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Referencias:

• Wilhelm, Progress towards the “a priori” design of chemical reactors (1962) Pure and Applied Chemistry, 5, p. 403
• Shinnar, Chemical reactor modelling — The desirable and the achievable (1978) Chemical Reaction Engineering Reviews, p. 1. , Washington
• Lapidus, Amundson, (1977) Chemical Reactor Theory, a Review, , Prentice-Hall, Englewood Cliffs, NJ
• Himmelblau, Bischoff, (1968) Process Analysis and Simulation: Deterministic Systems, , John Wiley, New York
• Shinnar, Chemical reactor modeling for purposes of controller design (1981) Chem. Engng Commun., 9, p. 73
• Windes, Schwedock, Ray, Dynamic models for the control of a highly exothermic packed bed reactor (1982) AIChE Meeting, Los Angeles, CA
• 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
• 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
• 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
• De Wasch, Froment, A two-dimensional heterogeneous model for fixed bed catalytic reactors (1971) Chem. Engng Sci., 26, p. 629
• Dixon, Creswell, Theoretical prediction of effective heat transfer parameters in packed beds (1979) AIChE J., 25, p. 663
• Pereira Duarte, Barreto, Lemcoff, Comparison of two-dimensional models of fixed bed catalytic reactors (1984) Chem. Engng Sci., 39, p. 1017
• Pereira Duarte, Ferretti, Lemcoff, A heterogeneous one-dimensional model for non-adiabatic fixed bed catalytic reactors (1984) Chemical Engineering Science, 39, p. 1025
• Ahmed, Fahien, Tubular reactor design — I. Two-dimensional model (1980) Chem. Engng Sci., 35, p. 889
• 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
• Bischoff, Effectiveness factors and temperature distributions for catalyst particles in non-uniform environments (1968) Chem. Engng Sci., 23, p. 451
• 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
• Pereira Duarte, Lemcoff, Analysis of fixed bed catalytic reactor models (1984) ACS Symposium Series No. 237, p. 239. , ACS, Washington, D.C
• 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
• Mears, Tests for transport limitations in experimental catalytic reactors (1971) Indust. Engng Chem. Process Des. Develop., 10, p. 541
• 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
• Young, Finlayson, Axial dispersion in nonisothermal packed bed chemical reactors (1973) Indust. Engng Chem. Fundam., 12, p. 412
• Mears, On criteria for axial dispersion in nonisothermal packed bed catalytic reactors (1976) Indust. Engng Chem. Fundam., 15, p. 20
• Demicheli, Ferretti, Laborde, Heat transfer effect on the behaviour of a natural gas steam reformer (1983) Latinoam. J. Heat Mass Transfer, 7, p. 281
• Li, Finlayson, Heat Transfer in packed beds. A reevaluation (1977) Chem. Engng Sci., 32, p. 1055
• 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
• Finlayson, (1980) Nonlinear Analysis in Chemical Engineering, , McGraw Hill, New York
• Van Welsenaere, Froment, Parametric sensitivity and runaway in fixed bed catalytic reactors (1970) Chem. Engng Sci., 25, p. 1503
• Rajadhyasksha, Vasudeva, Doraiswamy, Parametric sensitivity in fixed bed reactors (1975) Chemical Engineering Science, 30, p. 1399
• Froment, Bischoff, (1979) Chemical Reactor Analysis and Design, , John Wiley, New York
• Hyman, Simulate methane reformer reactions (1968) Hyd. Proc., 47, p. 131
• Emig, Hofmann, Friedrich, Ermittlung kinitischer parameter aus integralen labordaten (1972) Proc. 5th European Congress in Chemical Reaction Engineering, , Elsevier, Amsterdam
• Patterson, Carberry, Fixed bed catalytic reactor modeling The heat transfer problem (1983) Chemical Engineering Science, 38, p. 175
• Leva, Weintraub, Grummer, Clark, Cooling of gases through packed tubes (1948) Industrial & Engineering Chemistry, 40, p. 747
• Verschoor, Schuit, Heat transfer to fluids flowing through a bed of granular solids (1952) Appl. Sci. Res., 2 A, p. 97
• Wellauer, Cresswell, Newson, (1982) Heat transfer in packed reactor tubes suitable for selective oxidation, p. 257. , ACS Symposium Series 196, paper No. 41
• 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
• Vortmeyer, Berninger, Comments on the paper Theoretical prediction of effective heat transfer parameters in packed beds (1982) AIChE Journal, 28, pp. 508-525
• 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
• 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
• Crider, Foss, Effective wall heat transfer coefficients and thermal resistances in mathematical models packed beds (1965) AIChE Journal, 11, p. 1012
• Finlayson, Packed bed reactor analysis by orthogonal collocation (1971) Chem. Engng Sci., 26, p. 1081
• Sundaram, Froment, A comparison of simulation models for empty tubular reactors (1979) Chem. Engng Sci., 34, p. 117
• McGreavy, Turner, Model reduction of fixed bed catalytic reactors (1970) The Canadian Journal of Chemical Engineering, 48, p. 200
• Ahmed, Fahien, Tubular reactor design — II. A modifed one-dimensional model (1980) Chem. Engng Sci., 35, p. 897
• Villadsen, Michelsen, (1978) Solution of Differential Equation Models by Polynomial Approximation, , Prentice-Hall, Englewood Cliffs, New Jersey
• Villadsen, Michelsen, (1982) Numerical Methods in Reaction Engineering, , Danmarks Tekniske Hojskole, Lyngby, Denmark
• Seider, Model and algorithm synthesis in process analysis and design (1983) J Speech Hear Disord
• Mihail, Iordache, Performances of some numerical techniques used for simulation of fixed bed catalytic reactors (1976) Chem. Engng Sci., 31, p. 83
• Hlavacek, Van Rompay, Current problems of multiplicity stability and sensitivity of states in chemically reacting systems (1981) Chemical Engineering Science, 36, p. 1587

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