A mathematical modeling of catalytic milli-fixed bed reactor for Fischer–Tropsch synthesis: Influence of tube diameter on Fischer Tropsch selectivity and thermal behavior. (4th May 2015)

• Record Type: Journal Article
• Authors: Chabot, Giovanni; Guilet, Richard; Cognet, Patrick; Gourdon, Christophe
• Is Part Of: Chemical engineering science. Volume 127(2015)
• Page Start: 72
• Page End: 83
• Publication Date: 2015-05-04
• Subjects: Fischer–Tropsch synthesis -- Fixed bed reactor -- Milli-reactor -- Intensification -- Reactor modeling -- COMSOL multiphysics; Chemical engineering -- Periodicals; Génie chimique -- Périodiques; Chemical engineering; Periodicals; Electronic journals; 660
• DOI: 10.1016/j.ces.2015.01.015
• Languages: English
• ISSNs: 0009-2509

Abstract

Abstract: A two-dimensional pseudo-homogeneous model has been developed to investigate the influence of tube size on the thermal behavior and performance of packed fixed bed reactor for the low temperature Fischer–Tropsch (FT) synthesis over alumina supported cobalt. Velocity, temperature and composition fields are determined by solving the fundamental transport equations in porous media. Special attention was paid to the variation of transport properties with temperature and composition of the gas mixture. High dependency of the thermal behavior on the thermal conductivity of the gas mixture is highlighted, whereas viscosity and heat capacity of gas mixture have very little influence. Moreover for the considered catalyst, simulation results have displayed high heat removal for the millimetric scale with a tube inner diameter below 2.75 mm for an extended range of weight hourly space velocity ( 20 – 600 g syngas min − 1 kg cat . − 1, T =493 K and P =20 bar). With a millimetric reactor, high CO conversion ( X CO > 90 % ) is obtained for values of space velocity between 30 and 120 g syngas min − 1 kg cat . − 1 . For higher diameter tube than 3.11 mm, thermal runaway occurs and even worse, no convergence achieved due to the very low heat transfer global coefficient and the weak surface/volume ratio, leading to a significant decrease of liquid fuels selectivity and an increase of light hydrocarbon (C1 to C4 ) selectivity up to 14%. To conclude, results from scale-up study with the millimetric scale are outstanding, more than 2900 kg h − 1 m cat . − 3 of C 5 + could be produce after numbering-up 3033 tubes of 10 centimeters in length whereas conventional units (multitubular fixed bed reactors or slurry phase reactors) do not exceed 400 kg h − 1 m cat . − 3 . Abstract : Highlights: A two-dimensional pseudo-homogeneous model in packed bed reactors was built. Influence of tube reactor diameter for Fischer–Tropsch synthesis was investigated. Increasing tube diameter leads to hot spot within the reactor. Liquid hydrocarbons selectivity decreases if isothermal behavior is not fulfilled. High productivities in liquid hydrocarbons are obtained at millimeter scale.