搜索到1598篇“ MICROFILTRATION“的相关文章
2D phosphides heterostructures on titanium microfiltration membrane for enhanced ampere-level current density overall seawater splitting
2025年
The advancement of direct seawater electrolysis is a significant step towards sustainable hydrogen production,addressing the critical need for renewable energy sources and efficient resource utilization.However,direct seawater electrolysis has to face several challenges posed by the corrosiveness of highly concentrated chloride and the competitive chlorine evolution reaction(ClER).To overcome these issues,we designed a novel NiP_(2)@CoP electrocatalyst on a porous titanium microfiltration(Ti MF)membrane.The obtained bifunctional NiP_(2)@CoP catalyst outperforms the Pt/C and IrO_(2),as evidenced by its low overpotentials of 192 and 425 mV at a current density of 500 mA·cm^(-2) for hydrogen evolution reaction(HER)and oxygen evolution reaction(OER)in alkaline seawater(1 M KOH+0.5 M NaCl),respectively.Especially,only 231 and 569 mV overpotentials are required at the current density of 1500 mA·cm^(-2) towards HER and OER in alkaline seawater,respectively.More importantly,no ClER was observed,demonstrating its excellent selectivity to OER.The selection of porous Ti MF membrane as an electrode substrate further enhances the performance by providing a robust structure that promotes the fast generation and release of gas bubbles.Our promising outcomes obtained with NiP_(2)@CoP catalysts on Ti MF support,therefore,pave the way for the commercial viability of direct seawater electrolysis technologies at industrial-level current densities.
Wenjing DaiXin WangYulong MaSisi HeMing ChenZhaohui YinShuheng TianMaolin WangShixiang YuHang ZhangYuanzhe WangHong WangJianxin LiFaming GaoBowen ChengYun WangZhen YinDing Ma
Dewatering of Scenedesmus obliquus Cultivation Substrate with Microfiltration:Potential and Challenges for Water Reuse and Effective Harvesting
2024年
In the microalgae harvesting process,which includes a step for dewatering the algal suspension,directly reusing extracted water in situ would decrease the freshwater footprint of cultivation systems.Among various algae harvesting techniques,membrane-based filtration has shown numerous advantages.This study evaluated the reuse of permeate streams derived from Scenedesmus obliquus(S.obliquus)biomass filtration under bench-scale and pilot-scale conditions.In particular,this study identified a series of challenges and mechanisms that influence the water reuse potential and the robustness of the membrane harvesting system.In a preliminary phase of this investigation,the health status of the initial biomass was found to have important implications for the harvesting performance and quality of the permeate stream to be reused;healthy biomass ensured better dewatering performance(i.e.,higher water fluxes)and higher quality of the permeate water streams.A series of bench-scale filtration experiments with different combinations of cross-flow velocity and pressure values were performed to identify the operative conditions that would maximize water productivity.The selected conditions,2.4 m·s^(-1)and 1.4 bar(1 bar=105 Pa),respectively,were then applied to drive pilot-scale microfiltration tests to reuse the collected permeate as a new cultivation medium for S.obliquus growth in a pilot-scale photobioreactor.The investigation revealed key differences between the behavior of the membrane systems at the two scales(bench and pilot).It indicated the potential for beneficial reuse of the permeate stream as the pilot-scale experiments ensured high harvesting performance and growth rates of biomass in permeate water that were highly similar to those recorded in the ideal cultivation medium.Finally,different nutrient reintegration protocols were investigated,revealing that both macro-and micro-nutrient levels are critical for the success of the reuse approach.
Marco MalagutiLorenzo CraveriFrancesco RicceriVincenzo RiggioMariachiara ZanettiAlberto Tiraferri
关键词:MICROFILTRATIONHARVESTINGMICROALGAEPILOT-SCALE
Removal of endocrine disrupting chemicals from water through urethane functionalization of microfiltration membranes via electron beam irradiation
2024年
Polyethersulphone(PES)membranes modified with urethane functional groups were prepared through an interfacial reaction using electron beam irradiation.The removal of eight endocrine disrupting chemicals(EDCs)was studied using both pristine and functionalized PES membranes.The prepared membranes underwent characterization using several techniques,including attenuated total reflectance-Fourier transform infrared(ATR-FTIR)spectroscopy,scanning electron microscopy,contact angle analysis,and measurements of pure water flux.Furthermore,dynamic adsorption experiments were conducted to evaluate the adsorption mechanism of the prepared membrane toward the eight EDCs.The urethane functionalized membranes were hydrophilic(52°contact angle)and maintained a high permeate flux(26000 L/h m^(2) bar)throughout the filtration process.Dynamic adsorption results demonstrated that the introduction of urethane functional groups on the membranes significantly enhanced the removal efficiency of 17β-estradiol,estriol,bisphenol A,estrone,ethinylestradiol,and equilin.The adsorption loading of 17β-estradiol on the functionalized PES membrane was 6.7±0.7 mg/m^(2),exhibiting a 5-fold increase compared to the unmodified PES membrane.The membranes were successfully regenerated and reused for three adsorption cycles without experiencing any loss of adsorption capacity.
Zahra NiavaraniDaniel BreiteMuhammad YasirVladimir SedlarikAndrea PragerNadja SchönherrBernd AbelRoger GläserAgnes Schulze
关键词:MICROFILTRATION
连续式微滤膜分离乳清蛋白的研究
2024年
文章研究了跨膜压力对连续式微滤膜分离技术工艺参数、分离效果及组分组成的影响。以脱脂乳为原料,使用0.1μm陶瓷微滤膜三级连续在线洗滤工艺分离乳清蛋白和酪蛋白。实验使用0.08、0.11、0.14 MPa 3个梯度,在50℃,3.5倍浓缩的条件下连续生产240 min。计算跨膜压力并且检测截留液和透过液中的α-乳白蛋白(α-La),β-乳球蛋白(β-LG)含量及钾、钙、钠、镁等金属离子的含量。结果表明一级膜通量下降是导致整体膜通量下降的主要因素,经过240 min实验通量下降约17.2%。研究了不同跨膜压力下的膜通量变化情况,膜通量与跨膜压力呈正相关关系,水洗恢复率与跨膜压力呈负相关关系。随着实验时间的延长,膜表面形成不可逆的污堵层,乳清蛋白分离率下降,透过液中乳清蛋白含量下降,150 min后α-乳白蛋白浓度下降37%,β-乳球蛋白浓度下降36.5%。乳清蛋白中2种主要蛋白质比例会随着跨膜压力变化而变化,随着跨膜压力的升高β-乳球蛋白含量会逐渐升高。三级连续膜过滤后,乳清蛋白最高分离率90%左右(α-乳白蛋白为90.4%,β-乳球蛋白为92.7%)。乳中蛋白质的形态和功能受金属离子影响,分离过程中一价阳离子在膜两侧分布较均匀(脱除率大于80%),而二价阳离子则主要集中在截留液一侧(钙离子脱除率为38%)。透过液中的每克蛋白质所对应的金属离子比例远远大于其在截留液中的比例。
于声波刘宇白茹高增丽乌云曹文慧母智深
关键词:乳清蛋白
微滤技术在高盐废液中的应用
2024年
过滤技术的选择对企业的投资成本、装置的运行成本以及员工操作的实用性等会有不同程度的影响。针对不同的工况,过滤方式选择微滤还是超滤显得至关重要。选择微滤技术,并通过在阻燃剂装置离心脱水工段对产生的高盐废液中含有的少量超细固体粉末进行过滤脱除,达到了超细固体粉末完全脱除的效果,有效解决了阻燃剂装置生产过程中存在的问题。
田风宾
关键词:反冲洗粒径
微滤膜分离技术在微生物检验中的应用价值分析
2024年
目的探究微生物检验中使用微滤膜分离技术的有效性,以期为类似研究提供一定的参考。方法以仪征市疾病预防控制中心2021年8月至2023年10月接收的60份检验样本为对象,根据所用检验方法不同予以分组,对照组给予常规平板培养检验,研究组使用微滤膜分离技术实施检验,对比不同组别检验所用时间、样本污染率等指标情况。结果对照组样本检验时间为(28.71±4.38)h,研究组为(5.26±0.53)h,研究组样本检出率(93.33%)高于对照组(73.33%),且样本污染率比对照组低,差异存在统计学意义(P<0.05)。结论采用微滤膜分离技术对微生物实施检验,具有检出率高、样本污染率低等特点,还能缩短检测工作所用时间,具有在疾控中心推广使用的价值。
张梅闵敏赵姝旻
关键词:检出率污染率微生物检验
微生物检验过程中微滤膜分离技术的应用价值被引量:2
2024年
目的探讨微生物检验过程中微滤膜分离技术的应用价值。方法以2022年1月—2023年6月济南市疾病预防控制中心接收的86份微生物待检样本为研究对象。从每份待检样本中各取10 mL以平板计数法进行微生物检验,另各取10 mL基于微滤膜分离技术获取菌细胞进行微生物检验。比较2种检验方法的微生物检出率、微生物检验出报告时间与活菌回收率,评价检验效果。结果2种方法共检出阳性样本47份,其中微滤膜分离技术检出45份,占比为95.74%,平板计数法检出阳性样本47份,占比为100%。2种方法的初检86份样本的阳性检出率比较,差异无统计学意义(P>0.05);基于复检结果,微滤膜分离技术初诊漏检2例,2种方法的复检阳性率与漏检率比较,差异无统计学意义(P>0.05)。微滤膜分离技术的平均培养时间(20.24±3.17)h,短于平板计数法的(32.75±4.36)h,差异有统计学意义(P<0.05)。随机抽样回收率实验,微滤膜分离技术的阳性菌回收率分别为87.69%、87.50%、79.07%、67.86%、83.51%,高于平板计数法的72.01%、71.38%、64.19%、47.32%、65.64%,差异有统计学意义(P<0.05)。结论微生物检验中应用微滤膜分离技术的阳性检出率与平板计数法相当,但前者的培养时间更短,微生物检验出报告时间早,阳性菌回收率更高,效果优于平板计数法。
李新红李忠
关键词:微生物检验膜分离细菌培养
铸膜液中水的含量对聚醚砜微滤膜结构和性能的影响
2024年
通过蒸汽诱导相分离(VIPS)耦合非溶剂诱导相分离(NIPS)制备窄孔径分布聚醚砜(PES)微滤膜。本研究以PES为成膜材料,聚乙二醇为致孔剂,以水作为添加剂制备微滤膜,探究了铸膜液中水的质量分数对VIPS阶段蒸汽暴露时间及微滤膜结构与性能的影响.结果表明,铸膜液中水的质量分数从0%增加到3%,相似孔结构的形成所需的蒸汽暴露时间从90 s降低到30 s.膜的表面由致密皮层转变为大孔结构,孔径从0.087μm增加到0.193μm,孔径分布显著变窄,水接触角从83.6°增加到113.2°,拉伸强度从1.86 MPa增加到3.85 MPa,断裂伸长率从7%增加到16%,膜的力学性能显著增强,同时膜的纯水渗透率从5840 L/(m^(2)·h·MPa)增加到42300 L/(m^(2)·h·MPa).这表明,少量水的添加显著缩短了VIPS蒸汽暴露时间,同时改善了微滤膜的结构和性能.
孙茂林宋宗瑞何本桥何本桥
关键词:水含量非稳态
Microfiltration,ultrafiltration and nanofiltration as a post-treatment of biological treatment process with references to oil field produced water of Moran oilfield of Assam
2024年
The selection of an apt technology for the treatment of Oilfield Produced Water(OFPW)depends mainly on the quality of OFPW and methods of pre-and post-treatment processes.The most challenging part of the OFPW treatment process is the removal of Suspended Solid(SS),Oil&Grease(O&G)and dissolved organics.SS and O&G pose an acute problem to the membrane filtration system by fouling the membrane surface which increases operation&maintenance costs and decreases the life of the membrane.Fouling of the membrane surface is mainly attributed to the presence of low molecular weight aromatic compounds and naphthenic acids in the suspended and dissolved organic compounds.Thus,the removal of these suspended and dissolved organic compounds before membrane filtration proffers a challenge to the researchers.In this research,bioremediation process has been applied to remove the organic compounds and the performance and fouling behaviour of hollow fibre Microfiltration(MF),Ultrafiltration(UF)and Nanofiltration(NF)membranes after the bioremediation process has been analyzed in detail.The level of toxicity was determined by comparing the pollutants with the safe discharge limit for disposal into the environment set by Central Pollution Control Board(CPCB),India.The research presents its novelty by using a hydrocarbon-degrading bacteria,Pseudomonas aeruginosa for the Reduction of Organic Loads(ROL)from OFPW of Moran oil field of Upper Assam as a pre-treatment to membrane filtration.The Total Sum Corrected Area(TSCA)method through chromatographic analyses was used for this.The organic loads removal from OFPW by the TSCA method was found to be 67-100%,100%and 100%after 7,14 and 21 days of bioremediation respectively.The major parameters in feed OFPW of Moran oil field were found to be pH(7.5-9.3),Total Dissolved Solid(TDS)(1.79-4.75)ppt,O&G(1.78-2.8)ppt,Salinity(2.94-6.98)ppt,Chloride(Cl^(-))(1.6-3.86)ppt,Bicarbonate(HCO_(3)^(-))(2.89-4.03)ppt.It was observed that the ranges of pollutants removal by NF was highest such as TDS(26-86%),sa
Amarjit RajbongshiSubrata Borgohain Gogoi
磁微滤生物膜组合工艺在撬装式污水处理厂中的应用
2024年
某地因新增污水超出当地水厂接纳负荷,造成污水溢流、环境污染。为及时解决该部分溢流污水,同时考虑到占地、建设周期、使用周期等因素,选择磁微滤生物膜工艺的撬装式污水处理厂。本文介绍了该工艺的技术原理、工艺流程、设计参数及运行效果。水厂自下单生产到建成通水历时不到60天,投产运行后,出水水质稳定达到《四川省岷江、沱江流域水污染物排放标准》(DB51/2311-2016)。运营期间,平均药剂成本为0.18元/吨,平均能耗成本为0.25元/吨,污泥产量约为500kg/万m^(3)(绝干污泥),较传统工艺有较大成本优势。实践证明,该工艺在节约占地、节省运营费用等方面,具有较强的适用性和推广价值。
方国锋张宁迁
关键词:生物膜生活污水脱氮除磷

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龚军军
作品数:45被引量:116H指数:7
供职机构:中国人民解放军海军工程大学
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邓勇
作品数:4被引量:0H指数:0
供职机构:北京化工大学
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米宝霞
作品数:2被引量:3H指数:1
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研究主题:MF MEMBRANE_BIOREACTOR PAC ORGANIC_MATTER MICROFILTRATION
贾铭椿
作品数:113被引量:326H指数:9
供职机构:中国人民解放军海军工程大学船舶与动力学院核能科学与工程系
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张江朝
作品数:1被引量:3H指数:1
供职机构:天津大学环境科学与工程学院
研究主题:MF MEMBRANE_BIOREACTOR PAC ORGANIC_MATTER MICROFILTRATION