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Converting a stream containing heavy hydrocarbons into a stream containing hydrocarbons having a lower boiling range

机译:将含有重质烃的物流转化为沸程较低的烃类物流

摘要

Process for converting a stream containing heavy hydrocarbons comprising the steps of a) passing through a first conversion reactor (1) containing a conversion catalyst in the presence of hydrogen the stream at a temperature between 325 and 600 DEG C, a pressure between 1 and 30 MPa and at an hourly space velocity between 0.05 and 5 kg/1/hour to produce a primary converted stream; b) passing the primary converted stream to a first gas/liquid separator (4) and removing from the first gas/liquid separator (4) a gaseous stream and a liquid stream; c) passing the gaseous stream to a second conversion reactor (7); and d) passing through the second conversion reactor (7) containing a conversion catalyst in the presence of hydrogen the gaseous stream at a temperature between 325 and 600 DEG C, a pressure between 1 and 30 MPa and at an hourly space velocity between 0.1 and 10 kg/l/hour to produce a further converted stream having a lower boiling range. ;
机译:用于转化含有重烃的料流的方法,其包括以下步骤:a)在氢气存在下,使该料流在温度为325至600℃,压力为1至30的条件下,通过含有转化催化剂的第一转化反应器(1)。 MPa,时空速在0.05到5 kg / 1 /小时之间,以产生一次转化流; b)将初级转化物流送入第一气/液分离器(4),并从第一气/液分离器(4)中除去气态物流和液态物流; c)将气态物流送至第二转化反应器(7); d)在氢气存在下,在325〜600℃的温度,1〜30MPa的压力,时空速度为0.1〜20℃的条件下,通过含有转化催化剂的含有转化催化剂的第二转化反应器(7)。以10kg / l /小时的速度产生具有较低沸程的进一步转化的物流。 ;

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