Kinetic and reactor models for hdt of middle distillates

Computers and Chemical Engineering

Volumn 23, Issue SUPPL. 1, 1999, Pages

  Cotta, R M ^a   Wolf Maciel, M R ^b   Maciel Filho, R ^b  

^a PETROBRAS   (Brazil)

^b UNIVERSITY OF CAMPINAS   (Brazil)

Author keywords

Hydrogenation reactor; Kinetic model; Multiphase reactor; Reactor modelling

Indexed keywords

HYDRODESULFURIZATION; INTEGRAL EQUATIONS; KINETIC PARAMETERS; KINETIC THEORY; ORDINARY DIFFERENTIAL EQUATIONS; RATE CONSTANTS;

HYDRODENITROGENATION; HYDROGENATION REACTORS; KINETIC MODELING; MASS AND ENERGY BALANCE; MULTI-PHASE REACTOR; PSEUDO-HOMOGENEOUS MODELING; REACTOR MODELLING; RUNGE KUTTA GILL METHOD;

RUNGE KUTTA METHODS;

EID: 77949488468     PISSN: 00981354     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0098-1354(99)80194-X     Document Type: Conference Paper

References (4)

1. Girgis, M.J. and Gates, B. C. (1991), "Reviews Reactivities, Reaction Networks, and Kinetics in High-Pressure Catalytic Hydroprocessing". Ind. Eng. Chern. Res., 30, 2021-2058.
2. Marquardt, D.M. (1963), "An Algorithm for Least Squares Estimation ofNonlinear Parameters", J. Soc Indust. AppJ. Math., 11(2),431-441.
3. Tarhan, M.O. (1983), Catalytic Reactor Design. McGraw-Hili, Inc. New York.
4. Satterfield, C. N., Pelosof, A. A. and Sherwoord, T.K. (1969), "Mass Tranfer Limitations in a Trickle Bed Reactor". AIChe 1.,15,226-234.