使用CIMS离子交换膜分离Li+和[Bmim]+
作者:薛静怡, 汪润慈, 孟响, 袁中伟, 郑卫芳
单位: 中国原子能科学研究院 放射化学研究所, 北京 102413
关键词: Li+离子; 1-丁基-3-甲基咪唑阳离子; 电渗析; 分离
DOI号: 10.16159/j.cnki.issn1007-8924.2025.02.006
分类号: TQ028
出版年,卷(期):页码: 2025,45(2):48-55

摘要:
吸收式热泵是一种能有效节能的制冷技术,而工质对是该技术发展的瓶颈之一。三元工质对如LiBr-[Bmim]Cl-H2O具有性能优势,使用CIMS离子交换膜可以有效且环保地分离Li+和[Bmim]+。为了研究CIMS膜的分离机理,本文通过Ferry-Faxen方程测量了CIMS膜的膜孔径,通过电渗析实验测量了两种离子在CIMS膜中的分配系数和扩散系数,以及CIMS膜在不同电流密度下的分离系数,并利用能斯特-普朗克方程讨论了这两种离子的电渗析分离过程。实验结果表明,[Bmim]+水合离子的空间尺寸接近或大于膜孔径,[Bmim]+离子与CIMS膜表面的磺酸基团有较强的相互作用。上述两个原因使得CIMS膜可以有效分离这两种离子。
 
Absorption heat pump is a refrigeration technology that can effectively save energy, and the working pair is one of the bottlenecks in the development of this technology. The ternary working pairs such as LiBr-[Bmim]Cl-H2O has some performance advantages, and the electrodialysis using CIMS membrane can separate Li+ and [Bmim]+ efficiently and environmentally friendly. In order to study the separating mechanism of CIMS membrane, this paper reported the membrane pore size of CIMS membrane by Ferry-Faxen equation, the selectivity and the diffusion coefficient of the two ions in CIMS membrane, and the permselectivity of CIMS membrane at different current densities through electrodialysis experiments and discussed the process of electrodialysis separation of the two ions using Nernst-Planck equation. The experimental results indicated that the spatial size of [Bmim]+ hydrated ion was close to or larger than the membrane pore size, and [Bmim]+ ion had a strong interaction with the sulfonic acid groups on the surface of the CIMS membrane. The two reasons above led to the effective separation of two ions by CIMS membrane. 
 

基金项目:

作者简介:
薛静怡(1995-),女,甘肃灵台人,博士研究生,研究方向为核燃料循环与材料

参考文献:
[1]Zheng D, Dong L, Huang W, et al. A review of imidazolium ionic liquids research and development towards working pair of absorption cycle[J]. Renew Sust Energ Rev, 2014, 37: 47-68.
[2]Li Z, Ye X, Liu J. Performance analysis of solar air cooled double effect LiBr/H2O absorption cooling system in subtropical city[J]. Energy Convers Manage, 2014, 85: 302-312.
[3]Wu W, Wang B, You J, et al. Compression-assisted absorption cycles using ammonia and various ionic liquids for cleaner heating[J]. J Cleaner Prod, 2018, 195: 890-907.
[4]Wang Y, Li N, Luo C. Thermodynamic performance of absorption-compression hybrid refrigeration cycles based on lithium nitrate + 1-butyl-3-methylimidazolium nitrate/water working fluid[J]. Int J Energy Res, 2020, 44: 10394-10413.
[5]Kim L, Shin B, Lee H, et al. Refractive index and heat capacity of 1-butyl-3-methylimidazolium bromide and 1-butyl-3-methylimidazolium tetrafluoroborate, and vapor pressure of binary systems for 1-butyl-3-methylimidazolium bromide + trifluoroethanol and 1-butyl-3-methylimidazolium tetrafluoroborate + trifluoroethanol[J]. Fluid Phase Equilib, 2004, 218(2): 215-220.
[6]Shiflett M B, Yokozeki A. Absorption cycle utilizing ionic liquid as working fluid[P]. US20060197053A1. 2006-9-7.
[7]Zhang X, Hu D. Performance simulation of the absorption chiller using water and ionic liquid 1-ethyl-3-methylimidazolium dimethylphosphate as the working pair[J]. Appl Therm Eng, 2011, 31(16): 3316-3321.
[8]Luo C, Li Y, Li N, et al. Thermodynamic properties and evaluation of the lithium nitrate-imidazole IL-water ternary systems as new working fluids for a double-effect AHP cycle[J]. Int J Refrig, 2018, 90: 58-72.
[9]Li Y, Li N, Luo C, et al. Thermodynamic performance of a double-effect absorption refrigeration cycle based on a ternary working pair: Lithium bromide + ionic liquids + water[J]. Energies (Basel, Switz), 2019, 12: 4200.
[10]Zhang C, Shao Y, Zhu L, et al. Acute toxicity, biochemical toxicity and genotoxicity caused by 1-butyl-3-methylimidazolium chloride and 1-butyl-3-methylimidazolium tetrafluoroborate in zebrafish (Danio rerio) livers[J]. Environ Toxicol Pharmacol, 2017, 51: 131-137.
[11]Alisawi W A, Rahbarirad S, Walker K A, et al. Identification of metabolites produced during the complete biodegradation of 1-butyl-3-methylimidazolium chloride by an enriched activated sludge microbial community[J]. Chemosphere, 2017, 167: 53-61.
[12]Li W, Wang J, Nie Y, et al. Separation of soluble saccharides from the aqueous solution containing ionic liquids by electrodialysis[J]. Sep Purif Technol, 2020, 251: 117402.
[13]Meng H, Xiao L, Li L, et al. Concentration of ionic liquids from aqueous ionic liquids solution using electrodialyzer[J]. Desalin Water Treat, 2011, 34: 326-329.
[14]Trinh L, Lee Y, Lee J, et al. Recovery of an ionic liquid Cl from a hydrolysate of lignocellulosic biomass using electrodialysis[J]. Sep Purif Technol, 2013, 120: 86-91.
[15]Li H, Meng H, Li C, et al. Competitive transport of ionic liquids and impurity ions during the electrodialysis process[J]. Desalination, 2009, 245: 349-356.
[16]Xue J, Meng X, Wang R, et al. Experimental study on the separation of lithium and imidazolium ions using a cation exchange membrane[J]. Separations, 2024, 11(4): 123.
[17]Mir F Q, Shukla A. Sharp rise in resistance of ion exchange membranes in low concentration NaCl solution[J]. J Taiwan Inst Chem Eng, 2017, 72: 134-141.
[18]Kawabe H, Jacobson H, Miller I F, et al. Functional properties of cation-exchange membranes as related to their structures[J]. J Colloid Interface Sci, 1966, 21(1): 79-93.
[19]Ferry J D. Statistical evaluation of sieve constants in ultrafiltration[J]. J Gen Physiol, 1936, 20: 95-104.
[20]Nakao S. Determination of pore size and pore size distribution. 3. Filtration membranes[J]. J Membr Sci, 1994, 96(1-2): 131-165.
[21]Faxén H, About T. Bohlin’s paper: On the drag on rigid spheres, moving in a viscous liquid inside cylindrical tubes[J]. Kolloid - Z, 1959, 167(2): 146.
[22]Haynes W M. CRC Handbook of Chemistry and Physics, 97th Edition[M]// Boca Raton, FL: CRC Press, 2016: 1315-1316.
[23]Sata T. Ion exchange membranes: Preparation, characterization, modification and application[M]//Cambridge UK: The Royal Society of Chemistry, 2004: 118-119.
[24]Kononenko N, Nikonenko V, Grande D, et al. Porous structure of ion exchange membranes investigated by various techniques[J]. Adv Colloid Interface Sci, 2017, 246.
[25]Yazicigil Z. Salt splitting with cation-exchange membranes[J]. Desalination, 2007, 212: 70-78.
[26]Che Q, Zhou L, Wang J. Fabrication and characterization of phosphoric acid doped imidazolium ionic liquid polymer composite membranes[J]. J Mol Liq, 2015, 206: 10-18.
[27]Martins C F, Neves L, Coelhoso I M, et al. Temperature effects on the molecular dynamics of modified Nafion membranes incorporating ionic liquids’ cations: A 1H NMRD study[J]. Fuel Cells, 2013, 13: 1166-1176.
[28]Bai L, Wang X, Nie Y, et al. Study on the recovery of ionic liquids from dilute effluent by electrodialysis method and the fouling of cation-exchange membrane[J]. Sci China: Chem, 2013, 56: 1811-1816.
[29]Bontha J R, Pintauro P N. Water orientation and ion solvation effects during multicomponent salt partitioning in a Nafion cation exchange membrane[J]. Chem Eng Sci, 1994, 49(23): 3835-3851.
[30]Endo T, Osawa K, Tatsumi M, et al. Transport properties of various ionic liquids during electrodialysis[J]. J Solution Chem, 2015, 44: 2405-2415.
[31]Hayamizu K, Chiba Y, Haishi T. Dynamic ionic radius of alkali metal ions in aqueous solution: A pulsed-field gradient NMR study[J]. RSC Adv, 2021,11: 20252-20257.
[32]Chang T, Billeck S E. Structure, molecular Interactions, and dynamics of aqueous  mixtures: A molecular dynamics study[J]. J Phys Chem B, 2021, 125: 1227-1240.
[33]Kanj A B, Verma R, Liu M, et al. Bunching and immobilization of ionic liquids in nanoporous metal-organic framework[J]. Nano Lett, 2019, 19: 2114-2120.
[34]Shekaari H, Mousavi S S. Conductometric studies of aqueous ionic liquids, 1-alkyl-3-methylimidazolium halide, solutions at T=298.15-328.15 K[J]. Fluid Phase Equilib, 2009, 286: 120-126.
[35]Rubinstein I. Theory of concentration polarization effects in electrodialysis on counter-ion selectivity of ion-exchange membranes with differing counter-ion distribution coefficients[J]. J Chem Soc, Faraday Trans, 1990, 86(10): 1857.
 

服务与反馈:
文章下载】【加入收藏

《膜科学与技术》编辑部 地址:北京市朝阳区北三环东路19号蓝星大厦 邮政编码:100029 电话:010-64426130/64433466 传真:010-80485372邮箱:mkxyjs@163.com

京公网安备11011302000819号