首页> 外文会议>9th International Symposium on Salt(第九届世界盐业大会)论文集 >THE NON-EQUILIBRIUM SALT FORMING PHASE DIAGRAM: APPLICATION TO EFFECTIVELY UTILIZE BRITTEN RESOURCE
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THE NON-EQUILIBRIUM SALT FORMING PHASE DIAGRAM: APPLICATION TO EFFECTIVELY UTILIZE BRITTEN RESOURCE

机译:非平衡盐形成相图:在有效利用含盐资源中的应用

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The non-equilibrium state salt forming phase diagram, include primary region and extended Region, are different from solubility phase diagram and metastable phase diagram, which can be used to express the salt forming regions in the non-equilibrium state of evaporation and crystallization process in the high temperature for the multi-component salt-water systems. In this paper the residual brine resource of Tulantai salt-lake(China), Dongtai Salt-lake(China), Jilantai Salt-lake(China), Qarun Salt Lake(Egypt) and Seawater which after precipitation of pure sodium chloride, was analyzed. The benefit strategy needed by bittern utilization was given by compare 'Na2SO4 based plan' with 'MgSO4 based Plan'. The operations required by evaporation processes at 25°C, 75°C, 100°C and 150°C were simulated by a path through the solubility diagram and salt-forming diagram of Mg2+-Na+//SO42--Cl--H2O system. The yield and recovery rate of salt and sulfate were calculated. The results show, (1) more benefit of MgSO4 based plan than that of Na2SO4 based plan. (2) MgSO4 based plan can be putted in practice, but in the middle temperature and vacuum evaporation process. (3) the yield of NaCl for the several bittern in the MgSO4 based plan were 1.53,2.01,2.95,19.48 and 6.8 times respectively than that of Na2SO4 based plan in the normal temperature, the recovery rate of sulfate were increased by 18.46%, 27.51%, 38.23%, 55.13% and 79.99% respectively.
机译:非平衡态成盐相图包括初级区和扩展区,与溶解相图和亚稳态相图不同,可以用来表示蒸发和结晶过程中非平衡态下成盐区。多组分盐水系统的高温。本文分析了纯净氯化钠沉淀后的图兰台盐湖(中国),东台盐湖(中国),吉兰台盐湖(中国),卡伦盐湖(埃及)和海水中的残留盐水资源。 。通过比较“基于Na2SO4的计划”与“基于MgSO4的计划”,得出了卤水利用所需的利益策略。通过Mg2 + -Na + // SO42-Cl-H2O系统的溶解度图和成盐图的路径模拟了25°C,75°C,100°C和150°C蒸发过程所需的操作。计算了盐和硫酸盐的产率和回收率。结果表明,(1)基于MgSO4的方案比基于Na2SO4的方案具有更多的优势。 (2)基于MgSO4的计划可以付诸实践,但要在中温和真空蒸发过程中进行。 (3)常温下,基于MgSO4的计划中几个卤水的NaCl收率分别是基于Na2SO4的计划的1.53、2.01,2.95、19.48和6.8倍,硫酸盐的回收率提高了18.46%,分别为27.51%,38.23%,55.13%和79.99%。

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