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A REACTOR FOR CATALYTIC DEHYDROGENATION OF HYDROCARBONS WITH SELECTIVE OXIDATION OF HYDROGEN
A REACTOR FOR CATALYTIC DEHYDROGENATION OF HYDROCARBONS WITH SELECTIVE OXIDATION OF HYDROGEN
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机译:选择性催化氧化制氢的碳氢加氢反应器
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摘要
A reactor for catalytic dehydrogenation of dehydrogenatable hydrocar-bons, in particular C3 and/or C4 hydrocarbons, in a hydrocarbon-containingstream, with selective oxidation of hydrogen. The reactor comprises seri-ally connected in the flow direction of the hydrocarbon-containing stream: afirst catalyst zone (2), an oxygen admixing zone (3) provided with a means(5) for separate feeding of an oxygen-containing gas into the hydrocarbon-containing stream, and a second catalyst zone (4). The oxygen admixingzone (3) has a cross section area in the flow direction of the hydrocarbon-containing stream which is from 0.5 % to 75 % of the cross section area ofeach of the two catalysts zones (2, 4), so as to obtain a higher flow velocityin the oxygen-admixing zone (3) than in the catalyst zones. The means (5)for feeding oxygen-containing gas is designed to feed said gas with a flowvelocity which is at least 1 m/s and is up to 200 times higher than the flowvelocity of the hydrocarbon-containing stream in the oxygen-admixing zone.The oxygen-admixing zone (3) is free of catalyst at least in the region adja-cent to the oxygen feeding means (5).
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机译:用于可脱氢烃的催化脱氢的反应器含碳氢化合物中的碳氢化合物,尤其是C3和/或C4碳氢化合物物流,并选择性氧化氢。反应堆包括系列沿含烃物流的流动方向连接:第一催化剂区(2),设有装置的氧气混合区(3)(5)为将含氧气体分别供入烃中,包含料流和第二催化剂区(4)。氧气混合区域(3)在碳氢化合物的流动方向上具有横截面积-包含的流是其横截面积的0.5%至75%两个催化剂区域(2、4)的每个区域,以获得更高的流速在氧气混合区(3)中比在催化剂区中。手段(5)用于输送含氧气体的装置设计为以一定流量输送所述气体速度至少为1 m / s,比流量高200倍氧气混合区中含烃物流的最大速度。氧气混合区(3)至少在相邻区域没有催化剂分到氧气供给装置(5)。
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