首页> 外国专利> Improved process of production of base oils and middle distillates with a conversion-hydroisomerization followed by catalytic dewaxing.

Improved process of production of base oils and middle distillates with a conversion-hydroisomerization followed by catalytic dewaxing.

机译:通过转化-加氢异构化,然后进行催化脱蜡,改进了基础油和中间馏分油的生产工艺。

摘要

Process for the production of oils from a hydrocarbon charge, said process comprising the following successive steps: (a) conversion of the charge with simultaneous hydroisomerization of at least part of the n-paraffins of the load, said loads a sulfur content less than 1,000 ppm by weight, a nitrogen content of less than 200 ppm by weight, containing less metal to 50 ppm by weight and an oxygen content of at most 0, 2%, developing said step a a temperature of 200-500 under a pressure of 2-25 MPa, with a space velocity of 0, 1 to 10 h-1 in the presence of hydrogen and in the presence of a catalyst containing at least one noble metal deposited on a amorphous acid support, the noble metal dispersion being between 20 and 100%; (B) catalytic dewaxing of at least part of the effluent from step (a), conducted at a temperature of 200-500 under a pressure of 1-25 MPa, with an hourly volumetric flow rate of 0, 05-50 h -1,
机译:由烃进料生产油的方法,所述方法包括以下连续步骤:(a)将进料转化,同时将负载的至少一部分正链烷烃同时加氢异构化,所述负载的硫含量小于1,000在200℃至500℃的压力下,将所述步骤温度提高到200℃至500℃,氮含量小于200重量ppm,所含金属少于50重量ppm,氧含量至多为0、2%。 25 MPa,空速为0、1至10 h-1,在氢存在下,在含有至少一种沉积在无定形酸载体上的贵金属的催化剂存在下,贵金属分散体为20至100 %; (B)在200-500的温度,1-25 MPa的压力下,每小时体积流量为0、05-50 h -1的条件下,对步骤(a)的至少一部分废水进行催化脱蜡,

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