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Separation and purification apparatus and separation and purification method for unsaturated hydrocarbon

机译:不饱和烃的分离提纯装置及分离提纯方法

摘要

For example, an extractive distillation column 4 for separating and purifying butadiene, impurity concentration sensors 32 and 34 for detecting the concentration of specific impurities other than butadiene, a target concentration sensor for detecting the concentration of butadiene in the extractive distillation column, and the extractive distillation column 4. A separation and purification apparatus and a separation and purification method having a differential pressure sensor 30 for detecting a differential pressure between the tower top and the tower bottom. Based on the sensor, the concentration of a specific impurity after a predetermined time, the concentration of butadiene at the top of the tower, and the predicted value of the differential pressure between the top and the bottom of the tower are calculated. Based on the predicted value, the concentration prediction control means 60 Control. A raw material flow rate control valve 21a for controlling the amount of the raw material supplied to the extractive distillation column 4, a load detecting means 61 for detecting the load of the extractive distillation tower, and a load detected according to the detection value detected by the load detecting means 61 The raw material flow rate control valve 21a is controlled by the control means 62.
机译:例如,用于分离和纯化丁二烯的萃取蒸馏塔4,用于检测除丁二烯以外的特定杂质的浓度的杂质浓度传感器32和34,用于检测萃取蒸馏塔中的丁二烯浓度的目标浓度传感器和萃取剂。蒸馏塔4。分离纯化装置和分离纯化方法具有用于检测塔顶和塔底之间的压差的压差传感器30。基于传感器,计算预定时间后特定杂质的浓度,塔顶部的丁二烯浓度以及塔顶部和底部之间的压差预测值。基于该预测值,浓度预测控制单元60进行控制。原料流量控制阀21a,用于控制供给至萃取蒸馏塔4的原料的量;负荷检测装置61,其用于检测萃取蒸馏塔的负荷;以及负荷,其根据由图1所示的检测值进行检测。原料流量控制阀21a由控制装置62控制。

著录项

  • 公开/公告号JPWO2006025330A1

    专利类型

  • 公开/公告日2008-05-08

    原文格式PDF

  • 申请/专利权人 日本ゼオン株式会社;

    申请/专利号JP20060532677

  • 发明设计人 叶内 政信;有森 康彦;

    申请日2005-08-29

  • 分类号C07C7/08;B01D3/40;C07C11/167;C07C11/18;B01D3/42;

  • 国家 JP

  • 入库时间 2022-08-21 20:17:04

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