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Apparatus for the recovery of volatile constituents in liquids containing fractions having different boiling points

机译:用于回收含有沸点不同的馏分的液体中挥发性成分的设备

摘要

PICT:0673544/III/1 Liquid is evaporated by passing it through a heat-exchanger wherein it is heated by hot water and then introducing it into a film evaporator. The hot water for the heat-exchanger is obtained from a tank heated by steam, and the supply of steam is thermostatically controlled with respect to the temperature of the liquid about to enter the evaporator, or of the water leaving the heat-exchanger. The liquid-to-be-evaporated is pumped through heat-exchanger 14 and then through heat-exchanger 16 which lies behind heat-exchanger 14. Hot water is pumped from tank 17 to heat-exchanger 16 via pipes 19, 20, 21, and back again to the tank via pipes 22, 23, 24. The heated liquid passes through pipe 25 into evaporator 11. The water in tank 17 is heated by injection of steam through pipe 31; and the steam-supply is controlled by valve 32 operated by a diaphragm which is subject to air pressure in the valve part 33 which is connected by pipe 35 to regulator 34. The temperature-sensitive element of regulator 34 extends into the heated liquid as it enters the evaporator. The evaporator may be of the form disclosed in Specifications 595,597 and 673,543. The vapours from the evaporator are condensed in condenser 27, and the condensate is collected in tank 28. Unevaporated liquid leaves the evaporator through pipe 29, and is circulated through heat-exchanger 14, before finally passing out of the system through outlet 30. Specification 673,545 also is referred to.
机译:使液体通过热交换器进行蒸发,在热交换器中,液体被热水加热,然后引入薄膜蒸发器中。用于热交换器的热水是从被蒸汽加热的罐中获得的,并且蒸汽的供应相对于即将进入蒸发器的液体或离开热交换器的水的温度进行恒温控制。待蒸发的液体通过热交换器14泵送,然后通过位于热交换器14后面的热交换器16泵送。热水从水箱17经由管道19、20、21泵送到热交换器16。加热后的液体通过管道25进入蒸发器11。被加热的液体通过管道22、23、24返回到水箱。水箱17中的水通过通过管道31注入蒸汽而被加热。蒸汽供应是由阀32控制的,该阀32由一个隔膜驱动,该隔膜受到阀部分33中的气压的作用,该阀部分33通过管道35与调节器34相连。调节器34的温度敏感元件随着其进入加热的液体中进入蒸发器。蒸发器可以是在规格595,597和673,543中公开的形式。来自蒸发器的蒸气在冷凝器27中冷凝,冷凝物收集在水箱28中。未蒸发的液体通过管道29离开蒸发器,并通过热交换器14循环,最后最终通过出口30离开系统。也参考673,545。

著录项

  • 公开/公告号GB673544A

    专利类型

  • 公开/公告日1952-06-11

    原文格式PDF

  • 申请/专利号GB19490009452

  • 发明设计人

    申请日1949-04-07

  • 分类号B01D1/00;

  • 国家 GB

  • 入库时间 2022-08-24 01:01:14

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