高浓度含盐蔗糖溶液的纳滤分离实验研究
作者:唐元晖1,王迪1,杨忠霖1,燕志琴2,于漪1
单位: 1)中国矿业大学(北京)化学与环境工程学院,北京,100083 2)中国科协学会服务中心,100081
关键词: 蔗糖; 一二价盐; 分离; 纳滤; 废水处理
出版年,卷(期):页码: 2018,38(4):86-92

摘要:
 为探讨运用纳滤(NF)过程实现高浓度二糖和1、2价无机盐分离的可能性,本文选用商业纳滤膜NF270对高浓度蔗糖与1、2价盐离子的单组分和混合组分溶液开展了分离实验研究。首先,本文研究了物料浓度、操作压力等因素对高浓度蔗糖与盐的单组分体系分离效果的影响,明确了NF270膜对不同的单组分溶液的透过和截留性能;其次探究了NF270纳滤膜对高浓度蔗糖/NaCl和蔗糖/Na2SO4混合体系的分离效果。实验结果说明操作压力的降低和盐浓度的升高均能显著降低混合溶液的溶剂透过通量,且高浓度盐离子的存在会影响蔗糖截留率,而蔗糖对无机盐截留率影响不明显。在高操作压力下,NF270膜可实现对高浓度蔗糖/NaCl混合体系的高效分离。
 In order to explore the possibility of using nanofiltration (NF) membrane to separate the high concentrated sugar and chloride, in this paper, a commercial NF membrane (named as NF270) was employed in the permeation of the high concentrated sucrose and the single or the binary salt solutions of NaCl and Na2SO4. Firstly, the influences of the parameters including the operating pressure and the solute concentration on the separation performance were investigated to determine basic permeation and the rejection performance of the NF270 membrane for the single solution. Then for high concentratedsucrose and salt solutions, the results have shown that the flux increased with the increase of operating pressure and decrease of salt concentration. In addition, an increase in the salt concentration generally decreased the rejection to the sucrose,while the sucrose has a slight effecton the rejection to the salts.On a higher operating pressure,an efficient selective separation of chloride and the sucrose could be achieved by a NF270 membrane.
[作者简介]唐元晖,1986年出生,女,甘肃省兰州市人,博士后,从事相转化法膜制备的研究工作;Email: tangyuanhui@126.com

参考文献:
 [1]ShannonM, Bohn P, ElimelechM, et al. Science and technology for water purification in the coming decades[J]. Nature, 2008, 452:301–310.
[2]Pérez-GonzálezA,IbáñezR, GómezP, et al. Nanofiltration separation of ?polyvalent and monovalent anions in desalination brines[J].J Membr Sci,2015, 473:437-447.
[3]MurthyZ, ChaudhariL. Rejection behavior of nickel ions from synthetic wastewater containing Na2SO4, NiSO4, MgCl2 and CaCl2 salts by nanofiltration and characterization of the membrane[J].Desalination, 2009, 247:610-622.
[4]WangXL, ZhangCH, OuyangPK. The possibility of separating saccharides from a NaCl solution by ?using nanofiltration in diafiltration mode[J].J Membr Sci, 2002, 204:271–281.
[5]MikulášekaP, CuhorkaJ. Desalination and concentration of liquid dyes by nanofiltration[J].Desalin WaterTrea, 2015, 55:2711–2720. ?
[6]TuCH, FangYY, Zhu J, et al. Free energies of the ion equilibrium partition of KCl into nanofiltration membranes based on applied electrical potential and rejection[J]. Langmuir 2011, 27:10274-10281.
[7]Fang Y, Bian L, Bi Q, et al. Evaluation of the pore size distribution of a forward osmosis membrane in three different ways[J]. J Membr Sci, 2014, 454:390-397.
[8]Wang DX, SuM, YuZY, et al. Separation performance of a nanofiltration membrane influenced by species and concentration of ions[J]. Desalination, 2005, 175:219-225.
[9]王晓琳,张澄洪,欧阳平凯.应用纳滤膜分离糖和盐的实验研究[J].膜科学与技术,2001(1):44-47.
[10]KriegHM, ModiseSJ, KeizerK, et al. Salt rejection in nanofiltration for single and binary salt mixtures in view of sulphate removal[J]. Desalination, 2004, 171: 205-215.
[11]TanninenJ, MänttäriM, Nyström M. Effect of salt mixture concentration on fractionation with NF ?membranes[J].J Membr Sci, 2006, 283:57-64.
[12]付升,于养信,高光华,等.纳滤膜对电解质溶液分离特性的理论研究(I):单一电解质溶液[J]. 化学学报, 2006, 64(22):2241-2246.
[13]陈华新,董声雄.纳滤技术在食品及制药工业中的应用(下)[J].上海化工,2001, (10):23-25.
[14]宫慧慧,高群玉,陈慧音.纳滤膜技术在食品和发酵中的应用[J].食品工业科技, 2002, (10):87-89.
[15]SasakiK, TsugeY, KawaguchiH, et al. Sucrose purification and repeated ethanol production from sugars remaining in sweet sorghum juice subjected to a membrane separation process[J]. Appl Microbiol Biotechnol, 2017, 101:6007-6014.
[16]冯文亮,王静,贾晓江.纳滤技术生产高纯度低聚果糖的研究[J].乳液科学与技术,2003,3(3):102-105.
[17]MandaleS, JonesM. Interaction of electrolytes and non-electrolytes in nanofiltration[J]. Desalination, 2008, 219: 262-271.
[18]MohammadaAW, BashaRK, LeoCP. Nanofiltration of glucose solution containing salts: Effects of membrane characteristics, organic component and salts on retention[J]. J Food Eng, 2010, 97:510–518.
[19]王晓琳,张澄洪,赵杰.纳滤膜的分离机理及其在食品和医药行业中的应用[J].膜科学与技术,2000, 20(1):29-33.
[20]罗利华,杨刚,刑卫红,等.中性有机混合物溶液纳滤过程的实验考察[J].膜科学与技术,2004, 24(04): 21-26.
[21]韩永萍,林强,何续文.纳滤对糖溶液中一价盐离子的脱出研究[J].食品科技,2008, (4):95-99.
[22]顾春雷.含糖水溶液的纳滤过程研究[D]. 南京:南京工业大学,2005.
[23]Luo JQ, Wan YH, Effect of highly concentrated salt on retention of organic solutes by nanofiltration polymeric membranes[J].J Membr Sci, 2011, 372: 145-153.
[24]Wang D, Su M, Yu Z, et al. Separation performance of a nanofiltration membrane influenced by species and concentration of ions[J]. Desalination, 2005, 175:219-225.

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