首页> 外国专利> METHOD FOR TREATMENT OF SYNTHETIC OIL, PROCESS FOR PRODUCTION OF HYDROCARBON OIL, HYDROCARBON OIL FOR HYDROGEN PRODUCTION, HYDROCARBON OIL FOR THE SMOKE POINT IMPROVER FOR KEROSENE, AND HYDROCARBON OIL FOR DIESEL FUEL BASE

METHOD FOR TREATMENT OF SYNTHETIC OIL, PROCESS FOR PRODUCTION OF HYDROCARBON OIL, HYDROCARBON OIL FOR HYDROGEN PRODUCTION, HYDROCARBON OIL FOR THE SMOKE POINT IMPROVER FOR KEROSENE, AND HYDROCARBON OIL FOR DIESEL FUEL BASE

机译:合成油的处理方法,烃油的生产工艺,氢生产的碳氢油,煤油烟点导入的碳氢油和柴油基的碳氢油

摘要

A process characterized by comprising the step of subjecting synthetic oil obtained by the Fischer-Tropsch process to fractional distillation to obtain a middle distillate comprising at least 90% by mass of components having boiling points of 150 to 360°C and a heavy wax component, the step of hydrorefining the middle distillate in such a way that the increase after hydrorefining in the content (% by mass) of components having boiling points of 150°C or below is 9% by mass or below, the step of subjecting the hydrorefined middle distillate to fractional distillation to obtain the first cut comprising at least 90% by mass of components having boiling points of 150 to 250°C and the second heavy cut, the step of hydrocracking the heavy wax component, the step of subjecting the hydrocracked wax component to fractional distillation to obtain the third cut comprising at least 90% by mass of components having boiling points of 150 to 360°C, and the step of mixing the second heavy cut with the third cut.
机译:一种方法,其特征在于,包括将通过费-托法得到的合成油进行分馏以得到中间馏分的中间馏分,该中间馏分包含至少90质量%的沸点为150〜360℃的成分和重蜡成分,加氢精制中间馏分的步骤,使得加氢精制后的沸点为150℃以下的成分的含量(质量%)的增加为9质量%以下,该步骤是对加氢精制的中间产物进行加氢精制的步骤。馏分进行分馏,得到第一馏分和第二重馏分,第一馏分包括沸点为150-250℃的组分,该馏分的质量至少为90%,第二重馏分是将重蜡组分加氢裂化的步骤,将加氢裂化的蜡组分进行加氢裂化的步骤进行分馏以获得第三馏分,其包含至少90质量%的沸点为150至360℃的组分,并且将第二重馏分与第三切。

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