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STAGED FLUID CATALYTIC CRACKING PROCESSES INCORPORATING A SOLIDS SEPARATION DEVICE FOR UPGRADING NAPHTHA RANGE MATERIAL

机译:分阶段的流体催化裂化工艺,并结合了分离分离装置以升级萘酚系列材料

摘要

Processes and systems for the conversion of hydrocarbons herein may include separating an effluent from a moving bed reactor, the effluent including reaction product, first particulate catalyst, and second particulate catalyst. The separating may recover a first stream including the reaction product and first particulate catalyst and a second stream including second particulate catalyst. The second stream may be admixed with a regenerated catalyst stream including both first and second particulate catalyst at an elevated temperature. The admixing may produce a mixed catalyst at a relatively uniform temperature less than the elevated regenerated catalyst temperature, where the temperature is more advantageous for contacting light naphtha and heavy naphtha within the moving bed reactor to produce the effluent including the reaction product, the first particulate catalyst, and the second particulate catalyst.
机译:本文中用于烃的转化的方法和系统可包括从移动床反应器中分离出流出物,该流出物包括反应产物,第一颗粒催化剂和第二颗粒催化剂。分离可回收包含反应产物和第一颗粒催化剂的第一物流和包含第二颗粒催化剂的第二物流。第二物流可以在高温下与包括第一和第二颗粒催化剂的再生催化剂物流混合。所述掺混可在低于升高的再生催化剂温度的相对均匀的温度下产生混合催化剂,其中该温度更有利于使轻石脑油和重石脑油在移动床反应器内接触以产生包括反应产物,第一颗粒的流出物。催化剂和第二颗粒催化剂。

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