1,3-Butadiene Production Using Ash-Based Catalyst

被引:0
|
作者
Bojang, Adama A. [1 ]
Wu, Ho Shing [1 ]
机构
[1] Yuan Ze Univ, Dept Chem Engn & Mat Sci, 135 Yuan Tung Rd Chung Li, Taoyuan 32003, Taiwan
关键词
1; 3-butadiene; ash; magnesium oxide; ethanol; ETHANOL CONVERSION; BUTADIENE; MGO; COPRECIPITATION; ZN;
D O I
10.3390/catal13020258
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The production of 1,3-butadiene from ethanol was carried out using ash as a catalyst in combination with Zr and Mg. The catalytic experiments were carried out at 350-400 degrees C with a different weight hourly space velocity (WHSV). The catalysts that were used were combined as follows: Ash, Ash:MgO (weight ratio 1:1), Ash:MgO (1:2), Ash:MgO (1:3), and Ash: MgO/ZrO2 (1:1:1). The characterization of the catalyst was carried out using BET, SEM, XRD, TGA, and XPS, respectively. The yield of 1,3-butadiene using bare ash was 65% at 400 degrees C and 2.5 h(-1) of WHSV. Using the Ash:MgO (1:2) catalyst led to an ethanol conversion rate of 79 % at 350 degrees C; the yield and selectivity of 1,3-butadiene were 48% and 87.8 %, respectively. Using the Ash:MgO(1:3) catalyst led to a 1,3-butadiene yield of 25% and a selectivity of 82% at 350 degrees C. The Ash:MgO(1:2) catalyst had a 1,3-butadiene yield of 50% and selectivity of 83%, and the Ash:MgO(1:1) had a 1,3-butadiene yield of 30% and selectivity of 80%, while the Ash:MgO/ZrO2 (1:1:1) catalyst had a 1,3-butadiene yield of 50% and selectivity of 90.8% at 2.5 h(-1) of WHSV.
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页数:17
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