A cape of HDT industrial reactor for middle distillates

Computers and Chemical Engineering

Volumn 24, Issue 2-7, 2000, Pages 1731-1735

  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 modeling

Indexed keywords

ALGORITHMS; CATALYSTS; COMPUTER SIMULATION; DESULFURIZATION; HYDROGENATION; KINETIC THEORY; MATHEMATICAL MODELS; ORDINARY DIFFERENTIAL EQUATIONS; PETROLEUM DISTILLATES; RUNGE KUTTA METHODS;

ADIABATIC DIESEL; ENERGY BALANCE EQUATIONS; HYDRODENITROGENATION; HYDRODESULFURIZATION; HYDROTREATING TRICKLE BED REACTOR; KINETIC EQUATIONS; MARQUARDT METHOD; POWER LAW MODEL;

CHEMICAL REACTORS;

CALCULATION; CATALYST; CHEMICAL ENGINEERING; CHEMICAL INDUSTRY; CHEMICAL REACTION; CHEMICAL REACTION KINETICS; CONFERENCE PAPER; DESULFURIZATION; DISTILLATION; MATHEMATICAL ANALYSIS; MATHEMATICAL MODEL; REACTOR; SIMULATION;

EID: 0034660712     PISSN: 00981354     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0098-1354(00)00451-8     Document Type: Conference Paper

References (4)

1. Girgis, M. J., & Gates, B. C. (1991). Reviews - reactivities, reaction networks, and kinetics in high-pressure catalytic hydroprocessing. Industrial Engineering & Chemical Research, 30, 021-2058.
2. Marquardt, D. M. (1963). An algorithm for least squares estimation of nonlinear parameters. Journal of Social & Industrial Applications in Mathematics, 11(2), 431-441.
3. Satterfield, C. N., Pelosof, A. A., & Sherwoord, T. K. (1969). Mass transfer limitations in a trickle bed reactor. American Institute of Chemical Engineers Journal, 15, 226-234.
4. Tarhan, M. O. (1983). Catalytic reactor design. New York: McGraw-Hill.