Longitudinal mass and heat dispersion in tubular reactors

Industrial and Engineering Chemistry Research

Volumn 36, Issue 6, 1997, Pages 2031-2040

  Benneker, Arno H ^a  

^a UNIVERSITY OF TWENTE   (Netherlands)

Author keywords

[No Author keywords available]

Indexed keywords

CHEMICAL REACTIONS; HEAT TRANSFER; LAMINAR FLOW; MASS TRANSFER; MATHEMATICAL MODELS; NUMERICAL METHODS; REACTION KINETICS;

DISPERSED PLUG FLOW MODEL; LONGITUDINAL DISPERSION;

CHEMICAL REACTORS;

EID: 0031162652     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie960713j     Document Type: Article

References (5)

1. Cattaneo, C. A Form of Heat Conduction Equation Which Eliminates the Paradox of Instantaneous Propagation. Comp. Rend. 1958, 247, 431.
2. Danckwerts, P. V. Continuous Flow Systems. Distribution of Residence Times. Chem. Eng. Sci. 1953, 2, 1.
3. Deckwer, W.-D.; Mählmann, E. A. Dispersed Flow Reactors with Sections of Different Properties. Adv. Chem. Ser. 1974, 133, 334.
4. Deckwer, W.-D.; Mählmann, A. E. Boundary Conditions of Liquid Phase Reactor with Axial Dispersion. Chem. Eng. J. 1976, 11, 19.
5. Fock, V. A. Solution of a Problem of Diffusion Theory by Finite Difference Method and its Application to Diffusion of Light. Proc. State Opt. Inst. 1926, 4 (34), Leningrad (in Russian).