On the Influence of the Catalyst Physical Properties on the Stability of Forced Unsteady-State After-Burners

The influence of the physical and chemical properties of the catalyst on the stability of forced unsteady-state catalytic after-burners has been investigated in detail by numerical simulation, employing either a simplified or a complete two-phase one-dimensional model, having as an objective the optimization of the catalyst. If the aim is to obtain stable operation, feeding cold and lean VOC mixtures without auxiliary fuel, both heat capacity and thermal conductivity of the catalyst have been shown to play a role, not less important than kinetic activity, strongly influencing the minimum inlet VOC concentration required for autothermal operation. Perovskite-type catalysts, even if less active than noble metals over traditional commercial supports, show, for this specific application, better performances because of their high heat capacity and low thermal conductivity. Dilution of the adopted catalyst with an inert material having high thermal capacity has also been considered in order to increase the heat capacity of the bed (and, as a consequence, the ability of the system to keep the heat of reaction inside the catalytic bed).

[1]  A. Barresi,et al.  Nonstationary catalytic destruction of lean waste gases in a network of burners and a reverse-flow reactor under nonadiabatic conditions , 1997 .

[2]  Ulrich Nieken,et al.  Limiting cases and approximate solutions for fixed-bed reactors with periodic flow reversal , 1995 .

[3]  G. Bunimovich,et al.  Reverse-Flow Operation in Fixed Bed Catalytic Reactors , 1996 .

[4]  D. Kunii,et al.  Heat transfer characteristics of porous rocks , 1960 .

[5]  Hugo S. Caram,et al.  The design of reverse flow reactors for catalytic combustion systems , 1995 .

[6]  Antonello Barresi,et al.  Dynamics and control of forced-unsteady-state catalytic combustors , 2002 .

[7]  Andrew G. Salinger,et al.  The direct calculation of periodic states of the reverse flow reactior—I. Methodology and propane combustion results , 1996 .

[8]  Davide Fissore,et al.  Comparison between the reverse-flow reactor and a network of reactors for the oxidation of lean VOC mixtures , 2002 .

[9]  Gerhart Eigenberger,et al.  Fixed‐Bed Reactors , 2000 .

[10]  A. Barresi,et al.  Efficient design and scale up of reverse-flow catalytic combustors , 2000 .

[11]  Y. Matros,et al.  Unsteady-State Performance of Heterogeneous Catalytic Reactions , 1983 .

[12]  K. Westerterp,et al.  Operation of a catalytic reverse flow reactor for the purification of air contaminated with volatile organic compounds , 1997 .

[13]  Y. Matros,et al.  Forced unsteady‐state processes in heterogeneous catalytic reactors , 1996 .

[14]  Gerhart Eigenberger,et al.  Autothermal fixed-bed reactor concepts , 2000 .

[15]  Antonello Barresi,et al.  Simplified procedure for design of catalytic combustors with periodic flow reversal , 2001 .

[16]  Gaetano Continillo,et al.  Nonlinear dynamics and control in process engineering-recent advances , 2002 .

[17]  Antonello Barresi,et al.  Development and design of a forced unsteady-state reactor through numerical simulation , 2000 .

[18]  J. R. Schopper,et al.  Experimental and theoretical investigations on the influence of fluids, solids and interactions between them on thermal properties of porous rocks , 1998 .

[19]  E. Wicke,et al.  Zündzonen heterogener Reaktionen in gasdurchströmten Körnerschichten , 1959 .