pH对海藻酸钠膜污染的影响及热力学分析 |
作者:姚凌翔, 滕佳恒, 林红军 |
单位: 浙江师范大学 地理与环境科学学院 |
关键词: 超滤; 膜污染; 海藻酸钠; pH; 热力学分析 |
DOI号: 10.16159/j.cnki.issn1007-8924.2025.01.004 |
分类号: TU991.24; X703 |
出版年,卷(期):页码: 2025,45(1):30-39 |
摘要: |
滤膜技术以其操作简便和高效的分离能力,被认为是缓解全球水资源短缺问题的重要手段.然而,膜污染问题,尤其是由天然有机物(NOM)引起的膜污染,严重限制了该技术的广泛应用.为此,本研究选用海藻酸钠作为模型污染物,模拟了不同pH条件下的膜污染现象.死端过滤结果显示,当pH=3时,海藻酸钠的结垢现象最为严重,显著高于其他pH条件下的;随着pH升至7,膜污染显著减轻,比过滤阻力(SFR)下降了约77%.通过Zeta电位分析和接触角测定等方法表征了污染物的表面性质,并结合XDLVO理论进行界面热力学建模以深入探讨其潜在机制.结果发现,在不同pH环境下,污染物间的静电斥力以及污染物与膜之间的界面自由能变化是影响膜污染行为的关键.这些发现为深入理解膜污染问题提供了重要的理论支持,有望为膜污染控制策略的制定提供新的视角与思路. |
?Ultrafiltration (UF) membranes are widely recognized for their ease of operation and efficient separation capabilities, positioning them as a crucial tool in addressing global water scarcity. However, membrane fouling, particularly that caused by natural organic matter (NOM), has significantly hampered the widespread application of this technology. For this purpose, in this study, sodium alginate was taken as the model pollutant to simulate the membrane fouling phenomenon under different pH conditions. The dead-end filtration results indicated that the sodium alginate solution had severe scaling at pH=3, which was significantly higher than that under other pH conditions. As the pH rose to 7, the membrane fouling was significantly mitigated, and the specific filtration resistance (SFR) decreased by approximately 77%. The surface properties of the foulants were characterized using Zeta potential analysis and contact angle measurement, and interfacial thermodynamic modeling was conducted with the extended Derjaguin-Landau-Verwey-Overbeek (XDLVO) theory to investigate the underlying mechanisms thoroughly. Results indicated that under different pH environments, electrostatic repulsion between foulants and changes in interfacial free energy between the foulants and the membrane were critical factors influencing fouling behavior. These findings provide important theoretical support for understanding membrane fouling phenomena and offer new perspectives and strategies for developing effective fouling control measures. |
基金项目: |
浙江省自然科学基金项目(LQ24E080017) |
作者简介: |
姚凌翔(1997-),男,浙江台州人,硕士生,从事膜污染机理、污水处理及资源化研究等. |
参考文献: |
[1]Lu Z, Wei Y, Deng J, et al. Self-crosslinked MXene (Ti3C2Tx) membranes with good antiswelling property for monovalent metal ion exclusion[J]. ACS Nano, 2019, 13(9): 10535-10544. [2]Huang Z, Shen L, Lin H, et al. Fabrication of fibrous MXene nanoribbons (MNRs) membrane with efficient performance for oil-water separation[J]. J Membr Sci, 2022, 661: 120949. [3]Meng B, Liu G, Mao Y, et al. Fabrication of surface-charged MXene membrane and its application for water desalination[J]. J Membr Sci, 2021, 623: 119076. [4]Lin H, Gao W, Meng F, et al. Membrane bioreactors for industrial wastewater treatment: A critical review [J]. Crit Rev Env Sci Techol, 2012, 42(7): 677-740. [5]Chen J, Shen L, Zhang M, et al. Thermodynamic analysis of effects of contact angle on interfacial interactions and its implications for membrane fouling control[J]. Bioresource Technol, 2016, 201: 245-252. [6]Zhang M, Lin H, Shen L, et al. Effect of calcium ions on fouling properties of alginate solution and its mechanisms[J]. J Membr Sci, 2017, 525: 320-329. [7]Zhou Z, Meng F, Lu H, et al. Simultaneous alkali supplementation and fouling mitigation in membrane bioreactors by on-line NaOH backwashing [J]. J Membr Sci, 2014, 457: 120-127. [8]Zou H, Huang J, Zhang M, et al. Mitigation of protein fouling by magnesium ions and the related mechanisms in ultrafiltration process [J]. Chemosphere, 2023, 310: 136817. [9]Yao M, Ladewig B, Zhang K. Identification of the change of soluble microbial products on membrane fouling in membrane bioreactor (MBR)[J]. Desalination, 2011, 278(1): 126-131. [10]Kimura K, Kakuda T, Iwasaki H. Membrane fouling caused by lipopolysaccharides: A suggestion for alternative model polysaccharides for MBR fouling research[J]. Sep Purif Technol, 2019, 223: 224-233. [11]Kimura K, Naruse T, Watanabe Y. Changes in characteristics of soluble microbial products in membrane bioreactors associated with different solid retention times: Relation to membrane fouling[J]. Water Res, 2009, 43(4): 1033-1039. [12]Meng X, Luosang D, Meng S, et al. The structural and functional properties of polysaccharide foulants in membrane fouling[J]. Chemosphere, 2021, 268: 129364. [13]Jiang J K, Mu Y, Yu H Q. Differences in the colloid properties of sodium alginate and polysaccharides in extracellular polymeric substances with regard to membrane fouling[J]. J Colloid Interface Sci, 2019, 535: 318-324. [14]Zeng B, Pan Z, Shen L, et al. Effects of polysaccharides' molecular structure on membrane fouling and the related mechanisms[J]. Sci Total Environ, 2022, 836: 155579. [15]Yu W, Liu T, Crawshaw J, et al. Ultrafiltration and nanofiltration membrane fouling by natural organic matter: Mechanisms and mitigation by pre-ozonation and pH[J]. Water Res, 2018, 139: 353-362. [16]Jones K L, O'melia C R. Protein and humic acid adsorption onto hydrophilic membrane surfaces: Effects of pH and ionic strength [J]. J Membr Sci, 2000, 165(1): 31-46. [17]Day G M, Hart B T, Mckelvie I D, et al. Adsorption of natural organic matter onto goethite[J]. Colloid Surf A, 1994, 89(1): 1-13. [18]Lee J, Jeong S, Ye Y, et al. Protein fouling in carbon nanotubes enhanced ultrafiltration membrane: Fouling mechanism as a function of pH and ionic strength[J]. Sep Purif Technol, 2017, 176: 323-334. [19]Ribau T M, Rosa M J. pH adjustment for seasonal control of UF fouling by natural waters[J]. Desalination, 2003, 151(2): 165-175. [20]Katsoufidou K, Yiantsios S G, Karabelas A J. Experimental study of ultrafiltration membrane fouling by sodium alginate and flux recovery by backwashing [J]. J Membr Sci, 2007, 300(1/2): 137-146. [21]Lee S, Elimelech M. Relating organic fouling of reverse osmosis membranes to intermolecular adhesion forces[J]. Environ Sci Technol, 2006, 40(3): 980-987. [22]Van D B P, Zwijnenburg A, Smith G, et al. Effect of free calcium concentration and ionic strength on alginate fouling in crossflow membrane filtration[J]. J Membr Sci, 2009, 345(1/2): 207-216. [23]Meng F, Zhang S, Oh Y, et al. Fouling in membrane bioreactors: An updated review[J]. Water Res, 2017, 114: 151-180. [24]Motsa M M, Mamba B B, D’haese A, et al. Organic fouling in forward osmosis membranes: the role of feed solution chemistry and membrane structural properties [J]. J Membr Sci, 2014, 460: 99-109. [25]Zhang M, Hong H, Lin H, et al. Mechanistic insights into alginate fouling caused by calcium ions based on terahertz time-domain spectra analyses and DFT calculations[J]. Water Res, 2018, 129: 337-346. [26]Pan Z, Zeng B, Yu G, et al. Molecular insights into impacts of EDTMPA on membrane fouling caused by transparent exopolymer particles (TEP)[J]. Sci Total Environ, 2022, 853: 158650. [27]Wisniewski C, Grasmick A. Floc size distribution in a membrane bioreactor and consequences for membrane fouling [J]. Colloid Surf A, 1998, 138(2): 403-411. [28]Chen J, Zhang M, Li F, et al. Membrane fouling in a membrane bioreactor: High filtration resistance of gel layer and its underlying mechanism[J]. Water Res, 2016, 102: 82-89. [29]Pan Z, Zeng B, Yu G, et al. Mechanistic insights into Ca-alginate gel-associated membrane fouling affected by ethylene diamine tetraacetic acid (EDTA)[J]. Sci Total Environ, 2022, 842: 156912. [30]Long Y, Yu G, Dong L, et al. Synergistic fouling behaviors and mechanisms of calcium ions and polyaluminum chloride associated with alginate solution in coagulation-ultrafiltration (UF) process[J]. Water Res, 2021, 189: 116665. [31]You X, Teng J, Chen Y, et al. New insights into membrane fouling by alginate: Impacts of ionic strength in presence of calcium ions[J]. Chemosphere, 2020, 246: 125801. [32]Xu Y, Zhang W, Li Z, et al. Enhanced water permeability in nanofiltration membranes using 3D accordion-like MXene particles with random orientation of 2D nanochannels[J]. J Mater Chem A, 2022, 10(31): 16430-16438. [33]Zeng Y, Wang Z, Pan Z, et al. Novel thermodynamic mechanisms of co-conditioning with polymeric aluminum chloride and polyacrylamide for improved sludge dewatering: A paradigm shift in the field[J]. Environ Res, 2023, 234: 116420. [34]Pan Z, Zeng B, Lin H, et al. Fundamental thermodynamic mechanisms of membrane fouling caused by transparent exopolymer particles (TEP) in water treatment[J]. Sci Total Environ, 2022, 820: 153252. [35]Van O C J. Acid-base interfacial interactions in aqueous media[J]. Colloid Surf A, 1993, 78: 1-49. [36]Brant J A, Childress A E. Colloidal adhesion to hydrophilic membrane surfaces[J]. J Membr Sci, 2004, 241(2): 235-248. [37]Adam N K. Use of the term ‘Young’s equation’ for contact angles[J]. Nature, 1957, 180: 809. [38]Meinders J M, Van D M H C, Busscher H J. Deposition efficiency and reversibility of bacterial adhesion under flow [J]. J Colloid Interface Sci, 1995, 176(2): 329-341. [39]Dong Y, Dong W, Cao Y, et al. Preparation and catalytic activity of Fe alginate gel beads for oxidative degradation of azo dyes under visible light irradiation[J]. Catal Today, 2011, 175(1): 346-355. [40]Hong T, Yin J Y, Nie S P, et al. Applications of infrared spectroscopy in polysaccharide structural analysis: Progress, challenge and perspective[J]. Food Chem X, 2021, 12: 100168. [41]Sankalia M G, Mashru R C, Sankalia J M, et al. Reversed chitosan-alginate polyelectrolyte complex for stability improvement of alpha-amylase: optimization and physicochemical characterization[J]. Eur J Pharm Biopharm, 2007, 65(2): 215-232. [42]Yang B, Cheng X, Zhang Y, et al. Probing the roles of pH and ionic strength on electrostatic binding of tetracycline by dissolved organic matters: reevaluation of modified fitting model[J]. Environ Sci Ecotechnol, 2021, 8: 100133. [43]Zou H, Chen S, Zhang M, et al. Molecular-level insights into the mitigation of magnesium-natural organic matter induced ultrafiltration membrane fouling by high-dose calcium based on DFT calculation[J]. Chemosphere, 2022, 309: 136734. [44]Wang Z, Wan Y, Xie P, et al. Ultraviolet/persulfate (UV/PS) pretreatment of typical natural organic matter (NOM): Variation of characteristics and control of membrane fouling[J]. Chemosphere, 2019, 214: 136-147. [45]Li C W, Chen Y S. Fouling of UF membrane by humic substance: Effects of molecular weight and powder-activated carbon (PAC) pre-treatment[J]. Desalination, 2004, 170(1): 59-67. [46]Wu M, Zhang M, Shen L, et al. High propensity of membrane fouling and the underlying mechanisms in a membrane bioreactor during occurrence of sludge bulking[J]. Water Res, 2023, 229: 119456. [47]Manciu M, Ruckenstein E. Role of the hydration force in the stability of colloids at high ionic strengths[J]. Langmuir, 2001, 17(22): 7061-7070. |
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