超细TiO2粒子的超滤分离及回用特性

针对TiO2超细粒子的超滤分离特性进行了试验研究，探讨了操作压力、膜面流速、TiO2投量、pH、电解质等参数条件对膜通量的影响规律及作用机理，证实了浓差极化及滤饼层阻力是影响通量变化的主导因素，在此基础上确定了适宜的超滤工艺条件及膜清洗方式。以甲基橙为降解基质分别测试了经混凝与超滤分离后的TiO2光催化活性，结果表明，超滤不仅可实现TiO2粒子与水的彻底分离，且分离后TiO2催化活性与初次使用相当。研究表明超滤用于悬浮光催化体系的固液分离及催化剂再用是可行的。     

TiO2光催化复合分离膜对水中天然有机物的去除

在水源污染越来越严重、水质标准日益严格的背景下，超滤（UF）已逐渐成为替代饮用水常规处理技术的最佳选择之一。本研究中采用相转化法，将聚偏氟乙烯（PVDF）、聚乙二醇（PEG）和二氧化钛（TiO2）共混制得光催化复合分离膜并对其进行扫描电子显微镜（SEM）、原子力显微镜（AFM）和X射线能谱仪（EDS）等相应的表征。比较了有无光照条件下，PVDF-PEG和PVDF—PEG—TiO2膜对腐殖酸（HA）的截留和超滤过程中的膜污染情况。研究结果表明，TiO2光催化复合分离膜能提高对水中天然有机物的去除并同时降低膜污染。紫外光照强度越强，PVDF-PEG—TiO2膜的抗污染性能越好。另外，光催化能更有效地减少超滤初始浓度较低的腐殖酸溶液过程中的膜通量衰减。     

微米级负载型TiO_2催化剂在光催化-膜分离反应器中的应用

基于光催化-膜分离三相流化床反应器的结构特点及膜分离特性,以微米级MCM-41分子筛为载体,采用原位生成法制备微米级负载型TiO2催化剂。针对微米级负载型TiO2催化剂在光催化-膜分离反应器中的分布特性、悬浮特性、分离特性及膜污染特性进行研究。结果表明,曝气量一定的情况下,微米级负载型TiO2催化剂在光催化-膜分离反应器中具有良好的悬浮特性,且优于纳米TiO2。随着催化剂投加量的增加,悬浮浓度也随之增加。光催化反应器底部曝气0.3m3/h、催化剂投加量为1 g/L时为宜。膜分离器中催化剂悬浮浓度明显低于光催化反应器;该微米级催化剂与纳米TiO2相比具有不粘附、不堵塞膜孔等优良特性,能够有效降低膜污染,延长分离膜使用寿命。膜底曝气为0.1 m3/h时,反应器连续运行5 h(未加反冲洗)后,微米级负载型TiO2催化剂和纳米TiO2对膜组件的污染程度分别为膜通量衰减率4.3%和37.4%。反应器连续运行72 h,膜组件依然具有很好的分离特性。     

微米级负载型TiO2催化剂在光催化-膜分离反应器中的应用

基于光催化．膜分离三相流化床反应器的结构特点及膜分离特性，以微米级MCM-41分子筛为载体，采用原位生成法制备微米级负载型TiO2催化剂。针对微米级负载型TiO2催化剂在光催化一膜分离反应器中的分布特性、悬浮特性、分离特性及膜污染特性进行研究。结果表明，曝气量一定的情况下，微米级负载型TiO2催化剂在光催化一膜分离反应器中具有良好的悬浮特性，且优于纳米TiO2。随着催化剂投加量的增加，悬浮浓度也随之增加。光催化反应器底部曝气0．3m。／h、催化剂投加量为1g／L时为宜。膜分离器中催化剂悬浮浓度明显低于光催化反应器；该微米级催化剂与纳米TiO2相比具有不粘附、不堵塞膜孔等优良特性，能够有效降低膜污染，延长分离膜使用寿命。膜底曝气为0．1m3／h时，反应器连续运行5h（未加反冲洗）后，微米级负载型TiO2催化剂和纳米TiO2对膜组件的污染程度分别为膜通量衰减率4．3％和37．4％。反应器连续运行72h，膜组件依然具有很好的分离特性。     

TiO2光催化对微滤去除腐殖酸的膜污染控制研究

着重研究了不同紫外灯光源和照射时间条件下，TiO2光催化（PCO）对微滤去除腐殖酸过程中的膜污染控制，并探讨了膜污染的控制机理。研究结果表明，TiO2光催化能有效提高微滤对腐殖酸的去除，同时降低膜通量的下降，起到有效控制膜污染的作用。进一步的实验分析表明，TiO2光催化控制膜污染的主要机理在于将腐殖酸降解为易于被TiO2吸附的小分子量物质，吸附腐殖酸降解产物后的TiO2聚合颗粒粒径增大，易于在膜表面形成更为松散的沉积层，并使膜污染从以膜孔堵塞和沉积层污染为主转化为以沉积层污染为主的可逆性污染。     

TiO2光催化复合分离膜对水中天然有机物的去除

在水源污染越来越严重、水质标准日益严格的背景下,超滤(UF)已逐渐成为替代饮用水常规处理技术的最佳选择之一。本研究中采用相转化法,将聚偏氟乙烯(PVDF)、聚乙二醇(PEG)和二氧化钛(TiO₂)共混制得光催化复合分离膜并对其进行扫描电子显微镜(SEM)、原子力显微镜(AFM)和X射线能谱仪(EDS)等相应的表征。比较了有无光照条件下,PVDF-PEG和PVDF-PEG-TiO₂膜对腐殖酸(HA)的截留和超滤过程中的膜污染情况。研究结果表明,TiO₂光催化复合分离膜能提高对水中天然有机物的去除并同时降低膜污染。紫外光照强度越强,PVDF-PEG-TiO₂膜的抗污染性能越好。另外,光催化能更有效地减少超滤初始浓度较低的腐殖酸溶液过程中的膜通量衰减。     

固定化催化剂TiO2膜光催化降解三氯乙醛的研究

研究了负载于玻璃上的固定化催化剂TiO2膜光催化降解水中三氯乙醛的效果,探讨了TiO2膜光催化降解三氯乙醛的机理,考察了溶液pH值和三氯乙醛初始浓度埘TiO2膜光催化降解三氯乙醛的影响,并研究了固定化催化剂TiO2膜光催化降解三氯乙醛的动力学.结果表明,固定化催化剂TiO2膜光催化降解水中三氯乙醛的效果良好,当三氯乙醛初始浓度为2.25 mg/L时,在紫外光照时间3 h下,三氯乙醛的降解率高达100%.在相司紫外光照时间下,三氯乙醛的光催化降解率随着三氯乙醛初始浓度的增大而下降.在溶液pH=6.5时,三氯乙醛的降解效率最高.固定化催化剂TiO2膜光催化降解三氯乙醛的反应遵循一级反应动力学,反应速率常数随三氯乙醛初始浓度的增大而减小.     

纳米TiO_2光催化-超滤法处理模拟二级出水

采用纳米TiO_2光催化-超滤对模拟二级出水进行处理。分别考察了纳米TiO_2光催化剂的投加量、光催化反应时间、光催化过程曝气量、膜出水通量以及回流比对废水中污染物去除率的影响。结果表明:光催化反应最优处理工况,纳米TiO_2投加量250 mg/L、反应时间150 min、曝气量为1.0 L/min、膜出水通量为115 L/(m~2·h)、错流过滤的回流比200%;在此工况条件下,出水的UV254和TOC的去除率分别为96%和84%。     

TiO2光催化-微滤膜分离深度净化亚甲基蓝印染废水

采用悬浮式TiO2光催化膜反应器深度净化纺织工业园区含亚甲基蓝印染废水经生物处理二级出水,利用中空纤维微滤膜进行催化剂截留分离,研究催化剂投加量、运行时间、溶解氧、搅拌方式对出水水质及膜通量的影响。结果表明:光催化会消耗体系溶解氧,鼓风曝气搅拌可同时为系统供氧,优于机械搅拌;该耦合体系的催化剂最佳投加量为1 g/L,经光催化氧化-膜组合工艺处理后水质优于GB 4287-1992《纺织染整工业污染物排放标准》的I级标准,符合建设部颁布的《生活杂用水水质标准》(CJ/T 48-1999)。     

一体式光催化－膜分离三相流化床反应器膜污染特性

通过利用颗粒状 TiO2催化剂(平均粒径0.258/μm)对酸性红 B 模拟废水的催化降解实验,对一体式光催化氧化-膜分离三相流化床反应器的膜污染特性进行了研究.结果表明,TiO2是造成膜污染的主要污染物,且 TiO2浓度愈大,膜污染愈严重;本实验体系TiO2的适宜浓度为 2g/L.反应区曝气量在 3.6m3/h 时膜污染最小;膜组件底部曝气装置可大大减轻膜污染,且其曝气量以 0.6 m3/h 为宜.表面冲洗、气体反冲洗和碱洗均可有效地清除膜表面和膜孔内的污染物,使膜通量恢复至90%以上;"表面冲洗 碱洗"和"表面冲洗 碱洗 气体反冲"可进一步提高膜通量的恢复,但不十分明显.     

预涂动态膜强化渗透与截留性能研究

以二氧化钛粉体材料为涂膜剂,陶瓷管为基膜制备预涂动态膜,引入通量增强系数Zi和截留增强系数Fi研究了预涂动态膜制备条件对其强化渗透与截留性能的影响,并用SEM电镜对预涂动态膜和基膜表面形貌进行表征。结果表明:制备的预涂动态膜表面均匀密实,其孔径低于基膜平均孔径。预涂动态膜的渗透与截留性能随涂膜液pH值的增加而增加,在跨膜压差低于0.2 MPa、错流速度低于1.5 m/s,涂膜时间少于30 m in和涂膜液浓度低于0.4 g/L范围内,提高这些参数值有利于提高预涂动态膜的渗透与截留性能,超出此范围时,提高这些参数值对增强其渗透与截留性能的效果已不明显,其中错流速度的影响相对小些。跨膜压差为0.2 MPa,错流速度为1.5 m/s,涂膜时间30 m in,涂膜液浓度和pH值分别为0.4 g/L和10.2时为最佳制备条件。     

Microfibrous mesh coated with titanium dioxide: a self-sterilizing,self-cleaning filter

The utility of metal microfibrous mesh coated with titanium dioxide as a self-sterilizing, self-cleaning filter for air is explored. The low-cost mesh is produced via a roll-to-roll process similar to paper manufacturing. The titanium dioxide is applied by spraying an aqueous suspension of the photocatalyst on the surface of the mesh using an airbrush. Photocatalytic activity comparable to a powder layer is achieved at one quarter of the mass loading. The coating enhanced the separation of Escherichia coli (E. coli) from aqueous suspension, but also led to an increase in pressure drop in an air stream flowing through the mesh. The self-cleaning property of the coated mesh is established by recovery of pressure drop performance lost due to biofilm buildup. This is accomplished via a photocatalytic regeneration process involving exposing the mesh to ultraviolet light in air. Oxidation is confirmed by monitoring CO2 evolution during the regeneration. Scanning electron photomicrographs also provide visual evidence of successful regeneration via photocatalysis.     

支撑气膜法脱除／回收垃圾渗滤液中氨氮

利用由微孔疏水性聚丙烯中空纤维制成的工业级膜组件对垃圾渗滤液中氨氮进行支撑气膜法脱除研究，考察了泡沫分离．石灰絮凝等预处理技术对垃圾渗滤液表面张力及COD值的处理效果，在此基础上研究了物料因素和操作因素对膜传质性能的影响，并对该工艺的长期操作稳定性进行了研究。实验结果表明该预处理技术不仅可显著提高垃圾渗滤液的表面张力，还可大大降低其色度和COD值。当进料流量为100L／h、进料氨氮浓度为1000～3000mg／L、硫酸吸收液流量为200L／h、硫酸浓度为6％～10％、温度为20～30℃时，支撑气膜过程（两级膜组件串联）可有效脱除垃圾渗滤液中99％以上的氨氮，同时得到含10％～15％硫酸铵的水溶液作为副产品。工业级支撑气膜组件在连续运行的2个月内保持了良好的传质稳定性。     

膜生物反应器生物降解与膜分离共作用特性研究

膜生物反应器实质是生物降解与膜分离相互影响,共同作用的过程,污泥浓度与通量之间存在一定的相关关系,膜分离对生和性能尤其是细菌活性有着重要的影响,而生物反应器内细菌胞外聚合物,溶解性有机物及微细胶体可能成为形成凝胶层导致通量下降的主要因素。     

Kinetic analysis of photocatalytic oxidation of gas-phase formaldehyde over titanium dioxide

Degradation of formaldehyde with different initial concentration over titanium dioxide was carried out in a photocatalytic reactor. Photocatalytic rates were well described by the simplified Langmuir-Hinshelwood model. The kinetic analysis shows that the apparent first-order reaction coefficient is lower and half-life of photocatalysis is longer for low concentration than for high concentration formaldehyde. A network formation model of the photocatalytic products was established. Experimental results and analysis demonstrate that carbon dioxide concentration and carbon monoxide concentration in gas phase vary exponentially with the illumination time and may be even higher than gas-phase formaldehyde concentration if there is much pre-adsorbed formaldehyde in adsorption equilibrium on catalysts before illumination. Carbon monoxide is found to be one of the by-products during formaldehyde photooxidation.     

Photodegradation of monochlorobenzene in titanium dioxide aqueous suspensions

The photocatalytic degradation of monochlorobenzene using titanium dioxide aqueous suspensions was performed under solar-simulated irradiation. The effects of concentration of monochlorobenzene, amount of titanium dioxide and pH of solution on the degradation were examined. The intermediates identified were three monochlorophenols, chlorohydroquinone and hydroxy-hydroquinone.     

Carbamazepine degradation by photolysis and titanium dioxide photocatalysis

We investigated the degradation of carbamazepine by photolysis/ultraviolet (UV)-C only and titanium dioxide photocatalysis. The degradation of carbamazepine by UV-only and titanium-dioxide-only (adsorption) reactions were inefficient, however, complete degradation of carbamazepine was observed by titanium dioxide photocatalysis within 30 min. The rate of degradation increased as initial carbamazepine concentration decreased, and the removal kinetics fit well with the Langmuir-Hinshelwood model. The addition of methanol, a radical scavenger, decreased carbamazepine removal, suggesting that the hydroxide radical played an important role during carbamazepine degradation. The addition of oxygen during titanium dioxide photocatalysis accelerated hydroxide radical production, thus improving mineralization activity. The photocatalytic degradation was more efficient at a higher pH, whereas the removal of carbamazepine and acridine (a major intermediate) were more efficient under aerobic conditions. The mineralization of carbamazepine during photocatalysis produced various ionic by-products such as ammonium and nitrate by way of nitrogen dioxide.     

城市节假日前后碳通量特征及其与车流量关系

全球变化背景下,城市作为主要的碳源,对其碳循环的研究成为陆地生态系统碳循环的重点内容之一。以上海市奉贤区为研究对象,基于涡度相关技术,结合定点连续观测的车流量数据,分析节假日（元旦）前后CO2浓度和碳通量的变化特征,及其与车流量的关系。结果表明,CO2浓度和通量日变化呈现明显的双峰型曲线,节假日CO2浓度（385.6mg/L）平均值低于工作日（401.1 mg/L）。在本研究时段内该系统表现为碳源,尽管在白天的某些时段是碳汇,表明城市系统碳通量受自然和人为2个因素共同作用,自然因素比如该系统中的香樟、雪松等常绿植物的光合作用,人为因素由人类活动造成。基于车流量与交通流量的线性回归分析表明,机动车量碳排放对于碳通量变化产生18%的贡献。     

二氧化钛/碳纳米管/壳聚糖薄膜的制备及对苯的降解性能

研究了光催化降解挥发性有机化合物过程中催化剂二氧化钛/碳纳米管/壳聚糖薄膜的制备以及该催化剂对苯的光催化性能。首先采用溶胶-凝胶法制备纳米复合材料二氧化钛/碳纳米管,然后利用壳聚糖作为交联剂,制得二氧化钛/碳纳米管/壳聚糖复合材料催化薄膜。通过傅立叶红外光谱(FT-IR)、X射线衍射(XRD)透射电镜扫描(TEM)和紫外-可见光漫反射(UV-Vis)等技术分析了复合材料薄膜的组成、结构、形貌和对光的吸收性能,然后使用该催化剂对室内常见的污染物苯进行降解,并在同样的实验条件下,使用催化剂二氧化钛(P25)/壳聚糖对苯进行降解,对两者催化性能进行对比,结果表明,二氧化钛/碳纳米管/壳聚糖对苯有更强的吸附能力和更高的催化活性。     

Light-induced degradation of perfluorocarboxylic acids in the presence of titanium dioxide

The UV-photon-induced degradation of heptafluorobutanoic acid was investigated in acidic aqueous solutions in the presence of titanium dioxide. Heptafluorobutanoic acid could be degraded with this photocatalyst in a light-induced reaction generating carbon dioxide and fluoride anions. Carbon dioxide evolution in a significant amount occurred only in the presence of molecular oxygen and the photocatalyst. The light-induced degradation of trifluoroacetic acid, pentafluoropropanoic acid, nonafluorobutanoic acid, pentadecafluorooctanoic acid, nonafluorobutanesulfonic acid, and heptadecafluorooctanesulfonic acid in the presence of titanium dioxide was also studied. The perfluorocarboxylic acids under investigation are degraded to generate CO(2) and fluoride anions while both perfluorinated sulfonic acids are persistent under the experimental conditions employed in this study. For all compounds photonic efficiencies of the mineralization reaction were estimated to be smaller than 1x10(-5). To increase the photocatalytic activity mixed systems containing homogeneous phosphotungstic acid and heterogeneous titanium dioxide catalysts were also investigated. In the mixtures of these two photocatalysts, the formation rate of CO(2) increased with illumination time.