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A process for the treatment of nacl - saturated, kcl -, mgcl deep 2 -, mgso deep 4 - containing, in order to obtain a solutions on mgcl deep 2 has been swivelled up aet preferential solution
A process for the treatment of nacl - saturated, kcl -, mgcl deep 2 -, mgso deep 4 - containing, in order to obtain a solutions on mgcl deep 2 has been swivelled up aet preferential solution
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机译:为了获得对mgcl deep 2的溶液,已经解决了一种处理nacl-饱和,kcl-,mgcl deep 2-,mgso deep 4-的方法。
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摘要
Treatment of satd. NaCl solns. contg. KCl, MgCl2 and MgSO4, for the prepn. of a highly satd. soln. of MgCl2 contg. a reduced amt. of KCl, Nacl and MgSO4, plus high-grade KCl and K2SO4. The novelty is (a) soln. is decomposed with re-cycled carnallite salt to give a soln. contg. up to 300 g/l MgCl2 by enrichment with MgCl2 and also MgSO4 from the evaporated sa (b) KCl from (a) and the residual NaCl are removed as a moist decompsn. sa (c) soln. is heated to 90-130 degrees C and evaporated almost to saturation with KCl and NaCl, and re-cycled langbeinite seed crystals added to remove supersatd. MgSO4 so the soln. contains 25-55 g/l MgSO4; (d) the langbeinite obtd., free from NaCl and KCl is re-used in stage (c), and the soln. evaporated at 80-95 degrees C, cooled to 25-40 degrees C to obtain soln. and the salt for re-cycling. The conc. solns. of MgCl2 are used for mfg. Mg metal and Mg cpds.
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机译:饱和的治疗。氯化钠溶液。续用于制备的氯化钾,氯化镁和硫酸镁。高度满意的soln。氯化镁含量续减少了氯化钾,氯化钠和硫酸镁,再加上高级氯化钾和硫酸钾。 (a)新颖。用回收的角卤石盐分解,得到钠。续通过从蒸发的盐中富集MgCl2和MgSO4达到300 g / l MgCl2; (b)将(a)中的氯化钾和残留的氯化钠作为湿分解物除去。盐; (c)溶解。将其加热至90-130摄氏度,并用KCl和NaCl蒸发至几乎饱和,然后添加再循环的蓝贝氏体晶种以去除过饱和。故以MgSO4为溶剂。包含25-55 g / l MgSO4; (d)在步骤(c)中重新使用不含NaCl和KCl的兰贝特石块,然后重新使用。在80-95℃下蒸发,冷却至25-40℃以获得溶胶。和盐用于回收。浓。 solns。 MgCl 2用于制造。镁金属和镁cpds。
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