Theoretical analysis of reactant dosing concepts to perform parallel-series reactions

The possibility of enhancing selectivities and yields in networks of parallel and series reactions is investigated theoretically. Isothermal tubular reactors are considered where reactants can be introduced at the entrance and also over the wall. The latter way of dosing could be realised, e.g., in a membrane reactor where one or several reactants can be dosed through a porous reactor wall. Besides numerical solutions of the underlying mass balance equations of simplified reactor models, instructive analytical solutions were derived which are valid under certain constraints. Using these solutions an optimisation of the reactor performance could be performed. As objective function the molar fraction of a desired intermediate product at the reactor outlet was maximised. The impact of influencing via the dosing strategy applied the local composition (and thus the local reaction rates) and the component residence time distributions is elucidated.

[1]  Asterios Gavriilidis,et al.  Catalyst Design: Optimal Distribution of Catalyst in Pellets, Reactors, and Membranes , 2005 .

[2]  Andreas Seidel-Morgenstern,et al.  Concentration and residence time effects in packed bed membrane reactors , 2003 .

[3]  Achim Kienle,et al.  Nonlinear computation in DIVA — methods and applications , 2000 .

[4]  W. R. Moser,et al.  Analysis and optimization of cross-flow reactors with staged feed policies : isothermal operation with parallel-series, irreversible reaction systems , 1997 .

[5]  W. R. Moser,et al.  Oxidative coupling of methane using oxygen-permeable dense membrane reactors , 2000 .

[6]  M. Menéndez,et al.  Use of a ceramic membrane reactor for the oxidative dehydrogenation of ethane to ethylene and higher hydrocarbons , 1995 .

[7]  Miguel Menéndez,et al.  Methane oxidative coupling using porous ceramic membrane reactors. I: Reactor development , 1994 .

[8]  Miguel Menéndez,et al.  Methane oxidative coupling using porous ceramic membrane reactors—II. Reaction studies , 1994 .

[9]  W. R. Moser,et al.  Analysis and optimization of cross-flow reactors with distributed reactant feed and product removal , 1997 .

[10]  Andreas Seidel-Morgenstern,et al.  Performance Improvements of Parallel−Series Reactions in Tubular Reactors Using Reactant Dosing Concepts , 2004 .

[11]  Rate equations of solid-catalyzed reactions , 1991 .

[12]  Michael P. Harold,et al.  Intermediate product yield enhancement with a catalytic inorganic membrane—I. Analytical model for the case of isothermal and differential operation , 1993 .

[13]  H. Verweij,et al.  Oxidative coupling of methane in a mixed-conducting perovskite membrane reactor , 1995 .

[14]  Andreas Seidel-Morgenstern,et al.  Comparing porous and dense membranes for the application in membrane reactors , 1999 .

[15]  J. Luyten,et al.  Membrane performance: the key issues for dehydrogenation reactions in a catalytic membrane reactor , 2000 .

[16]  Intermediate product yield enhancement with a catalytic inorganic membrane—II. Nonisothermal and integral operation in a back-mixed reactor , 1997 .

[17]  R. Dittmeyer,et al.  Catalytic dehydrogenation of hydrocarbons in palladium composite membrane reactors , 2000 .

[18]  R. G. Minet,et al.  The study of ethane dehydrogenation in a catalytic membrane reactor , 1992 .

[19]  Yuehe Lin,et al.  Perovskite-type ceramic membrane: synthesis, oxygen permeation and membrane reactor performance for oxidative coupling of methane , 1998 .

[20]  T. Tsotsis,et al.  Propane dehydrogenation in a packed-bed membrane reactor , 1993 .