4.6 Article

Enhancing the stability of porous catalysts with supercritical reaction media

期刊

APPLIED CATALYSIS A-GENERAL
卷 212, 期 1-2, 页码 199-213

出版社

ELSEVIER
DOI: 10.1016/S0926-860X(00)00848-6

关键词

catalyst deactivation; enhancing catalyst stability; supercritical reaction media

向作者/读者索取更多资源

Adsorption/desorption and pore-transport are key parameters influencing the activity and product selectivity in porous catalysts. With conventional reaction media (gas or liquid phase), one of these parameters is generally favorable while the other is not. For instance, while desorption of heavy hydrocarbons from the catalyst is usually the rate-limiting step in gas-phase reactions, transport of the reactants/products is the limiting step in liquid-phase reaction media. With conventional media, it is difficult to achieve the desired combination of fluid properties for optimum system performance. In contrast, density and transport properties can be continuously pressure-tuned in the near-critical region to obtain unique fluid properties (e.g. gas-like transport properties, liquid-like solvent power and heat capacities), that have been exploited in several ways such as (a) the in situ extraction of heavy hydrocarbons (i.e. coke precursors) from the catalyst surface and their transport out of the pores before they are transformed to consolidated coke; (b) complete miscibility of reactants such as hydrogen in the reaction mixture and enhanced pore-transport of these reactants to the catalyst surface, thereby promoting desired reaction pathways; and (c) control of temperature rise in exothermic reactions. Experimental and theoretical investigations are presented to demonstrate beneficial pressure-tuning effects on catalyst activity and product selectivity during continuous processing of a variety of reactions such as these: geometric isomerization and alkylation on solid acid catalysts; Fischer-Tropsch (FT) synthesis on supported Fe catalysts; and fixed-bed hydrogenation on supported catalysts. The possibility to perform solid acid catalysis with extended activity tan environmentally safer alternative to liquid acid processes) and fixed-bed hydrogenations with tunable selectivity and controlled temperature rise (preferred over slurry phase operation) makes supercritical reaction media particularly appealing alternatives to conventional reactor operation. (C) 2001 Elsevier Science B.V. All rights reserved.

作者

我是这篇论文的作者
点击您的名字以认领此论文并将其添加到您的个人资料中。

评论

主要评分

4.6
评分不足

次要评分

新颖性
-
重要性
-
科学严谨性
-
评价这篇论文

推荐

暂无数据
暂无数据