Partial oxidation of propane to acrylic acid at a Mo-V-Te-Nb-oxide catalyst

被引:39
作者
Balcells, E
Borgmeier, F
Grisstede, I
Lintz, HG
Rosowski, F
机构
[1] Univ Karlsruhe, Inst Chem Verfahrenstech, D-76128 Karlsruhe, Germany
[2] BASF AG, D-67056 Ludwigshafen, Germany
关键词
partial oxidation; fropane; acrylic acid; mixed oxide catalyst; reaction network; first order reactions; kinetic coefficients; fixed bed; model calculation;
D O I
10.1016/j.apcata.2004.02.019
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 partial oxidation of propane has been investigated at a multicomponent oxidic catalyst in the temperature range 360 < T (degreesC) < 420. The kinetic measurements were carried out in an integrally operated fixed bed reactor with distributed local sampling. The oxygen-propane ratio in the feed has been varied in the range 1.5 < x(O2)/x(propane) < 4 and the water content was increased up to 50 vol.%. The results can be described quantitatively by a network of parallel and consecutive first order reactions. (C) 2004 Elsevier B.V. All rights reserved.
引用
收藏
页码:211 / 221
页数:11
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