Fe^3＋掺杂TiO2纳米膜的制备及光催化性能的研究

采用溶胶-凝胶法制备出掺杂Fe^3＋的TiO2纳米膜,并用x射线衍射方法进行表征;探讨了金属离子铁离子掺杂对TiO2纳米膜光催化降解性能的影响;研究了TiO2纳米膜及掺杂改性的TiO2纳米膜对甲基兰的降解作用,同时还尝试不同掺杂的TiO2纳米膜的杀菌功能。实验结果表明通过掺杂Fe的TiO2纳米膜有优良的光催化降解性能。     

溶胶-凝胶掺杂铁对微弧氧化TiO_2膜光催化性能影响

以磷酸钠为电解液,采用微弧氧化技术在钛片上直接制备TiO2膜,利用溶胶-凝胶法和硝酸铁掺杂方法对该膜表面进行修饰处理,以罗丹明B溶液模拟废水来评价TiO2膜光催化降解水中有机污染物的能力。利用EDX对微弧氧化膜表面成分进行分析。实验结果表明:微弧氧化TiO2膜具有一定的光催化活性。溶胶-凝胶法负载TiO2且硝酸铁掺杂处理后可以使铁离子进入微弧氧化TiO2负载膜,改善膜的光催化性能。溶胶-凝胶法负载TiO2膜对废水的光催化降解效率由13.8%提高到42.5%;铁离子掺杂1%可以使负载TiO2膜对废水的光催化效率由42.5%提高到68.9%。     

贵金属负载TiO_2光催化降解甲苯研究

采用Degussa P25 TiO2粉末,利用光沉积法制备贵金属负载光催化剂M/TiO2(M分别为Pt、Pd、Ag和Au)。通过气相甲苯光催化降解实验考察M/TiO2的光催化活性。实验结果表明:负载1.0 wt%的Pt、Pd、Ag和Au四种贵金属均可提高TiO2光催化降解甲苯的效率,其中Pt/TiO2的光催化活性最佳。循环伏安法(CV)、塔菲尔(Tafel)和Mott-Schottky电化学测试证明Pt的负载抑制光生电子和空穴的复合,提高载流子浓度,进而增强TiO2光催化活性。     

Ag/TiO_2-PVA改性无纺布的抗污染性能

以廉价的无纺布为基膜,采用NaBH4还原法制备了Ag/TiO2-PVA复合膜,研究了Ag/TiO2-PVA复合膜作为MBR膜组件处理人工废水的抗污染性能,并对Ag/TiO2-PVA复合膜进行了XRD表征。Ag/TiO2-PVA复合膜的XRD谱图显示出TiO2及Ag的特征峰,说明复合膜表面存在TiO2纳米粒子和单质银。MBR处理人工废水的实验结果表明,Ag/TiO2-PVA复合膜的跨膜压力明显低于对照组,而膜通量则明显高于对照组;膜污染阻力分析表明,Ag/TiO2-PVA复合膜对滤饼层阻力表现出很好的抑制作用;说明Ag/TiO2-PVA复合膜能明显抑制膜污染,具有较好的抗污染性能。Ag/TiO2-PVA复合膜的光催化作用,对废水中有机污染的降解有一定的强化作用,其出水COD平均值低于对照组。Ag/TiO2-PVA致密层的存在提高了无纺布的截留效率,使其出水的浊度低于也对照组。     

铁掺杂纳米二氧化钛溶胶的制备及性能研究

文章采用一种简单的方法于低温条件下制备出掺铁纳米TiO2溶胶。通过在可见光条件下对吖啶橙的光催化降解,对掺铁纳米TiO2溶胶和纳米TiO2溶胶的光催化活性进行了研究比较,结果表明掺铁纳米TiO2溶胶的光催化活性较高,铁的掺杂量为1%时光降解效果较好。     

铕掺杂纳米二氧化钛光催化实验研究

以钛酸丁酯为原料,乙醇为溶剂,硝酸为抑制剂。采用溶胶凝胶法制备纳米粒子TiO2,用30w的紫外光灯模拟光源,溴甲酚紫模拟水中难降解的有机污染物,采用稀土铕掺杂的方法来提高TiO2的活性。XRD研究结果表明,稀土铕掺杂TiO2没有改变纳米TiO2的晶相结构;光催化结果表明,稀土铕掺杂的确能较明显的提高TiO2的光催化降解能力。90min内达到降解率由80%提高到98%以上。     

低量Gd~3+掺杂TiO_2粉体的制备及催化活性

利用溶胶-凝胶法在700℃制备了纯的和不同Gd3+掺杂量的TiO2纳米粉体,并用XRD技术对样品进行了表征。研究了Gd3+掺杂量对样品相结构、晶粒尺寸和光催化降解亚甲基蓝的活性的影响,利用相结构与纳米TiO2光催化活性关系探讨了Gd3+掺杂对纳米TiO2的光催化活性。结果表明,与纯TiO2相比,适量掺杂Gd3+可以显著提高其光催化活性。当Gd3+掺杂量为0.2%(质量),TiO2复合纳米粉体的光催化活性最佳,降解率为86%,其金红石相含量为15.4%,平均晶粒粒径为15nm;Gd3+掺杂强烈地抑制TiO2由锐钛矿相向金红石相的转变、减小晶粒尺寸和晶格膨胀程度这三方面均有利于提高光催化活性。     

铁、锌、铁酸锌掺杂对纳米级二氧化钛光催化降解罗丹明B活性的影响

通过溶胶 凝胶法合成了掺杂Fe3+ 、Zn2 + 、ZnFe2 O4的纳米级TiO2 ,并进行了XRD、TEM表征 ,对罗丹明B的光催化实验表明 ,ZnFe2 O4的掺杂能明显提高TiO2 的光催化活性 ,而Zn2 + 的掺杂对TiO2 的光催化活性影响不大 ,Fe3+ 的掺杂则使TiO2 的光催化活性降低。     

锰离子掺杂纳米二氧化钛的制备及在造纸废水处理中的应用

以无机盐无水四氯化钛为原料,采用溶胶-凝胶法制备的锰离子掺杂型纳米TiO2作为光催化剂,在高压汞灯的光源照射下对河北省某造纸厂废水进行光催化降解。考察Mn2+/TiO2光催化剂的热处理温度、掺杂量、用量及溶液pH值、光照时间等因素对废水COD降解率的影响。实验结果表明:经460℃热处理1h的Mn2+/TiO2光催化效果较好,在进水ρ(COD)为400 mg/L,初始pH值为4.0、光催化剂用量1.5g/L、光照时间9h条件下,COD去除率可达80.3%。经深度处理的造纸废水,可实现达标排放。     

金属离子修饰纳米TiO2薄膜光催化降解苯酚

通过溶胶-凝胶法制备纳米TiO2薄膜，在制备过程中分别掺杂一定量的Fe^3 、Zn^2 、Pd^2 等金属离子。以高压汞灯做光源，用制得的纳米TiO2薄膜对苯酚作光催化降解实验，结果表明：掺杂Fe^3 、Zn^2 、Pd^2 的纳米TiO2催化剂光催化性能明显提高。并探讨了金属离子掺杂浓度和氧化剂对光催化的影响。     

Ag掺杂改性TiO_2催化降解水体中的邻苯二甲酸二甲酯

邻苯二甲酸酯是环境中普遍存在的有机污染物(内分泌干扰物)之一。通过湿式机械混合法制备Ag掺杂改性TiO2催化剂。光催化降解实验的结果表明Ag掺杂浓度为1×10-4mol/g,焙烧温度为400℃下所得的催化剂活性较好。对降解体系的研究表明,当催化剂的投加量为0.1~0.3 g/L、pH=5~8时降解效率较高(62.0%)。相对于催化剂的降解过程而言,其吸附作用是比较小的,而是以光催化反应为主。并利用荧光光谱对催化剂的性能进行了初步表征。     

掺入金属离子的TiO2纳米粒子光催化降解吖啶橙

利用酸催化溶胶－凝胶法（ｓｏｌ－ｇｅｌ）制备了 Ｆｅ３＋和 Ｃｒ３＋不同掺入量的 ＴｉＯ２半导体纳米粒子研究了这些纳米粒子对吖啶橙光催化氧化降解的影响．结果表明，微量 Ｆｅ３＋和 Ｃｒ３＋的掺入可明显提高 ＴｉＯ２的光催化活性．进一步研究表明，在 Ｆｅ３＋－ＴｉＯ２体系中，最佳掺入量为 ０．１％，而且中性介质和自然光有利于光催化氧化反应的进行，反应３ｈ后降解率可达９７．７５％．在Ｃｒ３＋－ＴｉＯ２体系中，弱碱性介质和自然光有利于光催化氧化反应，最佳掺入量为０．０５％，降解率可达８７．５４％．     

金属泡沫镍负载纳米TiO2光催化降解甲醛和VOCs

采用溶胶-凝胶法制备了3种掺杂金属离子的纳米TiO₂光催化剂,并将其负载于泡沫镍板上,以室内空气典型污染物甲醛和VOCs为模型反应物,研究了对甲醛和VOCs气体的光催化作用并讨论了La³⁺的最佳掺杂比例以及环境因素对光催化效率的影响.结果表明:该TiO₂催化剂具有良好的锐钛矿型结构;负载掺La 1.5%TiO₂的泡沫镍板90min对甲醛和VOCs的降解率分别为94%和87%,远高于未掺:83%和72%,掺Fe     

金属离子掺杂TiO_2薄膜光催化去除气相中甲醛

采用溶胶-凝胶法在普通玻璃表面制备TiO2,Fe3+/TiO2,La3+/TiO2三种光催化剂,研究了煅烧温度、煅烧时间、涂膜层数、Fe3+和La3+加入量等因素对光催化剂降解气相甲醛的影响。结果表明,La3+/TiO2光催化性能略好于TiO2,Fe3+/TiO2光催化性能最佳。当掺Fe3+的TiO2催化剂煅烧温度为450℃,煅烧时间为2h,Fe:T(imol)=0.3%,涂覆层数为4层,光催化反应3h,实验封闭体系中甲醛的降解率可达49.24%。     

Effect of platinum on the photocatalytic degradation of chlorinated organic compound

TiO2 nanoparticles, doped with di erent Pt contents, were prepared by a modified photodeposition method using Degussa P-25 TiO2, H2PtCl6 6H2O and methanol as the solvents. The physicochemical properties of Pt/TiO2 were investigated by the nitrogen adsorption and desorption isotherm measurement technique, X-ray di raction analysis and photoluminescence spectra, respectively. Reaction rates from photocatalytic removal of dichloromethane over Degussa P-25 TiO2 and Pt/TiO2 were evaluated. The average diameter and BET surface area of the TiO2 catalyst particles were 300 nm and 50 m2/g, respectively. The degradation e ciency was 99.0%, 82.7%, 55.2%, and 57.9% with TiO2 at inlet concentrations of 50, 100, 200, and 300 ppm, respectively. And the degradation e ciency was 99.3%, 79.7%, 76.5%, and 73.4% with a 0.005 wt.% Pt/TiO2 at inlet concentrations of 50, 100, 200, and 300 ppm, respectively. In addition, we found that the photoluminescence emission peak intensities decreased with increases in the doping amount of Pt, which indicates that the irradiative recombination was weakened. Furthermore, the results showed that the UV/0.005 wt.% Pt/TiO2 process was capable of e ciently decomposing gaseous DCM in air.     

Activated carbon supported TiO2-photocatalysis doped with Fe ions for continuous treatment of dye wastewater in a dynamic reactor

Fe-doped TiO2 coated on activated carbon (Fe-TiO2/AC, FTA) composites were prepared by an improved sol-gel method and characterized by scanning electron microscopy, X-ray photoelectron spectroscopy, X-ray di ractometry, inductively coupled plasma mass spectrometry and BET surface area analysis. Obtained FTA composites were applied to the continuous treatment of dye wastewater in a dynamic reactor. The e ects of Fe ion content, catalyst content, UV-lamp power and flowrate of the continuous treatment of dye wastewater on degradation e ciency were analyzed to determine the optimum operating conditions of dye wastewater degradation. Continuous photocatalytic experiments provided interesting results that FTA had a high chemical oxygen demand (COD) removal rate compared with TiO2, Fe doped TiO2 (FT) and TiO2 coated on activated carbon (TA). In particular, when using the FTA catalyst with a Fe ion content of 0.33%, the kinetic content (k = 0.0376) of COD removal was more than the sum of both TA (0.0205) and 0.33% FT (0.0166). FTA showed a high photoactivity because of a synergistic e ect between Fe ions and AC on TiO2, which is higher than the individual e ects of AC or Fe ions on TiO2. Additionally, for the photocatalytic degradation of dye wastewater, the optimum Fe ion content, catalyst content, UV-lamp power and flowrate were 0.33%, 6 g/L, 60 W (two lamps) and 300 mL/hr, respectively. An investigation of catalyst reuse revealed that the 0.33% FTA showed almost no deactivation in photocatalytic degradation of naturally treated wastewater.     

Synergistic photocatalytic degradation of pyridine using precious metal supported TiO2 with KBrO3

A series of precious metals catalysts （M/TiO/, M = Ru, Rh, Pd, Ag, Ir, Pt or Au） were prepared by a light deposition method and the synergistic photocatalytic degradations of pyridine （20 mg/L） under UV irradiation （365 nm） using M/TiO2 with electron capture agent KBrO3 have been investigated. The results show that KBrO3 has a greatly synergistic role on M/TiO2 and the photocatalytic activity of M/TiO2 is closely related to its work function. Ag could greatly enhance the activity of TiO2 due to the binding characteristics of pyridine on Ag. Under the conditions of 0.5 wt.% Ag loading, Ag/TiO2 concentration of 0.1 g/L, KlrO3 concentration of 10 mmol/L and reaction liquid pH value at 9, the pyridine can be degraded by 64% within 3 hr, doubled than TiO2 photocatalytic system. The degradation kinetics of pyridine follows first-order kinetics and k = 5.53 × 10-3 min^-1.