Haddad Andrew Z, Menon Akanksha K, Revanur Ravindra, Klare Jennifer, Urban Jeffrey J, Kostecki Robert
Energy Storage & Distributed Resources Division, Lawrence Berkeley National Laboratory, Berkeley, California 94720, United States.
George W. Woodruff School of Mechanical Engineering, Georgia Institute of Technology, Atlanta, Georgia 30332, United States.
Ind Eng Chem Res. 2025 Apr 2;64(15):7810-7817. doi: 10.1021/acs.iecr.4c03784. eCollection 2025 Apr 16.
Forward osmosis (FO) desalination using thermoresponsive ionic liquid (IL)-water mixtures is a promising technology for treating nontraditional water sources. However, its demonstration has primarily been at the lab-scale, with water flux and recovery values that are not representative of realistic applications. In this work, the performance of tetrabutyl-phosphonium trifluoroacetate (PTFA), as well as a new dual draw of PTFA with tetrabutyl-ammonium trifluoroacetate (NTFA) is characterized. The dual draw combines the higher osmolality of one IL with the lower critical solution temperature (LCST) of the second IL to outperform its constituents at the same total concentration of IL in water (70 wt %). Experiments were first performed in a lab-scale coupon tester to understand the effects of draw osmotic pressure and viscosity on water flux through the membrane. Bench-scale experiments were then performed in an element tester with a 1 m membrane area to evaluate the performance of IL-based FO for the desalination of produced water feed from oil and gas. Specifically, 10 kg of IL-water draw solution was used with 3 kg of real produced water feed, resulting in water recoveries of 60% with initial and final water fluxes of 14 LMH and 3 LMH, respectively. The bench-scale experimental results were used as inputs for a cost analysis, yielding a levelized cost of water (LCOW) of $1.18 per m. This reveals the potential of IL-based draw solutions for cost-effective desalination of challenging feedwaters using FO.
使用热响应性离子液体(IL)-水混合物的正向渗透(FO)脱盐技术是一种处理非传统水源的很有前景的技术。然而,其验证主要在实验室规模进行,水通量和回收率的值并不代表实际应用情况。在这项工作中,对四丁基鏻三氟乙酸盐(PTFA)以及PTFA与四丁基铵三氟乙酸盐(NTFA)的新型双汲取剂的性能进行了表征。双汲取剂将一种离子液体的较高渗透压与第二种离子液体的较低临界溶液温度(LCST)相结合,在水中离子液体总浓度相同(70 wt%)的情况下,其性能优于其成分。首先在实验室规模的试片测试仪中进行实验,以了解汲取渗透压和粘度对通过膜的水通量的影响。然后在具有1平方米膜面积的元件测试仪中进行中试规模实验,以评估基于离子液体的正向渗透技术对油气生产水进料进行脱盐的性能。具体而言,使用10千克离子液体-水汲取溶液和3千克实际生产水进料,水回收率为60%,初始和最终水通量分别为14 LMH和3 LMH。中试规模的实验结果用作成本分析的输入,得出的平准化水成本(LCOW)为每立方米1.18美元。这揭示了基于离子液体的汲取溶液在使用正向渗透技术对具有挑战性的进水进行经济高效脱盐方面的潜力。