Department of Chemistry, College of Natural Sciences, Seoul National University, Gwanak-ro 1, Gwanak-gu, Seoul 151-747, Republic of Korea.
Phys Chem Chem Phys. 2013 Nov 28;15(44):19510-7. doi: 10.1039/c3cp52613e.
Abrupt changes in effective concentration and osmotic pressure of lower critical solution temperature (LCST) mixtures facilitate the design of a continuous desalination method driven by a mild temperature gradient. We propose a prototype desalination system by circulating LCST mixtures between low and high temperature (low T and high T) units. Water molecules could be drawn from a high-salt solution to the LCST mixture through a semipermeable membrane at a temperature lower than the phase transition temperature, at which the effective osmotic pressure of the LCST mixture is higher than the high-salt solution. After transfer of water to the high T unit where the LCST mixture is phase-separated, the water-rich phase could release the drawn water into a well-diluted solution through the second membrane due to the significant decrease in effective concentration. The solute-rich phase could be recovered in the low T unit via a circulation process. The molar mass, phase transition temperature, and aqueous solubility of the LCST solute could be tuneable for the circulatory osmotic desalination system in which drawing, transfer, release of water, and the separation and recovery of the solutes could proceed simultaneously. Development of a practical desalination system that draws water molecules directly from seawater and produces low-salt water with high purity by mild temperature gradients, possibly induced by sunlight or waste heat, could be attainable by a careful design of the molecular structure and combination of the circulatory desalination systems based on low- and high-molar-mass LCST draw solutes.
LCST 混合物有效浓度和渗透压的急剧变化有助于设计一种由温和温度梯度驱动的连续脱盐方法。我们提出了一种原型脱盐系统,通过在低温(低 T)和高温(高 T)单元之间循环 LCST 混合物来实现。水分子可以在低于相变温度的温度下通过半透膜从高盐溶液中被抽到 LCST 混合物中,此时 LCST 混合物的有效渗透压高于高盐溶液。将水转移到 LCST 混合物发生相分离的高 T 单元后,由于有效浓度显著降低,富含水的相可以通过第二膜将抽到的水释放到稀释良好的溶液中。富溶质相可以通过循环过程在低 T 单元中回收。LCST 溶质的摩尔质量、相变温度和水溶解度可以通过循环渗透压脱盐系统进行调节,在该系统中,抽提、转移、释放水以及溶质的分离和回收可以同时进行。通过仔细设计基于低摩尔质量和高摩尔质量 LCST 抽提剂的循环脱盐系统的分子结构和组合,开发一种可以直接从海水中抽取水分子并通过温和温度梯度(可能由阳光或废热引起)生产高纯度低盐度水的实用脱盐系统是可行的。