)di-methoxy silane. The etherification reaction was systematically examined to determine the optimal reaction temperature, reaction time, catalyst loading, and glycerol to n-butanol ratio under autogenous pressure. The maximum glycerol conversion and di-glyceryl n-butyl ether (di-GNBE) selectivity were 59.09 and 51.50%, respectively, when the SO3H-KIT-6 catalyst with the highest acidity was applied. Interestingly, the presence of a methyl group on the catalyst surface prevented glycerol adsorption during the reaction process, leading to the inhibition of undesired product formation. The SO3H-KIT-6 catalyst could be reused up to three times, with only a 13% decrease in glycerol conversion being found. Moreover, the superior performance of the SO3H-KIT-6 catalyst for di-GNBE production was also demonstrated compared with conventional solid acid catalysts including HZSM-5, H-beta zeolite, Amberlyst-35, and Amberlyst-36.
引用
收藏
页码:182 / 189
页数:8
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