γ-射线辐照降解水中阿莫西林

研究了60Coγ-射线辐照条件下水中阿莫西林(AMX)的辐照降解,考察了AMX初始浓度、辐照剂量、p H、H2O2、自由基消除剂(碳酸氢钠和正丁醇)以及溶解氧等因素对AMX辐照降解的影响。结果表明,γ辐照可有效降解水中AMX,当AMX初始浓度为10.0 mg/L,辐照剂量为15 k Gy时,降解率达100%,随着AMX浓度增大,其降解率降低。碱性条件有利于AMX的降解,当p H为11,且辐照剂量大于10 k Gy时,AMX的降解率在90%以上。同时,加入H2O2可以促进AMX的降解;·OH自由基消除剂的存在和缺氧条件会明显抑制γ-射线对AMX的辐照降解,分析表明,AMX的降解主要是基于·OH自由基的氧化。     

铁屑还原及微波铁屑诱导氧化降解偶氮染料历程的研究

研究了铁屑内电解还原及微波诱导氧化降解偶氮染料的反应历程,采用胶束毛细管电泳法对跟踪了2种不同降解方法下的中间产物变化.实验结果表明,染料的偶氮键(-N=N-)易被铁屑内电解还原,反应过程中有中间产物苯胺生成.微波诱导铁屑氧化偶氮染料的反应过程中未检测到其他芳环类化合物生成,在微波辐照2 min时脱色率已达90%以上,TOC去除率也高达78%,矿化较为彻底;在微波辐照铁屑诱导氧化降解污染物的同时,也使铁屑自身得以活化再生,提高了铁屑的内电解能力.     

微波辐射Bi2O3/沸石-H2O2体系降解废水中的硝基苯

研究了微波辐射下，以负载于沸石上的三氧化二铋为催化剂，以双氧水为氧化剂的催化氧化体系处理硝基苯工艺。通过单因素实验法，从反应催化剂负载量、pH、双氧水用量、微波功率、反应时间、催化剂用量等方面初步考察了硝基苯在该体系中的催化氧化效果。在氧化铋负载量3%（质量比），pH=2，2 mL 30%双氧水，火力为中火，催化剂投加量为0.7 g，反应2 min，对降解过程所得的中间产物和终产物进行了分析。结果表明，该体系对硝基苯的去除率能够达到99.2%，COD去除率为73.91%。     

微波技术在污水处理中的研究进展和应用

微波技术因其独特的热效应和非热效应在水处理领域起着重要的作用。微波技术发展至今可分为4个方面:(1)微波直接辐射法处理污水;(2)微波场辅助活性炭处理污水;(3)微波与其他技术(光催化技术、金属催化剂等)联合应用处理污水;(4)微波辐照再生与制备催化剂。微波技术对各类污染物(如染料、氨氮废水、焦化废水和酚类、酸类和酯类等有机废水)的降解率影响显著。从降解效率的角度看,现代化微波工艺将朝着微波与高级氧化技术的联合应用方向发展,其联合反应机制和配套装置也有待做更多研究。     

氨的超临界水氧化研究进展

在超临界水氧化过程中,氨作为含氮有机物氧化的中间产物,其氧化是有机物在超临界水中氧化降解速率的控制步骤.综述了氧化剂、温度、过氧量、停留时间和催化剂等因素对氨的超临界水氧化降解效果的影响,并总结了目前常用的两种反应动力学模型.与双氧水或氧相比,NO-3氧化荆具有更强的氧化能力;通过提高温度、过氧量和停留时间都可以促进氨的超临界水氧化降解.在氨的超临界水氧化中,当无催化剂作用时,氨的降解率很低;加入MnO2/CeO2等催化剂,可以显著提高氨的降解率.为加快超临界水氧化法处理含氮有机废水的应用进程,未来应侧重氨氧化机制的研究和催化剂的开发.     

微波辐射Bi2O3/沸石-H2O2体系降解废水中的硝基苯

研究了微波辐射下,以负载于沸石上的三氧化二铋为催化剂,以双氧水为氧化剂的催化氧化体系处理硝基苯工艺。通过单因素实验法,从反应催化剂负载量、pH、双氧水用量、微波功率、反应时间、催化剂用量等方面初步考察了硝基苯在该体系中的催化氧化效果。在氧化铋负载量3%（质量比）,pH=2,2 mL 30%双氧水,火力为中火,催化剂投加量为0.7 g,反应2 m in,对降解过程所得的中间产物和终产物进行了分析。结果表明,该体系对硝基苯的去除率能够达到99.2%,COD去除率为73.91%。     

微波辐射Bi_2O_3/沸石-H_2O_2体系降解废水中的硝基苯

研究了微波辐射下,以负载于沸石上的三氧化二铋为催化剂,以双氧水为氧化剂的催化氧化体系处理硝基苯工艺。通过单因素实验法,从反应催化剂负载量、pH、双氧水用量、微波功率、反应时间、催化剂用量等方面初步考察了硝基苯在该体系中的催化氧化效果。在氧化铋负载量3%(质量比),pH=2,2 mL 30%双氧水,火力为中火,催化剂投加量为0.7 g,反应2 m in,对降解过程所得的中间产物和终产物进行了分析。结果表明,该体系对硝基苯的去除率能够达到99.2%,COD去除率为73.91%。     

微波/活性炭/双氧水协同降解甲基红废水的研究

对微波/活性炭/双氧水联合降解甲基红染料废水进行了研究。考察了活性炭量、双氧水量、甲基红初始浓度、微波功率、pH以及处理时间等因素对甲基红降解效果的影响。结果表明，对于100 mL 100 mg/L甲基红溶液，当加入0.5 g活性炭，1 mL 30%H₂O₂，调节微波功率至680 W，反应25 min后，甲基红降解率达到81.87%。通过对比试验，发现微波、活性炭及双氧水对甲基红的降解起协同作用。     

微波辅助Pb/ZrO_x光催化降解水中的对硝基苯酚

采用十六烷基三甲基溴化铵(CTAB)辅助水热法制备了适用于微波辅助光催化体系的高效Pb/ZrO_x催化剂,并对其进行了XRD、XPS、BET和SEM等表征,其XPS结果显示在Pb/ZrO_x表面,Zr以+2、+3和+4三种价态共存。考察了微波辅助光催化氧化(MW/PC)对硝基苯酚(PNP)过程中,微波辐照功率、催化剂投加量、溶液初始pH和PNP初始浓度对PNP去除效果的影响,得到最优操作条件为,PNP初始pH值为5,催化剂投加量为1.0 g·L~(-1),微波辐照功率为200 W。此条件下,初始浓度为50 mg·L~(-1)的PNP溶液反应12min后,PNP转化率达95%,TOC去除约70%。并且,Pb/ZrO_x能够在重复使用5次的情况下仍保持较好的活性。比较了MW、PC和MW/PC 3种体系,得到MW/PC体系将PNP去除率从单独PC体系的48%提高至95%。微波与紫外光存在良好的协同作用,MW/PC能够快速、高效去除水中PNP,为微波辅助光催化氧化去除污染物提供理论基础。     

微波辅助Cu(Ⅱ)-Fenton体系催化氧化处理对硝基苯酚废水

为了拓宽Fenton反应pH范围,提高降解效率、减少药剂用量,向Fenton体系中添加辅助催化剂Cu(Ⅱ),并对微波辅助催化氧化对硝基苯酚(PNP)模拟废水工艺进行了研究。提出微波辐照-放置处理工艺,并与普通全过程微波处理工艺进行了比较。结果表明,该体系处理工艺将Fenton反应最佳pH范围由2.0~3.5拓宽到2.0~5.5;在pH=5.0时,对于100 mg/L的PNP溶液,当[Cu2+]=0.8 mg/L、[Fe2+]=3.0 mg/L、[H2O2]=0.2 g/L,微波功率250 W,辐照2.0 min、放置4.0 min,PNP去除率可达98%以上;辅助催化剂Cu2+的加入增强了氧化效果,同时节约药品20%以上。通过对比实验发现,Cu2+与Fe2+发生了某种作用机制,联合促进了体系中·OH的生成。该反应体系不仅将传统Fenton反应体系狭窄的pH值范围延伸到接近中性的区域5.0~5.5,又可在短时间内使PNP去除率达到98%以上。     

Photocatalytic Degradation of an Organophosphorus Pesticide Phosalone in Aqueous Suspensions of Titanium Dioxide

Abstract

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).     

Photooxidative removal of the herbicide Acid Blue 9 in the presence of hydrogen peroxide: modeling of the reaction for evaluation of electrical energy per order (EEO)

The present work deals with photooxidative removal of the herbicide, Acid Blue 9 (AB9), in water in the presence of hydrogen peroxide (H₂O₂) under UV light illumination (30 W). The influence of the basic operational parameters such as amount of H₂O₂, irradiation time and initial concentration of AB9 on the photodegradation efficiency of the herbicide was investigated. The degradation rate of AB9 was not appreciably high when the photolysis was carried out in the absence of H₂O₂ and it was negligible in the absence of UV light. The photooxidative removal of the herbicide was found to follow pseudo-first-order kinetic, and hence the figure-of-merit electrical energy per order (E_Eo) was considered appropriate for estimating the electrical energy efficiency. A mathematical relation between the apparent reaction rate constant and H₂O₂ used was applied for prediction of the electricity consumption in the photooxidative removal of AB9. The results indicated that this kinetic model, based on the initial rates of degradation, provided good prediction of the E_Eo values for a variety of conditions. The results also indicated that the UV/H₂O₂ process was appropriate as the effective treatment method for removal of AB9 from the contaminated wastewater.     

Photocatalytic degradation of the herbicide pendimethalin using nanoparticles of BaTiO3/TiO2 prepared by gel to crystalline conversion method: A kinetic approach

Photocatalytic degradation of the herbicide, pendimethalin (PM) was investigated with BaTiO₃/TiO₂ UV light system in the presence of peroxide and persulphate species in aqueous medium. The nanoparticles of BaTiO₃ and TiO₂ were obtained by gel to crystallite conversion method. These photo catalysts are characterized by energy dispersive x-ray analysis (EDX), scanning electron microscope (SEM), x-ray diffraction (XRD), and Brunauer-Emmett-Teller (BET) adsorption isotherm and reflectance spectral studies. The quantum yields for TiO₂ and BaTiO₃ for the degradation reactions are 3.166 Einstein m^?2 s^?1 and 2.729 Einstein m^?2 s^?1 and catalytic efficiencies are 6.0444 × 10^?7 mg^?2h^?1L² and 5.403 × 10^?7 mg^?2h^?1L², respectively as calculated from experimental results. BaTiO₃ exhibited comparable photocatalytic efficiency in the degradation of pendimethalin as the most widely used TiO₂ photocatalyst. The persulphate played an important role in enhancing the rate of degradation of pendimethalin when compared to hydrogen peroxide. The degradation process of pendimethalin followed the first-order kinetics and it is in agreement with Langmuir-Hinshelwood model of surface mechanism. The reason for high stability of pendimethalin for UV-degradation even in the presence of catalyst and oxidizing agents were explored. The higher rate of degradation was observed in alkaline medium at pH 11. The degradation process was monitored by spectroscopic techniques such as ultra violet-visible (UV-Vis), infrared (IR) and gas chromatography mass spectroscopy (GC-MS). The major intermediate products identified were: N-propyl-2-nitro-6-amino-3, 4-xylidine, (2, 3-dimethyl-5-nitro-6-hydroxy amine) phenol and N-Propyl-3, 4-dimethyl-2, 6-dinitroaniline by GC-MS analysis and the probable reaction mechanism has been proposed based on these products.     

Treatment of polychlorinated biphenyls in two surface soils using catalyzed H₂O₂ propagations

Two surface soils contaminated with polychlorinated biphenyls (PCBs) collected from Superfund sites in the New England region of the United States, Fletcher Paints and Merrimack Industrial Metals, were evaluated for field treatment at the bench level using catalyzed H₂O₂ propagations (CHP—modified Fenton’s reagent). The two soils were first evaluated for the potential for in situ treatment based on two criteria: (1) temperature (<40 °C after CHP reagent addition), and (2) hydrogen peroxide longevity (>24 h). In situ CHP remediation was more applicable to the Fletcher soil, while the Merrimack soil was better suited to ex situ treatment based on temperature increases and hydrogen peroxide lifetimes. Using the highest hydrogen peroxide concentrations appropriate for in situ treatment in each soil, PCB destruction was 94% in the Fletcher soil but only 48% in the Merrimack soil. However, 98% PCB destruction was achieved in the Merrimack soil using conditions more applicable to ex situ treatment (higher hydrogen peroxide concentrations with temperatures >40 °C). Analysis of degradation products by gas chromatography/mass spectroscopy showed no detectable chlorinated degradation products, suggesting that the products of PCB oxidation were rapidly dechlorinated and degraded. The results of this research document that the two PCB-contaminated soils studied can be effectively treated using aggressive CHP conditions, and that such a detailed bench study provides important information before implementing field treatment.     

TiO2/Ni PECO体系降解DMP的动力学和光电协同作用研究

以采用微波辅助法制备的TiO₂/Ni光电极为阳极，纤维状石墨毡材料(graphite felt,GF)为阴极，饱和甘汞电极(saturated calomel electrode, SCE)为参比电极建立TiO₂/Ni 光电催化氧化（PECO）体系。以邻苯二甲酸二甲酯（dimethy phthalate,DMP）为目标物，研究其光电催化降解反应动力学和光电协同作用。结果显示：DMP的降解符合拟一级动力学规律；当DMP初始浓度一定时，影响DMP光电催化降解速率的因素由强到弱依次为：催化剂有效面积，紫外光强度，曝氧速率，外加偏转电压等。实验证明本体系中光电之间具有协同作用。     

Carbofuran removal in continuous-photocatalytic reactor: Reactor optimization,rate-constant determination and carbofuran degradation pathway analysis

Carbofuran (CBF) removal in a continuous-flow photocatalytic reactor with granular activated carbon supported titanium dioxide (GAC-TiO₂) catalyst was investigated. The effects of feed flow rate, TiO₂ concentration and addition of supplementary oxidants on CBF removal were investigated. The central composite design (CCD) was used to design the experiments and to estimate the effects of feed flow rate and TiO₂ concentration on CBF removal. The outcome of CCD experiments demonstrated that reactor performance was influenced mainly by feed flow rate compared to TiO₂ concentration. A second-order polynomial model developed based on CCD experiments fitted the experimental data with good correlation (R² ～ 0.964). The addition of 1 mL min^?1 hydrogen peroxide has shown complete CBF degradation and 76% chemical oxygen demand removal under the following operating conditions of CBF ～50 mg L^?1, TiO₂ ～5 mg L^?1 and feed flow rate ～82.5 mL min^?1. Rate constant of the photodegradation process was also calculated by applying the kinetic data in pseudo-first-order kinetics. Four major degradation intermediates of CBF were identified using GC-MS analysis. As a whole, the reactor system and GAC-TiO₂ catalyst used could be constructive in cost-effective CBF removal with no impact to receiving environment through getaway of photocatalyst.     

掺Al-TiO2改性膨润土去除微污染水中COD和NH4-N

采用掺Al-TiO2作为改性剂制备改性膨润土,考察了微波辐射功率、辐射时间、TiO2改性剂用量、铝盐掺杂量、pH值对微污染水中COD和NH4-N去除效果的影响。实验表明,微波辐射功率为460 W,辐射时间为8 min,TiO2改性剂用量为1.3 mmol/g,铝盐掺杂量为0.2 mmol/g为最佳制备条件。pH值为6.0,改性膨润土投加量为40 mg/L,沉淀时间为30min时,对微污染水中初始浓度15 mg/L的COD和5 mg/L的NH4-N去除率分别达到92%和59%以上。     

O3/H2O2处理嘧啶废水的研究

采用O3/H2O2法对嘧啶废水进行处理,考察了不同反应条件对嘧啶和COD去除率的影响,并对O3/H2O2降解嘧啶的反应机制和动力学进行了初步探讨.实验结果表明,在pH值为11,反应时间为70 min,O3流量为4g/h,H2O2投加量为50 mmol/L的条件下,废水的嘧啶和COD的去除率分别达到86.46%和74.9...     

Photocatalytic removal of organic pollutants in aqueous solution by Bi(4)Nb(x)Ta((1-x))O(8)I

In this work, Bi₄Nb_xTa_(1−x)O₈I photocatalysts have been synthesized by solid state reaction method and characterized by powder X-ray diffraction, scanning electron microscope and UV-Vis near infrared diffuse reflectance spectroscopy. The photocatalytic activity of these photocatalysts was evaluated by the degradation of methyl orange (MO) in aqueous solutions under visible light, UV light and solar irradiation. The effects of catalyst dosage, initial pH and MO concentration on the removal efficiency were studied, and the photocatalytic reaction kinetics of MO degradation as well. The results indicated that Bi₄Nb_xTa_(1−x)O₈I exhibited high photocatalytic activity for the removal of MO in aqueous solutions. For example, the removal efficiency of MO by Bi₄Nb_0.1Ta_0.9O₈I was as high as 92% within 12 h visible light irradiation under the optimal conditions: initial MO concentration of 5-10 mg L⁻¹, catalyst dosage of 6 g L⁻¹ and natural pH (6-8), the MO molecules could be completely degradated by Bi₄Nb_0.1Ta_0.9O₈I within 40 min under UV light irradiation, and the photodegradation efficiency reaches to 60% after 7 h solar irradiation. Furthermore, the photocatalytic degradation of Bisphenol A (BPA) was also investigated under visible light irradiation. It is found that 99% BPA could be mineralized by Bi₄Nb_0.1Ta_0.9O₈I after 16 h visible light irradiation. Through HPLC/MS, BOD, TOC, UV-Vis measurements, we determined possible degradation products of MO and BPA. The results indicated that MO was degradated into products which are easier to be biodegradable and innocuous treated, and BPA could be mineralized completely. Furthermore, the possibility for the photosensitization effect in the degradation process of MO under visible light irradiation has been excluded.