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Experimental assessment of stirring effects in freeze desalination of brackish and seawater 半咸淡水和海水冷冻脱盐搅拌效果的实验评价
IF 9.8 1区 工程技术 Q1 ENGINEERING, CHEMICAL Pub Date : 2025-12-13 DOI: 10.1016/j.desal.2025.119757
Muhammad I. Rashad , Taha A. Elaghoury , Youssef Mohab , Lama A. Elsdeek , A.M. Kader , Shehab Ahmed , Mohamed A. Farahat
This study investigates the effect of stirring and freezing termination conditions on the performance of a batch Freeze Desalination (FD) system operating with brackish water (15,000 ppm) and seawater (40,000 ppm). To provide a comprehensive assessment of process efficiency, a new Composite Performance Index (CPI) is introduced, which integrates Recovery Ratio (RR), Salt Rejection (SR), and Specific Energy Consumption (SEC) into a single performance metric. A vapor compression refrigeration cycle was employed, and experiments were conducted under both static conditions and with mechanical stirring at 10, 20, and 30 rpm. At 30 rpm, brackish water achieved a maximum RR of 38.6 %, SR of 90.9 %, and a CPI of 12.2, compared to 35.5 %, 79.7 %, and 9.8 under static conditions, respectively. For seawater, stirring at 30 rpm increased RR from 23.8 % to 27.9 % and reduced product salinity from 1857 ppm to 1253 ppm, while SEC dropped from 908.1 to 432.4 kWh/m3. Additionally, the freezing process was extended in some cases until the brine reached twice the feed salinity, which further improved performance. At 30 rpm, increasing the cutoff salinity from 1.5× to 2× raised RR from 38.6 % to 51.6 % and CPI from 12.2 to 21.2, while SEC decreased from 286.5 to 221.4 kWh/m3. These results demonstrate that both stirring and extended freezing can significantly enhance system performance and water quality, offering practical strategies to improve FD efficiency under varying salinity conditions.
本研究考察了搅拌和冻结终止条件对在微咸水(15,000 ppm)和海水(40,000 ppm)条件下运行的间歇式冷冻脱盐(FD)系统性能的影响。为了提供对工艺效率的综合评估,引入了一种新的综合性能指数(CPI),它将回收率(RR)、除盐率(SR)和比能耗(SEC)整合到一个单一的性能指标中。采用蒸汽压缩制冷循环,在静态条件下和10、20和30 rpm的机械搅拌下进行了实验。在30rpm时,微咸水的最大RR为38.6%,SR为90.9%,CPI为12.2,而在静态条件下分别为35.5%,79.7%和9.8。对于海水,以30 rpm搅拌可将RR从23.8%提高到27.9%,将产品盐度从1857 ppm降低到1253 ppm,而SEC从908.1 kWh/m3下降到432.4 kWh/m3。此外,在某些情况下,冷冻过程被延长,直到盐水达到饲料盐度的两倍,这进一步提高了性能。在30 rpm时,将截止矿化度从1.5×提高到2×,使RR从38.6%提高到51.6%,CPI从12.2提高到21.2,而SEC从286.5降低到221.4 kWh/m3。这些结果表明,搅拌和延长冻结都能显著提高系统性能和水质,为在不同盐度条件下提高FD效率提供了实用策略。
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引用次数: 0
Configuring 5TiO2·2H2O/C composite-type adsorbents for effectively recovering Li+ from original Salt Lake brines 配置5TiO2·2H2O/C复合吸附剂,有效回收盐湖原始盐水中的Li+
IF 9.8 1区 工程技术 Q1 ENGINEERING, CHEMICAL Pub Date : 2025-12-13 DOI: 10.1016/j.desal.2025.119758
Xuemei Zhuo , Chunxi Hai , Yanxia Sun , Shengde Dong , Luxiang Ma , Xin He , Qi Xu , Masayoshi Fuji , Takashi Shirai , Yuan Zhou
Spinel-structured titanium‑lithium adsorbents have emerged as a promising solution for efficiently recovering Li+ from Salt Lake brines with high Mg/Li ratio, owing to their stable structure, minimal dissolution loss, and excellent cycling stability. However, their practical application remains limited due to low adsorption capacity and prolonged equilibration times. In this study, we developed a novel 5TiO2·2H2O/C adsorbents, synthesized by eluting Li4Ti5O12/C precursors with 0.15 mol/L HCl, which exhibits high adsorption capacity and minimal dissolution loss. Under optimal conditions, the 5TiO2·2H2O/C adsorbents reached adsorption equilibrium within 5 h at 60 °C in a 600 ppm LiOH solution, with a maximum adsorption capacity of 41.84 mg/g and a titanium dissolution loss of only 0.29 %. The adsorption selectivity of the 5TiO2·2H2O/C adsorbents was found to be strongly pH-dependent. In a 170 ppm Li+ solution, the adsorbents demonstrated superior cycling stability in original Salt Lake brines, outperforming those in LiCl and Li2SO4 solutions. This study provides valuable insights into the formation and mechanisms of action of these adsorbents, offering significant implications for the efficient recovery of Li+ from various brines.
尖晶石结构的钛锂吸附剂由于其稳定的结构、最小的溶解损失和优异的循环稳定性,已成为从高Mg/Li比的盐湖盐水中高效回收Li+的有前途的解决方案。然而,由于吸附能力低和平衡时间长,它们的实际应用仍然受到限制。在本研究中,我们开发了一种新型的5TiO2·2H2O/C吸附剂,以0.15 mol/L的HCl洗脱Li4Ti5O12/C前驱体,具有较高的吸附容量和最小的溶解损失。在最佳条件下,5TiO2·2H2O/C吸附剂在600 ppm LiOH溶液中,在60℃条件下5 h内达到吸附平衡,最大吸附量为41.84 mg/g,钛溶解损失仅为0.29%。5TiO2·2H2O/C吸附剂的吸附选择性对ph值有很强的依赖性。在170 ppm的Li+溶液中,吸附剂在原始盐湖盐水中表现出优越的循环稳定性,优于LiCl和Li2SO4溶液。该研究为这些吸附剂的形成和作用机制提供了有价值的见解,为从各种盐水中有效回收Li+提供了重要的意义。
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引用次数: 0
Mn–MOF–74 coupled with biochar derived from chestnut shell for catalytic electrochemical oxidation in a peroxymonosulfate system to degrade metformin Mn-MOF-74与栗子壳生物炭在过氧单硫酸盐体系中催化电化学氧化降解二甲双胍
IF 9.8 1区 工程技术 Q1 ENGINEERING, CHEMICAL Pub Date : 2025-12-11 DOI: 10.1016/j.desal.2025.119746
Thi-Kim-Tuyen Nguyen , Thanh-Binh Nguyen , Chiu-Wen Chen , Wei-Hsin Chen , Thai Van Anh , Shuchen Hsieh , Cheng-Di Dong
Metformin (MET), one of the most widely prescribed antidiabetic drugs, is now frequently detected in aquatic environments, raising concerns about its ecological impact. Here, we report a robust Mn–MOF–74@CB composite prepared by anchoring Mn–MOF–74 onto chestnut shell–derived biochar to enhance structural stability and catalytic efficiency. In an electrochemically assisted peroxymonosulfate (PMS) activation system, the Mn–MOF–74@CB catalyst achieved >80 % MET removal under optimized conditions with low energy input. The material showed excellent reusability and structural integrity, with manganese leaching remaining below U.S. EPA safety limits across successive cycles. Mechanistic analyses demonstrated that degradation proceeded predominantly through non-radical pathways involving singlet oxygen (1O2), superoxide radical (O2•−), and high-valent manganese-oxo species (MnV=O), rather than classical hydroxyl (HO) or sulfate (SO4•−) radicals. Ecotoxicity assays using Chlorella sorokiniana Kh12 confirmed reduced toxicity after treatment, while 3D excitation–emission matrix (EEM) fluorescence spectroscopy indicated extensive mineralization without accumulation of harmful intermediates. These results highlight the Mn–MOF–74@CB/PMS/EO system as an energy-efficient, stable, and environmentally benign platform for advanced removal of metformin from contaminated waters.
二甲双胍(Metformin, MET)是最广泛使用的降糖药之一,现在在水生环境中经常被检测到,这引起了人们对其生态影响的关注。在这里,我们报道了一种坚固的Mn-MOF - 74@CB复合材料,通过将Mn-MOF - 74锚定在栗子壳衍生的生物炭上,以提高结构稳定性和催化效率。在电化学辅助过氧单硫酸盐(PMS)活化体系中,Mn-MOF - 74@CB催化剂在优化条件下以低能量输入实现了80%的MET去除率。该材料表现出优异的可重复使用性和结构完整性,锰浸出在连续循环中保持低于美国环保署的安全限制。机理分析表明,降解主要通过非自由基途径进行,包括单线态氧(1O2)、超氧自由基(O2•−)和高价锰氧(MnV=O),而不是经典的羟基(HO•)或硫酸盐(SO4•−)自由基。用小球藻Kh12进行的生态毒性试验证实,处理后毒性降低,而3D激发发射基质(EEM)荧光光谱显示,矿化广泛,没有有害中间体的积累。这些结果表明,Mn-MOF - 74@CB/PMS/EO系统是一种节能、稳定、环保的平台,可用于从污染水中深度去除二甲双胍。
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引用次数: 0
Diamine grafted poly (acrylonitrile-co-glycidyl methacrylate) membranes for separation permeance and fouling mitigation: Role of diamine molecular weight 二胺接枝聚丙烯腈-甲基丙烯酸缩水甘油酯膜的分离、渗透和减少污染:二胺分子量的作用
IF 9.8 1区 工程技术 Q1 ENGINEERING, CHEMICAL Pub Date : 2025-12-11 DOI: 10.1016/j.desal.2025.119745
Jian Li , Yuanqi Liu , Tianyu Tang , Yanxun Guo , Fei Liu , Zhenyu Zhao
Amine-based grafting is an easy method to increase polymeric membrane rejection and antifouling properties. However, the effect of diamine molecular weight on the membrane separation and antifouling performance remains poorly understood. Herein, in this study, poly (acrylonitrile-co-glycidyl methacrylate) (P(AN-co-GMA)) membranes were grafted using 5 linear aliphatic diamines with varying molecular weights (i.e., ethylenediamine, butanediamine, hexanediamine, octanediamine, and decanediamine) for dye removal and fouling mitigation. In addition to a comprehensive characterization of membrane physicochemical structures, long-term (72 h) filtration was performed with 4 dye solutions to probe the membrane separation characteristics. Furthermore, membrane antifouling performance was characterized via permeance recovery rate by filtrating bovine serum albumin and humic acid solutions. Our results showed that the hydrophilicity, negative surface charge, and pore size of the P(AN-co-GMA) membrane surface decreased with increasing diamine molecular weight, while the membrane surface roughness and rejection increased. Notably, the increase of diamine molecular weight did not significantly influence membrane porosities. Further increasing diamine molecular weight offered limited rejection enhancement while decreasing membrane permeance. Octanediamine-grafting significantly enhanced P(AN-co-GMA) membrane rejection (99.2 % for Congo red, 99.2 % for Methyl blue, 91.7 % for Neutral red, and 90.2 % for Methyl violet) while maintaining a relatively high pure water permeance (120 LMH/bar). Notably, the membrane with a reduced pore size showed an enhanced permeance recovery rate (>90 % in each cycle) and reduced irreversible fouling, with values of 8.51 % for bovine serum albumin and 9.35 % for humic acid, suggesting that a constricted pore structure could mitigate irreversible fouling formation inside the membrane matrix.
胺基接枝是提高聚合物膜截留性能和防污性能的一种简便方法。然而,二胺分子量对膜分离和防污性能的影响尚不清楚。本研究采用5种不同分子量的直线型脂肪族二胺(乙二胺、丁二胺、己二胺、辛二胺和癸二胺)接枝聚丙烯腈-共甲基丙烯酸缩水甘油酯(P(AN-co-GMA))膜,以去除染料和减轻污垢。除了对膜的物理化学结构进行全面表征外,还对4种染料溶液进行了长时间(72 h)过滤,以探测膜的分离特性。此外,通过过滤牛血清白蛋白和腐植酸溶液的渗透回收率来表征膜的防污性能。结果表明,P(AN-co-GMA)膜的亲水性、表面负电荷和孔径随二胺分子量的增加而减小,膜表面粗糙度和截留率增加。值得注意的是,二胺分子量的增加对膜孔隙率没有显著影响。进一步增加二胺的分子量可以有限地增强排斥反应,同时降低膜透性。辛烷二胺接枝显著提高了P(AN-co-GMA)膜的去除率(刚果红99.2%,甲基蓝99.2%,中性红91.7%,甲基紫90.2%),同时保持了较高的纯水透过率(120 LMH/bar)。值得注意的是,缩小孔径的膜具有增强的渗透回收率(每次循环90%)和减少不可逆污垢的能力,其中牛血清白蛋白和腐植酸的渗透率分别为8.51%和9.35%,这表明收缩的孔隙结构可以减轻膜基质内部不可逆污垢的形成。
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引用次数: 0
Mechanistic insights into singlet‑oxygen-driven Fenton-like system using 2D/2D MXene/ZnFe-LDH heterostructure for ciprofloxacin removal 利用2D/2D MXene/ZnFe-LDH异质结构研究单重态氧驱动类芬顿体系去除环丙沙星的机理
IF 9.8 1区 工程技术 Q1 ENGINEERING, CHEMICAL Pub Date : 2025-12-11 DOI: 10.1016/j.desal.2025.119739
Soyeon Kim , Yuri Park , Doo-Hee Lee , Dimuthu Wijethunge , Aijun Du , Yuhoon Hwang
To address the widespread occurrence of ciprofloxacin (CIP) in water, which poses serious risks to both public health and environmental safety, a novel and environmentally benign MXene with ZnFe-LDH (MX@LDH) 2D/2D heterogeneous catalyst was developed for activating peroxymonosulfate (PMS). First, we developed the MXene preparation method, including nitric acid treatment, to remove the fluorine residuals caused by the conventional hydrochloric acid and lithium fluoride method and to introduce oxygen vacancies. Subsequently, ZnFe-LDH was successfully immobilized onto the MXene surface via a co-precipitation method, enabling the formation of a 2D/2D heterostructure. MX@LDH provided more active sites for PMS activation with improved electron transfer. MX@LDH-4 (34.3 % MXene) exhibited 96.7 % CIP removal and 75.8 % TOC removal within 90 min under conditions of 40 mg/L CIP, 4 mM PMS, and pH = 6. MX@LDH maintained stable catalytic performance between pH 4 and pH 10. The singlet oxygen (1O2) and superoxide radicals (·O2) were the main reactive oxygen species, and singlet oxygen could be produced by the radical pathway, as well as mediated electron transfer. The calculated mutagenicity and bioaccumulation factor of transformation products detected by liquid chromatography-tandem mass spectrometer were lower than those of CIP, implying the effectiveness of the MX@LDH/PMS system in reducing the ecotoxicity of CIP. Owing to the high resistance to inorganic ions and humic acid, the outstanding catalytic performance toward various pharmaceuticals, even in real water, stable chemical structure, and recyclable features, the 2D/2D heterogeneous MX@LDH/PMS system could be utilized for the decomposition of organic pollutants in water.
针对环丙沙星(CIP)在水中广泛存在,对公众健康和环境安全构成严重威胁的问题,研制了一种新型环保型MXene - ZnFe-LDH (MX@LDH) 2D/2D非均相催化剂,用于活化过氧单硫酸盐(PMS)。首先,我们开发了MXene的制备方法,包括硝酸处理,以去除常规盐酸和氟化锂方法产生的氟残留,并引入氧空位。随后,通过共沉淀法将ZnFe-LDH成功固定在MXene表面,形成2D/2D异质结构。MX@LDH为PMS活化提供了更多的活性位点,并改善了电子转移。MX@LDH-4 (34.3% MXene)在40 mg/L CIP、4 mM PMS、pH = 6条件下,90 min内CIP去除率为96.7%,TOC去除率为75.8%。MX@LDH在pH 4 ~ pH 10范围内保持稳定的催化性能。单线态氧(1O2)和超氧自由基(·O2−)是主要的活性氧,单线态氧可以通过自由基途径产生,也可以通过电子转移介导。液相色谱-串联质谱检测转化产物的致突变性和生物蓄积因子均低于CIP,表明MX@LDH/PMS体系在降低CIP的生态毒性方面是有效的。2D/2D非均相MX@LDH/PMS体系对无机离子和腐植酸具有较高的抗性,对多种药物具有优异的催化性能,即使在真实水中也能催化,化学结构稳定,可循环利用,可用于水中有机污染物的分解。
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引用次数: 0
Analysis of feed fluctuations on Ocean Wave-Powered Reverse Osmosis (WPRO) desalination using transient model 利用瞬态模型分析海浪反渗透海水淡化过程中的进料波动
IF 9.8 1区 工程技术 Q1 ENGINEERING, CHEMICAL Pub Date : 2025-12-10 DOI: 10.1016/j.desal.2025.119676
Xian Wu, Xiaofan Li, Lei Zuo
Wave-Powered Reverse Osmosis (WPRO) represents a promising convergence of ocean energy harvesting and advanced Reverse Osmosis (RO) desalination techniques. The significant fluctuations in pressures and flow rates within the integrated WPRO system present a critical challenge, necessitating an accurate transient model for effective performance estimation. This study presents a two-dimensional transient model based on pressure-correction algorithm to simulate channel flow with membrane boundary conditions under varying inlet conditions. The coupled dynamics of pressure, velocity, and salt concentration are addressed iteratively by decoupling and updating each term separately. The model investigates the performance of RO systems under different input conditions, including constant, sinusoidal, and irregular flow. The results indicate that constant input with higher pressure and lower flow rate achieves a better Recovery Ratio (RR). It is emphasized that for WPRO systems, a fair comparison requires choosing the same average power or pressure when evaluating different inputs. Under equivalent input power, sinusoidal waves result in a lower RR compared to constant inputs due to reduced average pressure. Conversely, under equivalent inlet pressure and flow rate, sinusoidal waves achieve a higher RR than constant inputs due to the phase difference between pressure-driven permeate velocity and diffusion-driven Concentration Polarization (CP). Specifically, sinusoidal inputs with higher frequency and higher amplitude display a higher RR. Additionally, irregular input yields a higher RR than constant inputs, as mean pressure and power can be maintained at levels comparable to those of constant input. The model’s adaptability to diverse flow regimes — from steady to sinusoidal and irregular fluctuations — highlights its potential as a critical tool for optimizing RO desalination processes powered by renewable ocean energy.
波浪动力反渗透(WPRO)代表了海洋能量收集和先进的反渗透(RO)海水淡化技术的有前途的融合。集成WPRO系统内压力和流量的显著波动是一个严峻的挑战,需要一个准确的瞬态模型来进行有效的性能估计。本文提出了一种基于压力校正算法的二维瞬态模型,用于模拟不同进口条件下膜边界条件下的通道流动。压力、速度和盐浓度的耦合动力学通过分别解耦和更新来迭代处理。该模型研究了RO系统在不同输入条件下的性能,包括恒定流、正弦流和不规则流。结果表明,在一定的输入压力和较低的流量条件下,采收率较好。需要强调的是,对于WPRO系统,公平的比较要求在评估不同输入时选择相同的平均功率或压力。在同等输入功率下,由于平均压力降低,正弦波比恒定输入产生更低的RR。相反,在相同的进口压力和流量下,由于压力驱动的渗透速度和扩散驱动的浓度极化(CP)之间的相位差,正弦波比恒定输入具有更高的RR。具体来说,高频率和高幅度的正弦输入显示出更高的RR。此外,不规则输入比恒定输入产生更高的RR,因为平均压力和功率可以保持在与恒定输入相当的水平。该模型对各种流动状态的适应性——从稳定到正弦和不规则波动——突出了它作为优化由可再生海洋能源驱动的反渗透海水淡化过程的关键工具的潜力。
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引用次数: 0
Electrochemical cleaning in membrane distillation: Mechanisms and operation strategies 膜蒸馏中的电化学清洗:机理与操作策略
IF 9.8 1区 工程技术 Q1 ENGINEERING, CHEMICAL Pub Date : 2025-12-10 DOI: 10.1016/j.desal.2025.119696
Junghyun Kim , Seonkyu Lee , Juhyung Lee , Leonard Tijing , Ho Kyong Shon , Seungkwan Hong
Membrane distillation (MD) effectively treats highly concentrated solutions due to its unique rejection mechanism, making it suitable for applications such as zero liquid discharge. However, inorganic scaling significantly limits its practical operation under high-recovery conditions. Electrochemical cleaning (EC) utilizing electrically conductive membranes emerges as an innovative strategy, overcoming limitations associated with conventional hydraulic flushing and chemical cleaning methods. In this study, the effectiveness and mechanisms of EC using direct current (DC) and alternating current (AC) operations were systematically investigated. AC-driven electrochemical cleaning outperforms DC, as it maintains flux recovery above 95 % at 1.0 V, whereas DC drops to 87.88 %. After three cycles, the flux-decline rate is lower with AC and energy consumption is reduced. Unlike DC, whose efficiency fades as the membrane recharges and crystals nucleate, AC's electrokinetic vibration and ionic convection prevent scale adhesion and enhance flushing. Thus, EC-AC offers a robust, energy-efficient pathway to sustain high-performance MD under severe scaling conditions.
膜蒸馏(MD)由于其独特的排斥机制,可以有效地处理高浓度溶液,使其适用于零液体排放等应用。然而,无机结垢严重限制了其在高回收率条件下的实际操作。利用导电膜的电化学清洗(EC)是一种创新的方法,克服了传统液压冲洗和化学清洗方法的局限性。在这项研究中,系统地研究了使用直流(DC)和交流(AC)操作的EC的有效性和机制。交流驱动的电化学清洗优于直流,在1.0 V时,其通量回收率保持在95%以上,而直流则下降到87.88%。三次循环后,带交流的磁通衰减率较低,能耗降低。与直流电不同,直流电的效率随着膜充电和晶体成核而下降,交流电的电动振动和离子对流防止了水垢的粘附,增强了冲洗。因此,EC-AC提供了一种在严重结垢条件下维持高性能MD的稳健、节能途径。
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引用次数: 0
Seasonal variations in feed-water chemistry and fouling dynamics of reverse-osmosis systems: A global climate lens 反渗透系统给水化学和污染动力学的季节变化:全球气候透镜
IF 9.8 1区 工程技术 Q1 ENGINEERING, CHEMICAL Pub Date : 2025-12-10 DOI: 10.1016/j.desal.2025.119744
Nasser Zareei, Hazim Qiblawey
Reverse osmosis desalination plants are built for worst-case conditions, yet seasonal variations in feed water quality often outpace their design assumptions, leading to avoidable membrane performance losses. Temperature swings of 10–15 °C, along with changes in salinity, organic matter, and microbial activity, drive predictable membrane fouling dynamics that static protocols cannot accommodate. This review synthesizes RO studies published from 2015 to 2025 across hot-desert, Mediterranean, temperate, and tropical climate zones using Köppen-Geiger climate classification as an organizing framework, the first systematic climate-resolved synthesis of seasonal fouling mechanisms and adaptive responses. Through this review, three principal findings emerge. First, climate-specific seasonal fouling regimes are distinct and mechanistically predictable patterns: arid coasts (BWh) experience summer biofouling synergistically amplified by gypsum scaling; temperate systems (Cfa, Dwa) face winter organic fouling from recalcitrant humics despite reduced microbial activity; and tropical intakes (Aw, Am) endure monsoonal pulses that increase both colloidal fouling and dissolved organics by 5–100× relative to dry-season baselines. Second, static protocols impose severe performance penalties: flux decline rates can reach 70–85 %, membrane cleaning frequency doubling, and energy consumption rising despite viscosity-driven efficiency gains in warm periods, demonstrating that single-parameter optimization fails under coupled thermal-chemical-biological forcing. Third, predictive-adaptive systems demonstrate step-change improvements: predictive models enable accurate, real-time antiscalant dosing, while temperature-responsive pretreatment maintains higher permeate flux and reduces energy demand by up to nearly 20 %; quorum-sensing-inhibitor coatings reduce biofilm thickness by 60–69 %; and ceramic ultrafiltration eliminates harmful-algal-bloom capacity losses that degrade polymeric membranes by 30–40 %. Yet critical gaps persist hot-arid (BWh) and Mediterranean (Csa) zones, most monitoring datasets are short-term, and temperature-dependent fouling relationships remain unclear due to inconsistent findings. Closing these gaps requires multi-year monitoring across all climate zones and economic validation under climate variability. Seasonal adaptation must evolve from reactive adjustment to fundamental design criterion. Future installations should align membrane materials, pretreatment systems, and control algorithms with site-specific hydrological calendars.
反渗透海水淡化厂是为最坏的情况而建造的,但给水水质的季节性变化往往超过其设计假设,导致可避免的膜性能损失。10-15°C的温度波动,以及盐度、有机物和微生物活性的变化,驱动可预测的膜污染动力学,这是静态协议无法适应的。本文以Köppen-Geiger气候分类为组织框架,综合了2015年至2025年在热沙漠、地中海、温带和热带气候带发表的RO研究,首次系统地综合了气候解决的季节性污染机制和适应响应。通过这一审查,出现了三个主要发现。首先,气候特定的季节性污染机制是独特的和机械可预测的模式:干旱海岸(BWh)经历夏季生物污染,石膏结垢协同放大;温带系统(Cfa, Dwa)尽管微生物活性降低,但冬季仍面临顽固性腐殖质的有机污染;热带地区(Aw, Am)承受季风的冲击,使胶体污垢和溶解有机物比旱季基线增加5 - 100倍。其次,静态协议会带来严重的性能损失:通量下降率可能达到70 - 85%,膜清洗频率翻倍,尽管在温暖时期粘度驱动的效率有所提高,但能耗却在上升,这表明单参数优化在热-化学-生物耦合强迫下失败。第三,预测自适应系统显示出阶跃变化的改进:预测模型能够实现准确、实时的抗结垢剂剂量,而温度响应预处理保持较高的渗透通量,并将能量需求降低近20%;群体感应抑制剂涂层可使生物膜厚度减少60 - 69%;陶瓷超滤消除了有害的藻华容量损失,使聚合物膜降解30 - 40%。然而,干旱热区(BWh)和地中海区(Csa)仍然存在严重差距,大多数监测数据集是短期的,由于研究结果不一致,依赖温度的污染关系仍不清楚。要缩小这些差距,需要对所有气候带进行多年监测,并在气候变率下进行经济验证。季节适应必须从被动调整演变为基本设计准则。未来的安装应该使膜材料、预处理系统和控制算法与特定地点的水文日历相一致。
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引用次数: 0
Dual-functional electrochemical membrane reactor based on Fe-doped carbon membranes for simultaneous highly efficient tetracycline degradation and Na+ electrosorption 铁掺杂碳膜双功能电化学膜反应器同时高效降解四环素和Na+电吸附
IF 9.8 1区 工程技术 Q1 ENGINEERING, CHEMICAL Pub Date : 2025-12-09 DOI: 10.1016/j.desal.2025.119747
Yuxuan Zhu , Hanlin Wang , Haikuo Lei , Zitian Liu , Shuai Liu , Han Zhao , Heli Zhao
To simultaneously achieve tetracycline (TC) degradation and desalination, a dual-functional electrochemical membrane reactor (EMR) was developed. This reactor uses Fe-doped carbon membranes (FeM) as functional electrodes, integrating two core functions: TC degradation at the anode and Na+ electrosorption at the cathode. Among the FeM series, FeM2 (with 2 % Fe doping) exhibited outstanding performance, featuring a 34.8 nm average pore size, 44.1 % porosity, 8.5 MPa bending strength, 3942 S/m electrical conductivity, and 802.3 m2/g specific surface area. Density functional theory (DFT) simulations confirmed that FeM2 had a stronger adsorption affinity for TC (adsorption free energy: −388.3 kJ/mol). At an applied voltage of 1.2 V, the FeM2 anode achieved 94.8 % TC degradation (a process dominated by ·OH, with Cl migrating through the anion exchange membrane to maintain charge balance), while the FeM2 cathode reached an equilibrium Na+ electrosorption capacity of 57.7 mg/g. In contrast, single-electrode systems (EMR-A for anode-only TC degradation; EMR-C for cathode-only Na+ electrosorption) lacked dual-functional synergy, resulting in lower efficiency. FeM2 also showed excellent stability: negligible performance loss after 10 cycles of operation, and no iron leaching was detected during 120 h of continuous operation. This dual-functional EMR provides an efficient, low-voltage solution for the simultaneous removal of TC and Na+.
为同时实现四环素(TC)降解和脱盐,研制了一种双功能电化学膜反应器(EMR)。该反应器采用掺铁碳膜(FeM)作为功能电极,集阳极TC降解和阴极Na+电吸附两大核心功能于一体。在FeM系列中,掺2% Fe的FeM2表现优异,平均孔径为34.8 nm,孔隙率为44.1%,抗弯强度为8.5 MPa,电导率为3942 S/m,比表面积为802.3 m2/g。密度泛函理论(DFT)模拟证实,FeM2对TC具有较强的吸附亲和力(吸附自由能:−388.3 kJ/mol)。在1.2 V电压下,FeM2阳极的TC降解率为94.8%(该过程以·OH为主,Cl−通过阴离子交换膜迁移以维持电荷平衡),而FeM2阴极的平衡Na+电吸附容量为57.7 mg/g。相比之下,单电极系统(EMR-A用于纯阳极TC降解,EMR-C用于纯阴极Na+电吸附)缺乏双功能协同作用,导致效率较低。FeM2也表现出优异的稳定性:运行10个循环后性能损失可以忽略不计,连续运行120 h未检测到铁浸出。这种双功能EMR为同时去除TC和Na+提供了高效、低压的解决方案。
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引用次数: 0
Dual-functional hydrogel evaporator with CQDs loaded TiO2 and CNTs for efficient eutrophic water body purification 具有负载TiO2和CNTs的CQDs的双功能水凝胶蒸发器用于富营养化水体的高效净化
IF 9.8 1区 工程技术 Q1 ENGINEERING, CHEMICAL Pub Date : 2025-12-09 DOI: 10.1016/j.desal.2025.119752
Guiqun Liu , Qisheng Ma , Zheng Li , Jialong Zhang , Kuan Lei , Ding Li , Min Xue , Wenli Wu , Jianghua Du , Xiaoli Zhang
Solar photothermal interfaces garner widespread attention as an economical and efficient water purification technology, particularly in applications such as seawater desalination and wastewater treatment. However, their relatively limited capacity to degrade organic pollutants in real wastewater, especially in addressing eutrophic water bodies commonly encountered in daily life, hinders their broader practical deployment. Herein, we synthesize a novel bifunctional hydrogel material, PSTCC (PAM/SA/TiO2 -CQDs/CNTs), which integrates both photothermal and photocatalytic functionalities. We also design and fabricate a 3D structured hydrogel device to systematically evaluate its potential for eutrophic water purification. By incorporating carbon quantum dot - modified TiO2 and carbon nanotubes into a polyacrylamide–sodium alginate composite matrix, the hydrogel exhibits significantly enhanced photothermal conversion efficiency while effectively tuning the bandgap of TiO2, thereby improving its photocatalytic activity. Furthermore, using a 3D structured mold and demolding process, we construct a PSTCC hydrogel evaporator featuring surface convex protrusions and vertically aligned internal capillary channels, which achieves a high evaporation rate of 2.56 kg m−2 h−1 under one sun irradiation. The device also demonstrates excellent performance in the removal of organic pollutants, achieving a photocatalytic degradation efficiency of 85.5 % for methylene blue and an inactivation rate of 58.7 % for Chlorella vulgaris. This evaporator and its associated device are expected to offer a novel paradigm for treating typical organic pollutants in eutrophic water bodies, holding broad application prospects in the field of green, efficient, and energy-saving water treatment.
太阳能光热界面作为一种经济高效的水净化技术,在海水淡化和废水处理等方面的应用受到了广泛的关注。然而,它们对实际废水中有机污染物的降解能力相对有限,特别是在处理日常生活中常见的富营养化水体时,阻碍了它们更广泛的实际部署。在此,我们合成了一种新型双功能水凝胶材料PSTCC (PAM/SA/TiO2 -CQDs/CNTs),它集光热和光催化功能于一体。我们还设计和制造了一个三维结构水凝胶装置,以系统地评估其对富营养化水净化的潜力。通过将碳量子点修饰的TiO2和碳纳米管掺入聚丙烯酰胺-海藻酸钠复合基质中,水凝胶光热转换效率显著提高,同时有效调节TiO2的带隙,从而提高其光催化活性。此外,利用三维结构模具和脱模工艺,我们构建了一个表面凸突出,内部毛细管通道垂直排列的PSTCC水凝胶蒸发器,在一次太阳照射下实现了2.56 kg m−2 h−1的高蒸发速率。该装置在去除有机污染物方面也表现出优异的性能,对亚甲基蓝的光催化降解效率为85.5%,对小球藻的光催化失活率为58.7%。该蒸发器及其配套装置有望为富营养化水体中典型有机污染物的处理提供一种新的范例,在绿色、高效、节能水处理领域具有广阔的应用前景。
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引用次数: 0
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Desalination
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