基于动态降温结晶工艺的盐湖卤水镁锂分离研究
Study on Separation of Magnesium and Lithium from Salt Lake Brine Based on Dynamic Cooling Crystallization Process 
投稿时间:2021-12-09  修订日期:2022-01-03
DOI:10.12119/j.yhyj.202301006
中文关键词:  盐湖卤水  分 离  非平衡  动 态  结 晶
英文关键词:Salt lake brine  Separation  Non-Equilibrium  Dynamic  Crystallization
基金项目:国家自然科学基金(U20A20149,51874194,21908137);山西省研究生教育创新项目(2021Y139)
作者单位
张成卓 山西大学资源与环境工程研究所,山西 太原 030006 
成怀刚 山西大学资源与环境工程研究所,山西 太原 030006
青海大学化工学院,青海 西宁 810016 
李琳琳 山西大学资源与环境工程研究所,山西 太原 030006 
薛芳斌 山西大学资源与环境工程研究所,山西 太原 030006 
李恩泽 山西大学资源与环境工程研究所,山西 太原 030006 
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中文摘要:
      青海盐湖卤水锂资源储量丰富,高镁锂比卤水存在镁锂分离难的问题。基于非平衡动态降温过程中不同盐组分结晶行为存在差异的原理,开展了强制分离高镁锂比卤水的研究,考察了卤水镁锂比、降温速率、流体状态和卤水温度对镁锂分离效果的影响,并分析了结晶过程中镁锂分离的介稳性特点。结果表明,通过非平衡动态降温结晶析出MgCl2·6H2O,可以实现卤水脱镁和镁锂分离,当降温速率为-1.25 ℃/min、卤水温度在70 ℃至50 ℃范围内,镁锂比在10∶1~80∶1时,镁锂分离因子最高可达到1.876,结晶的MgCl2·6H2O纯度最高为99.42%。非平衡动态降温结晶工艺相较于经典的盐田工艺,最多可将锂损失率从模拟盐田工艺的38.39%降至7.56%。该工艺为盐湖卤水镁锂分离提供了一条新的思路,也为后续高纯锂盐的制备奠定了基础。
英文摘要:
      Qinghai salt lake brine with rich lithium resources,and high magnesium-lithium ratio has the problem of difficult separation of magnesium-lithium from the brine.Based on the principle of the difference in crystallization behavior of different salt components during the non-equilibrium dynamic cooling process,this paper carried out a study on the forced separation of brine with a high magnesium-lithium ratio,and investigated the effect of brine magnesium-lithium ratio,cooling rate,fluid state and brine temperature on the separation of magnesium-lithium.The effect and the metastability characteristics of magnesium-lithium separation during the crystallization process were analyzed.The results show that by non-equilibrium dynamic cooling and crystallization to precipitate MgCl2·6H2O,brine demagnesium and magnesium-lithium separation can be realized.When the cooling rate is -1.25 ℃/min,the brine temperature is in the range from 70 ℃ to 50 ℃,the magnesium-to-lithium ratio is 10∶1 to 80∶1,the maximum separation factor of magnesium and lithium can reach 1.876,and the maximum purity of crystallized MgCl2·6H2O is 99.42%.Compared with the classic salt field process,the non-equilibrium dynamic cooling crystallization process can reduce the lithium loss rate from 38.39% of the simulated salt field process to 7.56% at most.This process provides a new idea for the separation of magnesium and lithium from salt lake brine,and also lays a foundation for the subsequent preparation of high-purity lithium salts.
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