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PROCESS AND APPARATUS FOR HEAT AND/OR MASS TRANSFER FROM ONE LIQUID TO ANOTHER

机译:从一种液体到另一种液体的传热和/或传质的方法和装置

摘要

1,243,803. Flash distillation apparatus; desalination of water. A. KOGAN. 26 Sept., 1968 [1 Oct., 1967; 15 May, 1968; 26 Aug., 1968], No. 45731/68. Heading B1B. Fresh water is obtained from saline water by heating it and introducing it through conduit 29 (Fig. 2) into a housing 16 where vapour flashes from the saline water as it flows through the housing; the vapours and gases pass through apertures in partitions 28 and the vapours condense in a stream of fresh water, introduced through conduit 32, flowing over the partitions. The pressure in the vapour space below partitions 28 must be maintained such that fresh water on the partitions cannot flow through the apertures. The housing is divided into stages by partitions 27 and baffles 34; and other housings may be connected in series with that shown. The saline water flows up into each stage through a perforated plate 36. Air and non-condensable gases are evacuated from the upper regions of each of the stages. The apertures in partitions 28 are preferably of conical or bell shape, taper in the direction of vapour flow, and are inclined in the direction of fresh water flow. The partitions 28 should preferably be made of insulating material, e.g. plastic, to prevent vapour from condensing on the underside thereof. The saline water is partly pre-heated by heat exchange with fresh water withdrawn from the housing through conduit 35. Fig. 9 shows a housing wherein the saline water rises from stage to stage through diverging risers 73, 75, 77, the fresh water flows down from stage to stage through U-passages, and the vapour passes through perforations into the fresh water stream as it flows through the horizontal passages 83, 86, 89. Distillation systems are also described wherein the vapour is condensed as it rises into a stream of a waterimmiscible liquid, e.g. a hydrocarbon or chlorinated hydrocarbon. The feed saline water is preheated by direct contact with the immiscible liquid after it has been separated from the condensate. The feed saline water may be heated by contacting it with hot pebbles.
机译:1,243,803。闪蒸装置;淡化水。 A.科甘。 1968年9月26日[1967年10月1日; 1968年5月15日; 1968年8月26日],编号45731/68。标题B1B。通过加热盐水并通过导管29(图2)将其引入到外壳16中,可以从盐水中获得淡水,当盐水流过外壳时,蒸汽会从盐水中闪蒸出来。蒸汽和气体通过隔板28中的孔,并且蒸汽在通过导管32引入的新鲜水流中冷凝,流过隔板。隔板28下方的蒸气空间中的压力必须保持使得隔板上的淡水不能流过孔。外壳由隔板27和挡板34划分成几级;其他外壳可以与所示的外壳串联。盐水通过多孔板36向上流入每个级。从每个级的上部区域排出空气和不可冷凝气体。隔板28中的孔优选为圆锥形或钟形,在蒸气流动方向上逐渐变细,并且在新鲜水流动方向上倾斜。隔板28应优选地由绝缘材料制成,例如绝缘材料。塑料,以防止蒸汽在其底面上冷凝。盐水通过与通过导管35从壳体中抽出的淡水进行热交换而被部分预热。图9显示了一个壳体,其中盐水通过分叉的立管73、75、77逐级上升,淡水流过通过U通道从一个阶段降到另一个阶段,当蒸汽流经水平通道83、86、89时,蒸汽穿过穿孔进入淡水流。还描述了蒸馏系统,其中蒸汽在上升为流时被冷凝与水不混溶的液体,例如碳氢化合物或氯化碳氢化合物。进料盐水从凝结水中分离后,通过与不混溶的液体直接接触而预热。饲料盐水可以通过与热卵石接触而被加热。

著录项

  • 公开/公告号FR1584858A

    专利类型

  • 公开/公告日1970-01-02

    原文格式PDF

  • 申请/专利权人

    申请/专利号FRD1584858

  • 发明设计人

    申请日1968-10-01

  • 分类号B01D1/14;

  • 国家 FR

  • 入库时间 2022-08-23 10:41:45

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