Modeling of fixed bed catalytic reactors
The simulation of a fixed-bed catalytic reactor requires the selection of a model, which is a set of balance equations that describes the reactor, as well as correlations for the model parameters involved. In this work general criteria, leading to a better choice of a model that fulfills the objecti...
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| Formato: | Capítulo de libro |
| Lenguaje: | Inglés |
| Publicado: |
1985
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| Acceso en línea: | Registro en Scopus DOI Handle Registro en la Biblioteca Digital |
| Aporte de: | Registro referencial: Solicitar el recurso aquí |
| LEADER | 10746caa a22010337a 4500 | ||
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| 001 | PAPER-1050 | ||
| 003 | AR-BaUEN | ||
| 005 | 20230518203024.0 | ||
| 008 | 190411s1985 xx ||||fo|||| 00| 0 eng|d | ||
| 024 | 7 | |2 scopus |a 2-s2.0-0020867383 | |
| 040 | |a Scopus |b spa |c AR-BaUEN |d AR-BaUEN | ||
| 030 | |a CCEND | ||
| 100 | 1 | |a Martinez, O.M. | |
| 245 | 1 | 0 | |a Modeling of fixed bed catalytic reactors |
| 260 | |c 1985 | ||
| 270 | 1 | 0 | |m Lemcoff, N.O. |
| 506 | |2 openaire |e Política editorial | ||
| 504 | |a Wilhelm, Progress towards the “a priori” design of chemical reactors (1962) Pure and Applied Chemistry, 5, p. 403 | ||
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| 504 | |a Lapidus, Amundson, (1977) Chemical Reactor Theory, a Review, , Prentice-Hall, Englewood Cliffs, NJ | ||
| 504 | |a Himmelblau, Bischoff, (1968) Process Analysis and Simulation: Deterministic Systems, , John Wiley, New York | ||
| 504 | |a Shinnar, Chemical reactor modeling for purposes of controller design (1981) Chem. Engng Commun., 9, p. 73 | ||
| 504 | |a Windes, Schwedock, Ray, Dynamic models for the control of a highly exothermic packed bed reactor (1982) AIChE Meeting, Los Angeles, CA | ||
| 504 | |a Deans, Lapidus, A computational model for predicting and correlating the behaviour of fixed bed reactors I Deviation of model for nonreactive systems (1960) AIChE Journal, 6, p. 656 | ||
| 504 | |a Deans, Lapidus, A computational model for predicting and correlating the behaviour of fixed bed reactors II Extension to chemically reactive systems (1960) AIChE Journal, 6, p. 663 | ||
| 504 | |a Olbrich, A two phase diffusional model to describe heat transfer processes in a non-adiabatic packed tubular bed (1970) Proc. Chemeca 70 Conference, p. 101. , Butterworths, London | ||
| 504 | |a De Wasch, Froment, A two-dimensional heterogeneous model for fixed bed catalytic reactors (1971) Chem. Engng Sci., 26, p. 629 | ||
| 504 | |a Dixon, Creswell, Theoretical prediction of effective heat transfer parameters in packed beds (1979) AIChE J., 25, p. 663 | ||
| 504 | |a Pereira Duarte, Barreto, Lemcoff, Comparison of two-dimensional models of fixed bed catalytic reactors (1984) Chem. Engng Sci., 39, p. 1017 | ||
| 504 | |a Pereira Duarte, Ferretti, Lemcoff, A heterogeneous one-dimensional model for non-adiabatic fixed bed catalytic reactors (1984) Chemical Engineering Science, 39, p. 1025 | ||
| 504 | |a Ahmed, Fahien, Tubular reactor design — I. Two-dimensional model (1980) Chem. Engng Sci., 35, p. 889 | ||
| 504 | |a Vortmeyer, Schaefer, Equivalence of one- and two-phase models for heat transfer processes in packed beds: One-dimensional theory (1974) Chem. Engng Sci., 29, p. 485 | ||
| 504 | |a Bischoff, Effectiveness factors and temperature distributions for catalyst particles in non-uniform environments (1968) Chem. Engng Sci., 23, p. 451 | ||
| 504 | |a Hlavacek, Kubicek, Modeling of chemical reactors—XX Heat and mass transfer in porous catalyst The particle in a non-uniform external field (1970) Chemical Engineering Science, 25, p. 1527 | ||
| 504 | |a Pereira Duarte, Lemcoff, Analysis of fixed bed catalytic reactor models (1984) ACS Symposium Series No. 237, p. 239. , ACS, Washington, D.C | ||
| 504 | |a Hlavacek, Marek, Modeling of chemical reactors II Tubular non-isothermal non-adiabatic packed bed reactor; problems in the design of a reactor with radial heat transfer for the reaction A → B (1967) Collection of Czechoslovak Chemical Communications, 32, p. 3309 | ||
| 504 | |a Mears, Tests for transport limitations in experimental catalytic reactors (1971) Indust. Engng Chem. Process Des. Develop., 10, p. 541 | ||
| 504 | |a Gonzo, Gottifredi, Rational approximations of effectiveness factor and general diagnostic criteria for heat and mass transport limitations (1983) Cat. Rev. Sci. Engng, 25, p. 119 | ||
| 504 | |a Young, Finlayson, Axial dispersion in nonisothermal packed bed chemical reactors (1973) Indust. Engng Chem. Fundam., 12, p. 412 | ||
| 504 | |a Mears, On criteria for axial dispersion in nonisothermal packed bed catalytic reactors (1976) Indust. Engng Chem. Fundam., 15, p. 20 | ||
| 504 | |a Demicheli, Ferretti, Laborde, Heat transfer effect on the behaviour of a natural gas steam reformer (1983) Latinoam. J. Heat Mass Transfer, 7, p. 281 | ||
| 504 | |a Li, Finlayson, Heat Transfer in packed beds. A reevaluation (1977) Chem. Engng Sci., 32, p. 1055 | ||
| 504 | |a Pereira Duarte, Martínez, Lemcoff, (1983) Predicción del hot spot en reactores catalíticos de lecho fijo, , Jornadas sobre Investigaciones en Ciencias de la Ingeniería Química y Química Aplicada, Tucumán, Argentina, XIIdas | ||
| 504 | |a Finlayson, (1980) Nonlinear Analysis in Chemical Engineering, , McGraw Hill, New York | ||
| 504 | |a Van Welsenaere, Froment, Parametric sensitivity and runaway in fixed bed catalytic reactors (1970) Chem. Engng Sci., 25, p. 1503 | ||
| 504 | |a Rajadhyasksha, Vasudeva, Doraiswamy, Parametric sensitivity in fixed bed reactors (1975) Chemical Engineering Science, 30, p. 1399 | ||
| 504 | |a Froment, Bischoff, (1979) Chemical Reactor Analysis and Design, , John Wiley, New York | ||
| 504 | |a Hyman, Simulate methane reformer reactions (1968) Hyd. Proc., 47, p. 131 | ||
| 504 | |a Emig, Hofmann, Friedrich, Ermittlung kinitischer parameter aus integralen labordaten (1972) Proc. 5th European Congress in Chemical Reaction Engineering, , Elsevier, Amsterdam | ||
| 504 | |a Patterson, Carberry, Fixed bed catalytic reactor modeling The heat transfer problem (1983) Chemical Engineering Science, 38, p. 175 | ||
| 504 | |a Leva, Weintraub, Grummer, Clark, Cooling of gases through packed tubes (1948) Industrial & Engineering Chemistry, 40, p. 747 | ||
| 504 | |a Verschoor, Schuit, Heat transfer to fluids flowing through a bed of granular solids (1952) Appl. Sci. Res., 2 A, p. 97 | ||
| 504 | |a Wellauer, Cresswell, Newson, (1982) Heat transfer in packed reactor tubes suitable for selective oxidation, p. 257. , ACS Symposium Series 196, paper No. 41 | ||
| 504 | |a Pereira Duarte, Martínez, Ferretti, Lemcoff, (1983) Coeficiente de transferencia de calor unidimensional seudohomogéneo para un reactor cata lítico de lecho fijo, , Jornadas sobre Investigaciones en Ciencias de la Ingeniería Química y Química Aplicada, Tucumán, Argentina, XIIdas | ||
| 504 | |a Vortmeyer, Berninger, Comments on the paper Theoretical prediction of effective heat transfer parameters in packed beds (1982) AIChE Journal, 28, pp. 508-525 | ||
| 504 | |a Cresswell, Dixon, Reply to comments by Vortmeyer and Berninger on the paper“theoretical prediction of effective heat transfer parameters in packed beds(AIchE J., 25, 663, 1979)” (1982) AIChE Journal, 28, p. 511. , Reply to comments | ||
| 504 | |a Pereira Duarte, Lemcoff, Martínez, Ferretti, Coeficientes de transferencia de calor para un modelo heterogéneo unidimensional (1982) Proc. 1er. Congreso Latinoamericano de Transferencia de Calor y Materia, 2, p. 1011 | ||
| 504 | |a Crider, Foss, Effective wall heat transfer coefficients and thermal resistances in mathematical models packed beds (1965) AIChE Journal, 11, p. 1012 | ||
| 504 | |a Finlayson, Packed bed reactor analysis by orthogonal collocation (1971) Chem. Engng Sci., 26, p. 1081 | ||
| 504 | |a Sundaram, Froment, A comparison of simulation models for empty tubular reactors (1979) Chem. Engng Sci., 34, p. 117 | ||
| 504 | |a McGreavy, Turner, Model reduction of fixed bed catalytic reactors (1970) The Canadian Journal of Chemical Engineering, 48, p. 200 | ||
| 504 | |a Ahmed, Fahien, Tubular reactor design — II. A modifed one-dimensional model (1980) Chem. Engng Sci., 35, p. 897 | ||
| 504 | |a Villadsen, Michelsen, (1978) Solution of Differential Equation Models by Polynomial Approximation, , Prentice-Hall, Englewood Cliffs, New Jersey | ||
| 504 | |a Villadsen, Michelsen, (1982) Numerical Methods in Reaction Engineering, , Danmarks Tekniske Hojskole, Lyngby, Denmark | ||
| 504 | |a Seider, Model and algorithm synthesis in process analysis and design (1983) J Speech Hear Disord | ||
| 504 | |a Mihail, Iordache, Performances of some numerical techniques used for simulation of fixed bed catalytic reactors (1976) Chem. Engng Sci., 31, p. 83 | ||
| 504 | |a Hlavacek, Van Rompay, Current problems of multiplicity stability and sensitivity of states in chemically reacting systems (1981) Chemical Engineering Science, 36, p. 1587 | ||
| 520 | 3 | |a The simulation of a fixed-bed catalytic reactor requires the selection of a model, which is a set of balance equations that describes the reactor, as well as correlations for the model parameters involved. In this work general criteria, leading to a better choice of a model that fulfills the objectives of the simulation, are established. Different ways in which the parameters can be obtained are analyzed, and the numerical methods for solving the model equations are discussed. © 1985. |l eng | |
| 536 | |a Detalles de la financiación: Acknowledgement-The authors are grateful to the Consejo National de Investigaciones Clientificas y Tecnicas, Argentina, for their financial assistance, which made this work possible. | ||
| 593 | |a Departamento Ingeniería Química, Universidad Nacional La Plata, 1900 La Plata, Argentina | ||
| 593 | |a PINMATE, Departamento de Industrias, Facultad de Ciencias Exactas y Naturales, Ciudad Universitaria, 1428 Buenos Aires, Argentina, Argentina | ||
| 690 | 1 | 0 | |a COMPUTER SIMULATION |
| 690 | 1 | 0 | |a MATHEMATICAL MODELS |
| 690 | 1 | 0 | |a MATHEMATICAL TECHNIQUES - DIFFERENTIAL EQUATIONS |
| 690 | 1 | 0 | |a FIXED-BED REACTOR |
| 690 | 1 | 0 | |a HETEROGENEOUS MODELS |
| 690 | 1 | 0 | |a MODEL PARAMETERS |
| 690 | 1 | 0 | |a TRANSFER PARAMETERS |
| 690 | 1 | 0 | |a CHEMICAL EQUIPMENT |
| 700 | 1 | |a Pereira Duarte, S.I. | |
| 700 | 1 | |a Lemcoff, N.O. | |
| 773 | 0 | |d 1985 |g v. 9 |h pp. 535-545 |k n. 5 |p Comput. Chem. Eng. |x 00981354 |w (AR-BaUEN)CENRE-304 |t Computers and Chemical Engineering | |
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| 856 | 4 | 0 | |u https://doi.org/10.1016/0098-1354(85)80028-4 |y DOI |
| 856 | 4 | 0 | |u https://hdl.handle.net/20.500.12110/paper_00981354_v9_n5_p535_Martinez |y Handle |
| 856 | 4 | 0 | |u https://bibliotecadigital.exactas.uba.ar/collection/paper/document/paper_00981354_v9_n5_p535_Martinez |y Registro en la Biblioteca Digital |
| 961 | |a paper_00981354_v9_n5_p535_Martinez |b paper |c PE | ||
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| 999 | |c 62003 | ||