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MULTI-STAGE DISTILLER.

机译:多级蒸馏器。

摘要

1,232,309. Multiple-effect distillation apparatus; desalination of water. GENERAL ELECTRIC CO. 1 Oct., 1968 [5 Oct., 1967], No. 46436/68. Heading B1B. Saline water is desalinated in a multipleeffect distillation apparatus wherein the effects are disposed one above another, the first effect 4 being uppermost, each effect comprising a header 20, a vapour chest through which vertical double fluted heat-exchange tubes 24 extend, a liquid/vapour separator 22, and a heat-exchanger 40. The vapour chest 8 of the first effect is supplied with steam through connection 18, and the steam-condensate is returned to the steam-generator through line 16. The saline water is pumped up through heatexchangers 40 and lines 36 to the topmost header 20, filling all the other headers 20 in the process via lines 34. The saline water is sprayed from the headers 20 into the interior of the tubes 24 of each effect, so that the feed is supplied to the effects in parallel. A mixture of steam and brine emerges from the lower ends of each set of tubes 24 into the corresponding separator 22. The separated brine flows through line 26 into the separator of the next lower effect; and the steam flows through line 28 into the vapour chest of the next lower effect or, in the case of the last (i.e. lowermost) effect, to a condenser. The distillate formed in each vapour chest (except the first) drains through line 29 and line 28 into the vapour chest of the next lower effect. Desalinated water is withdrawn from the bottom of the apparatus through manifold 60. Brine is discharged from sump 64. Each brine drainline 26 is associated with a float valve for maintaining the required pressure differential between the effects.
机译:1,232,309。多效蒸馏装置;淡化水。通用电气公司,1968年10月1日[1967年10月5日],第46436/68号。标题B1B。盐水在多效蒸馏设备中脱盐,其中效果彼此叠置,第一效果4位于最上方,每个效果包括一个集管20,一个蒸气箱,垂直双槽式热交换管24穿过该蒸气箱延伸,液体/蒸汽分离器22和热交换器40。首先通过连接18向蒸汽室8供给蒸汽,并且蒸汽冷凝水通过管线16返回到蒸汽发生器。盐水被泵送通过热交换器40和管线36到达最顶部的集管20,在此过程中通过管线34填充所有其他集管20。将盐水从集管20喷射到每种效果的管24的内部,从而供给饲料并行的效果。蒸汽和盐水的混合物从每组管24的下端流出到相应的分离器22中。分离出的盐水通过管线26进入下一个效果较差的分离器中。蒸汽通过管线28进入下一个较低效果的蒸气室,或者在最后一个(即最低)效果的情况下,流至冷凝器。在每个蒸气箱(第一个蒸气箱除外)中形成的馏出物通过管线29和28排入下一个效果较低的蒸气箱。脱盐水通过歧管60从设备的底部抽出。盐水从贮槽64中排出。每个盐水排放管线26都与一个浮阀相连,以维持作用之间所需的压力差。

著录项

  • 公开/公告号NL163430C

    专利类型

  • 公开/公告日1980-09-15

    原文格式PDF

  • 申请/专利号NL19680013760

  • 发明设计人

    申请日1968-09-26

  • 分类号B01D3/00;B01D1/06;B01D1/26;

  • 国家 NL

  • 入库时间 2022-08-22 18:29:21

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