Catalytic activity of cerium-doped Ru/AlO during ozonation of dimethyl phthalate

In this paper, factors influencing the mineralization of dimethyl phthalate (DMP) during catalytic ozonation with a cerium-doped Ru/Al₂O₃ catalyst were studied. The catalytic contribution was calculated through the results of a comparison experiment. It showed that doping cerium significantly enhanced catalytic activity. The total organic carbon (TOC) removal over the doped catalyst at 100 min reached 75.1%, 61.3% using Ru/Al₂O₃ catalyst and only 14.0% using ozone alone. Catalytic activity reached the maximum when 0.2% of ruthenium and 1.0% of cerium were simultaneously loaded onto Al₂O₃ support. Results of experiments on oxidation by ozone alone, adsorption of the catalyst, Ce ion’s and heterogeneous catalytic ozonation confirmed that the contribution of heterogeneous catalytic ozonation was about 50%, which showed the obvious effect of Ru–Ce/Al₂O₃ on catalytic activity.     

Removal of elemental mercury with Mn/Mo/Ru/Al2O3 membrane catalytic system

In this work, a catalytic membrane using Mn/Mo/Ru/Al₂O₃ as the catalyst was employed to remove elemental mercury (Hg⁰) from flue gas at low temperature. Compared with traditional catalytic oxidation (TCO) mode, Mn/Al₂O₃ membrane catalytic system had much higher removal efficiency of Hg⁰. After the incorporation of Mo and Ru, the production of Cl₂ from the Deacon reaction and the retainability for oxidants over Mn/Al₂O₃ membrane were greatly enhanced. As a result, the oxidization of Hg⁰ over Mn/Al₂O₃ membrane was obviously promoted due to incorporation of Mo and Ru. In the presence of 8 ppmv HCl, the removal efficiency of Hg⁰ by Mn/Mo/Ru/Al₂O₃ membrane reached 95% at 423 K. The influence of NO and SO₂ on Hg⁰ removal were insignificant even if 200 ppmv NO and 1000 ppmv SO₂ were used. Moreover, compared with the TCO mode, the Mn/Mo/Ru/Al₂O₃ membrane catalytic system could remarkably reduce the demanded amount of oxidants for Hg⁰ removal. Therefore, the Mn/Mo/Ru/Al₂O₃ membrane catalytic system may be a promising technology for the control of Hg⁰ emission.     

TiO2/浮石光催化降解水中邻苯二甲酸二甲酯

采用溶胶.凝胶法制备,TiO2/浮石催化剂,光催化氧化水中内分泌干扰物邻苯二甲酸二甲酯(DMP).考察催化剂用量、pH值对降解率的影响;同时分析降解动力学和有机物矿化程度.结果表明,催化剂最佳投放量为40 g·L-1,最佳pH为6.5.在最佳条件下,DMP初始质量浓度20.0 mg·L-1,5 h DMP降解率达90%以上.降解速率符合准一级动力学方程,动力学方程为:Ln(p0/p)=0.470t-0.050,速率常数=0.470h-1.考察降解过程水样的矿化程度,前4 h矿化率没有明显变化,4 h后矿化率逐渐加快,7 h矿化率达到70%.TiO2/浮石具有成本低、易回收利用、能充分与被降解物接触等优势,用于治理水体中DMP具有一定的实际可行性.     

Catalytic ozonation performance and surface property of supported Fe3O4 catalysts dispersions

Fe₃O₄ was supported on mesoporous Al₂O₃ or SiO₂ (50 wt.%) using an incipient wetness impregnation method, and Fe₃O₄/Al₂O₃ exhibited higher catalytic efficiency for the degradation of 2,4-dichlorophenoxyacetic acid and para-chlorobenzoic acid aqueous solution with ozone. The effect and morphology of supported Fe₃O₄ on catalytic ozonation performance were investigated based on the characterization results of X-ray diffraction, X-ray photoelectron spectroscopy, BET analysis and Fourier transform infrared spectroscopy. The results indicated that the physical and chemical properties of the catalyst supports especially their Lewis acid sites had a significant influence on the catalytic activity. In comparison with SiO₂, more Lewis acid sites existed on the surface of Al₂O₃, resulting in higher catalytic ozonation activity. During the reaction process, no significant Fe ions release was observed. Moreover, Fe₃O₄/Al₂O₃ exhibited stable structure and activity after successive cyclic experiments. The results indicated that the catalyst is a promising ozonation catalyst with magnetic separation in drinking water treatment.     

Photocatalytic degradation of chlorophenols using Ru(bpy) 3 2+ /S2O 8 2−

Advanced oxidation processes, such as photocatalysed oxidation, provide an important route for degradation of wastes. In this study, the lowest excited state (³MLCT) of Ru(bpy)₃²⁺ is used to break down chlorophenol pollutant molecules to harmless products. This has the advantage of using visible light and a short-lived catalytically active species. Photolysis of deaerated aqueous solutions of a variety of mono- and poly-substituted chlorophenols has been followed in the presence of Ru(bpy)₃²⁺/S₂O₈²⁻ with near visible light (λ > 350 nm) by UV/visible absorption spectroscopy, luminescence, potentiometry, NMR and HPLC techniques. Upon irradiation, a decrease is observed in the chlorophenol concentration, accompanied by the formation of Cl⁻, H⁺ and SO₄²⁻ ions as the main inorganic products. Benzoquinone, phenol, dihydroxybenzenes and chlorinated compounds were the dominant organic products. As the ruthenium(II) complex is regenerated in the reaction, the scheme corresponds to an overall catalytic process. The kinetics of the rapid chlorophenol photodechlorination has been studied, and are described quite well by pseudo-first order behaviour. Further studies on this were made by following Cl⁻ release with respect to the initial Ru(bpy)₃²⁺ and S₂O₈²⁻ concentrations. A comparison is presented of the photodechlorination reactivity of the mono and polychlorophenols studied at acidic and alkaline pH.     

Catalytic ozonation of organic compounds in water over the catalyst of RuO2/ZrO2-CeO2

This research investigates the performances of RuO₂/ZrO₂-CeO₂ in catalytic ozonation for water treatment. The results show that RuO₂/ZrO₂-CeO₂ was active for the catalytic ozonation of oxalic acid and possessed higher stability than RuO₂/Al₂O₃ and Ru/AC. In the catalytic ozonation of dimethyl phthalate (DMP), RuO₂/ZrO₂-CeO₂ did not enhance the DMP degradation rate but significantly improved the total organic carbon (TOC) removal rate. The TOC removal in catalytic ozonation was 56% more than that in noncatalytic ozonation. However this does not mean the catalyst was very active because the contribution of catalysis to the overall TOC removal was only 30%. The adsorption of the intermediates on RuO₂/ZrO₂-CeO₂ played an important role on the overall TOC removal while the adsorption of DMP on it was negligible. This adsorption difference was due to their different ozonation rates. In the catalytic ozonation of disinfection byproduct precursors with RuO₂/ZrO₂-CeO₂, the reductions of the haloacetic acid and trihalomethane formation potentials (HAAFPs and THMFPs) for the natural water samples were 38%–57% and 50%–64%, respectively. The catalyst significantly promoted the reduction of HAAFPs but insignificantly improved the reduction of THMFPs as ozone reacts fast with the THMs precursors. These results illustrate the good promise of RuO₂/ZrO₂-CeO₂ in catalytic ozonation for water treatment.     

还原温度对Pd-CeO2/Al2O3催化剂加氢脱硫性能的影响

采用浸渍法制备CeO2改性的Pd/Al2O3加氢脱硫催化剂,考察了还原温度和还原-氧化预处理对Pd/Al2O3和Pd-CeO2/Al2O3催化剂加氢脱硫性能的影响.结果表明,Pd/Al2O3的活性受还原温度的影响很小.Pd-CeO2/Al2O3还原温度的升高使CeO2发生迁移,导致催化剂表面Pd原子数减少,同时削弱了Pd-Ce界面效应,从而使催化剂的活性降低.还原-氧化预处理使Pd-CeO2/Al2O3的活性有较大提高,预处理能促使Pd的再分散,增加了对H2的吸附活化能力,在Pd-Ce的界面效应共同作用下使催化剂拥有较高的活性.     

过渡金属对Pt Rh Pd/Al2O3催化剂性能的影响

研究了过渡金属(重点考察了铜)对Pt Rh Pd／Al2O3催化剂尾气净化效能的影响,并应用XRD,TPD,TPR等手段对过渡金属在Pt Rh Pd／Al2O3催化剂中的作用机制进行了探讨．结果表明,过渡金属对Pt Rh Pd／Al2O3催化剂具有较大的改性作用,过渡金属与混合贵金属产生的协同效应有利于催化剂活性的提高．     

Role of Rh promoter on increasing stability of Au/Al2O3 catalyst for CO oxidation at low temperature

The Au/Al₂O₃ and Au–Rh/Al₂O₃ catalysts were prepared by deposition–precipitation. The promotional effect of Rh on the performance of the Au/Al₂O₃ catalyst for CO oxidation was studied. The results indicate that using Au/Al₂O₃ catalyst, CO can be completely oxidized at 0°C or much lower temperature but the catalyst deactivated very fast. Rh can improve the stability of Au/Al₂O₃ catalyst more than 10 times, which gives an important hint to develop high stable catalyst for CO oxidation at low temperature.     

The effect of preparation conditions of Pt/Al2O3 on its catalytic performance for the H2-SCR in the presence of oxygen

Selective catalytic reduction of NO _x by H₂ in the presence of oxygen has been investigated over Pt/ Al₂O₃ catalysts pre-treated under different conditions. Catalyst preparation conditions exert significant influence on the catalytic performance, and the catalyst pre-treated by H₂ or H₂ then followed by O₂ is much more active than that pre-treated by air. The higher surface area and the presence of metallic Pt over Pt/Al₂O₃ pre-treated by H₂ or pretreated by H₂ then followed by O₂ can contribute to the formation of NO₂, which then promotes the reaction to proceed at low temperatures.     

CO2和O3体积分数升高对银杏希尔反应活力和叶绿体ATP酶活性的影响

近年来,随着温室气体体积分数不断上升,研究CO2和O3体积分数升高对植物的影响已取得一定进展,但二者对植物的复合作用及生理研究不够深入。文章利用开顶式气室研究了大气CO2和O3体积分数升高对银杏(Ginkgo biloba L.)光合特性的影响。结果表明,在整个生长季内,与对照相比,在大气CO2体积分数为700×10-6条件下,银杏叶片净光合速率显著增加(P<0.05),希尔反应活力增大,Ca2 /Mg2 -ATPase活性增强,光合产物可溶性糖和淀粉含量增多;而在O3体积分数为80×10-9的情况下,银杏叶片净光合速率下降,希尔反应活力减小,Ca2 /Mg2 -ATPase活性减弱,光合产物可溶性糖和淀粉含量减少;在CO2和O3复合作用(700×10-6 80×10-9)条件下,银杏叶片净光合速率、希尔反应活力、可溶性糖和淀粉均有所增加,且淀粉含量增加极显著(P<0.01),而Ca2 -ATPase活性先增强后减弱,Mg2 -ATPase活性先减弱后增强。说明CO2可缓解O3对银杏的负效应,而O3亦对CO2的正效应有削弱作用。     

磁性Fe3O4/石墨烯异质结固定漆酶特性及其对水中双酚A的降解研究

以磁性石墨烯为载体制备了磁性石墨烯固定化漆酶,考察了固定化漆酶的酶学特性及其对双酚A（BPA）的降解效能。结果表明,氧化石墨烯的比表面积高达726.34 m2·g-1,与游离漆酶相比,经过石墨烯固定化后漆酶对酸的适应能力、耐热性和贮存稳定性均有所提高,pH值2.0~4.0范围内固定化漆酶活性较为稳定;加入变性剂尿素（1 mol·L-1）后,固定化漆酶的相对活性为87%,游离漆酶相对活性仅为63.02%,固定化导致抗变性剂能力增强。固定化漆酶和游离漆酶活性分别在45和40℃时达到最大值。与游离漆酶相比,固定化漆酶最佳反应温度升高了5℃,且在50℃时,固定化漆酶的相对活性依然保持在95.11%;25℃,pH值4.0条件下保存10 d,固定化漆酶活性为最初活性的82.57%;固定化漆酶具有良好的重复利用性,重复利用10次后,漆酶活性仍为最初活性的82.01%。固定化酶的米氏常数Km为5.38×10-4 mol·L-1,较游离酶的大,说明固定化酶与底物的亲和力比游离酶小。磁性石墨烯固定化漆酶具有良好的吸附能力,可吸附-催化氧化水中的 BPA,且石墨烯良好的吸附作用促进了催化反应,水中BPA质量浓度为15 mg·L-1时,经过18 h反应,BPA的去除率能达到82.14%左右。本研究的结果为石墨烯新型材料固定化漆酶及其应用提供了参考。     

V2O5/AC催化剂对氨还原NO的研究

考察了V2O5/AC催化剂对NH3选择催化还原NO的影响，结果表明，以浓硝酸预氧化处理的活性焦为载体对催化剂活性有很大提高，这是由于浓硝酸预氧化后，活性焦表面产生了较多的含氧官能团可能吸附更多的NH3,并且提高了活性组分V2O5的含量，反应气氛中加入SO2后，二都活性都增加，但差异消失，这是由于SO2存在时，反应生成的SO4^2-离子的酸性强于浓硝酸预氧化产生的含氧官能团的酸性，催化剂在使用前经过煅烧和氧化对催化剂活性有很大改善。SO2存在时，V2O5含量为1wt%的催化剂活性提高。     

Fe2O3/AC脱除煤气中的Hg0

利用固定床反应器在模拟煤气条件下研究了活性焦(AC)负载Fe_2O_3催化剂(Fe_2O_3/AC)对气态Hg~0的脱除,考察了Fe_2O_3负载、煅烧温度、空速、Hg~0浓度、H_2S等对Fe_2O_3/AC催化剂脱除Hg~0的影响及Fe_2O_3/AC催化剂的再生性能,采用扫描电镜(SEM)表征了Fe_2O_3在Fe_2O_3/AC上的分布状态.结果表明,Fe_2O_3/AC具有较高的脱除Hg~0能力,明显高于载体AC,主要缘于Fe_2O_3对Hg~0的催化氧化作用.Fe_2O_3/AC催化剂上负载的活性组分Fe_2O_3并不是均匀的分布在载体AC表面上,而是成块簇状分布状态.300℃煅烧温度下制备的Fe_2O_3/AC催化剂脱除Hg~0的能力最高.在5000—15000 h~(-1)的空速和21—200μg·m~(-3)的Hg~0浓度范围内,Fe_2O_3/AC催化剂具有良好的脱除Hg~0的能力.H_2S与Hg~0在Fe_2O_3活性位上存在竞争吸附、反应会降低Fe_2O_3/AC对Hg~0的脱除能力,但H_2S反应生成的单质S和FeS_x又可促进Hg~0的脱除.脱除Hg~0后的Fe_2O_3/AC催化剂可进行再生,再生后Fe_2O_3/AC仍具有良好的脱除Hg~0的能力.