Position:Home >> Abstract

The synthesis of disc-shaped potassium ion sieve membrane and its separation performance in the electric drive process
Authors: QI Shanshan2,3, YUAN Junsheng1,3*, ZHANG Chengkai1,3
Units: 1.School of Marine Science and Engineering, Hebei University of Technology, Tianjin 300130; 2. School of Chemical Engineering, Hebei University of Technology, Tianjin 300130; 3. Engineering Research Center of Seawater Utilization of Ministry of Education; Tianjin 300130
KeyWords: Disc-shaped potassium ion sieve membrane; Separation performance in the electric drive process; Extraction of potassium from concentrated seawater
ClassificationCode:TQ028.8
year,volume(issue):pagination: 2017,37(1):27-35

Abstract:
 α-Al2O3 supported potassium ionic sieve membrane was synthesized by the secondary hydrothermal growth method with the synthetic liquid ratio of n(Si):n(Al):n(template):n(KOH): n(H2O)= 36.8:8:1:24.8:771 under 200℃. Further studies on the synthetic time, template agent and number of synthesis of the influence on the potassium ion sieve membrane crystal growth were carried. Then it was characterized by XRD, SEM, EDS and gas permeation. It turns out that the potassium ion sieve membrane about 30μm thickness was synthesized successfully. The permeability of H2 is 20.6×10-6mol·m-2·s-1·Pa-1 while N2 8.1×10-6mol·m-2·s-1·Pa-1. And the separation factor of H2/N2 is 2.54.The permeation flux of K+ , Na+ , Ca2+ and Mg2+ are 852.61mmol/(m2·h), 112.38mmol/(m2·h), 12.44mmol/(m2·h), 5.26mmol/(m2·h) respectively in the electric drive experiments. The separation factors of K+/Na+, K+/Mg2+ and K+/Ca2+ are equal 7.25, 69.85, 166.06. Ion flux are increased with the increase of concentration, voltage and temperature. Ion selective are decreased with the increase of concentration and temperature but increased with voltage. The results show that the disc-shaped ion sieve membrane for the separation of potassium ion has a good performance under the effect of DC field.

Funds:
国家科技支撑计划项目(2015BAB09B00);长江学者和创新团队发展计划(IRT14R14)

AuthorIntro:
作者简介:齐珊珊(1991-),女,河南省滑县,硕士,河北工业大学,研究方向:海洋化学资源利用与环境保护,E-mail:13652108680@163.com 通讯作者:袁俊生(1961-),男,博士,教授,研究方向:海水资源综合利用,E-mail:jsyuan2012@126.com

Reference:
 [1] 马鸿文,苏双青,刘浩,等.中国钾资源与钾盐工业可持续发展[J].地学前缘,2010,17(1):294-310.
[2] 杨卉芃,曹菲.世界钾资源研究系列之一——资源概况及供需分析[J].矿产保护与利用,2015,(1):75-78.
[3] 袁俊生,韩惠如.海水提钾技术研究进展[J].河北工业大学学报,2004,33(2):140-147.
[4] Zhao Lin, Chen Yuanxin, Wang Bo, et al. Multilayer polymer/zeolite Y composite membrane structure for CO2 capture from ?ue gas[J]. Journal of Membrane Science, 2016, 498:1-13.
[5] Zhou Liang, Yang Jianhua, Li Gang, et al. Highly H2 permeable SAPO-34 membranes by steam-assisted conversion seeding [J]. International journal of hydrogen energy, 2014, 39:14949-14954.
[6] Chisholm Nicholas O., Anderson Grace C., McNally Jordan F., et al. Increasing H2/N2 separation selectivity in CHA zeolite membranes by adding a third gas [J]. Journal of Membrane Science, 2015, 496:118-124.
[7] Maghsoudi Hafez, Soltanieh Mohammad. Simultaneous separation of H2S and CO2 fromCH4 by a high silica CHA-type zeolite membrane [J]. Journal of Membrane Science, 2014, 470:159-165.
[8] Chai Lijun, Li Huazheng, Zheng Xiaoqin, et al. Pervaporation separation of ethanol–water mixtures through B-ZSM-11 zeolite membranes on macroporous supports [J]. Journal of Membrane Science, 2015, 491:168-175.
[9] Shu X, Wang X, Kong Q, et al. N Xu.High-flux MFI zeolite membrane supported on YSZ hollow fiber for separation of ethanol/water [J]. Industrial and Engineering Chemistry Research,2012,51:12073-12080
[10] Chen Zan, Yin Dehong, Wang Jinqu, et al. Functional defect-patching of a zeolite membrane for the dehydration of acetic acid by pervaporation[J].Journal of Membrane Science, 2011,369 :506-513.
[11] Zhu Bo, Myat Darli T., Shin Jin-Wook, et al. Application of robust MFI-type zeolite membrane for desalination of saline wastewater [J]. Journal of Membrane Science, 2015, 475:167-174.
[12] 柳学芳.ZSM-5分子筛膜制备方法的研究进展[J].石油化工应用,2014,33(12)13-16.
[13] 苑昊,厉刚.FeCrAl丝网负载FAU沸石膜的制备及其催化性能[J].燃料化学学报, 2012,40:558-563.
[14] 王东超,王晓东,黄伟. FAU型沸石膜的研究进展[J].化工新型材料,2014,42(6) 32-34.
[15] 梅金凤,周志辉,刘红,等. NaA 沸石膜的制备及在一氯甲烷脱水中的应用[J].硅酸盐学报,2012,40(9)1363-1368.
[16] 游在鑫,李邦民,王金渠. NaY沸石膜的合成及用于渗透汽化分离苯-环己烷[J].石油化工,2007,36(8)804-807.
[17] 王季平,刘丽娟,邵国林,等.二次生长法FAU型沸石膜的合成与表征[J].膜科学与技术,2007,27(6)9-12.
[18] 周亮,杨建华,王金渠,等.蒸汽相转化涂晶法SAPO-34分子筛膜的制备及表征[J].无机材料学报,2015,30(3)294-298.
[19] 金鸽,周志辉,刘红,等.无模板剂ZSM-5沸石膜在乙酸乙酯渗透汽化脱水中的应用[J].石油学报(石油加工),2015,31(1)31-37.
[20] Kazemimoghadam Mansoor, Mohammadi Toraj. Synthesis of MFI zeolite membranes for water desalination [J].Desalination, 2007, 206: 547-553.
[21] Li L.X., Dong J.H., Tina M. Desalination by reverse osmosis using MFI zeolite membrane [J]. Journal of Membrane Science, 2004, 243:401-404.
[22] Yuan Junsheng, Zhao Yingying, Li Qinghui. Preparation of potassium ionic sieve membrane and its application on extracting potash from seawater [J]. Separation and Purification Technology, 2012, 99:55-60.
[23] 卢亚哲.钾离子高效吸附剂的合成研究[D]:[学位论文].天津:河北工业大学,2005.45-48.
[24] 袁俊生,郭兆寿,张林栋.新型钾分子筛的表征及其对K+的交换性能[J].过程工程学报,2006,6(6):903-906.
[25] 张帆.钾离子筛膜的合成及其性能测定[D]:[学位论文].天津:河北工业大学,2008.35-45.
[26] 袁俊生,刘崇国.钾离子筛膜的合成[J].膜科学与技术,2010,30(3):27-29.
[27] Nikolay Kosinov, Jorge Gascon, Freek Kapteijn, et al.Recent developments in zeolite membranes for gas separation[J].Journal of Membrane Science, 2016,499:65-79.
[28] 孙炜,陈中,黄素逸.浓度对NaCl水溶液的分子动力学模拟[J].武汉理工大学学报,2005,27(7):26-29.
[29] 袁俊生,包捷.钾、钠、氯离子水化现象的分子动力学模拟[J].计算机与应用化学,2009,26(10):1295-1299.
[30] 李非.钙、镁、氯离子水化现象的研究[D]:[学位论文].天津:河北工业大学,2011.45-49.
[31] 谢德华,施周,陈世洋,等.基于唐南渗析原理阳离子交换膜对Cu2+、Mn2+、Zn2+去除能力的研究[J].环境科学,2010,31(9):2100-2104.
[32] 张铨昌,杨华蕊,韩成.天然沸石离子交换性能及其应用[M].北京:科学出版社,1986.27.
[33] Yamaguchi T.,Ohzono H.,Yamagami M., et al.Ion hydration in aqueous solutions of lithium chloride, nickel chloride, and caesium chloride in ambient to supercritical water. Journal of Molecular Liquids, 2010, 153:2-8.
[34] 袁俊生,杨永春.钠型斜发沸石在K+-Na+-NH4+和K+-Na+-Ca2+水溶液体系中的离子交换平衡[J].离子交换与吸附,2008,24(6): 496-503.
 

Service:
Download】【Collect

《膜科学与技术》编辑部 Address: Bluestar building, 19 east beisanhuan road, chaoyang district, Beijing; 100029 Postal code; Telephone:010-80492417/010-80485372; Fax:010-80485372 ; Email:mkxyjs@163.com

京公网安备11011302000819号