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在磺酸改性催化剂上,通过生物柴油衍生甘油与乙醇的醚化反应制备燃料配方。

Etherification of biodiesel-derived glycerol with ethanol for fuel formulation over sulfonic modified catalysts.

机构信息

Department of Chemical and Environmental Technology, ESCET, Universidad Rey Juan Carlos, C/Tulipán s/n, E-28933 Móstoles, Madrid, Spain.

出版信息

Bioresour Technol. 2012 Jan;103(1):142-51. doi: 10.1016/j.biortech.2011.09.105. Epub 2011 Oct 1.

Abstract

The present study is focused on the etherification of biodiesel-derived glycerol with anhydrous ethanol over arenesulfonic acid-functionalized mesostructured silicas to produce ethyl ethers of glycerol that can be used as gasoline or diesel fuel biocomponents. Within the studied range, the best conditions to maximize glycerol conversion and yield towards ethyl-glycerols are: T=200 °C, ethanol/glycerol molar ratio=15/1, and catalyst loading=19 wt%. Under these reaction conditions, 74% glycerol conversion and 42% yield to ethyl ethers have been achieved after 4 h of reaction but with a significant presence of glycerol by-products. In contrast, lower reaction temperatures (T=160 °C) and moderate catalyst loading (14 wt%) in presence of a high ethanol concentration (ethanol/glycerol molar ratio=15/1) are necessary to avoid the formation of glycerol by-products and maximize ethyl-glycerols selectivity. Interestingly, a close catalytic performance to that achieved using high purity glycerol has been obtained with low-grade water-containing glycerol.

摘要

本研究集中于在芳族磺酸功能化介孔硅上用无水乙醇醚化生物柴油衍生的甘油,以生产可用作汽油或柴油燃料生物成分的甘油乙基醚。在所研究的范围内,最大程度地提高甘油转化率和甘油乙基醚产率的最佳条件为:T=200°C,乙醇/甘油摩尔比=15/1,催化剂负载量=19wt%。在这些反应条件下,反应 4 小时后可实现 74%的甘油转化率和 42%的乙基醚产率,但存在大量的甘油副产物。相比之下,在高乙醇浓度(乙醇/甘油摩尔比=15/1)存在下,较低的反应温度(T=160°C)和适度的催化剂负载量(14wt%)是避免甘油副产物形成并最大化乙基醚选择性所必需的。有趣的是,即使使用低等级含水甘油,也可以获得与使用高纯度甘油相当的催化性能。

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