TiO2膜光催化降解4，4’-二溴联苯的研究

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4,4’-二溴联苯（4,4’-DBB）的效果,考察了溶液pH值和4,4’-DBB初始浓度等对TiO2膜光催化降解4,4’-DBB的影响,探讨了降解机理。结果表明,TiO2膜光催化降解水中4,4’-DBB的效果良好,紫外光照射8h,初始浓度为4mg／L的4,4’-DBB的降解率高达94％,降解速率随着4,4’-DBB初始浓度的增大而下降。在溶液pH：1时,4,4’-DBB的降解效率最高。超声的加入使降解反应的速率加快。经拟合发现4,4’-DBB的降解符合拟一级反应规律,并推导出动力学方程。     

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.     

TiO2膜光催化降解4, 4’-二溴联苯的研究

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4, 4’-二溴联苯（4, 4’-DBB）的效果,考察了溶液pH值和4, 4’-DBB初始浓度等对TiO2膜光催化降解4,4’-DBB的影响,探讨了降解机理。结果表明,TiO₂膜光催化降解水中4, 4’-DBB的效果良好,紫外光照射8 h,初始浓度为4 mg/L的4, 4’-DBB的降解率高达94%,降解速率随着4,4’-DBB初始浓度的增大而下降。在溶液pH=1时,4, 4’-DBB的降解效率最高。超声的加入使降解反应的速率加快。经拟合发现4, 4’-DBB的降解符合拟一级反应规律,并推导出动力学方程。     

一种光催化体系光催化降解苯胺的研究

以钛酸丁酯为原料．以膨润土为载体,用酸性溶胶法合成TiO2纳米复合物,并利用该复合物作催化剂,在H2O2存在下进行光催化降解苯胺溶液。结果表明,该催化剂在UV／H2O2系统中对苯胺溶液有很好的光催化降解效果,其效果优于纯TiO2;H2O2的存在提高了苯胺光催化降解速率,在本实验条件下其最佳摩尔浓度是5mmol／L;溶液pH是影响反应速率的重要因素．pH在中性范围内具有更强的光催化活性;该体系中苯胺能够有效地被降解,其光催化反应遵循一级反应动力学规律。     

磷钨酸光催化降解甲基橙溶液的研究

以磷钨酸为光催化剂,在紫外灯照射下,对模拟染料废水甲基橙溶液进行光催化降解,并研究了催化剂加入量、pH值、甲基橙初始浓度和外加氧化剂H2O2对光催化降解效果的影响.结果表明,磷钨酸光催化剂加入量为300 mg/100 mL,pH=2.5时,甲基橙溶液的降解率明显高于其他pH值的降解率;在较低浓度下,甲基橙溶液的光催化降解反应符合一级动力学方程;外加氧化剂H2O2可提高光催化反应速率.     

TiO2薄膜光催化降解双酚A的研究

采用sol-gel法制备TiO2薄膜.以该薄膜为催化剂,研究了在H2O2存在的条件下,对内分泌干扰物质双酚A的光催化降解反应.分别讨论了pH值、H2O2的加入量、双酚A的初始浓度以及光照时间对降解反应的影响.结果表明,在pH=4,30 mg/L的H2O2中对初始浓度为50 mg/L的双酚A溶液光照180 min有较好的降解效果.     

磷钨酸光催化降解甲基橙溶液的研究

以磷钨酸为光催化刺，在紫外灯照射下。对模拟染料废水甲基橙溶液进行光催化降解，并研究了催化剂加入量、pH值、甲基橙初始浓度和外加氧化剂H2O2对光催化降解效果的影响。结果表明，磷钨酸光催化剂加入量为300mg／100mL，pH=2．5时，甲基橙溶液的降解率明显高于其他pH值的降解率；在较低浓度下，甲基橙溶液的光催化降解反应符合一级动力学方程；外加氧化剂H2O2可提高光催化反应速率。     

纳米TiO2对酚红溶液光催化的性能

采用锐钛矿相纳米TiO2粉体对酚红溶液进行光催化降解。考察了酚红溶液初始pH对光降解速率的影响，并就其影响因素进行了探讨，同时对酚红溶液光降解反应的动力学模型进行了初步研究。     

超声协同TiO_2光催化降解4,4′-二溴联苯

以纳米TiO2膜为光催化剂,对4,4′-二溴联苯水溶液进行了超声光催化(US+UV)、光催化(UV)和超声(US)降解,探讨了初始浓度、超声的声强和频率等对降解4,4′-二溴联苯的影响。结果表明,4,4′-二溴联苯的超声光催化降解存在协同效应,降解率随4,4′-二溴联苯初始浓度的增大而下降,随声强和频率的增大而增大。超声光催化过程符合一级动力学方程,反应数率常数为0.011 min-1。超声光催化与光催化的降解产物不同。     

超声协同TiO2光催化降解4,4′-二溴联苯

以纳米TiO2膜为光催化剂,对4,4′-二溴联苯水溶液进行了超声光催化（US＋UV）、光催化（UV）和超声（US）降解,探讨了初始浓度、超声的声强和频率等对降解4,4′-二溴联苯的影响。结果表明,4,4′-二溴联苯的超声光催化降解存在协同效应,降解率随4,4′-二溴联苯初始浓度的增大而下降,随声强和频率的增大而增大。超声光催化过程符合一级动力学方程,反应数率常数为0.011 min^-1。超声光催化与光催化的降解产物不同。     

TiO2纳米管催化降解4，4’-二溴联苯的影响因素和动力学研究

利用TiO₂纳米管催化降解水中的4,4’-二溴联苯,对催化降解过程和影响因素进行研究。结果表明,TiO₂纳米管对其有较高的催化降解效率且降解过程符合Langmuir-Hinshelwood动力学模式。不同光源、4,4’-二溴联苯的初始浓度、纳米管添加量和pH值对催化降解过程都有较大影响,其中pH值的影响最为明显。反应液在中性状态下的降解率明显低于pH=1或11的情况。在pH=1时,4,4’-二溴联苯的降解率达86%。     

Photocatalytic degradation of the herbicide erioglaucine in the presence of nanosized titanium dioxide: comparison and modeling of reaction kinetics

The present work mainly deals with photocatalytic degradation of a herbicide, erioglaucine, in water in the presence of TiO2 nanoparticles (Degussa P-25) under ultraviolet (UV) light illumination (30 W). The degradation rate of erioglaucine was not so high when the photolysis was carried out in the absence of TiO2 and it was negligible in the absence of UV light. We have studied the influence of the basic photocatalytic parameters such as pH of the solution, amount of TiO2, irradiation time and initial concentration of erioglaucine on the photodegradation efficiency of erioglaucine. A kinetic model is applied for the photocatalytic oxidation by the UV/TiO2 system. Experimental results indicated that the photocatalytic degradation process could be explained in terms of the Langmuir-Hinshelwood kinetic model. The values of the adsorption equilibrium constant, K, and the second order kinetic rate constant, k, were 0.116 ppm-1 and 0.984 ppm min-1, respectively. In this work, we also compared the reactivity between the commercial TiO2 Degussa P-25 and a rutile TiO2. The photocatalytic activities of both photocatalysts were tested using the herbicide solution. We have noticed that photodegradation efficiency was different between both of them. The higher photoactivity of Degussa P-25 compared to that of rutile TiO2 for the photodegradation of erioglaucine may be due to higher hydroxyl content, higher surface area, nano-size and crystallinity of the Degussa P-25. Our results also showed that the UV/TiO2 process with Degussa P-25 as photocatalyst was appropriate as the effective treatment method for removal of erioglaucine from a real wastewater. The electrical energy consumption per order of magnitude for photocatalytic degradation of erioglaucine was lower with Degussa P-25 than in the presence of rutile TiO2.     

Trichloroethylene degradation by photocatalysis in annular flow and annulus fluidized bed photoreactors

The effects of trichloroethylene (TCE) gas flow rate, relative humidity, TiO(2) film thickness, and UV light intensity on photodegradation of TCE have been determined in an annular flow type photoreactor. Phosgene and dichloroacetyl chloride formation could be controlled as a function of TCE gas flow rate and photodegradation of TCE decreased with increasing relative humidity. The optimum thickness of TiO(2) film was found to be approximately 5 mum and the photocatalytic reaction rate of TCE increased with square root of UV light intensity. In addition, the effects of the initial TCE concentration, phase holdup ratio of gas and solid phases (epsilon(g)/epsilon(s)), CuO loading on the photodegradation of TCE have been determined in an annulus fluidized bed photoreactor. The TCE photodegradation decreased with increasing the initial TCE concentration. The optimum conditions of the phase holdup ratio (epsilon(g)/epsilon(s)) and CuO wt.% for the maximum photodegradation of TCE was found to be 2.1 and 1.1 wt.%, respectively. Therefore, an annulus fluidized bed photoreactor is an effective tool for TCE degradation over TiO(2)/silica gel with efficient utilization of photon energy.     

Performance of photocatalytic reactors using immobilized TiO2 film for the degradation of phenol and methylene blue dye present in water stream

TiO2 thin film photocatalyst was successfully synthesized and immobilized on glass reactor tube using sol-gel method. The synthesized TiO2 coating was transparent, which enabled the penetration of ultra-violet (UV) light to the catalyst surface. Two photocatalytic reactors with different operating modes were tested: (a) tubular photocatalytic reactor with re-circulation mode and (b) batch photocatalytic reactor. A new proposed TiO2 synthesized film formulation of 1 titanium isopropoxide: 8 isopropanol: 3 acetyl acetone: 1.1 H2O: 0.05 acetic acid (in molar ratio) gave excellent photocatalytic activity for degradation of phenol and methylene blue dye present in the water. The half-life time, t1/2 of photocatalytic degradation of phenol was 56 min at the initial phenol concentration of 1000 microM in the batch reactor. In the tubular photocatalytic reactor, 5 re-circulation passes with residence time of 2.2 min (single pass) degraded 50% of 40-microM methylene blue dye. Initial phenol concentration, presence of hydrogen peroxide, presence of air bubbling and stirring speed as the process variables were studied in the batch reactor. Initial methylene blue concentration, pH value, light intensity and reaction temperature were studied as the process variables in the tubular reactor. The synthesized TiO2 thin film was characterized using SEM, XRD and EDX analysis. A comparative performance between the synthesized TiO2 thin film and commercial TiO2 particles (99% anatase) was evaluated under the same experimental conditions. The TiO2 film was equally active as the TiO2 powder catalyst.     

Photocatalytic degradation of an organophosphorus pesticide phosalone in aqueous suspensions of titanium dioxide

The present work deals with photocatalytic degradation of an organophosphorus pesticide, phosalone, in water in the presence of TiO2 particles under UV light illumination (1000 W). The influence of the basic photocatalytic parameters such as pH of the solution, amount of TiO2, irradiation time, stirring rate, and distance from UV source, on the photodegradation efficiency of phosalone was investigated. The degradation rate of phosalone was not high when the photolysis was carried out in the absence of TiO2 and it was negligible in the absence of UV light. The half-life (DT50) of a 20 ppm aqueous solution of phosalone was 15 min in optimized conditions. The plot of lnC (phosalone) vs. time was linear, suggesting first order reaction (K=0.0532 min(-1)). The half-life time of photomineralization in the concentration range of 7.5-20 ppm was 13.02 min. The efficiency of the method was also determined by measuring the reduction of Chemical Oxygen Demand (COD). During the mineralization under optimized conditions, COD decreased by more than 45% at irradiation time of 15 min. The photodegradation of phosalone was enhanced by addition of proper amount of hydrogen peroxide (150 ppm).     

亚甲基蓝表面修饰纳米TiO2降解造纸废水动力学

以亚甲基蓝(MB)作为表面修饰剂,采用简单的化学吸附法制备亚甲基蓝表面修饰的纳米TiO2光催化剂(TiO2-MB)。经表面修饰后,TiO2-MB光催化剂波长响应范围红移至可见光区575 nm处。探讨了光催化剂量、光照时间和溶液pH值对TiO2-MB光催化降解造纸废水的影响;研究了纳米TiO2-MB对造纸废水的暗吸附规律和光降解性能。结果表明:纳米TiO2-MB对造纸废水的吸附规律都较好地符合Langmuir和Freundlich吸附等温模型,属于吸热反应;光催化降解动力学符合Langmuir-Hinshelwood动力学模型。在160 W高压汞灯光照80 min,3.0 g/L纳米TiO2-MB光催化降解pH=2.0的造纸废水(COD:2 069.8 mg/L),COD去除率可达94.7%,处理效果远高于避光条件下。光催化剂经8次使用仍具有较高的催化活性。     

TiO2光催化降解水中土霉素的动力学研究

环境中抗生素的出现及其引起的危害正受到越来越多的关注。以高压汞灯为光源,选用较为广泛的抗生素土霉素（OTC）为处理对象。考察了初始质量浓度、反应过程中光照、催化剂投加量、溶液起始pH、溶液中DOM和NO^-₃对光催化降解的影响,研究了其光降解动力学。结果表明,TiO₂光催化氧化法能够有效去除水中半微量的OTC,OTC的光降解过程符合一级反应动力学模型;UV/TiO₂联用工艺对TOC也有很好的去除效果,反应90 min,TOC去除率可达74%;OTC的初始浓度从30 mg/L增大到90 mg/L,反应速率从0.0619 min^-1降低到0.0130 min^-1;随着光催化剂投加量的增大,光降解速率常数先增大后减小;增加溶液的pH值,速率常数逐渐减小;溶液中的DOM和NO^-₃也可以影响光降解效率。