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Recovery of benzene and benzene derivatives from gasoline fraction and refinery streams

机译:从汽油馏分和炼油厂流中回收苯和苯衍生物

摘要

A process for the separation of the aromatic compounds benzene, toluene and xylene from an aromatics-containing reformate gasoline and pyrolysis gasoline or a coke-oven light oil or an aromatics-containing refinery stream, in which the aromatics are separated by an extractive distillation uses a novel solvent combination made up of the compounds n,n′-diformyl piperazine or 2,2′-bis-(cyanoethyl)ether in a combination with n-formyl morpholine as a second solvent for extractive distillation so that the solvent combination obtained shows a higher selectivity with regard to the aromatics to be extracted so that a lower solvent load is required. The aromatics-containing feed mixture is first submitted to a pre-distillation so that the obtained fraction has a narrow boiling point range. This fraction is then submitted to an extractive distillation in a first column, in which an aromatics-lean head product of predominantly paraffinic hydrocarbons is obtained as well as an aromatics-enriched bottom product. The bottom product is passed to a second column in which an aromatics-rich raffinate is obtained by reducing the pressure or increasing the temperature so that the extracting solvent combination obtained as bottom product can be recycled into the process.
机译:从含芳族化合物的重整产品汽油和热解汽油或焦炉轻油或含芳族化合物的炼油流中分离芳族化合物苯,甲苯和二甲苯的方法,其中通过萃取蒸馏分离芳族化合物由化合物n,n'-二甲酰基哌嗪或2,2'-双-(氰乙基)醚与n-甲酰基吗啉组合作为萃取蒸馏的第二种溶剂的新型溶剂组合,从而得到的溶剂组合显示对于要萃取的芳族化合物具有较高的选择性,因此需要较低的溶剂量。首先将含芳族化合物的进料混合物进行预蒸馏,以使所获得的馏分具有较窄的沸点范围。然后将该馏分在第一塔中进行萃取蒸馏,在该塔中获得主要为链烷烃的贫芳烃头产物以及富芳烃的塔底产物。将塔底产物通入第二塔,在第二塔中,通过降低压力或升高温度获得富含芳族化合物的萃余液,使得作为塔底产物获得的萃取溶剂组合可以再循环到工艺中。

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