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PURIFICATION OF SOLVENT USED FOR EXTRACTIVE RECTIFICATION SEPARATION OF STYRENE AND STYRENE SEPARATION METHOD

机译:苯乙烯萃取精分离中所用溶剂的精制及苯乙烯分离方法

摘要

A method for purifying a solvent used for extractive rectification separation of styrene, comprising: introducing a styrene-containing raw material from a center portion into an extractive rectification column; introducing an extractive rectification solvent from an upper portion into the extractive rectification column; following extractive rectification, discharging a raffinate oil from the top of the extractive rectification column, and discharging a styrene-rich rich solvent from the bottom of the extractive rectification column; introducing the rich solvent from the center portion into a solvent recovery column; following reduced pressure distillation, discharging the crude styrene from the top of the solvent recovery column; discharging a poor solvent from the bottom of the solvent recovery column and recycling the same to the upper portion of the extractive rectification column; diverting a portion of the rich solvent to a solvent purification region and introducing water into the solvent purification region; following liquid-liquid extraction, discharging a mixture of styrene polymer and styrene from the top of the solvent purification region; and discharging a purified water-containing solvent from the bottom of the solvent purification region. An application of the above method effectively removes the styrene polymer in the extractive rectification solvent, and simplifies the solvent purifying agent treatment step, thereby ensuring the extractive rectification capabilities of the solvent, and prolonging stable operating time of the device.
机译:一种纯化用于苯乙烯的萃取精馏分离的溶剂的方法,该方法包括:将含苯乙烯的原料从中心部分引入萃取精馏塔中;以及将苯乙烯的原料从萃取塔中引入。从上部将萃取精馏溶剂引入萃取精馏塔中;萃取精馏后,从萃取精馏塔的顶部排出萃余油,并从萃取精馏塔的底部排出富含苯乙烯的富溶剂。将富溶剂从中心部分引入溶剂回收塔;减压蒸馏后,从溶剂回收塔的顶部排出粗苯乙烯。从溶剂回收塔的底部排出不良溶剂,并将其再循环至萃取精馏塔的上部;将一部分富溶剂转移至溶剂纯化区域,并将水引入溶剂纯化区域;进行液-液萃取后,从溶剂纯化区域的顶部排出苯乙烯聚合物和苯乙烯的混合物;从溶剂纯化区域的底部排出纯化的含水溶剂。上述方法的应用有效地去除了萃取精馏溶剂中的苯乙烯聚合物,简化了溶剂纯化剂处理步骤,从而确保了溶剂的萃取精馏能力,并延长了装置的稳定运行时间。

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