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Brief description of the hydrotreatment and hydroisomerization of charges from the biomass in which the effluent to hydrotreating and the flow of 1996 contain a content of carbon monoxide limited

机译:对生物质中加氢处理和加氢异构化的简要说明,其中进行加氢处理的废水和1996年的水流量包含一氧化碳的限量

摘要

It describes a process for the production of middle distillates from a load comprising at least a fraction of the load from a single source, said process comprising at least: a) a hydrotreatment step in which said load is placed in contact with a hydrotreatment catalyst in a fixed bed, said catalyst comprising a water-soluble - dehydrogenating function and an amorphous support, b) a step of separation of at least a portion of the effluent from step a) in at least one gaseous fraction comprising hydrogen, at least of the co and of the co and the compounds c4 -, and at least one hydrocarbon liquid effluent, c) a step for hydroisomerisation of at least a portion of the hydrocarbon liquid effluent from step b), in the presence of a hydroisomerisation catalyst in a fixed bed, d) a fractionation step of the effluent from step c) in order to obtain at least one middle distillate fraction, a process in which it returns to step a) at least a portion of the gaseous fraction separated in step b), the gaseous fraction transmitted in step a) comprising a co content of between 0% and 3% by volume.
机译:它描述了由包括至少一个来源的一部分负载的负载物生产中间馏分的方法,所述方法至少包括:a)加氢处理步骤,其中所述负载物与加氢处理催化剂接触。固定床,所述催化剂包含水溶性-脱氢功能和无定形载体,b)将步骤a)的至少一部分流出物分离成至少一种包含氢气的气态馏分的步骤, co和co以及化合物c4-和至少一种烃类液体流出物,c)在加氢异构化催化剂的存在下,将步骤b)中至少一部分烃类液体流出物加氢异构化的步骤床,d)来自步骤c)的流出物的分馏步骤,以获得至少一种中间馏出物馏分,在该方法中,其返回步骤a)至少一部分在步骤b)中分离的气态馏分,在步骤a)中传输的气态馏分的co含量为0体积%至3体积%。

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