Multicomponent Dosing in Membrane Reactors Including Recycling-Concept and Demonstration for the Oxidative Dehydrogenation of Propane

被引:11
作者
Hamel, Christof [1 ,2 ]
Wolff, Tanya [2 ]
Subramaniam, Pushpavanam [3 ]
Seidel-Morgenstern, Andreas [1 ,2 ]
机构
[1] Otto Von Guericke Univ, Inst Proc Engn, D-39106 Magdeburg, Germany
[2] Max Planck Inst Dynam Complex Tech Syst, D-39106 Magdeburg, Germany
[3] Indian Inst Technol, Dept Chem Engn, Madras 600036, Tamil Nadu, India
关键词
PARALLEL-SERIES REACTIONS; CROSS-FLOW REACTORS; OXIDE CATALYSTS; SELECTIVE OXIDATION; KINETICS; ETHANE; OPTIMIZATION; ETHYLENE; FEED; PURE;
D O I
10.1021/ie2001692
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The potential of a multicomponent distributed reactant dosing via membranes for enhancing selectivity and yield in a network of series and parallel reactions is investigated in this work. In a preliminary theoretical feasibility study, the optimal local concentrations of the various reactants used to improve the selectivity and conversion of the desired intermediate product were determined. These results were extended to a case study. For this examination, the oxidative dehydrogenation of propane to the kinetically limited intermediate product propylene on a VO(x)/gamma-Al(2)O(3) catalyst was considered. The kinetic equations and parameters were first estimated. It is shown that, compared to a single-component dosing of O(2) via membranes, the yield of propylene can be almost trebled via a controlled simultaneous dosing of oxygen and propane.
引用
收藏
页码:12895 / 12903
页数:9
相关论文
共 34 条
[21]   The temperature-scanning plug flow reactor (TSPFR) applied to complex reactions - Oxidative dehydrogenation of propane as an example [J].
Kolkowski, M ;
Keil, FJ ;
Liebner, C ;
Wolf, D ;
Baerns, M .
CHEMICAL ENGINEERING JOURNAL, 2005, 108 (03) :219-226
[22]   A high-speed method for obtaining kinetic data for exothermic or endothermic catalytic reactions under non-isothermal conditions illustrated for the ammonia synthesis [J].
Liebner, C ;
Wolf, D ;
Baerns, M ;
Kolkowski, M ;
Keil, FJ .
APPLIED CATALYSIS A-GENERAL, 2003, 240 (1-2) :95-110
[23]  
Liebner C, 2003, THESIS U BERLIN BERL
[24]   Analysis and optimization of cross-flow reactors for oxidative coupling of methane [J].
Lu, YP ;
Dixon, AG ;
Moser, WR ;
Ma, YH .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1997, 36 (03) :559-567
[25]   Analysis and optimization of cross-flow reactors with distributed reactant feed and product removal [J].
Lu, YP ;
Dixon, AG ;
Moser, WR ;
Ma, YH .
CATALYSIS TODAY, 1997, 35 (04) :443-450
[26]  
Marquardt D., 1963, SIAM J APPL MATH, V11, P431, DOI [DOI 10.1137/0111030, 10.1137/0111030]
[27]  
Moulijn J.A., 2001, HIGH THROUGHPUT EXPT
[28]  
Oppermann H., 1983, VANADIUM OXIDE
[29]  
Seidel-Morgenstern A., 2010, Membrane Reactors: Distributing Reactants to Improve Selectivity and Yield
[30]  
Sundmacher K, 2005, INTEGRATED CHEMICAL PROCESSES: SYNTHESIS, OPERATION, ANALYSIS, AND CONTROL, P1, DOI 10.1002/3527605738