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    • 2. 发明授权
    • Commercial fischer-tropsch reactor
    • 商业费托反应堆
    • US07012103B2
    • 2006-03-14
    • US10395912
    • 2003-03-24
    • Rafael L. EspinozaJianping ZhangHarold A. WrightTodd H. Harkins
    • Rafael L. EspinozaJianping ZhangHarold A. WrightTodd H. Harkins
    • C07C27/00
    • C10G2/341B01J8/06B01J8/067B01J12/00B01J23/745B01J23/75B01J2208/00053B01J2208/00061B01J2208/00097B01J2208/00212
    • A process for producing hydrocarbons comprises providing a multi-tubular reactor having at least 100 tubes units containing a catalyst, each tube being between 2 and 5 meters tall and in thermal contact with a cooling fluid; feeding hydrogen and carbon monoxide to each tube at a linear gas superficial velocity less than about 60 cm/s; and converting the gas feedstream to hydrocarbons on the catalyst, wherein the yield of hydrocarbons in each tube is greater than 100 (kg hydrocarbons)/hr/(m3 reaction zone). Each tube may have an internal diameter greater than 2 centimeters. The catalyst may be active for Fischer Tropsch synthesis and may comprise cobalt or iron. The maximum difference in the radially-averaged temperature between two points that are axially spaced along the reactor is less than 15° C., preferably less than 10° C. The catalyst loading or intrinsic activity may vary along the length of the reactor.
    • 制备烃的方法包括提供具有至少100个含有催化剂的管单元的多管式反应器,每个管的高度在2和5米之间并与冷却流体热接触; 以低于约60cm / s的线性气体表观速度向每个管供给氢气和一氧化碳; 并将气体进料流转化为催化剂上的烃,其中每个管中的烃的产率大于100(kg碳氢化合物)/ hr /(m 3)反应区)。 每根管子的内径可以大于2厘米。 该催化剂可用于费 - 托合成,并且可以包含钴或铁。 沿着反应器轴向间隔的两个点之间的径向平均温度的最大差异小于15℃,优选小于10℃。催化剂负载或固有活性可以沿着反应器的长度而变化。