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In relation to this article, we declare that there is no conflict of interest.
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Received December 20, 2008
Accepted January 21, 2009
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Effect of Cs(x)H(3-x)PW(12)O(40) addition on the catalytic performance of ZnFe(2)O(4) in the oxidative dehydrogenation of n-butene to 1,3-butadiene

School of Chemical and Biological Engineering, Institute of Chemical Processes, Seoul National University, Shinlim-dong, Gwanak-gu, Seoul 151-744, Korea 1SK Energy Corporation, Yuseong-gu, Daejeon 305-712, Korea
inksong@snu.ac.kr
Korean Journal of Chemical Engineering, July 2009, 26(4), 994-998(5), 10.1007/s11814-009-0165-z
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Abstract

Oxidative dehydrogenation of n-butene to 1,3-butadiene over ZnFe(2)O(4) catalyst mixed with Cs(x)H(3-x)PW(12)O(40) heteropolyacid (HPA) was performed in a continuous flow fixed-bed reactor. The effect of Cs(x)H(3-x)PW(12)O(40) addition on the catalytic performance of ZnFe(2)O(4) was investigated. Cs(x)H(3-x)PW(12)O(40) itself showed very low catalytic performance in the oxidative dehydrogenation of n-butene. However, addition of small amount of Cs(x)H(3-x)PW(12)O(40) into ZnFe(2)O(4) enhanced the catalytic performance of ZnFe(2)O(4) catalyst. The catalytic performance of ZnFe(2)O(4)-Cs(x)H(3-x)PW(12)O(40) mixed catalysts was closely related to the surface acidity of Cs(x)H(3-x)PW(12)O(40). Among the catalysts tested, ZnFe(2)O(4)-Cs(2.5)H(0.5)PW(12)O(40) mixed catalyst showed the best catalytic performance. Strong acid strength and large surface acidity of Cs(2.5)H(0.5)PW(12)O(40) was responsible for high catalytic performance of ZnFe(2)O(4)-Cs(2.5)H(0.5)PW(12)O(40) mixed catalyst. Thus, Cs(2.5)H(0.5)PW(12)O(40) could be utilized as an efficient promoter and diluent in formulating ZnFe(2)O(4) catalyst for the oxidative dehydrogenation of n-butene.

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