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Process for the production of solid magnesium sulphate monohydrate

机译:固体一水硫酸镁的生产方法

摘要

PICT:0450987/III/1 Magnesium sulphate monohydrate is obtained by heating a concentrated magnesium sulphate solution, preferably by stages, to a temperature situated on the descending branch of the solubility curve, but at which the separation of solid salts does not take place, and then cooling the solution, preferably by stages, by spontaneous evaporation, to temperatures situated on the ascending branch of the solubility curve and which still lie within the range of formation of the monohydrate. As shown in the Figure, a saturated solution of magnesium sulphate at 75 DEG C. is forced by a pump 2 through the heaters 3, 4 and 5 in succession in which it is heated by stages, to 90 DEG , 105 DEG and 125 DEG C. respectively. The solution then flows in succession through the evaporators 6, 7 and 8 in which it is cooled by stages to 110 DEG , 95 DEG and 75 DEG C. respectively. The evaporators 6 and 7 may be injection evaporators and the evaporator 8 be provided with stirring mechanism. From vessel 8 the solution passes to a separator 9 for removal of deposited salt and the mother liquor is then recirculated through the heaters, evaporators, and separator together with fresh solution from tank 1. The hot vapours from evaporators 7 and 6 are used respectively for heating the heaters 3 and 4, the heater 5 being heated by live steam. The Specification as open to inspection under Sect. 91, comprises also the following subject-matter: the application of the process to the recovery of ferrous sulphate, manganese sulphate, sodium carbonate, or ferric chloride in the form of salts having a low content of water of crystallization. This subject-matter does not appear in the Specification as accepted.
机译:通过将浓硫酸镁溶液(最好分阶段加热)至溶解度曲线下降分支上的温度来加热一水硫酸镁,但不进行固体盐分离放置,然后优选地通过自发蒸发逐步地将溶液冷却至位于溶解度曲线的上升分支上的温度,并且该温度仍处于一水合物形成的范围内。如图所示,由泵2迫使硫酸镁在75℃的饱和溶液依次通过加热器3、4和5,在该加热器中分阶段地将其加热到90、105和125℃。 C.分别。然后溶液依次流过蒸发器6、7和8,在其中分别分阶段冷却至110℃,95℃和75℃。蒸发器6和7可以是喷射蒸发器,并且蒸发器8设置有搅拌机构。溶液从容器8进入分离器9,以除去沉积的盐,然后将母液与加热器,蒸发器和分离器一起与罐1的新鲜溶液一起再循环。来自蒸发器7和6的热蒸汽分别用于加热加热器3和4,加热器5被新鲜蒸汽加热。该规范可供本节检查。 91,还包括以下主题:该方法在回收具有低结晶水含量的盐形式的硫酸亚铁,硫酸锰,碳酸钠或氯化铁中的应用。该主题未在接受的规范中出现。

著录项

  • 公开/公告号GB450987A

    专利类型

  • 公开/公告日1936-07-28

    原文格式PDF

  • 申请/专利权人 METALLGESELLSCHAFT AKTIENGESELLSCHAFT;

    申请/专利号GB19350008409

  • 发明设计人

    申请日1935-03-18

  • 分类号C01F5/40;

  • 国家 GB

  • 入库时间 2022-08-24 06:04:27

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