首页> 外国专利> Residue-free processing of carnallitic crude potassium salts from conventional mining degradation method, comprises e.g. milling the carnallitic crude salt, contacting with cold water and dissolving carnallite

Residue-free processing of carnallitic crude potassium salts from conventional mining degradation method, comprises e.g. milling the carnallitic crude salt, contacting with cold water and dissolving carnallite

机译:用常规的采矿降解方法无残留地处理钙质粗钾盐,包括研磨肉碱盐,与冷水接触并溶解肉碱

摘要

Residue-free processing of carnallitic crude potassium salts from conventional mining degradation method, comprises milling the carnallitic crude salt to a grain size of less than 10 mm, preferably less than 8 mm, contacting with cold water at a solution temperature, dissolving carnallite, halite, optionally sylvite (potassium chloride) and other soluble potash mineral, separating the solvent residue from chloride-free kieserite and anhydrite, evaporating, cooling to obtain magnesium sulfate-rich kieserite as magnesium sulfate concentrate or as a salable additional product. Residue-free processing of carnallitic crude potassium salts from conventional mining degradation method, comprises milling the carnallitic crude salt to a grain size of less than 10 mm, preferably less than 8 mm, contacting with cold water at a solution temperature of 5-25[deg] C, preferably less than 15[deg] C within 15 minutes, preferably 8-10 minutes, completely dissolving carnallite, halite, optionally sylvite (potassium chloride) and other soluble potash mineral in the form of a chloride-based solution, separating the solvent residue from chloride-free kieserite and anhydrite, evaporating, cooling to processed salable potassium chloride, sodium chloride and a concentrated magnesium chloride solution to obtain magnesium sulfate-rich kieserite as magnesium sulfate concentrate or as a salable additional product. The amount of potassium chloride, magnesium chloride and sodium chloride are in the same ratio as in the crude salt.
机译:通过常规采矿降解方法对残留的钙盐粗钾盐进行无残渣处理,包括将钙盐粗盐研磨至小于10毫米,优选小于8毫米的粒度,在溶液温度下与冷水接触,溶解钙盐,盐石,可选地为钾盐(氯化钾)和其他可溶性钾盐矿物,将溶剂残留物与无氯的钾矾石和硬石膏分离,蒸发,冷却,得到富含硫酸镁的钾矾石,作为硫酸镁浓缩物或可销售的附加产品。通过常规采矿降解方法对残留的钙质粗钾盐进行无残渣处理,包括将钙质粗盐研磨成小于10毫米(优选小于8毫米)的粒度,并在5-25的溶液温度下与冷水接触。在15分钟内,优选在8-10分钟内,优选小于15℃,以氯化物基溶液的形式完全溶解角砾石,盐石,任选地钾盐(氯化钾)和其他可溶性钾盐矿物,分离将无氯的钾矾石和无水石膏中的溶剂残留物蒸发,冷却至加工后的可销售的氯化钾,氯化钠和浓氯化镁溶液,得到富含硫酸镁的钾矾石,为硫酸镁浓缩物或可出售的附加产品。氯化钾,氯化镁和氯化钠的量与粗盐中的比例相同。

著录项

  • 公开/公告号DE102012010299A1

    专利类型

  • 公开/公告日2013-11-28

    原文格式PDF

  • 申请/专利权人 K-UTEC AG SALT TECHNOLOGIES;

    申请/专利号DE20121010299

  • 发明设计人 KAPS STEPHAN;SCHERZBERG HEINZ;

    申请日2012-05-24

  • 分类号C01D3/08;

  • 国家 DE

  • 入库时间 2022-08-21 15:38:00

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