首页> 外国专利> AN IMPROVED RESIDUAL CONVERSION METHOD INTEGRATING DEEP HYDROCONVERSION STEPS INTO A DRIVEN BED AND A DISASPHALTAGE STEP

AN IMPROVED RESIDUAL CONVERSION METHOD INTEGRATING DEEP HYDROCONVERSION STEPS INTO A DRIVEN BED AND A DISASPHALTAGE STEP

机译:一种改进的残差转换方法,将深层水力转换步骤集成到驱动床和泄油步骤中

摘要

The invention relates to a process for converting heavy hydrocarbon feedstocks at least 50 wt% at a temperature of at least 300 ° C, and in particular residues under vacuum. The feeds are subjected to a first step a) of deep hydroconversion into a driven bed, possibly followed by a step b) of separation of a light fraction, and a heavy residual fraction obtained from step b) is obtained. at least 80% by weight of which has a boiling point of at least 250 ° C. Said fraction resulting from step b) or the effluent resulting from step a) is then subjected to a second step c) deep hydroconversion into a driven bed. The overall hourly space velocity for steps a) to c) is less than 0.1 hr-1. The effluent from step c) is fractionated to separate a light fraction. The heavy fraction obtained, 80% by weight of which is at a temperature of at least 300 ° C., is sent to a deasphalting step e). The deasphalted fraction DAO is then preferably converted into a step f) chosen from bubbling bed hydroconversion, fluidized bed catalytic cracking and fixed bed hydrocracking.
机译:本发明涉及一种在至少300℃的温度下转化至少50wt%的重烃原料的方法,特别是在真空下转化残余物的方法。将进料进行第一步加氢转化为驱动床的第一步,然后进行分离轻馏分的步骤b),得到从步骤b)获得的重质残余物。至少80重量%的其沸点至少为250℃。然后将由步骤b)得到的所述馏分或由步骤a)得到的流出物进行第二步骤c)深度加氢转化为驱动床。步骤a)至c)的总时空速度小于0.1 hr-1。将步骤c)的流出物分馏以分离出轻质馏分。将所获得的重质馏分(按重量计80%处于至少300°C的温度)送至脱沥青步骤e)。然后优选将脱沥青的馏分DAO转化为选自鼓泡床加氢转化,流化床催化裂化和固定床加氢裂化的步骤f)。

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