The relevance of overall heat transfer coefficients in the simulation of catalytic fixed bed reactors with the heterogeneous one-dimensional model

Author:

Berto C.A.,Barreto G.F.

Publisher

Elsevier BV

Subject

Applied Mathematics,Modelling and Simulation

Reference22 articles.

1. Reactor scaleup methodology;Trambouze;Chem. Engrg. Prog.,1990

2. Development of optimal fixed bed catalytic reaction systems;Cropley;Chem. Engrg. Prog.,1990

3. Heat transfer in packed beds;Lemcoff;Rev. Chem. Engrg.,1990

4. On the validity limits of packed bed reactor continuous models with respect to tube to particle diameter ratio;Vortmayer;Chem. Engrg. Sci.,1984

5. Theoretical prediction of heterogeneous one-dimensional heat trasnfer coefficients for fixed bed reactors;Pereira Duarte;A.I.Ch.E.J.,1985

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1. A Heterogeneous Multiscale Dynamic Model for Simulation of Catalytic Reforming Reactors;International Journal of Chemical Kinetics;2016-03-22

2. A heterogeneous dynamic model for the simulation and optimisation of the steam methane reforming reactor;International Journal of Hydrogen Energy;2012-11

3. Heat transfer — a review of 1992 literature;International Journal of Heat and Mass Transfer;1994-06

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