The influence of operating and coke-related variables on the regeneration of fixed beds of catalyst
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Abstract The regeneration of fixed bed catalytic reactors has been simulated a pseudo-homogenous model. The influence of a number of variables on the temperature rise has been studied. In particular the effect of coke content and composition have been determined. It was found that fixed beds with series and parallel types of coke distribution behave differently when these variables are changed. Regeneration policies in which a stepped oxygen feed is employed, are discussed.
[1] G. Froment,et al. Kinetic data and product distributions from fixed bed catalytic reactors subject to catalyst fouling , 1962 .
[2] C. C. Watson,et al. Temperature profiles in packed beds of catalyst during regeneration , 1962 .
[3] R. G. Haldeman,et al. On the Nature of the Carbon Deposit of Cracking Catalysts , 1959 .
[4] G. Froment,et al. Non-steady state behaviour of fixed bed catalytic reactors due to catalyst fouling , 1961 .