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首页> 外文期刊>ACS Omega >Performance Evaluation of 1-Cyclohexylpiperidine as a Draw Solute for Forward Osmosis Water Separation and CO2 Recovery
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Performance Evaluation of 1-Cyclohexylpiperidine as a Draw Solute for Forward Osmosis Water Separation and CO2 Recovery

机译:1-环己基哌啶的性能评价为前渗透水分离和CO2回收的溶液

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Membrane-based technologies, such as forward osmosis (FO), offer the advantage of treating water through a spontaneous process that requires minimal energy input while achieving favorable water permeability and selectivity. However, the FO process still has some challenges that need to be solved or improved to become entirely feasible. The main impediment for this technology is the recovery of the draw solute used to generate the osmotic potential in the process. In this paper, we discuss the use of a switchable polarity solvent, 1-cyclohexylpiperidine (CHP), as a draw solute that responds to external stimuli. Specifically, the miscibility of CHP can be switched by the presence of carbon dioxide (CO_(2)) and is reversible by applying heat. Thus, in this study, the hydrophobic CHP is first converted to the hydrophilic ammonium salt (CHPH~(+)), and its capability as a draw solution (DS) is thoroughly evaluated against the typical osmotic agent, sodium chloride (NaCl). Our results show that the water permeability across the thin film composite membrane increases by 69% when CHPH~(+) is used as the DS. Also, the water permeability when using different feed solutions: aqueous solutions of (a) urea and (b) NaCl were evaluated. In both cases, the CHPH~(+) generates water fluxes in the range of 65 ± 4 LMH and 69 ± 2 LMH, respectively. We then separate the diluted DS by applying 75 °C to the solution to recover the pure CHP and water. The results of this work provide a proof-of-concept of a CHP wastewater and desalination method via an FO process.
机译:基于膜的技术,例如前渗透(Fo),通过自发过程提供处理水的优点,该方法需要最小的能量输入,同时实现有利的水渗透性和选择性。然而,FO过程仍然存在需要解决或改进的一些挑战,以完全可行。该技术的主要障碍是恢复用于在该过程中产生渗透潜力的绘制溶质。在本文中,我们讨论了可切换极性溶剂,1-环己基哌啶(CHP)的用途,作为响应外部刺激的汲取溶质。具体地,CHP的混溶可以通过存在二氧化碳(CO_(2))来切换,并且通过施加热来可逆。因此,在该研究中,疏水CHP首先将其转化为亲水性铵盐(CHPH〜(+)),并且其作为涂抹溶液(DS)的能力彻底地评价典型的渗透剂,氯化钠(NaCl)。我们的研究结果表明,当CHPH〜(+)用作DS时,薄膜复合膜穿过薄膜复合膜的水渗透率增加了69%。此外,使用不同进料溶液时的渗透性:评估(A)尿素和(B)NaCl的水溶液。在这两种情况下,CHPH〜(+)分别在65±4 LMH和69±2 LMH的范围内产生水量。然后,我们将稀释的DS分离通过将75℃施加到溶液中以回收纯CHP和水。该工作的结果通过FO方法提供了CHP废水和脱盐方法的概念。

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