Phenomenological approach to interpret the effect of liquid flow modulation in trickle bed reactors at the particle scale

This work analyzes the influence of liquid flow modulation on the behavior of a reaction occurring in a spherical porous particle within a trickle bed reactor. A single first-order reaction between a gaseous reactant and a non-volatile liquid reactant is considered. Non-steady-state mass balances fo...

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Autor principal: Ayude, M.A
Otros Autores: Cassanello, M.C, Martínez, O.M, Haure, P.M
Formato: Acta de conferencia Capítulo de libro
Lenguaje:Inglés
Publicado: 2005
Acceso en línea:Registro en Scopus
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024 7 |2 scopus  |a 2-s2.0-22744431790 
040 |a Scopus  |b spa  |c AR-BaUEN  |d AR-BaUEN 
030 |a CESCA 
100 1 |a Ayude, M.A. 
245 1 0 |a Phenomenological approach to interpret the effect of liquid flow modulation in trickle bed reactors at the particle scale 
260 |c 2005 
270 1 0 |m Haure, P.M.; INTEMA, CONICET, UNMDP, J.B. Justo 4302, 7600 Mar del Plata, Buenos Aires, Argentina; email: phaure@fi.mdp.edu.ar 
506 |2 openaire  |e Política editorial 
504 |a Banchero, M., Manna, L., Sicardi, S., Ferri, A., Experimental investigation of fast-mode liquid modulation in a trickle-bed reactor (2004) Chemical Engineering Science, 59, pp. 4149-4154 
504 |a Boelhouwer, J.G., (2001) Nonsteady Operation of Trickle-bed Reactors: Hydrodynamics, Mass and Heat Transfer, , Ph.D. Thesis, Technische Universiteit Eindhoven, The Netherlands 
504 |a Dudukovic, M.P., Larachi, F., Mills, P.L., Multiphase catalytic reactors: A perspective on current knowledge and future trends (2002) Catalysis Reviews, 44, pp. 123-246 
504 |a Goto, S., Smith, J.M., Trickle bed reactor performance: 1. Hold-up and mass transfer effects (1975) A.I.Ch.E. Journal, 21 (6), pp. 706-713 
504 |a Gupta, R., Pulsed flow vapour-liquid reactor (1985) US Patent 4, 526, p. 757 
504 |a Harold, M.P., Ng, K.M., Effectiveness enhancement and reactant depletion in a partially wetted catalyst (1987) A.I.Ch.E. Journal, 33 (9), pp. 1448-1465 
504 |a Haure, P., Hudgins, R.R., Silveston, P.L., Periodic operation of a trickle bed (1989) A.I.Ch.E. Journal, 35, pp. 1437-1444 
504 |a Herskowitz, M., Wetting efficiency in trickle-bed reactors: Its effect on the reactor performance (1981) Chemical Engineering Journal, 22, pp. 167-175 
504 |a Khadilkar, M., Al-Dahhan, M.H., Dudukovic, M.P., Parametric study of unsteady-state flow modulation in trickle-bed reactors (1999) Chemical Engineering Science, 54, pp. 2585-2595 
504 |a Kouris, Ch., Neophytides, St., Vayenas, C.G., Tsamopoulos, J., Unsteady state operation of catalytic particles with constant and periodically changing degree of external wetting (1998) Chemical Engineering Science, 53, pp. 3129-3142 
504 |a Lange, R., Hanika, J., Stradiotto, D., Hudgins, R.R., Silveston, P.L., Investigations of periodically operated trickle-bed reactors (1994) Chemical Engineering Science, 49, pp. 5615-5622 
504 |a Lange, R., Gutsche, R., Hanika, J., Forced periodic operation of a trickle-bed reactor (1999) Chemical Engineering Science, 54, pp. 2569-2573 
504 |a Lee, C.K., Bailey, J.E., Diffusion waves and selectivity modifications in cyclic operation of porous catalyst (1974) Chemical Engineering Science, 29, pp. 1157-1163 
504 |a Muzen, A., Fraguío, M.S., Cassanello, M., Ayude, M.A., Haure, P.M., Martínez, O.M., Clean oxidation of alcohols in a trickle-bed reactor with liquid flow modulation (2005) Industrial and Engineering Chemistry Research, , to be published. Web release date: 05 February 2005. Submitted for publication in the special issue: In honor of Milorad P. Dudukovic 
504 |a Skala, D., Hanika, J., Periodic operations of trickle-bed reactor (2002) Proceedings of the CHISA 2002 - 15th International Congress of Chemical and Process Engineering, , Praga, Zchec Republic, August 2002 
504 |a Stegasov, A.N., Kirillov, V.A., Silveston, P.L., Modeling of catalytic SO2 oxidation for continuous and periodic liquid flow through a trickle bed (1994) Chemical Engineering Science, 49, pp. 3699-3710 
504 |a Tukac, V., Hanika, J., Chyba, V., Periodic state of wet oxidation in trickle-bed reactor (2003) Catalysis Today, 79-80, pp. 427-431 
520 3 |a This work analyzes the influence of liquid flow modulation on the behavior of a reaction occurring in a spherical porous particle within a trickle bed reactor. A single first-order reaction between a gaseous reactant and a non-volatile liquid reactant is considered. Non-steady-state mass balances for gas and liquid reactants are formulated and solved under isothermal conditions in order to focus the analysis on the mass transport effects. Dynamic reactant profiles inside the catalytic particle are obtained for different cycling and system conditions. The enhancement factor (ε) due to periodic operation is defined to evaluate the impact of induced liquid flow modulation on reaction rate. Influence of cycling and system parameters on the enhancement factor is also reported for a wide range of conditions. Experimental trends observed by several authors can be explained with this approach. © 2005 Elsevier Ltd. All rights reserved.  |l eng 
536 |a Detalles de la financiación: Umweltbundesamt 
536 |a Detalles de la financiación: Fundación Antorchas 
536 |a Detalles de la financiación: Universidad Nacional de La Plata, UNLP 
536 |a Detalles de la financiación: Agencia Nacional de Promoción Científica y Tecnológica 
536 |a Detalles de la financiación: Consejo Nacional de Investigaciones Científicas y Técnicas 
536 |a Detalles de la financiación: Financial support from CONICET, UBA, UNMdP, UNLP, ANPCyT and Fundación Antorchas are gratefully acknowledged. 
593 |a INTEMA, CONICET, UNMDP, J.B. Justo 4302, 7600 Mar del Plata, Buenos Aires, Argentina 
593 |a PINMATE, Dep. Industrias, FCEyN-UBA, Int. Güiraldes 2620, C1428BGA Buenos Aires, Argentina 
593 |a Dep. Ing. Química, UNLP-CINDECA, Calle 47 No 257, 1900 La Plata, Argentina 
690 1 0 |a CHEMICAL REACTORS 
690 1 0 |a LIQUID FLOW MODULATION 
690 1 0 |a MATHEMATICAL MODEL 
690 1 0 |a MULTIPHASE REACTIONS 
690 1 0 |a TRANSIENT RESPONSE 
690 1 0 |a TRICKLE BED REACTORS 
690 1 0 |a MASS TRANSPORTATION 
690 1 0 |a POROUS MATERIALS 
690 1 0 |a REACTION KINETICS 
690 1 0 |a LIQUID FLOW MODULATION 
690 1 0 |a REACTION RATE 
690 1 0 |a TRICKLE BED REACTORS 
690 1 0 |a CHEMICAL REACTORS 
690 1 0 |a LIQUID FLOW 
690 1 0 |a MATHEMATICAL MODELING 
690 1 0 |a TRICKLE BED REACTOR 
700 1 |a Cassanello, M.C. 
700 1 |a Martínez, O.M. 
700 1 |a Haure, P.M. 
711 2 |d 22 August 2005 through 24 August 2005  |g Código de la conferencia: 65305 
773 0 |d 2005  |g v. 60  |h pp. 6262-6269  |k n. 22  |p Chem. Eng. Sci.  |n Chemical Engineering Science  |x 00092509  |w (AR-BaUEN)CENRE-291  |t 7th International Conference on Gas-Liquid and Gas-Liquid-Solid Reactor Engineering 
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856 4 0 |u https://doi.org/10.1016/j.ces.2005.03.019  |y DOI 
856 4 0 |u https://hdl.handle.net/20.500.12110/paper_00092509_v60_n22_p6262_Ayude  |y Handle 
856 4 0 |u https://bibliotecadigital.exactas.uba.ar/collection/paper/document/paper_00092509_v60_n22_p6262_Ayude  |y Registro en la Biblioteca Digital 
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