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Process improvement of aromatic and naphthene aromatics diesel cuts

机译:芳烃和环烷芳烃柴油馏分的工艺改进

摘要

"The process of improvement of aromatic and naphthene aromatics diesel cuts.The transformation process of a cutting gas to produce a fuel that has a quality according to strict specifications in terms of sulphur content, content of aromatic compounds.Cetane index, temperature, boiling T95, 95% of the compounds and density, D15 / 4, 15 198 C.This process comprises a step of hidrorrefinau00e7u00e3o and a stage of hydrocracking, this last using a catalyst which contains at least one zeolite.The conversion into products which have a boiling point less than 150 198 C is, for the whole of the two stages hydrocracking and hidrorrefinau00e7u00e3o, less than 40% in weight, andFor the step of hidrorrefinau00e7u00e3o, between 1 and 15% by weight.The temperature, TR2, stage of hydrocracking, is lower than the temperature of the stage of hidrorrefinau00e7u00e3o, Tr1, and the difference between the temperatures Tr1 and TR2 is between 0 and 80 198 C.
机译:“改善芳烃和环烷芳烃柴油馏分的过程。切割气转化为燃料的转化过程,该燃料的质量符合严格的硫含量,芳族化合物含量,十六烷值,温度,沸腾的T95,95%的化合物和密度,D15 / 4、15 <198>C。此过程包括hidrorrefina u00e7 u00e3o步骤和加氢裂化步骤,最后使用含有至少一种沸石的催化剂在整个加氢裂化和Hidrorrefina u00e7 u00e3o的两个阶段中,转化为沸点低于150°C的产品的重量均小于40%,对于Hidrorrefina u00e7 u00e3o的步骤而言在加氢裂化阶段的温度TR2低于Hidrorrefina u00e7 u00e3o阶段Tr1的温度,温度Tr1和TR2之间的差在0至80 < 198>C。

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