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,烃油的生产方法,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

THE METHOD FOR PROCESSING SYNTHETIC OIL OF THE PRESENT INVENTION IS CHARACTERIZED IN THAT IT INCLUDES: A FIRST FRACTIONAL-DISTILLATION STEP OF SUBJECTING A MATERIAL TO BE PROCESSED, WHICH COMPRISES SYNTHETIC OIL OBTAINED BY FISCHER TROPSCH SYNTHESIS, TO FRACTIONAL DISTILLATION TO OBTAIN A MIDDLE DISTILLATE, WHICH CONTAINS A FRACTION HAVING A BOILING POINT OF 150 TO 360oC AT 90% BY MASS OR MORE, AND A WAX DISTILLATE WHICH IS HEAVIER THAN THE MIDDLE DISTILLATE; A HYDROTREATING STEP OF SUBJECTING THE MIDDLE DISTILLATE OBTAINED IN THE FIRST FRACTIONAL-DISTILLATION STEP TO HYDROTREATING BY BRINGING THE SAME INTO CONTACT WITH HYDROTREATING CATALYST IN THE PRESENCE OF HYDROGEN SO THAT A FRACTION HAVING A BOILING POINT OF 150°C OR LOWER OF THE MIDDLE DISTILLATE HAS A CONTENT (% BY MASS) WITH AN INCREASE RATE OF 9% BY MASS OR LESS AFTER THE CONTACT WITH THE CATALYST; A SECOND FRACTIONAL-DISTILLATION STEP OF SUBJECTING THE MIDDLE DISTILLATE HAVING PASSED THROUGH THE HYDROTREATING STEP TO FRACTIONAL DISTILLATION TO OBTAIN A FIRST FRACTION, WHICH CONTAINS A FRACTION HAVING A BOILING POINT OF 150 TO 250°C AT 90% BY MASS OR MORE, AND A SECOND FRACTION, WHICH IS HEAVIER THAN THE FIRST FRACTION; A HYDROCRACKING STEP OF SUBJECTING THE WAX DISTILLATE OBTAINED IN THE FIRST FRACTIONAL-DISTILLATION STEP TO HYDROCRACKING BY BRINGING THE SAME INTO CONTACT WITH HYDROCRACKING CATALYST IN THE PRESENCE OF HYDROGEN; A THIRD FRACTIONAL-DISTILLATION STEP OF SUBJECTING THE WAX DISTILLATE HAVING PASSED THROUGH THE HYDROCRACKING STEP TO FRACTIONAL DISTILLATION TO OBTAIN A THIRD FRACTION, WHICH CONTAINS A FRACTION HAVING A BOILING POINT OF 150 TO 360°C AT 90% BY MASS OR MORE; AND A MIXING STEP OF MIXING THE SECOND FRACTION AND THE THIRD FRACTION.
机译:本发明的合成油的处理方法的特征在于,其包括:分馏的第一步是对要处理的材料进行处理,该材料包括由费歇尔·托普尔合成得到的合成油,以进行分馏的目的是要进行分馏。包含馏分的沸点在150%到360oC(按质量计或更多)为90%,并且蜡馏分重于中馏分;加氢步骤:将在第一个分馏步骤中获得的中间蒸馏物加氢处理,方法是在氢存在下使加氢催化剂与加氢催化剂接触,使得沸点或沸点保持在150点左右。与催化剂接触后,其质量含量(以质量%计)增加或降低9%;分馏的第二个蒸馏步骤是使中间馏分通过加氢蒸馏的馏分达到第一个馏分,该馏分包含沸点为150到250°C或90%M以上的馏分第二部分,比第一部分重;通过在氢存在下与加氢裂化催化剂接触使其完全接触的加氢裂化步骤,使在第一级分馏步骤中获得的蜡馏分进入加氢裂化;第三馏分蒸馏步骤是使蜡馏分通过加氢裂化步骤通过,然后通过分数馏分获得第三馏分,该馏分包含沸点为150至360°C或按质量计90%的馏分以及混合第二部分和第三部分的混合步骤。

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