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    • 2. 发明授权
    • Purification of caustic soda
    • 苛性钠的净化
    • US6113657A
    • 2000-09-05
    • US41691
    • 1998-03-13
    • Dieter SchlaferMichael MaussMatthias RaulsDieter Baumann
    • Dieter SchlaferMichael MaussMatthias RaulsDieter Baumann
    • C01D1/30
    • C01D1/30
    • In a process for preparing crystalline NaOH.3.5H.sub.2 O, NaOH.3.5H.sub.2 O is allowed to crystallize from an aqueous sodium hydroxide solution which contains sodium chloride and is saturated in respect of NaOH.3.5H.sub.2 O and the crystals formed are separated from the solution using a mechanical solid/liquid separation apparatus, wherein the solid/liquid separation is carried out under conditions under which the crystalline NaOH.3.5H.sub.2 O is freed sufficiently of residual solution adhering to the surface for the sodium chloride content of the crystalline NaOH.3.5H.sub.2 O obtained to be less than 100 mg per kg. The crystalline NaOH.3.5H.sub.2 O is subjected to an additional purification step, which may include the at least superficial melting or the at least superficial dissolution of the crystals, in combination with a solid/liquid separation step. The additional purification step. The additional purification step comprises washing the crystalline NaOH.3.5H.sub.2 O separated off.
    • 在制备结晶NaOH.3.5H2O的方法中,使NaOH.3.5H2O从含有氯化钠的氢氧化钠水溶液中结晶,并且在NaOH.3.5H 2 O下饱和,并将形成的晶体与溶液分离,使用 机械固/液分离装置,其中固/液分离在结晶NaOH.3.5H2O充分释放残留溶液附着在表面上的条件下进行,得到的结晶NaOH.3.5H2O的氯化钠含量为 小于100mg / kg。 结晶NaOH.3.5H2O经受另外的纯化步骤,其可以包括与固/液分离步骤组合的晶体的至少表面熔融或至少表面溶解。 额外的净化步骤。 另外的纯化步骤包括洗涤析出的结晶NaOH.3.5H2O。
    • 4. 发明授权
    • Recovery of substantially potassium-free hydrated magnesium chloride from contaminated aqueous solutions
    • 从污染水溶液中回收大量无钾水合氯化镁
    • US3852044A
    • 1974-12-03
    • US87630669
    • 1969-11-13
    • GREAT SALT LAKE MINERALS
    • NEITZEL UFLINT HLUKES J
    • C01F5/30B01D9/02C01D1/30C01F5/26
    • C01F5/30C01P2006/80
    • Aqueous solutions containing magnesium chloride as the major dissolved salt but contaminated with sulfate, potassium and sodium to the extent that magnesium chloride produced by evaporating the solution is unacceptably contaminated with potassium, sodium, and sulfate impurities are concentrated to at least near magnesium chloride hexahydrate saturation and are then cooled sufficiently to reduce the potassium concentration to below about 1 mole and the sodium concentration to below about 1 1/2 moles per 1000 moles water. The thus-concentrated solutions are then treated to the extent necessary to reduce the concentration of sulfate to below about 4 moles per 1000 moles water. The remaining brine is evaporated to obtain substantially pure, hydrated magnesium chloride, usually bischofite, containing no more than a few parts per million of potassium impurity. The process is particularly adapted to the production of substantially pure bischofite from brines of the type occuring in the Great Salt Lake of Utah.
    • 含有氯化镁作为主要溶解盐但被硫酸盐,钾和钠污染的水溶液,使得通过蒸发溶液产生的氯化镁被不可接受地被钾,钠和硫酸盐杂质污染的程度被浓缩至至少接近氯化镁六水合物饱和度 然后充分冷却以将钾浓度降低至低于约1摩尔,并将钠浓度降低至低于每1000摩尔水约11/2摩尔。 然后将如此浓缩的溶液处理至必需的程度,以将硫酸盐浓度降低至每1000摩尔水低于约4摩尔。 将剩余的盐水蒸发以获得基本上纯的,水合的氯化镁,通常是二水合镁,其含有不超过百万分之几的钾杂质。 该方法特别适用于从位于犹他州大盐湖的盐水生产基本上纯的双草铁矿。