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1-环己基哌啶作为正向渗透水分离和CO回收的汲取溶质的性能评估

Performance Evaluation of 1-Cyclohexylpiperidine as a Draw Solute for Forward Osmosis Water Separation and CO Recovery.

作者信息

Cruz-Tato Perla, Richardson Tra-My Justine, Romero-Mangado Jaione, Flynn Michael, Nicolau Eduardo

机构信息

Department of Chemistry, University of Puerto Rico, Rio Piedras Campus, 17 University Ave. 1701, San Juan, Puerto Rico 00925, United States.

Molecular Sciences Research Center, University of Puerto Rico, 1390 Ponce De Leon Ave, Suite 2, San Juan, Puerto Rico 00931-3346, United States.

出版信息

ACS Omega. 2020 Oct 1;5(40):25919-25926. doi: 10.1021/acsomega.0c03301. eCollection 2020 Oct 13.

Abstract

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) 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.

摘要

基于膜的技术,如正向渗透(FO),具有通过自发过程处理水的优势,该过程所需的能量输入极少,同时能实现良好的水渗透性和选择性。然而,FO过程仍存在一些挑战,需要解决或改进才能完全可行。该技术的主要障碍是回收用于在过程中产生渗透势的汲取溶质。在本文中,我们讨论了使用可切换极性溶剂1-环己基哌啶(CHP)作为对外部刺激有响应的汲取溶质。具体而言,CHP的混溶性可通过二氧化碳(CO₂)的存在进行切换,并且通过加热可逆转。因此,在本研究中,首先将疏水性的CHP转化为亲水性铵盐(CHPH),并针对典型的渗透剂氯化钠(NaCl)对其作为汲取溶液(DS)的能力进行了全面评估。我们的结果表明,当使用CHPH作为DS时,通过复合薄膜的水渗透率提高了69%。此外,还评估了使用不同进料溶液时的水渗透率:(a)尿素水溶液和(b)NaCl水溶液。在这两种情况下,CHPH分别产生65±4 LMH和69±2 LMH范围内的水通量。然后通过将溶液加热至75°C来分离稀释后的DS,以回收纯CHP和水。这项工作的结果为通过FO过程的CHP废水和脱盐方法提供了概念验证。

https://cdn.ncbi.nlm.nih.gov/pmc/blobs/2186/7558060/c5586bf1aee1/ao0c03301_0007.jpg

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