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Fluid catalytic cracking process for hydrocarbon feed, particularly a high basic nitrogen content feed.

机译:用于烃进料,特别是高碱性氮含量进料的流化催化裂化方法。

摘要

A fluid catalytic cracking (FCC) process for the cracking of a hydrocarbon charge, partic. one contg. a high basic N content in a tubular reaction zone comprises: - a supply of catalyst particles (at least in part regenerated) to the upper part of the reaction zone; - introduction and dispersion of the charge to be treated in the upper part of the reactor (beneath the entry pt. of the catalyst); - co-current circulation in mutual contact in the reaction zone of the catalyst and charge to be treated; - sepn. at the lower part of the reaction zone, of the deactivated catalyst from the reaction prods.; - stripping of the deactivated catalyst; - regeneration of at least part of the stripped catalyst in a regeneration zone; - recycling of the regenerated catalyst to the upper reaction zone, and - transfer of the cracked prods. to a sepn. zone. The process has the following characteristics: the catalyst circulates from top to bottom co-currently with the charge in the tubular zone; a catalyst is used which in equilibrium state (150 degrees C and 5 mbars) adsorbs less than 250 mu moles (pref. 50 mu moles)/g of pyridine and retains after heating at 350 degrees C in a vacuum, no more than 20% (pref. 10%) of the amt. absorbed.
机译:用于裂化碳氢化合物装料的流化催化裂化(FCC)工艺。一等管状反应区中高的碱性氮含量包括:-向反应区的上部供应催化剂颗粒(至少部分再生); -将要处理的装料引入和分散到反应器的上部(在催化剂入口下方); -在催化剂的反应区与待处理的装料相互接触的并流循环; -九月在反应区的下部,来自反应产物的失活催化剂。 -汽提失活的催化剂; -在再生区中再生至少部分汽提的催化剂; -将再生的催化剂再循环到上部反应区,和-将裂化的产物转移。到九月。区。该方法具有以下特征:催化剂与进料在管状区中从上到下并流循环;使用的催化剂在平衡状态(150摄氏度和5毫巴)下吸附的吡啶少于250摩尔(优选<50摩尔)/克,在350摄氏度的真空下加热后不超过20摩尔%(占10%)。吸收。

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