Towards a comprehensive model for liquid flow modulation in trickle bed reactors
The response of an isothermal TBR to a liquid flow modulation ON-OFF strategy is examined through a model aimed at the reactor scale. The reaction is gas-limited and first order with respect to both reactants. Liquid hydrodynamic behavior is considered by means of two different approaches: the Liqui...
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| Formato: | Capítulo de libro |
| Lenguaje: | Inglés |
| Publicado: |
2009
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| Acceso en línea: | Registro en Scopus DOI Handle Registro en la Biblioteca Digital |
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| LEADER | 08335caa a22009377a 4500 | ||
|---|---|---|---|
| 001 | PAPER-8341 | ||
| 003 | AR-BaUEN | ||
| 005 | 20230518203809.0 | ||
| 008 | 190411s2009 xx ||||fo|||| 00| 0 eng|d | ||
| 024 | 7 | |2 scopus |a 2-s2.0-75149184585 | |
| 040 | |a Scopus |b spa |c AR-BaUEN |d AR-BaUEN | ||
| 030 | |a CMEJA | ||
| 100 | 1 | |a Ayude, M.A. | |
| 245 | 1 | 0 | |a Towards a comprehensive model for liquid flow modulation in trickle bed reactors |
| 260 | |c 2009 | ||
| 270 | 1 | 0 | |m Ayude, M.A.; INTEMA, CONICET, UNMdP., J.B. Justo 4302, 7600 Mar del Plata, Argentina; email: mayude@fi.mdp.edu.ar |
| 506 | |2 openaire |e Política editorial | ||
| 504 | |a Schadlich, K., Hofmann, H., Periodical operation of chemical processes and evaluation of conversion improvements (1983) Chem. Eng. Sci., 38, pp. 1375-1384 | ||
| 504 | |a Silveston, P.L., Hanika, J., Challenges for the periodic operation of trickle-bed catalytic reactors (2002) Chem. Eng. Sci., 57, pp. 3373-3385 | ||
| 504 | |a Liu, G., Zhang, X., Wang, L., Zhang, S., Mi, Z., Unsteady-state operation of trickle-bed reactor for dicyclopentadiene hydrogenation (2008) Chem. Eng. Sci., 63, pp. 4991-5002 | ||
| 504 | |a Lange, R., Gutsche, R., Hanika, J., Forced periodic operation of a trickle-bed reactor (1999) Chem. Eng. Sci., 54, pp. 2569-2573 | ||
| 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) Chem. Eng. Sci., 49, pp. 3699-3710 | ||
| 504 | |a Khadilkar, M.R., Al-Dahhan, M.H., Dudukovic, M.P., Multicomponent flow-transport-reaction modeling of trickle bed reactors: application to unsteady state liquid flow modulation (2005) Ind. Eng. Chem. Res., 44, pp. 6354-6370 | ||
| 504 | |a Lange, R., Schubert, M., Dietrich, W., Grünewald, M., Unsteady-state operation of trickle-bed reactors (2004) Chem. Eng. Sci., 59, pp. 5355-5361 | ||
| 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) Chem. Eng. Sci., 53, pp. 3129-3142 | ||
| 504 | |a Dietrich, W., Grunewald, M., Agar, D.W., Dynamic modelling of periodically wetted catalyst particles (2005) Chem. Eng. Sci., 60, pp. 6254-6261 | ||
| 504 | |a Ayude, M.A., Cassanello, M.C., Martinez, O.M., Haure, P.M., Phenomenological approach to interpret the effect of liquid flow modulation in trickle-bed reactors at the particle scale (2005) Chem. Eng. Sci., 60, pp. 6262-6269 | ||
| 504 | |a Ayude, M.A., Cassanello, M.C., Haure, P.M., Martínez, O.M., Periodic operation of trickle bed reactors: an approach to catalyst design through modeling at the particle scale (2005) Ind. Eng. Chem. Res., 44, pp. 9594-9600 | ||
| 504 | |a Boelhouwer, J.G., (2001) Nonsteady Operation of Trickle-bed Reactors: Hydrodynamics, Mass and Heat Transfer, , PhD Thesis, Technische Universiteit Eindhoven, The Netherlands | ||
| 504 | |a Borremans, D., Rode, S., Wild, G., Liquid flow distribution and particle-fluid heat transfer in trickle bed reactors: the influence of periodic operation (2004) Chem. Eng. Process., 43, pp. 1403-1410 | ||
| 504 | |a Giakoumakis, D., Kostoglou, M., Karabelas, A.J., Induced pulsing in trickle beds-characteristics an attenuation pulses (2005) Chem. Eng. Sci., 60, pp. 5185-5199 | ||
| 504 | |a Trivizadakis, M.E., Karabelas, A.J., A study of local liquid/solid mass transfer in packed beds under trickling and induced pulsing flow (2006) Chem. Eng. Sci., 61, pp. 7684-7696 | ||
| 504 | |a Aydin, B., Fries, D., Lange, R., Larachi, F., Slow-mode induced pulsing in trickle-bed reactors at elevated temperature (2006) AIChE J., 52, pp. 3891-3901 | ||
| 504 | |a Brkljac, B., Bludowsky, T., Dietrich, W., Grünewald, M., Agar, D.W., Modelling of unsteady-state hydrodynamics in periodically operated trickle-bed reactors: influence of the liquid-phase physical properties (2007) Chem. Eng. Sci., 62, pp. 7011-7019 | ||
| 504 | |a Ayude, M.A., Martinez, O.M., Cassanello, M.C., Modulation of liquid holdup along a trickle bed reactor with periodic operation (2007) Chem. Eng. Sci., 62, pp. 6002-6014 | ||
| 504 | |a Muzen, A., Fraguío, M.S., Cassanello, M.C., Ayude, M.A., Haure, P.M., Martínez, O.M., Clean oxidation of alcohols in a trickle-bed reactor with liquid flow modulation (2005) Ind. Eng. Chem. Res., 44, pp. 5275-5284 | ||
| 504 | |a Tukac, V., Hanika, J., Chyba, V., Periodic state of wet oxidation in trickle-bed reactor (2003) Catal. Today, 79-80, pp. 427-433 | ||
| 504 | |a Khadilkhar, M.R., Mills, P.L., Dudukovic, M.P., Trickle bed reactor models for systems with a volatile liquid phase (1999) Chem. Eng. Sci., 54, pp. 2421-2431 | ||
| 504 | |a Goto, S., Smith, J.M., Trickle bed reactor performance. 1. Hold-up and mass transfer effects (1975) AlChE J., 21, pp. 706-713 | ||
| 504 | |a Kehinde, A., Hudgins, R., Silveston, P., Measurement of mass transfer in packed beds at low Reynolds numbers by imperfect pulse chromatography (1983) J. Chem. Eng. Jpn., 16, pp. 483-488 | ||
| 504 | |a Herskowitz, M., Wetting efficiency in trickle-bed reactors: its effect on the reactor performance (1981) Chem. Eng. J., 22, pp. 167-175 | ||
| 504 | |a Sáez, A., Carbonell, R., Hydrodynamic parameters for gas-liquid cocurrent flow in packed beds (1985) AlChE J., 31, pp. 52-62 | ||
| 520 | 3 | |a The response of an isothermal TBR to a liquid flow modulation ON-OFF strategy is examined through a model aimed at the reactor scale. The reaction is gas-limited and first order with respect to both reactants. Liquid hydrodynamic behavior is considered by means of two different approaches: the Liquid Draining Approach, based on experimental results and the ideal, Square Wave Approach. Model allows the evaluation of, among other variables, the liquid holdup, the liquid velocity and the liquid reactant conversion time variations at different axial positions within the reactor. An enhancement factor due to periodic operation is defined by computing a temporal average of the liquid reactant conversion during an invariant cycling state, referred to its corresponding steady-state conversion. For all the conditions investigated, attainable enhancements are lower when the actual draining model is assumed. © 2009 Elsevier B.V. All rights reserved. |l eng | |
| 593 | |a INTEMA, CONICET, UNMdP., J.B. Justo 4302, 7600 Mar del Plata, Argentina | ||
| 593 | |a Dep. Ing. Química, FI-UNLP-CINDECA, Calle 47, No 257, 1900 La Plata, Argentina | ||
| 593 | |a PINMATE, Dep. Industrias, FCEyN-UBA Int., Güiraldes 2620, C1428BGA Buenos Aires, Argentina | ||
| 690 | 1 | 0 | |a HYDRODYNAMICS |
| 690 | 1 | 0 | |a LIQUID FLOW MODULATION |
| 690 | 1 | 0 | |a MODELING AT THE REACTOR SCALE |
| 690 | 1 | 0 | |a TRICKLE BED REACTORS |
| 690 | 1 | 0 | |a AXIAL POSITIONS |
| 690 | 1 | 0 | |a COMPREHENSIVE MODEL |
| 690 | 1 | 0 | |a ENHANCEMENT FACTOR |
| 690 | 1 | 0 | |a FIRST ORDER |
| 690 | 1 | 0 | |a HYDRODYNAMIC BEHAVIOR |
| 690 | 1 | 0 | |a LIQUID DRAINING |
| 690 | 1 | 0 | |a LIQUID FLOW MODULATION |
| 690 | 1 | 0 | |a LIQUID HOLD UPS |
| 690 | 1 | 0 | |a LIQUID REACTANT |
| 690 | 1 | 0 | |a LIQUID VELOCITIES |
| 690 | 1 | 0 | |a MODELING AT THE REACTOR SCALE |
| 690 | 1 | 0 | |a PERIODIC OPERATION |
| 690 | 1 | 0 | |a SQUARE WAVES |
| 690 | 1 | 0 | |a STEADY-STATE CONVERSIONS |
| 690 | 1 | 0 | |a TRICKLE BED REACTOR |
| 690 | 1 | 0 | |a CHEMICAL REACTORS |
| 690 | 1 | 0 | |a FLUID DYNAMICS |
| 690 | 1 | 0 | |a HYDRODYNAMICS |
| 690 | 1 | 0 | |a MODULATION |
| 690 | 1 | 0 | |a LIQUIDS |
| 700 | 1 | |a Haure, P.M. | |
| 700 | 1 | |a Martínez, O.M. | |
| 700 | 1 | |a Cassanello, M.C. | |
| 773 | 0 | |d 2009 |g v. 154 |h pp. 162-167 |k n. 1-3 |p Chem. Eng. J. |x 13858947 |w (AR-BaUEN)CENRE-4151 |t Chemical Engineering Journal | |
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| 856 | 4 | 0 | |u https://doi.org/10.1016/j.cej.2009.03.042 |y DOI |
| 856 | 4 | 0 | |u https://hdl.handle.net/20.500.12110/paper_13858947_v154_n1-3_p162_Ayude |y Handle |
| 856 | 4 | 0 | |u https://bibliotecadigital.exactas.uba.ar/collection/paper/document/paper_13858947_v154_n1-3_p162_Ayude |y Registro en la Biblioteca Digital |
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