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Dewatering of Scenedesmus obliquus Cultivation Substrate with Microfiltration:Potential and Challenges for Water Reuse and Effective Harvesting
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作者 Marco Malaguti Lorenzo Craveri +3 位作者 Francesco Ricceri Vincenzo Riggio Mariachiara Zanetti Alberto Tiraferri 《Engineering》 SCIE EI CAS CSCD 2024年第7期155-163,共9页
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 alga... 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. 展开更多
关键词 Scenedesmus obliquus microfiltration Permeate reuse HARVESTING MICROALGAE PILOT-SCALE
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Application of Box-Behnken Experimental Design in the Optimization of Cleaning Microfiltration Ceramic Filters Using Sodium Hydroxide
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作者 Ngiongboung Nguiamba Celestine Asobo Yanu Placide Désiré Belibi Belibi 《Journal of Materials Science and Chemical Engineering》 2024年第12期80-87,共8页
Chemical cleaning has been reported as the best method to restore ceramic filters flow rate by removing fouling agents. Even though there are several chemicals that can be used as cleaning agents, sodium hydroxide (Na... Chemical cleaning has been reported as the best method to restore ceramic filters flow rate by removing fouling agents. Even though there are several chemicals that can be used as cleaning agents, sodium hydroxide (NaOH) has been widely used as a cleaning agent. Literature reports that main factors of this cleaning are sodium hydroxide concentration, treatment temperature and contact time. However, the most significant factors have not been determined nor the interactions between them. The aim of this study was to determine the most significant parameter and the interactions between sodium hydroxide concentration, treatment temperature and contact time. This was done using Box-Behnken experimental design. The results, based on ANOVA analyses, showed that temperature is the most significant factor and that interaction between sodium hydroxide concentration and treatment temperature is the most significant interaction. 展开更多
关键词 Chemical Cleaning Ceramic Filters microfiltration Box-Behnken OPTIMIZATION
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锂电池生产废水处理工程设计和运行实例 被引量:1
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作者 杨伟球 史广宇 《工业水处理》 北大核心 2025年第3期206-211,共6页
针对锂电池生产废水水质特征,采用阴极废水预处理去除重金属离子后和阳极废水合并,然后通过电Fenton-混凝反应-DF-厌氧反应器-AO组合工艺对锂电池生产废水进行处理。研究结果表明,该工艺对锂电池废水中的污染物有较高的去除率,对Ni^(2+)... 针对锂电池生产废水水质特征,采用阴极废水预处理去除重金属离子后和阳极废水合并,然后通过电Fenton-混凝反应-DF-厌氧反应器-AO组合工艺对锂电池生产废水进行处理。研究结果表明,该工艺对锂电池废水中的污染物有较高的去除率,对Ni^(2+)、COD_(Cr)、BOD_(5)、NH_(3)-N、TN、TP和SS的去除率分别达到了89.3%、98.7%、97.6%、94.9%、84.5%、93.6%和98.5%,出水水质可以达到《电池工业污染物排放标准》(GB 30484—2013)表2新建企业水污染物间接排放标准要求。最后对工程投资和运行费用进行了分析,采用该工艺处理锂电池生产废水,设计处理量为1000 m^(3)/d,工程投资共计866万元,其中土建投资435万元,设备投资431万元,运行费用包括电费、药剂费、人工费和污泥处置费,实际水量为900 m^(3)/d时,运行费用合计为7.48元/m^(3),为类似企业生产废水的处理提供参考。 展开更多
关键词 锂电池废水 重金属 混凝沉淀 电FENTON 管式微滤膜 厌氧反应器
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饮用水微滤膜预处理技术膜污染机制研究 被引量:3
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作者 刘子惠 程丽华 《水处理技术》 北大核心 2025年第2期110-115,共6页
微滤膜技术因过滤精度高、滤速快、操作压力低等特点,在高品质饮用水生产中作为纳滤的预处理工艺逐渐得到应用,但膜污染一直是影响其运行稳定性及使用寿命的问题之一。本文基于生产性微滤-纳滤双膜法饮用水处理工艺试验,通过特征污染物... 微滤膜技术因过滤精度高、滤速快、操作压力低等特点,在高品质饮用水生产中作为纳滤的预处理工艺逐渐得到应用,但膜污染一直是影响其运行稳定性及使用寿命的问题之一。本文基于生产性微滤-纳滤双膜法饮用水处理工艺试验,通过特征污染物截留能力与膜解剖表征分析,对微滤膜的膜污染机制进行了研究。结果表明:运行初期,膜污染主要为微滤膜的机械截留作用以及驱动压力作用,导致原水中的颗粒性污染物在膜表面发生中间/完全孔堵,形成松散堆积的滤饼层;后期因滤饼层的形成促进了有机污染、生物污染以及结垢性污染的形成与发展,最终造成了致密性膜污染的发生。研究成果可为微滤膜处理单元的膜污染控制提供技术支撑。 展开更多
关键词 饮用水 微滤 膜解剖 膜污染 膜清洗
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微滤和巴氏杀菌对脱脂驼乳体外消化性的影响
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作者 陶秀梅 陈尚卫 +3 位作者 刘大松 刘羿飞 张杰龙 周鹏 《食品与发酵工业》 北大核心 2025年第11期185-191,共7页
采用激光共聚焦显微镜、SDS-PAGE、体积排阻色谱和ELISA等方法,比较1.4μm孔径微滤和72℃下15 s巴氏杀菌处理对脱脂驼乳在体外模拟婴幼儿胃肠液中消化的影响。结果表明,微滤驼乳在模拟胃液中的絮凝物结构和持水量、酪蛋白残留率、游离... 采用激光共聚焦显微镜、SDS-PAGE、体积排阻色谱和ELISA等方法,比较1.4μm孔径微滤和72℃下15 s巴氏杀菌处理对脱脂驼乳在体外模拟婴幼儿胃肠液中消化的影响。结果表明,微滤驼乳在模拟胃液中的絮凝物结构和持水量、酪蛋白残留率、游离氨基释放量、产生蛋白水解物的分子质量分布都与脱脂生驼乳更接近,而巴氏杀菌则降低了驼乳在模拟胃液中酪蛋白的降解速率,表明巴氏杀菌使酪蛋白对消化酶的抗性增加。此外,微滤更大程度地保留了脱脂驼乳中的免疫球蛋白G,且使免疫球蛋白G和胰岛素在消化过程中的保留更多。微滤驼乳具有与脱脂生驼乳相似的胃肠消化特性和活性成分保留。该研究可为高活性驼乳制品的生产提供理论依据。 展开更多
关键词 微滤 巴氏杀菌 驼乳 体外消化 蛋白降解 活性成分
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基于SO/DOP混合稀释剂策略构建高性能UHMWPP微滤膜
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作者 盖文强 王静 +1 位作者 许山山 乔志华 《水处理技术》 北大核心 2025年第11期56-61,共6页
为提高微滤膜对复杂废水中纳米污染物的分离性能,本研究采用热致相分离(TIPS)技术,以超高分子量聚丙烯(UHMWPP)为膜材料,大豆油(SO)与邻苯二甲酸二辛酯(DOP)作为混合稀释剂,制备了一种具有优异分离性能的微滤膜。系统探究了SO/DOP比例... 为提高微滤膜对复杂废水中纳米污染物的分离性能,本研究采用热致相分离(TIPS)技术,以超高分子量聚丙烯(UHMWPP)为膜材料,大豆油(SO)与邻苯二甲酸二辛酯(DOP)作为混合稀释剂,制备了一种具有优异分离性能的微滤膜。系统探究了SO/DOP比例对膜结构演变与分离性能的调控机制,揭示了非溶剂-良溶剂协同作用对相分离行为及孔结构的影响。结果表明,随着SO占比的增加,体系相容性改善,相分离过程得到有效调控,膜孔数目有所增加,孔径有所减小。同时,膜表面粗糙度显著增加,亲水性明显改善,整体孔隙率由55.2%提升至67.1%。当SO/DOP比例为8∶2时,制备的UHMWPP微滤膜展现出最优的综合性能(渗透通量:383 L/(m^(2)·h·bar),炭黑截留率:96%)。此外,该膜还具有一定的抗污染性能,其通量恢复率达到95.6%。本研究为开发高性能聚丙烯微滤膜提供了新的制备策略和理论依据,在高效油墨废水处理领域具有广阔的应用前景。 展开更多
关键词 热致相分离 超高分子量聚丙烯 微滤膜 混合稀释剂 炭黑截留
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工业废水处理中膜分离技术的应用研究 被引量:2
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作者 史勤恺 《山西化工》 2025年第5期217-219,225,共4页
工业废水处理是应对环境污染、保护水资源的关键环节。随着工业活动的扩张,废水中复杂的污染物构成了严重的生态威胁,而膜分离技术因其高效的分离能力和广泛的适用性,已逐步成为工业废水处理中的重要手段。详细介绍了不同膜分离技术的... 工业废水处理是应对环境污染、保护水资源的关键环节。随着工业活动的扩张,废水中复杂的污染物构成了严重的生态威胁,而膜分离技术因其高效的分离能力和广泛的适用性,已逐步成为工业废水处理中的重要手段。详细介绍了不同膜分离技术的原理、优势和局限,探讨其在各种工业废水处理中的应用,以及膜污染与清洁的挑战,旨在为膜分离技术的优化与未来发展提供参考。 展开更多
关键词 膜分离技术 工业废水处理 反渗透 纳滤 微滤
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碳纳米管改性聚四氟乙烯微孔过滤膜的制备及性能研究 被引量:1
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作者 谭善和 唐子伦 周敏 《广州化工》 2025年第3期46-49,共4页
通过硫酸和硝酸的酸化,将羟基引入碳纳米管的表面,并采用真空抽滤的方法将酸化后的碳纳米管抽滤至聚四氟乙烯(PTFE)微孔过滤膜的表面,进而制备得到碳纳米管改性的PTFE微孔过滤膜。研究结果表明,碳纳米管的引入,可提高PTFE微孔过滤膜的... 通过硫酸和硝酸的酸化,将羟基引入碳纳米管的表面,并采用真空抽滤的方法将酸化后的碳纳米管抽滤至聚四氟乙烯(PTFE)微孔过滤膜的表面,进而制备得到碳纳米管改性的PTFE微孔过滤膜。研究结果表明,碳纳米管的引入,可提高PTFE微孔过滤膜的亲水性能,且制备得到的碳纳米管改性PTFE微孔过滤膜具有良好的稳定性。此外,基于羟基与金属离子的静电吸引作用,碳纳米管改性的PTFE微孔过滤膜可用于吸附Fe(III)离子。本文工作对于PTFE微孔过滤膜的改性具有一定的参考意义,在金属离子的吸附上也有潜在的应用价值。 展开更多
关键词 碳纳米管 聚四氟乙烯微孔过滤膜 改性 金属离子 吸附
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板框-滤膜耦合腌制液循环工艺及补料对皮蛋品质影响
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作者 徐晓雨 刘玉环 +3 位作者 崔宪 刘晓成 黄娜 李锐 《南昌大学学报(理科版)》 2025年第4期406-415,共10页
针对传统皮蛋生产过程中废弃腌制液循环利用率低及环境污染等问题,系统优化了高压板框-滤膜耦合工艺的腌制液循环利用技术,并评估补料策略对皮蛋品质的影响。通过对比高压板框(0.8 MPa)、微滤(孔径为0.22、0.45、1μm)的净化效能,发现... 针对传统皮蛋生产过程中废弃腌制液循环利用率低及环境污染等问题,系统优化了高压板框-滤膜耦合工艺的腌制液循环利用技术,并评估补料策略对皮蛋品质的影响。通过对比高压板框(0.8 MPa)、微滤(孔径为0.22、0.45、1μm)的净化效能,发现高压板框和微滤联用工艺显著降低腌制液浊度、沉淀物与悬浮物和化学需氧量(COD)含量;将新液和过滤液基于质量比8∶2混合可恢复循环液性能,在关键理化参数(pH值、碱度、Cu2+浓度)指标上,新液和复液无明显差异(P>0.05);28 d腌制实验表明,复液腌制皮蛋的蛋白硬度(除14 d外)及蛋黄的弹性(除7 d外)与新液腌制的皮蛋无明显差异(P>0.05);复液腌制的皮蛋色泽参数(L^(*)、a^(*)和b^(*))与新液的色泽参数无明显差异(P>0.05)。此外,感官评价显示其外观评分和总体接受度接近于新液。因此,多级膜分离技术结合适宜的补料策略,可实现皮蛋腌制液的高效再利用。 展开更多
关键词 皮蛋腌制液 高压板框 微滤 皮蛋品质
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保安过滤器滤芯剖析及微滤膜亲水改性研究
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作者 王崧合 潘明 《现代塑料加工应用》 北大核心 2025年第2期27-30,共4页
对现有两种滤芯及其微滤膜材料进行差异分析和对比,采用微波高温固相接枝技术对性能较好的滤芯微滤膜进行亲水改性,改性后的膜通量上升40%以上,抗污堵能力显著提升。
关键词 微滤膜 污堵 亲水改性 微波
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发酵法生产L-色氨酸提取工艺研究
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作者 李银行 《工业微生物》 2025年第2期10-12,共3页
本研究对发酵法生产L-色氨酸的提取工艺进行了优化处理。在L-色氨酸发酵液发酵结束后,通过管道将其输送至加热器,并瞬间加热至65℃。加热后的L-色氨酸发酵液经旋流器旋流,得到富含L-色氨酸晶体的下旋液和含少量色氨酸晶体的上旋液。下... 本研究对发酵法生产L-色氨酸的提取工艺进行了优化处理。在L-色氨酸发酵液发酵结束后,通过管道将其输送至加热器,并瞬间加热至65℃。加热后的L-色氨酸发酵液经旋流器旋流,得到富含L-色氨酸晶体的下旋液和含少量色氨酸晶体的上旋液。下旋液经过沉降处理,排掉上部悬浮液,加微滤清液漂洗3~4次,得到高纯度色氨酸晶浆液。同时晶浆液经降温、离心、烘干处理,直接获得L-色氨酸成品。上旋液经微滤、纳滤、浓缩、结晶、烘干处理,获得纯度达98%以上的L-色氨酸成品。同时离心母液经过浓缩、真空带式干燥,获得30%L-色氨酸产品。该工艺产出的98%含量色氨酸晶体颗粒大、收率高、提取过程简单,且其质量符合GB/T 25735—2010标准。 展开更多
关键词 L-色氨酸 旋流器 微滤 纳滤 真空带式干燥
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支撑层对聚酰胺膜形成及分离性能影响研究进展
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作者 高舒嘉 晋长杨 +1 位作者 张海跃 李俊 《净水技术》 2025年第5期23-33,56,共12页
【目的】通过界面聚合法制备的聚酰胺膜,因其成本低、能耗小、选择性高、渗透性强等优点,已成为解决水处理与资源回收问题的重要技术之一。然而,膜的性能仍受到多种因素的制约,特别是支撑层的理化特性对聚酰胺膜的通量和选择性具有显著... 【目的】通过界面聚合法制备的聚酰胺膜,因其成本低、能耗小、选择性高、渗透性强等优点,已成为解决水处理与资源回收问题的重要技术之一。然而,膜的性能仍受到多种因素的制约,特别是支撑层的理化特性对聚酰胺膜的通量和选择性具有显著影响。因此,需要系统整理和分析当前支撑层结构特性及其优化策略对聚酰胺膜性能的调控机制。【方法】文章综述了支撑层的孔径、亲水性及复合支撑层等因素对聚酰胺复合膜性能的影响,重点分析了以微滤膜和超滤膜为支撑层对界面层形成的影响,并探讨了支撑层的优化与改性策略,包括中间层引入、共混掺杂以及反应性支撑层等技术对膜性能的调控作用。【结果】合理调控孔径有利于均匀释放单体,减少缺陷形成,防止胺单体堵塞,从而兼顾高通量与高选择性;合理改善支撑层亲水性能够促进水相单体均匀分布,形成更薄且均匀的聚酰胺层。此外,共混掺杂技术可有效调控支撑层的孔隙分布与亲水性,而通过引入中间层或反应性支撑层技术,能够改善聚酰胺界面层与支撑层之间的结合力,提升膜的机械强度与耐受性。【结论】针对未来发展,支撑层的功能化设计及新型改性技术是提高聚酰胺复合膜性能的有效手段,应聚焦于同时实现高通量、高选择性以及长期抗污染性能,以满足工业水处理与资源回收的实际应用需求,为高效膜分离技术的发展提供理论与实践支持。 展开更多
关键词 界面聚合 聚酰胺 支撑层 微滤 超滤
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湿垃圾沼液处理中进水含油率、SS超负荷运行对策
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作者 吴晓晖 《净水技术》 2025年第S2期75-82,共8页
【目的】针对湿垃圾沼液悬浮物(SS)浓度较高、可生物降解有机物含量较低、氮和磷的含量较高且营养物质之间的比例失衡的特点,设计给出了采用“好氧+膜法(超滤+纳滤)”工艺组合的工艺路线。实际运行中,仍有生产状况、设备发生变化等,导... 【目的】针对湿垃圾沼液悬浮物(SS)浓度较高、可生物降解有机物含量较低、氮和磷的含量较高且营养物质之间的比例失衡的特点,设计给出了采用“好氧+膜法(超滤+纳滤)”工艺组合的工艺路线。实际运行中,仍有生产状况、设备发生变化等,导致在运行过程中出现了一些和设计不一致的情况。为解决运行中突出的进水含油率、SS超负荷问题,本文分析了产生超负荷的原因,并提出经过验证的解决方法。【方法】以上海某湿垃圾处理项目为例,对于高含油率及SS超设计负荷问题的原因有三方面的分析:一是前端工艺设备的不确定性;二是沼液处理工艺中对碳氮比失调,改用了浆液作为碳源的工艺调整;三是运行时间增加后系统本身的污染物累积。针对这三方面原因对水质影响的程度,提出了采用“曲面格栅+气浮”的工艺进行改善。在验证过程中,发现曲面格栅的去除效果随时间降低,且后续维护和检修工作较多,自动化程度低。因此,后续改为“微滤机+气浮”工艺。【结果】经过实践验证的解决方案最终为采用“微滤机+气浮”的工艺提高对于含油率和SS的去除率,满足原设计进水的要求。对含油率和SS去除率可以达到40%,具有自动化程度高、检修频率低的优点。【结论】采用“微滤机+气浮”的工艺经多年的运行验证稳定可靠,经验证本预处理工艺路线是可复制的,供相关设计人员和运行操作人员借鉴。 展开更多
关键词 湿垃圾沼液 含油率 悬浮物(SS) 气浮 微滤机
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Evaluation of Four Measurement Operation Modes of Streaming Potential for Microfiltration and Ultrafiltration Membranes 被引量:3
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作者 王志 赵媛媛 +3 位作者 叶楠 王纪孝 赵之平 王世昌 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2006年第4期456-463,共8页
Surface charge characteristics of a membrane can be determined by the streaming potential. In order to obtain more accurate streaming potential value during the measurement, four measurement operation modes were inves... Surface charge characteristics of a membrane can be determined by the streaming potential. In order to obtain more accurate streaming potential value during the measurement, four measurement operation modes were investigated in this study, and among the four modes, the steady mode with pressure stepped downward was considered the best one. Experimental results showed that the effects of compaction on the streaming potential measurement for a microfiltration membrane was more obvious than that for a ultrafiltration membrane. Both feed pH and presoaking could affect the measurement of streaming potential. 展开更多
关键词 charge characteristics streaming potential microfiltration ULTRAFILTRATION adsorption kinetics
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Modeling of Continuous Cross-flow Microfiltration Process in an Airlift External-loop Slurry Reactor 被引量:3
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作者 Zheng Bo Tang Xiaojin +1 位作者 Zhang Zhanzhu Zong Baoning 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2019年第1期117-122,共6页
New modified combination mathematical models including the pores blocking models and the cake layer models were developed to describe the continuous cross-flow microfiltration in an airlift external loop slurry reacto... New modified combination mathematical models including the pores blocking models and the cake layer models were developed to describe the continuous cross-flow microfiltration in an airlift external loop slurry reactor. The pores blocking models were created based on the standard blocking law and the intermediate blocking law, and then the cake layer models were developed based on the hydrodynamic theory in which the calculation method of porosity of cake layer was newly corrected. The Air-Water-FCC equilibrium catalysts cold model experiment was used to verify the relevant models.Results showed that the calculated values fitted well with experimental data with a relative error of less than 10%. 展开更多
关键词 AIRLIFT external-loop SLURRY reactor CROSS-FLOW microfiltration filtration resistance mathematical model
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Preparation and Characterization of the Modified Polyvinylidene Fluoride (PVDF) Hollow Fibre Microfiltration Membrane 被引量:2
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作者 Laizhou SONG Zunju ZHANG +1 位作者 Shizhe SONG Zhiming GAO 《Journal of Materials Science & Technology》 SCIE EI CAS CSCD 2007年第1期55-60,共6页
A novel thermally induced graft polymerization technique was used to modify a polyvinylidene fluoride (PVDF) hollow fibre microfiltration membrane. An artificial neural network (ANN) was applied to optimize the pr... A novel thermally induced graft polymerization technique was used to modify a polyvinylidene fluoride (PVDF) hollow fibre microfiltration membrane. An artificial neural network (ANN) was applied to optimize the prepared condition of the membrane. The optimized dosing of acrylic acid (AA), acrylamide (AM), N, N'- methylenebisacrylamide (NMBA) and potassium persulphate (KSP) designed by ANN was that AA was 40.63 ml/L; AM acted as 6.25 g/L; NMBA was 1.72 g/L and KSP was 1.5 g/L, respectively. The thermal stability of the PVDF modified hollow fibre membrane (PVDF-PAA) was investigated by thermogravimetric (TG) and differential scanning calorimetry (DSC) analysis. The polycrystallinity of the PVDF-PAA membrane was evaluated by X-ray diffraction (XRD) analysis. The complex formation of the modified membrane was ascertained by Fourier transform infrared spectroscopy (FTIR). The morphology of the PVDF-PAA membrane was studied by environmental scanning electron microscopy (ESEM). The surface compositions of the membrane were analyzed by X-ray photoelectron spectroscopy (XPS). The adsorption capacity of Cu^2+ ion on the PVDF-PAA hollow fibre membrane was also investigated. 展开更多
关键词 microfiltration hollow fibre membrane Graft polymerization modification Acrylic acid Polyvinylidene fluoride Cu^2+ ion
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Treatment of phosphate-containing oily wastewater by coagulation and microfiltration 被引量:1
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作者 ZHANG Jin SUN Yu-xin +2 位作者 HUANG Zhi-feng LIU Xing-qin MENG Guang-yao 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2006年第4期629-633,共5页
The oily wastewater generated from pretreatment unit of electrocoating industry contains oils, phosphate, organic solvents, and surfactants. In order to improve the removal efficiencies of phosphate and oils, to mitig... The oily wastewater generated from pretreatment unit of electrocoating industry contains oils, phosphate, organic solvents, and surfactants. In order to improve the removal efficiencies of phosphate and oils, to mitigate the membrane fouling, coagulation for ceramic membrane microfiltration of oily wastewater was performed. The results of filtration tests show that the membrane fouling decreased and the permeate flux and quality increased with coagulation as pretreatment. At the coagulant Ca (OH)2 dosage of 900 mg/L, the removal efficiency of phosphate was increased from 46.4% without coagulation to 99.6%; the removal of COD and oils were 97.0% and 99.8%, respectively. And the permeate flux was about 70% greater than that when Ca(OH)2 was not used. The permeate obtained from coagulation and microfiltration can be reused as make-up water, and the recommended operation conditions for pilot and industrial application are transmembrane pressure of 0.10 MPa and cross-flow velocity of 5 m/s. The comparison results show that 0.2 μm ZrO2 microfilter with coagulation could be used to perform the filtration rather than conventional ultrafilter, with very substantial gain in flux and removal efficiency of phosphate. 展开更多
关键词 ceramic membrane crossflow microfiltration COAGULATION phosphate removal fouling mitigation phosphate-containing oily wastewater
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Roles of membrane and organic fouling layers on the removal of endocrine disrupting chemicals in microfiltration 被引量:1
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作者 Wenchao Xue Kang Xiao +1 位作者 Peng Liang Xia Huang 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2018年第10期176-184,共9页
To understand the adsorption behavior of endocrine disrupting chemicals(EDCs) is important for enhancing the treatment performance and preventing potential secondary pollution caused by EDCs desorption in a microfil... To understand the adsorption behavior of endocrine disrupting chemicals(EDCs) is important for enhancing the treatment performance and preventing potential secondary pollution caused by EDCs desorption in a microfiltration system. The dynamic adsorption of four representative EDCs, namely estriol(E3), 17β-estradiol(E2), 17α-ethynylestradiol(EE2), and 4-nonylphenol(4-NP) in a microfiltration system was investigated using the Thomas' model.The product of the equilibrium constant and the total adsorption capacity of the membrane,Ka, for E3, E2, EE2, and 4-NP were 4.91, 9.78, 15.6, and 826, respectively, strongly correlating with the compound octanol–water partition coefficient(KOW). Adsorption appeared to be enhanced when organic fouling formed on the surface of membrane, indicating the role of an additional adsorption column for EDCs acted by a fouling layer in microfiltration. Results of a comparison between the Ka values for clean membrane and fouled membrane illustrated that the significant contribution made by fouling layers may be attributed to the foulant layer's hydrophobicity(in the case of calcium humate layer) and thickness(in the case of calcium alginate layer). This study provided a novel perspective to quantitatively analyze the dynamic adsorption behavior of trace pollutants in membrane process. 展开更多
关键词 Endocrine disrupting chemicals microfiltration membrane Dynamic adsorption Thomas' model Organic membrane fouling
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Purifying chylous plasma by precluding triglyceride via carboxylated polyethersulfone microfiltration membrane 被引量:1
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作者 Yang Liu Qiu Han +5 位作者 Guiliang Li Haibo Lin Fu Liu Gang Deng Dingfeng Lv Weijie Sun 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2022年第9期130-139,共10页
Precluding the excessive lipoproteins from plasma rapidly and effectively is highly needed for biomedical detection and reducing plasma product scrap in blood donation stations.The current centrifugation procedure is ... Precluding the excessive lipoproteins from plasma rapidly and effectively is highly needed for biomedical detection and reducing plasma product scrap in blood donation stations.The current centrifugation procedure is high-cost and time-consuming.Herein,we fabricated an anionic microfiltration polyethersulfone(PES)membrane modified by interface swelling and implanting of acrylic acid(AA)for screening out large particle lipoprotein chylomicron(CM)and adsorbing cationic very low-density lipoproteins(VLDL).To improve the separation efficiency,a two-stage filtration through carboxylated polyethersulfone microfiltration membranes with the mean pore size of 0.45 and 0.22μm respectively were conducted.Attenuated total reflection Fourier transform infrared technique(ATR-FTIR),water contact angle(WCA),Zeta potential and scanning electron microscope(SEM)were employed to characterize the modified membrane.To test the effectiveness of this membrane,plasma flux and concentration variation of plasma components were examined to study the purification effectiveness.Furthermore,the hemocompatibility of modified membranes was tested to confirm its practicability on bloodcontacting materials.The carboxylated polyethersulfone microfiltration membrane shows its promising potential application to purify chylous plasma. 展开更多
关键词 Chylous plasma CHYLOMICRONS Very low-density lipoproteins Carboxylated polyethersulfone microfiltration membrane
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Study on Separation of Water and Alumina Fine Particles by Cross-Flow Microfiltration 被引量:1
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作者 Zheng Bo Tang Xiaojin +1 位作者 Hou Shuandi Zong Baoning 《China Petroleum Processing & Petrochemical Technology》 SCIE CAS 2017年第2期96-103,共8页
A cross-flow microfiltration process had been developed to separate alumina fine particles from the suspension using a stainless steel membrane tube with a pore size of 10 μm. The influence of cross-flow velocity and... A cross-flow microfiltration process had been developed to separate alumina fine particles from the suspension using a stainless steel membrane tube with a pore size of 10 μm. The influence of cross-flow velocity and trans-membrane pressure on the permeate flux and the solid holdup in permeate had been investigated. It was found that both the permeate flux and the solid holdup in permeate decreased with time. Moreover, the permeate flux increased with an increasing transmembrane pressure but the influence of cross-flow velocity on the permeate flux was quite complex. Both the permeate flux and the solid holdup in permeate in long term filtration had been studied. The operation of cross-flow microfiltration could be carried out stably for 10 hours with the permeate flux values ranging from 520.5 to 936 L/(m^2·h) at rs=1%, while it could continue in 10 hours with the permeate flux values ranging from 226 to 432 L/(m^2·h) at rs=5%. The solid holdup in permeate had been less than 10 mg/L during the whole operating cycle. 展开更多
关键词 CROSS-FLOW microfiltration permeate FLUX REJECTION rate ALUMINA FINE particles
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