溶液中阴离子和腐殖酸对UV/H2O2降解2,4-二氯酚的影响

研究了UV/H2O2工艺对2,4-二氯酚(2,4-DCP)的去除效果和水中阴离子、腐殖酸对该工艺降解2,4-DCP的影响.结果表明:UV/H2O2工艺可以有效地去除水中2,4-DCP,光降解过程符合一级反应动力学模型;在H2O2投加量为8 mg/L、1个30 W低压汞灯照射下,2,4-DCP在蒸馏水和自来水中反应速率常数分别为0.023 2、0.016 2 min-1;NO-3、Cl-、HCO-3对2,4-DCP光降解有抑制作用,当3种阴离子摩尔浓度为0.5、10.0、20.0 mmol/L时,对2,4-DCP光降解的抑制程度为HCO-3＞NO-3＞Cl-;腐殖酸在低浓度时,促进光降解反应进行,在高浓度时,2,4-DCP的光降解受到抑制.自来水中的反应速率常数低于蒸馏水中的反应速率常数是由于水中多种阴离子和腐殖酸影响的结果.     

溶液中阴离子对UV/H2O2降解十二烷基苯磺酸钠的影响及其机理

研究了UV/H2O2工艺对十二烷基苯磺酸钠(LAS)的去除效果、溶液中阴离子对LAS降解的影响及机理.结果表明:UV/H2O2工艺可以有效地去除水中的LAS;在H2O2投加量为8 mg/L,14 W低压汞灯照射下,LAS在蒸馏水和自来水中的反应速率常数分别为0.018 0 、0.012 2 min-1;NO-3、Cl-、SO2-4和HCO-3对LAS光降解有抑制作用,当该4种离子摩尔浓度均分别为5、10、15 mmol/L时,对LAS光降解的抑制程度为HCO-3》NO-3》Cl-》SO2-4,且随着离子摩尔浓度的增大,抑制作用增强;LAS在自来水中的反应速率常数低于在蒸馏水中的反应速率常数是由于水中多种离子影响的结果.     

抗菌剂三氯卡班在水溶液中的光降解

研究了抗菌剂三氯卡班(triclocarban,TCC)在水溶液中的光降解过程及其影响因素,考察了不同光源、溶液pH值、初始TCC浓度、添加光催化剂TiO2及自然界水体中常见阴离子(如Cl-、NO-3和SO2-4)存在的影响。结果表明,TCC在紫外光照射下能进行光降解,其反应符合假一级反应动力学。pH值对TCC在紫外光下的光解过程影响显著,且其降解速率随着pH值的升高而增大。适量添加TiO2能促进TCC的光解速率。无机阴离子Cl-、NO-3和SO2-4的存在阻碍了TCC的光解。此外,还对TCC的降解机理进行了初步推测。     

三种藻类引发水中17α-乙炔基雌二醇的光降解实验研究

研究了普通小球藻、铜绿微囊藻和柱孢鱼腥藻3种藻类引发水中17α-乙炔基雌二醇(EE2)的光降解.结果表明,在250 W高压汞灯(HPML,nm)的照射下,一定藻浓度下,EE2的光降解率可达19%-20%.另外,还研究光强、藻悬浮液浓度和EE2初始浓度等对EE2光降解速率的影响,发现在本实验体系中,光通量大、藻浓度高及EE2初始浓度低有利于提高EE2的光降解速率.     

雌酮在铁(Ⅲ)-草酸盐配合物体系中的光降解

以125 W高压汞灯为光源,研究了水中雌酮(E1)在铁(Ⅲ)-草酸盐体系中的光降解;考察了初始pH值、铁(Ⅲ)/草酸盐配比、E1初始浓度对E1光降解的影响.结果表明,铁(Ⅲ)/草酸盐体系能引发E1的光降解.在pH=3.5,Fe(Ⅲ)/Ox配比为10/120μmol/L时,2 mg/L E1光照160 min可以降解59%.在pH 3～6范围内,pH为3～4时E1降解效率最高;在2～10 mg/L范围内,光降解效率随水溶液中E1初始浓度的增加而降低.     

IC反应器厌氧氨氧化启动与运行特性研究

采用一套有效容积为20 L的IC反应器,接种啤酒废水厌氧处理池污泥,保持反应器进水NH+4-N浓度为120 mg/L,NO-2-N浓度为150 mg/L,在温度为30±1 ℃的条件下,对ANAMMOX反应过程的启动和运行特性进行了研究.结果表明反应器的启动经历了污泥低负荷驯化期、负荷提高期和高负荷运行期3个阶段;在反应器运行到第130 d,反应器启动成功;NH+4-N和NO-2-N的去除率分别约82.1%和94.5%;去除的NH+4-N和NO-2-N及生成的NO-3-N三者之间的比值为11.160.3;在反应器中形成了粒径为1～2 mm的颗粒污泥.     

反硝化生物滤池用于再生水脱氮效能及动力学研究

采用反硝化生物滤池处理城市污水厂二级出水,研究了反硝化生物滤池脱氮效能及其影响因素,构建了反硝化生物滤池脱氮动力学模型。结果表明,反硝化生物滤池启动7d后出水水质稳定,对NO-3-N的去除率达到90%以上,NO-2-N积累现象消失;当外加乙酸钠作碳源并使C/N≥4.7时,对NO-3-N的去除率达到90%以上,出水NO-3-N浓度在1.0mg/L以下;反硝化生物滤池具有较高的处理负荷,当HRT≥5 min时,对NO-3-N的去除率能达到90%以上;在实验水质条件下,滤池反硝化反应遵循一级反应动力学,且反应速率常数与流速成正比。     

溶液中Fe~(2+)强化Fe~0还原NO_3~-的机制

通过不同条件下Fe0还原NO-3的研究发现,在中性条件下溶液中Fe~(2+)明显强化了Fe0对NO-3的还原,最终还原产物以NH+4-N为主,而反应过程中Fe~(2+)消耗与NO-3还原量存在明显的正相关性。在Fe~(2+)初始浓度为1~8 mmol·L-1条件下,6 g·L-1的Fe0对初始浓度为100 mg·L-1NO-3的还原符合零级反应动力学过程,结合电化学和X射线衍射分析,证明Fe~(2+)通过沉积到Fe0表面,加速了电子传递过程,促进Fe0表面活性,从而强化了Fe0对NO-3的还原。     

雌酮在铁（Ⅲ）-草酸盐配合物体系中的光降解

以125W高压汞灯为光源，研究了水中雌酮（E1）在铁（Ⅲ）-草酸盐体系中的光降解；考察了初始pH值、铁（Ⅲ）／草酸盐配比、E1初始浓度对E1光降解的影响。结果表明，铁（Ⅲ）／草酸盐体系能引发E1的光降解。在pH=3．5，Fe（Ⅲ）／Ox配比为10／120／zmol／L时，2mg／LE1光照160min可以降解59％。在pH3-6范围内，pH为3～4时E1降解效率最高；在2-10mg／L范围内，光降解效率随水溶液中E1初始浓度的增加而降低。     

生物滤池外加碳源脱氮研究

以葡萄糖、甲醇、乙醇、乙酸4种有机物为碳源,以中试二沉池出水为原水,研究了生物滤池的反硝化效能,并分析了水温和水力负荷对反硝化效果的影响.结果表明,投加4种碳源后生物滤池均能有效脱氮,对NO-3-N的去除率达67.1％～83.7％.乙酸为碳源时,NO-3-N在生物滤池内浓度下降最快;甲醇为碳源时,NO-3-N浓度下降最...     

Photodegradation of the novel fungicide fluopyram in aqueous solution: kinetics,transformation products,and toxicity evolvement

The aqueous photodegradation of fluopyram was investigated under UV light (λ?≥?200 nm) and simulated sunlight irradiation (λ?≥?290 nm). The effect of solution pH, fulvic acids (FA), nitrate (NO₃ ^?), Fe (III) ions, and titanium dioxide (TiO₂) on direct photolysis of fluopyram was explored. The results showed that fluopyram photodegradation was faster in neutral solution than that in acidic and alkaline solutions. The presence of FA, NO₃ ^?, Fe (III), and TiO₂ slightly affected the photodegradation of fluopyram under UV irradiation, whereas the photodegradation rates of fluopyram with 5 mg L^?1 Fe (III) and 500 mg L^?1 TiO₂ were about 7-fold and 13-fold faster than that without Fe (III) and TiO₂ under simulated sunlight irradiation, respectively. Three typical products for direct photolysis of fluopyram have been isolated and characterized by liquid chromatography tandem mass spectrometry. These products resulted from the intramolecular elimination of HCl, hydroxyl-substitution, and hydrogen extraction. Based on the identified transformation products and evolution profile, a plausible degradation pathway for the direct photolysis of fluopyram in aqueous solution was proposed. In addition, acute toxicity assays using the Vibrio fischeri bacteria test indicated that the transformation products were more toxic than the parent compound.     

Treatment of tannery wastewater in a pilot-scale hybrid constructed wetland system in Bangladesh

This paper reports the pollutant removal performances of a hybrid wetland system in Bangladesh for the treatment of a tannery wastewater. The system consisted of three treatment stages: a subsurface vertical flow (VF) wetland, followed by a horizontal flow (HF) and a VF wetland. The wetlands were planted with common reed (Phragmites australis), but employed different media, including organic coco-peat, cupola slag and pea gravel. In the first stage, experimental results demonstrated significant removal of ammonia (52%), nitrate (54%), BOD (78%), and COD (56%) under high organics loading rate (690 g COD m⁻² d⁻¹); simultaneous nitrification, denitrification, and organics degradation were attributed to the unique characteristics of the coco-peat media, which allowed greater atmospheric oxygen transfer for nitrification and organic degradation, and supply of organic carbon for denitrification. The second stage HF wetland produced an average PO₄ removal of 61%, primarily due to adsorption by the iron-rich cupola slag media. In the third treatment stage, which was filled with gravel media, further BOD removal (78%) from the tannery wastewater depleted organic carbon, causing the accumulation of NO₃ in the wastewater. Overall, the average percentage removals of NH₃-N, NO₃-N, BOD, COD, and PO₄ were 86%, 50%, 98%, 98% and 87%, respectively, across the whole hybrid system. The results provided a strong evidence to support widespread research and application of the constructed wetland as a low-cost, energy-efficient, wastewater treatment technology in Bangladesh.     

Photodegradation of 4-tert octylphenol in aqueous solution promoted by Fe(III)

4-Tert-octylphenol (4-t-OP), a kind of endocrine-disrupting compounds, is widely distributed in natural water surroundings but can hardly be biodegraded. The advanced oxidation processes (AOPs) have been proved to be an efficient method to degrade 4-t-OP. In this study, the photodegradation of 4-t-OP in aqueous solution promoted by Fe(III) and the photooxidation mechanism were investigated. The ferric perchlorate was added into the aqueous solution for the production of hydroxyl radical. The efficiency of mineralization was monitored by total organic carbon analyzer, and photooxidation products were determined by high-performance liquid chromatography and liquid chromatography-mass spectrometer. 4-t-OP (2.4?×?10^?5 M) in aqueous solution was completely degraded after 45 min in the presence of Fe(III) (1.2?×?10^?3 M) under UV irradiation (λ?=?365 nm). The optimal pH was 3.5. Higher Fe(III) concentration or lower initial 4-t-OP concentration led to increased photodegradation efficiency of 4-t-OP. The reaction was almost completely inhibited in the presence of 2-propanol. About 70 % mineralization of the solution was obtained after 50 h. The photooxidation product was supposed to be 4-tert-octyl catechol. 4-t-OP in aqueous solution can be degraded in the presence of Fe(III) under the solar irradiation. The photoinduced degradation is due to the reaction with hydroxyl radicals. It shows that the 4-t-OP is mineralized by the inducement of Fe(III) aquacomplexes, which exposes to solar light. Therefore, the results would provide useful information for the potential application of the AOPs to remove 4-t-OP in water surroundings.     

分段进水SBR短程生物脱氮过程中N2O产生及控制

利用SBR,控制曝气量为60 L/h,利用在线pH曲线控制曝气时间,成功实现了短程生物脱氮过程,并考察了不同进水方式下SBR运行性能及N2O产量。结果表明,分段进水能够有效降低短程生物脱氮过程中外加碳源投加量。在原水进水碳氮比较低时,采用递增进水量的进水方式,能够有效降低生物脱氮过程中NO-2积累量,从而降低系统N2O产量。1次进水、2次等量进水和2次递增进水方式下,生物脱氮过程中N2O产量分别为11.1、8.86和5.04 mg/L。硝化过程中NO-2-N的积累是导致系统N2O产生的主要原因。部分氨氧化菌(AOB)在限氧条件下以NH+4-N作为电子供体,NO-2-N作为电子受体进行反硝化,最终产物是N2O。     

固态碳源去除地下水硝酸盐的模拟实验

选取了5种研究较少的固体材料,棉花、丝瓜络、甘蔗渣、可降解餐盒、木屑作为去除地下水硝酸盐的外加碳源。在锥形瓶中进行反硝化对比实验,研究了不同固态碳源下NO3--N、NO2--N、NH4+-N及pH的变化情况,分析了NO3--N及总氮的去除率。研究结果表明,反硝化过程中pH呈升高趋势,在6.9～8.5范围内浮动。可降解餐盒和丝瓜络相对于其他的固态碳源来说,对NO3--N和总氮有较高的去除率,但丝瓜络的总氮去除率明显低于可降解餐盒。可降解餐盒的硝酸盐去除率达到98.28%,总氮去除率达到93.48%。可降解餐盒能够有效地去除地下水硝酸盐,达到以废治废的效果,是经济有效的最佳固态碳源。     

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.     

Direct and indirect photolysis of two quinolinecarboxylic herbicides in aqueous systems

The photodegradation of two quinolinecarboxylic herbicides, 7-chloro-3-methylquinoline-8-carboxylic acid (QMe) and 3,7-dichloroquinoline-8-carboxylic acid (QCl), was studied in aqueous solution at different irradiation wavelengths. The effect of sunlight irradiation was investigated also in the presence of titanium dioxide (TiO₂). UV irradiation degraded rapidly QMe affording 7-chloro-3-methylquinoline (MeQ) through a decarboxylation reaction. The reaction rate was lower in the presence of dissolved organic carbon (DOC) because of the adsorption of the herbicide on the organic components. Instead, QCl was stable under both UV light and sunlight irradiation. The irradiation of QMe or QCl solutions with simulated sunlight in the presence of TiO₂ produced the complete mineralization of the two herbicides.     

混合固定化硝化菌和好氧反硝化菌处理焦化废水

对传统的聚乙烯醇(PVA)固定化方法进行了改进,试制了加入麦秸粉末的固定化球和以活性炭纤维膜为载体膜固定化细胞产品。混合固定化硝化细菌和好氧反硝化细菌对经过厌氧折流板反应器酸化后的焦化废水进行脱氮,焦化废水在厌氧折流板反应器中经过18 h的酸化后,pH在8.0左右,开始进入好氧槽进行脱氮。在有效容积为5 L好氧槽中经过12 h的曝气处理,加入麦秸粉末的固定化球对氨氮的去除率高达94.3%;纤维膜固定化细胞产品对氨氮的去除率为85%。整个脱氮过程无NO^-₂-N和NO^-₂-N的积累,实现了好氧条件下的同时硝化和反硝化。     

基于SIMULINK的硝化反应动力学模型的仿真

利用MATLAB/SIMULINK对序批式生物膜反应器内的氨氧化细菌与亚硝酸盐氧化菌的生化反应进行仿真预测。模型的验证结果表明,适当的选择模型中的溶解氧浓度、碱度以及温度3种参数,SIMULINK仿真动力学模型能够比较准确地对氨氧化细菌与亚硝酸氧化细菌处理生活污水的过程进行仿真和预测.NH4+-N、NO2--N和NO3--N 3种基质仿真值的绝对平均误差最大为15.88,最小为1.13;NH4+-N、NO2--N和NO3--N的Nash.Suttcliffe模拟效率系数分别为99.36%、98.64%和99.25%;此外,还对SIMULINK仿真动力学模型中的溶解氧浓度、碱度以及温度进行了灵敏度分析,结果表明,温度的灵敏度最大、溶解氧次之、碱度灵敏度相对最小。     

组合阳极联合气体扩散阴极电催化降解苯胺

采用气体扩散电极为阴极,钛基氧化物（Ti／SnO2-Sb2O5-IrO2）和金属铁构成组合阳极,构建了新型电化学氧化体系用于降解有机污染物。利用该氧化体系,在不同实验条件下考察了苯胺降解的效果与降解过程的相关规律。结果表明,阴极电位、铁阳极通电时间以及苯胺初始浓度均显著影响苯胺的降解效果。当阴极电位为-0．7V,pH3．0,铁阳极通电时间20min时,电化学处理200mg／L苯胺480min,TOC的去除效率达到80．4％,矿化电流效率（MCE）为8．6％,显示了该氧化体系具有良好的有机物降解能力。此外,苯胺降解过程中氨氮和硝态氮浓度的变化表明,苯胺分子中的氮主要转化为NH4和NO3^-。