Slurry bubble reactor operated in well-mixed gas flow regime

C - Chemistry – Metallurgy – 07 – C

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C07C 1/04 (2006.01) C07C 27/00 (2006.01) C07C 27/06 (2006.01)

Patent

CA 2470380

A gas-agitated multiphase reactor system for the synthesis of hydrocarbons gives high catalyst productivity and reactor capacity. The system includes operating a multi-phase reactor in the well-mixed gas flow regime, with a Peclet number less than 0.175 and a single pass conversion ranging from 35% to 75%, wherein the inlet superficial gas velocity decreases with the decreasing of the reactor aspect ratio, and is preferably at least 20 cm/sec.

L'invention se rapporte à un système de réacteur multiphase à gaz en mouvement pour la synthèse d'hydrocarbures offrant une productivité de catalyseur et une capacité de réacteur élevée. Ce système consiste à faire fonctionner un réacteur multiphase dans le régime à flux gazeux homogène activé avec un nombre de Péclet inférieur à 0,175 et une conversion à simple passage qui varie de 35 % à 75 %, la vitesse du gaz superficiel d'entrée diminue en même temps que le rapport de cadre du réacteur diminue, et est de préférence d'au moins 20cm/sec.

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