Dehydration-hydrogenation of glycerol into 1,2-propanediol at ambient hydrogen pressure

被引:168
作者
Akiyama, Masaki [1 ]
Sato, Satoshi [1 ]
Takahashi, Ryoji [2 ]
Inui, Kanichiro [3 ]
Yokota, Masahiro [4 ]
机构
[1] Chiba Univ, Grad Sch Engn, Inage Ku, Chiba 2638522, Japan
[2] Ehime Univ, Grad Sch Sci & Engn, Bunkyo Ku, Matsuyama, Ehime 7908577, Japan
[3] Chisso Petrochem Corp, Ichihara, Chiba 2908551, Japan
[4] Chisso Corp, Chiyoda Ku, Tokyo 1008105, Japan
关键词
Dehydration; Glycerol; 1,2-Propanediol; Hydroxyacetone; Hydrogenation; Copper; GAS-PHASE DEHYDRATION; SELECTIVE HYDROGENOLYSIS; SUSTAINABLE PRODUCTION; PROPYLENE-GLYCOL; CATALYTIC DEHYDRATION; ACROLEIN; BIOMASS; CONVERSION; ACID; BASE;
D O I
10.1016/j.apcata.2009.09.029
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 vapor-phase reaction of glycerol was performed over copper metal catalysts at ambient hydrogen pressure. Glycerol was converted into 1,2-propanediol (1,2-PDO) through the dehydration into hydroxyacetone, followed by the hydrogenation into 1,2-PDO. The yield of 1,2-PDO was limited up to 80% at a constant temperature of 190 degrees C because of a trade-off problem between the dehydration and the hydrogenation. The dehydration needs relatively high reaction temperatures, whereas the hydrogenation favors low temperatures and high hydrogen concentration. We developed an efficient process during which glycerol was converted into 1,2-PDO with yield higher than 96% in hydrogen flow at gradient temperatures; the dehydration into hydroxyacetone was catalyzed at ca. 200 degrees C, and the following hydrogenation into 1,2-PDO was completed at ca. 120 degrees C. The developed process controls the thermodynamic equilibrium of the second-step hydrogenation. (C) 2009 Elsevier B.V. All rights reserved.
引用
收藏
页码:60 / 66
页数:7
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