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Collect. Czech. Chem. Commun. 1967, 32, 3309-3333
https://doi.org/10.1135/cccc19673309

Modelling 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

M. Marek and V. Hlaváček

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  • Herskowitz M., Hagan P. S.: Accurate one‐dimensional fixed‐bed reactor model based on asymptotic analysis. AIChE Journal 1988, 34, 1367. <https://doi.org/10.1002/aic.690340815>
  • Hagan P. S., Herskowitz M., Pirkle C.: A Simple Approach to Highly Sensitive Tubular Reactors. SIAM J. Appl. Math. 1988, 48, 1083. <https://doi.org/10.1137/0148064>
  • HENNING GABRIELA P., PÉREZ GUSTAVO A., INTEC: A GENERALIZATION OF TWO INTRINSIC CRITERIA FOR RUNAWAY IN FIXED BED CATALYTIC REACTORS PART I DEVELOPMENT OF THE CRITERIA. Chemical Engineering Communications 1987, 59, 107. <https://doi.org/10.1080/00986448708911989>
  • Patnaik P.R., Rao Ch.Durgaprasada: Application of Multi-Step Rate Models in the Stability Analysis of Fixed-Bed Catalytic Reactors Part II. Stability Analysis of the Reactors. The Chemical Engineering Journal 1982, 23, 125. <https://doi.org/10.1016/0300-9467(82)80002-6>
  • Lopez A.Soria, De Lasa H.I., Porras J.A.: Parametric sensitivity of a fixed bed catalytic reactor. Chemical Engineering Science 1981, 36, 285. <https://doi.org/10.1016/0009-2509(81)85007-5>