Bubble-column reactor with draft-tube and process for the...

B - Operations – Transporting – 01 – J

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B01J 38/00 (2006.01) B01J 8/22 (2006.01) B01J 38/48 (2006.01) C07C 1/04 (2006.01) C10G 2/00 (2006.01)

Patent

CA 2264572

Continuous process for the production of prevalently heavy hydrocarbons starting from syn-thesis gas in the presence of a gas phase, a liquid and a solid catalyst, the above process being car-ried out using a bubble column, characterized in that the bubble column internally has: (a) at least one draft-tube; (b) at least one device for the inlet of the synthesis gas; (c) at least one device for the inlet of the regenerating gas; (d) at least one device for activating/interrupting the stream of regenerat-ing gas; (e) optional devices suitable for minimizing the mixing of the synthesis gas with the regenerat-ing gas.

L'invention concerne un procédé continu pour la production d'hydrocarbures lourds à partir d'un gaz de synthèse en présence d'une phase gazeuse, d'un liquide et d'un catalyseur solide. Le procédé susmentionné est mis en oeuvre à l'aide d'une colonne à bulles. Cet appareil se caractérise en ce qu'il comprend (a) au moins un tube de circulation, (b) au moins un dispositif pour l'admission du gaz de synthèse, (c) au moins un dispositif pour l'admission du gaz de régénération, (d) au moins un dispositif pour activer/interrompre le courant de gaz de régénération, (e) des dispositifs facultatifs pour minimiser le mélange du gaz de synthèse avec le gaz de régénération.

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