首页> 外国专利> Apparatus for the recovery of volatile constituents in liquids containing fractions having different boiling points

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:0673545/III/1 PICT:0673545/III/2 Liquids are evaporated by passing the liquid through two heat exchangers connected in series and then introducing the heated liquid into a film evaporator. The first heat exchanger comprises three concentric tubes wherein the feed-liquid flows through the inner tube, the hot concentrated liquid from the evaporator flows through the annular passage between the inner and the intermediate tubes, and cooling water flows through the annular passage between the intermediate and outer tubes. The evaporation, which is preferably carried out under reduced pressure, is particularly useful in the concentration of fruit juices in the temperature-range of 170 DEG to 190 DEG F. Liquid-to-be-evaporated is pumped via pipe 21 into the inlet 25 of heat- PICT:0673545/III/3 exchanger 22 which comprises, Fig. 6, three sections of pipes 23 connected by bends 24, three tubes 28 concentric with pipes 23 and provided with headers 27, and three more tubes 32 connected by headers 29 disposed between pipes 23 and tubes 28. The liquid-to-be-evaporated flows through pipes 23. Unevaporated liquid leaves evaporator 11 through pipe 54, enters the heat-exchanger at inlet 30, flows through the annular passages between pipes 23 and 32, and leaves the heat-exchanger at outlet 31. Cooling water supplied through pipe 33, is passed through the outer annular passages of heat-exchanger 22. The partially-heated liquid leaving heat-exchanger 22 through outlet 26 is passed to heat-exchanger 35, Fig. 4, which is disposed behind heat-exchanger 22 in Fig. 1. Heat-exchanger 35 is also a system of three concentric pipes. The innermost pipes are connected by bend 37, and the others by headers 40 and 38. The liquid-to-be-evaporated flows through the inner annular passage of heat-exchanger 35; while hot water from tank 19 is pumped countercurrently to said liquid via pipes 47, 48 through the innermost pipe and through the outer annular passage of the heat-exchanger. The water leaving heat-exchanger 35 through outlets 51, 52, is returned to tank 19 via pipe 53. The heated liquid, which preferably only remains in heat-exchanger 35 for 3 to 8 seconds, is passed to evaporator 11 via pipe 44. The vapours from the evaporator are condensed in condenser 15, and the condensate is collected in vessel 17. The evaporator may be of the type disclosed in Specifications 595,597 and 673,543. Specification 673,544 also is referred to.
机译: 通过使液体经过两个串联连接的热交换器,然后将加热的液体引入薄膜蒸发器中来蒸发液体。第一热交换器包括三个同心管,其中进料液体流经内管,来自蒸发器的热浓缩液流经内管和中间管之间的环形通道,冷却水流经中间管之间的环形通道和外管。蒸发最好在减压下进行,对于浓缩温度在170至190°F的果汁特别有用。将要蒸发的液体通过管道21泵入入口25热量-交换器22包括图6中的三部分,通过弯管24连接的管道23,与管道23同心并设有集管27的三个管道28,以及另外三个与管道32连接的管道待蒸发的液体通过设置在管道23和管道28之间的集管29通过管道23流动。未蒸发的液体通过管道54离开蒸发器11,在入口30进入热交换器,流过管道23之间的环形通道。热交换器32和32在出口31处离开热交换器。通过管33供应的冷却水通过热交换器22的外部环形通道。通过出口26离开热交换器22的部分加热的液体被传热。 -交换器35,图4热交换器35在图1中布置在热交换器22的后面。热交换器35也是由三个同心管组成的系统。最里面的管子通过弯头37连接,其余的通过集管40和38连接。要蒸发的液体流过热​​交换器35的内部环形通道;而在热交换器35的内部环形通道中,待蒸发的液体流过热​​交换器35。而来自水箱19的热水则通过最里面的管子和热交换器的外部环形通道,通过管子47、48逆流地泵送到所述液体中。通过出口51、52离开热交换器35的水通过管53返回到水箱19。加热后的液体(最好仅保留在热交换器35中3至8秒)通过管44进入蒸发器11。来自蒸发器的蒸气在冷凝器15中冷凝,并且冷凝物收集在容器17中。蒸发器可以是在规格595,597和673,543中公开的类型。也参考规格673,544。

著录项

  • 公开/公告号GB673545A

    专利类型

  • 公开/公告日1952-06-11

    原文格式PDF

  • 申请/专利号GB19490009453

  • 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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