In situ catalyst activity control in a novel membrane reactor-Reaction driven wireless electrochemical promotion of catalysis

被引:7
作者
Poulidi, D. [1 ]
Metcalfe, I. S. [1 ]
机构
[1] Univ Newcastle, Sch Chem Engn & Adv Mat, Univ Res Ctr Catalysis & Intensified Proc, Newcastle Upon Tyne NE1 7RU, Tyne & Wear, England
基金
英国工程与自然科学研究理事会;
关键词
Wireless electrochemical promotion of catalysis; Metal support interactions; Oxygen spillover; Catalyst activation and deactivation; Membrane reactors; ETHYLENE OXIDATION; CONDUCTING MEMBRANE;
D O I
10.1016/j.ces.2009.06.013
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
A dual chamber membrane reactor was used in order to study the effect of macroscopically applied oxygen chemical potential differences to a platinum catalyst supported on a mixed oxygen ion and electronic conducting membrane. It is believed that the oxygen chemical potential difference imposed by the use of an oxygen sweep in one of the reactor chambers causes the back-spillover of oxygen species from the support onto the catalyst surface, resulting in the modification of the catalytic activity. The use of different sweep gases, such as ethylene and hydrogen was investigated as the means to reverse the rate modification by removing the spilt over species from the catalyst surface and returning the system to its initial state. Oxygen sweep in general had a positive effect on the reaction rate with rate increases up to 20% measured. Experimental results showed that hydrogen is a more potent sweep gas than ethylene in terms of the ability to reverse rate modification. A 10% rate loss was observed when using an ethylene sweep as compared with an almost 60% rate decrease when hydrogen was used as the sweep gas. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:446 / 450
页数:5
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