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METHOD OF CONTINUOUS SEPARATION BY COUNTERCURRENT ABSORPTION IN GASEOUS PHASE

机译:气相中逆吸收连续分离的方法

摘要

1,213,523. Separation of gaseous mixtures. SOC. DE RECHERCHES TECHNIQUES ET INDUSTRIELLES. 24 Jan., 1968 [31 Jan., 1967; 18 Aug., 1967], No. 3641/68. Heading B1L. A gaseous mixture whose components are to be separated is fed to an intermediate point of a column by line 1, down through which colmn as passing a granular support material which is impregnated with a suitable differential absorbing liquid, so that as the gas passes up the column through the impregnated material ithe streams are moving in countercurrent. The least strongly absorbed components are withdrawn at 2 and the most strongly absorbed components are taken off at 3. As the support material and absorbent passes down the column it passes in turn through purge zone 13, the gas flow leaving which is recycled as desired by line 4 to input line 1, through depletion zone 19, through enrichment zone 21 and finally through desorption zone 15 before leaving through flow regulator 22. The temperature in the various zones is maintained at the appropriate levels by heat exchangers 38, 39 and 40. Gas leaving the colmn by line 27 is separated from fires in cyclone 28 and then passes by line 30 to pneumatic transport unit 25 to carry impregnated solid leaving flow meter 23 up through line 26 to separator 16 and thence back to the head of the column. The binary separation process described is capable of elaboration for the separation of n-component mixtures, and is described in detail in connection with Fig. 3 (not shown) for the separation of a tertiary mixture. A particularly suitable support material is Celite C22 (registered Trade Mark) impregnated as suitable with hydrocarbons, esters, ethers, glycols, silicones and certain other specific solvents, a large number of such absorbing liquids being specified. The process may be applied to the separation of mixtures of hydrocarbons, alcohols, sterols, aldehydes, ketones, amines (including pyridines and picolines), and organic halogen and sulphur compounds.
机译:1,213,523。分离气体混合物。 SOC。 DE RECHERCHES ET INDUSTRIELLES。 1968年1月24日[1967年1月31日; 1967年8月18日],第3641/68号。标题B1L。将要分离其成分的气体混合物通过管线1送入塔的中间点,向下流经的颗粒状物料经过浸渍有合适的差分吸收液的颗粒状支撑材料,从而随着气体向上流经色谱柱。通过浸渍材料的塔,物流逆流移动。吸收最弱的组分在2处排出,吸收最强的组分在3处排出。当载体材料和吸收剂向下通过色谱柱时,它依次通过吹扫区13,所流出的气流按需要通过管线4到输入管线1,经过耗尽区19,经过富集区21,最后经过解吸区15,然后再离开流量调节器22。热交换器38、39和40将各个区的温度保持在适当的水平。由管线27离开柱状物的气体在旋风除尘器28中与火分离,然后由管线30传递到气动输送单元25,将离开流量计23的浸渍固体通过管线26向上带到分离​​器16,然后回到塔的顶部。所描述的二元分离方法能够精巧地分离出n组分混合物,并结合图3(未示出)进行了详细描述,以分离出第三级混合物。一种特别合适的载体材料是硅藻土C22(注册商标),其浸渍有烃,酯,醚,二醇,硅酮和某些其他特定溶剂,其中有大量这种吸收液体。该方法可用于烃,醇,固醇,醛,酮,胺(包括吡啶和甲基吡啶)以及有机卤素和硫化合物的混合物的分离。

著录项

  • 公开/公告号GB1213523A

    专利类型

  • 公开/公告日1970-11-25

    原文格式PDF

  • 申请/专利号GB19680003641

  • 发明设计人

    申请日1968-01-24

  • 分类号B01D53/02;C07C7/12;G01N30/42;G01N30/58;

  • 国家 GB

  • 入库时间 2022-08-23 09:17:19

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