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Process for the thermal cracking of a residual hydrocarbon oil

机译:残余烃油热裂解的方法

摘要

Process for the thermal cracking of a residual hydrocarbon oil wherein a final 520 DEG C+ conversion of at least 35 % by weight is attained, which process comprises the steps of: (a) heating the residual hydrocarbon oil feed in a furnace to a temperature in the range of from 400 to 510 DEG C for sufficient time to achieve 30 to 45 % of the final 520 DEG C+ conversion; (b) feeding the partially converted, hot hydrocarbon oil produced in step (a) and a hot hydrogen-containing gas into a soaker, said hydrogen-containing gas having a sufficiently high temperature to maintain the temperature of the hydrocarbon oil in the soaker by means of direct heat exchange at a value in the range of from 420 to 650 DEG C, in which soaker the remainder up to 100 % of the final 520 DEG C+ conversion takes place; and (c) recovering a gaseous fraction containing the hydrogen-containing gas and a cracked residue from the soaker.
机译:热裂解残余烃油的方法,其中最终的520℃+转化率至少达到35%(重量),该方法包括以下步骤:(a)在炉中将残余烃油进料加热到25℃的温度。在400至510℃的范围内保持足够的时间,以达到最终520℃+转化率的30%至45%; (b)将在步骤(a)中产生的部分转化的热烃油和热的含氢气体进料到浸泡器中,所述的含氢气体具有足够高的温度以通过以下方式维持浸泡器中的烃油的温度:以420至650℃范围内的值进行直接热交换的方法,在该方法中,余热达到最终520℃+转化率的100%。 (c)从所述浸液器中回收含有含氢气体和裂化残余物的气态馏分。

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