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

FIELD: oil and gas industry.;SUBSTANCE: method involves the first stage of fractional distillation, at which the material that shall be treated and that contains synthetic oil obtained by means of Fisher-Tropsch synthesis is subject to fractional distillation in order to obtain middle distillate that contains the fraction having boiling temperature of 150-360°C, in quantity of 90 wt % or more in view to middle distillate, and paraffin distillate that is heavier than middle distillate; hydrotreatment stage at which middle distillate obtained at the first fractional distillation stage is subject to hydrotreatment by bringing the above middle distillate into contact with hydrotreatment catalyst in presence of hydrogen so that the fraction having boiling temperature of 150°C or less than that of middle distillate has content (wt %) with degree of increase of 9 wt %, or less after contact with catalyst; the second fractional distillation stage at which middle distillate that passed through hydrotreatment stage is subject to fractional distillation so that the first fraction is obtained, which contains the fraction having boiling temperature of 150-250°C, in quantity of 90 wt % or more with view to the first fraction, and the second fraction that is heavier than the first one; hydrocracking stage at which paraffin distillate obtained at the first fractional distillation stage is subject to hydrocracking by bringing the above paraffin distillate into contact with hydrocracking catalyst in presence of hydrogen; the third fractional distillation stage at which paraffin distillate that passed through hydrocracking stage is subject to fractional distillation so that the third fraction is obtained, which contains the fraction having boiling temperature of 150-360°C, in quantity of 90 wt % or more with a view to the third fraction; and mixing stage at which the second and the third fractions are mixed. Invention also refers to hydrocarbon oil and method for obtaining hydrocarbon oils.;EFFECT: obtaining hydrocarbon oils with high yield, achieving economy of the process for obtaining fuel at high levels.;9 cl, 15 ex, 4 tbl, 2 dwg
机译:领域:石油和天然气工业;物质:方法涉及分馏的第一阶段,在该阶段中,应处理的物料和包含通过费雪合成法获得的合成油的物料均应进行分馏以得到中间产物包含沸点为150-360℃的馏分的馏出物,相对于中间馏出物为90重量%以上,并且包含比中间馏出物重的链烷烃馏出物;通过在氢气存在下使上述中间馏分与加氢处理催化剂接触,使在第一分馏阶段获得的中间馏分进行加氢处理,以使沸点低于中间馏分的馏分为150℃以下。与催化剂接触后,具有以重量计增加9%或更少的含量(重量%);在第二分馏阶段中对经过加氢处理阶段的中间馏分进行分馏,从而得到第一馏分,其包含沸点为150-250℃的馏分的量为90重量%以上。查看第一部分,以及比第一部分重的第二部分;加氢裂化阶段,在氢气的存在下,通过使上述链烷烃馏出物与加氢裂化催化剂接触,使在第一分馏阶段获得的石蜡馏出物进行加氢裂化。在第三分馏阶段中,对通过加氢裂化阶段的石蜡馏出物进行分馏,从而得到第三馏分,其包含沸点为150〜360℃的馏分的含量为90重量%以上。展望第三部分;在第二阶段和第三阶段混合的混合阶段。本发明还涉及烃油和获得烃油的方法。效果:以高收率获得烃油,实现高水平获得燃料的方法的经济性; 9 cl,15 ex,4 tbl,2 dwg

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