Bubble-column reactor with draft-tube and process for regeneration of catalyst contained therein

一种在有气相、液相和固体催化剂存在的条件下,由合成气生产主要是重质烃的连续方法,所述方法利用泡罩塔进行,其特征在于泡罩塔内有:(a)至少一个通流管;(b)至少一个引入合成气的装置;(c)至少一个引入再生气体的装置;(d)至少一个启动/中断再生气流的装置;(e)一个适合于使合成气和再生气体混合最小的任选装置。 PCT No. PCT/EP98/03874 Sec. 371 Date Mar. 18, 1999 Sec. 102(e) Date Mar. 18, 1999 PCT Filed Jun. 20, 1998 PCT Pub. No. WO99/00191 PCT Pub. Date J...

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1. Verfasser: C. MARETTO,V. PICCOLO,D. CASANAVE
Format: Patent
Sprache:chi ; eng
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Zusammenfassung:一种在有气相、液相和固体催化剂存在的条件下,由合成气生产主要是重质烃的连续方法,所述方法利用泡罩塔进行,其特征在于泡罩塔内有:(a)至少一个通流管;(b)至少一个引入合成气的装置;(c)至少一个引入再生气体的装置;(d)至少一个启动/中断再生气流的装置;(e)一个适合于使合成气和再生气体混合最小的任选装置。 PCT No. PCT/EP98/03874 Sec. 371 Date Mar. 18, 1999 Sec. 102(e) Date Mar. 18, 1999 PCT Filed Jun. 20, 1998 PCT Pub. No. WO99/00191 PCT Pub. Date Jan. 7, 1999Continuous process for the production of prevalently heavy hydrocarbons starting from synthesis gas in the presence of a gas phase, a liquid and a solid catalyst, the above process being carried 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 regenerating gas; (e) optional devices suitable for minimizing the mixing of the synthesis gas with the regenerating gas.