首页> 外国专利> FLUIDIZED BED CATALYTIC CRACKING OF HYDROCARBON FEEDSTOCK PARTICULARLY FEEDSTOCK HAVING HIGH CONTENT OF BASIC NITROGENCOMPOUND

FLUIDIZED BED CATALYTIC CRACKING OF HYDROCARBON FEEDSTOCK PARTICULARLY FEEDSTOCK HAVING HIGH CONTENT OF BASIC NITROGENCOMPOUND

机译:含高氮基本成分的烃类废料,特别是杂物的流化床催化裂化

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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