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Process and apparatus for the separation of two-or multicomponent mixtures by multi-stage fractional crystallization

机译:通过多阶段分步结晶分离两组分或多组分混合物的方法和设备

摘要

1,229,022. Progressive purification. METALLWERK A.G. BUCHS. 16 April, 1968 [14 April, 1967], No. 17849/68. Heading B1G. A process for progressive purification of a constituent of a liquid mixture in a plurality of crystallization stages employs a crystallization and melting circuit comprising a crystallizer A and a heater B, the circuit being fed successively with liquid from each of a plurality of vessels (10 as shown) containing liquids of progressively increasing concentration with respect to the constituent. The circuit may also include a vessel E for washing liquid. The crystallizer A is an indirect heat exchanger having a separate coolant circuit and a crystal layer forms on the cooled surfaces of the heat exchanger. The liquid being treated may flow over the cooled surfaces as a film or stream. The crude liquid mixture is fed to vessel I, mother liquor is withdrawn from vessel F, and the desired purified constituent is finally withdrawn from vessel G. At an intermediate stage in the process, liquid from vessel n is circulated through crystallizer A to. form a crystal layer, the resulting mother liquor being discharged to vessel n-1. Further liquid of the same composition may then be passed from vessel E to crystallizer A after heating in heater B, thereby washing residual liquid from the crystal layer and dissolving a portion of the layer, and the wash liquid discharged to vessel n. Liquid from vessel n+I is then circulated through crystallizer A after heating in heater B, thereby dissolving the crystal layer, whereafter heating by heater B is discontinued and a further crystal layer is formed. A smooth layer may be built up by repeated alternate crystallization and partial redissolution. After completion of the stage, residual liquid on the surfaces of the heat exchanger may be cooled to form crystal nuclei before commencement of the next stage. The plurality of stages may be repeated to form a continuous process.
机译:1,229,022。逐步纯化。 METALLWERK A.G.布希。 1968年4月16日[1967年4月14日],编号17849/68。标题B1G。在多个结晶阶段中逐步纯化液体混合物成分的方法采用了包括结晶器A和加热器B的结晶和熔化回路,该回路从多个容器(10个如图所示)包含相对于该成分浓度逐渐增加的液体。该回路还可以包括用于洗涤液体的容器E。结晶器A是具有单独的冷却剂回路的间接热交换器,并且在热交换器的冷却表面上形成晶体层。被处理的液体可能以薄膜或流的形式流过冷却表面。将粗制液体混合物进料至容器I,从容器F中抽出母液,最后从容器G中抽出所需的纯化成分。在该过程的中间阶段,来自容器n的液体通过结晶器A循环至。形成结晶层,将所得母液排入容器n-1。然后,在加热器B中加热之后,可以将具有相同组成的另外的液体从容器E输送到结晶器A,从而从晶体层洗净残留的液体并且溶解该层的一部分,并且将洗净液体排出到容器n。在加热器B中加热之后,来自容器n + 1的液体然后在结晶器A中循环,从而溶解晶体层,此后,停止由加热器B的加热并且形成另外的晶体层。可以通过重复交替的结晶和部分再溶解来建立光滑层。在该阶段完成之后,可以在下一阶段开始之前将热交换器表面上的残留液体冷却以形成晶核。可以重复多个阶段以形成连续过程。

著录项

  • 公开/公告号GB1229022A

    专利类型

  • 公开/公告日1971-04-21

    原文格式PDF

  • 申请/专利权人 BUCHS METALLWERK AG;

    申请/专利号GB19680017849

  • 发明设计人

    申请日1968-04-16

  • 分类号B01D9/02;B01D9/00;B02C23/04;C07C7/14;C07C51/43;

  • 国家 GB

  • 入库时间 2022-08-23 09:15:24

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