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process and installation for the preparation of a simple solution based on the solution composition.

机译:用于基于溶液组成的简单溶液制备的过程和安装。

摘要

A continuous process for obtaining a solution of a single component having a negative heat of solution, wherein a compound solution containing said component and others is evaporated under sub-atmospheric pressure so that crystals of the required component are formed; both the vapours and the crystals being withdrawn from the evaporator and introduced into a direct-contact condenser in which a solution of said single component is circulating, and from which PICT:0655084/III/1 part of said circulating solution is continuously withdrawn. The heat of condensation of the vapours is thus utilized for dissolving the crystals. The solution obtained by digesting raw phosphate with dilute nitric acid is introduced through pipe 3 into a circulating system comprising pump 4, evaporator 1, and crystallizer 2. A 50 per cent solution of calcium nitrate is circulated by pump 7 through cooler 8, direct-contact condenser 5, and reservoir 6. The entire system is evacuated by steam-ejector 9. The evaporator 1 is maintained at 4.3 mm. whereby the digestion-liquor evaporates at 15 DEG C. and deposits crystals of calcium nitrate; these crystals are separated from mother-liquor in centrifuge 11 and then introduced in reservoir 6. The vapours from the evaporator pass to the condenser through pipe 10. The temperature of the solution circulating in the condenser is maintained at 3.2 DEG C. by cooler 8; and the solution is maintained at the required concentration by adding water through pipe 14. Part of the solution is continuously withdrawn through line 15.
机译:一种用于获得具有负溶液热的单一组分的溶液的连续方法,其中将包含所述组分和其他组分的化合物溶液在低于大气压的压力下蒸发,从而形成所需组分的晶体;蒸气和晶体都从蒸发器中抽出并引入直接接触式冷凝器中,所述单一组分的溶液在该直接循环式冷凝器中循环,并且从中连续抽出一部分 。蒸气的冷凝热因此被用于溶解晶体。将稀磷酸盐用稀硝酸消化后得到的溶液通过管道3引入到包含泵4,蒸发器1和结晶器2的循环系统中。硝酸钾的50%溶液由泵7通过冷却器8进行循环,直接通过接触冷凝器5和储存器6。整个系统由蒸汽喷射器9抽成真空。蒸发器1保持在4.3mm。消化液在15℃蒸发并沉积硝酸钙晶体。这些晶体在离心机11中从母液中分离出来,然后引入容器6中。来自蒸发器的蒸气通过管子10进入冷凝器。在冷凝器中循环的溶液的温度通过冷却器8保持在3.2℃。 ;然后通过管道14加水将溶液保持在所需浓度。部分溶液通过管线15连续抽出。

著录项

  • 公开/公告号LU28940A1

    专利类型

  • 公开/公告日1948-04-20

    原文格式PDF

  • 申请/专利权人 DIRECTIE STAATSMIJNEN NL;

    申请/专利号LU19480028940

  • 发明设计人

    申请日1948-02-20

  • 分类号B01D1;B01D9;B01F1;C05C5;

  • 国家 LU

  • 入库时间 2022-08-24 02:46:40

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