首页> 外国专利> METHOD FOR OBTAINING HYDROCARBON SOLVENTS WITH A BOILING TEMPERATURE EXCEEDING 300 ° C AND A TEMPERATURE TEMPERATURE LESS THAN OR EQUAL -25 ° C

METHOD FOR OBTAINING HYDROCARBON SOLVENTS WITH A BOILING TEMPERATURE EXCEEDING 300 ° C AND A TEMPERATURE TEMPERATURE LESS THAN OR EQUAL -25 ° C

机译:沸腾温度超过300°C且温度低于或等于-25°C的烃类溶剂的获得方法

摘要

The method of obtaining hydrocarbon solvents with a sulfur content of less than 10 million, with an aromatic content less than 500 million, with an initial boiling point greater than or equal to 300 ° C, and with a final boiling point less than or equal to 500 ° C, with a boiling range of not more than 100 ° C, and the method contains the steps of dewaxing the hydrocarbon fraction, the boiling point of which exceeds 300 ° C and which comes after the distillation of the gas oil fraction; hydrodearomatization of all or part of the dewaxed stream in the presence of a catalyst containing nickel on alumina base at a pressure in the range from 6.0 to 20.0 MPa and at a temperature in the range from 80 to 250 ° C; separation of the dewaxed and dearomatised fraction; distillation of the dewaxed and de-aromatized fraction into fractions; the allocation of at least one fraction "300 ° C +" with a temperature of fluidity less than -25 ° C, and this fraction has a boiling range of less than 100 ° C.
机译:一种获得硫含量小于1000万,芳烃含量小于5亿,起始沸点大于或等于300℃,最终沸点小于或等于烃溶剂的烃类溶剂的方法。 500℃,沸程不超过100℃,该方法包括将馏分在粗柴油馏分之后的烃馏分脱蜡的步骤;在氧化铝上含有镍的催化剂存在下,在6.0至20.0 MPa的压力和80至250°C的温度下,对全部或部分脱蜡流进行加氢脱芳香化;脱蜡和脱芳烃馏分的分离;将脱蜡和脱香的馏分蒸馏为馏分;分配至少一个流动性温度低于-25°C的馏分“ 300°C +”,并且该馏分的沸程低于100°C。

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