首页> 外国专利> Brief description of the isomerisation of the fractions rich in paraffin c5 - c8 paraffins has more than 7 carbon atoms.

Brief description of the isomerisation of the fractions rich in paraffin c5 - c8 paraffins has more than 7 carbon atoms.

机译:富含链烷烃c5-c8链烷烃的馏分的异构化的简要说明具有7个以上的碳原子。

摘要

Isomerization of C5-C8 paraffin fractions rich in paraffins with more than 7 C atoms is carried out by treating the feed in a reaction zone comprising of a supported catalyst containing at least a halogen and a metal of group VIII, in fix bed, the reaction being carried out between 30-150 deg.C. The totality of the effluent of the first hydroisomerization section passes through the second section. The separation section is based after the hydroisomerization sections, the feed is mixed with the recycled linear paraffins from the separation section and the resulting mix is sent to the first hydroisomerization section. The effluent from the first hydroisomerization section is mixed with the flux rich in mono-branched paraffins from the separation section which is then sent to the second hydroisomerization section and the effluent from that section is then sent to the separation section. The separation section is also located before the hydroisomerization sections, the feed is mixed with the flux resulting from the second hydroisomerization section and the resulting mixture is sent to separation section. The effluent rich in linear paraffins section is sent to the first hydroisomerization section and the flux rich in mono-branched paraffins from the separation section is added to the effluent from the first hydroisomerization section and the resulting mixture is sent to the second hydroisomerization section.
机译:通过在固定床中在反应区中处理进料来进行进料,所述富含C 5 -C 8链烷烃的C 5 -C 8链烷烃馏分在固定床中进行反应,所述反应区包括至少包含卤素和VIII族金属的负载型催化剂在30-150℃之间进行。第一加氢异构化段的总流出物通过第二段。分离区位于加氢异构化区之后,将进料与来自分离区的循环线性链烷烃混合,然后将所得混合物送入第一加氢异构化区。将来自第一加氢异构化段的流出物与来自分离段的富含单支链烷烃的助熔剂混合,然后将其送至第二加氢异构化段,然后将来自该段的流出物送至分离段。分离区也位于加氢异构化区之前,进料与第二加氢异构化区产生的助熔剂混合,并将所得混合物送入分离区。将富含线性链烷烃段的流出物送至第一加氢异构化段,并将来自分离段的富含单支链烷烃的通量添加至来自第一加氢异构化段的流出液中,并将所得混合物送至第二加氢异构化段。

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