Na型粉末树脂回收废水中低浓度氨氮

为探究Na型粉末树脂回收废水中低浓度氨氮的可行性,分别采用静态摇瓶与动态树脂柱方法进行实验研究。结果表明:预处理仅使粉末树脂吸附氨氮的能力降低了5%;在中性与酸性条件下,Na型粉末树脂对低浓度氨氮去除率均可达到99%;每增加2 g·L~(-1)树脂投加量,氨氮去除率会提高20%,但吸附容量下降2.85 mg·g~(-1);钙镁离子的存在会降低Na型粉末树脂对氨氮的吸附容量,最大降低量为3.5 mg·g~(-1);由于钾离子与氨氮为同价离子,其影响不显著。Na型粉末树脂对氨氮的吸附符合Langmuir吸附等温线,吸附过程符合准二级动力学。根据实验结果,Na型粉末树脂静态运行方式适用于低浓度氨氮的回收,但动态运行方式下粉末树脂达到吸附饱和时间更短,因此,需要对运行方式进一步研究。     

Maximum nitrogen removal in the step-feed activated sludge process.

This paper presents a mathematical framework that can be used to determine the flow distributions for a step-feed activated sludge process that result in maximum nitrogen removal. The model indicates that nitrogen removal efficiency in a step-feed activated sludge process is highly dependent on the ultimate biochemical oxygen demand (BOD(L))-to-total Kjeldahl nitrogen (TKN) ratio of the wastewater. For typical domestic wastewater, which has a relatively high BOD(L)-to-TKN ratio, the step-feed process will outperform the Modified Ludzack-Ettinger process for nitrogen removal, when the flow to each step is optimally distributed. Using plant-specific water quality data and operating conditions from a 1-year period, nitrogen removal performance for four step-feed activated sludge plants operated by the Sanitation Districts of Los Angeles County (California) was calculated using the developed model. The calculated nitrogen removal efficiencies match well with the actual plant performance data. These results validate the model as a useful tool for predicting nitrogen removal in a step-feed activated sludge process. Other analyses revealed that improvements in nitrogen removal at existing facilities are achievable by adjusting the split of primary effluent flow to each anoxic zone several times during the day. The timing of the adjustments and the optimal flow splits can be determined from data on diurnal fluctuations in BOD(L) and TKN concentrations. An example is provided to illustrate the application of such an operating strategy and the potential enhancement of nitrogen removal.     

Quantification of the dissolved organic matter effect on the sorption of hydrophobic organic pollutant: application of an overall mechanistic sorption model

This study presents an overall sorption model to estimate the sorption equilibrium coefficients of hydrophobic organic pollutants for heterogeneous aquatic systems. This proposed model combines a series of sorption equilibrium relationships including the adsorption of dissolved organic matters on particulates, the binding between organic pollutants and dissolved organic matters, and the sorption of organic pollutants on particulates with or without the presence of dissolved organic matters. By using this model, variations among the sorption equilibrium coefficients with the concentrations of dissolved organic matters are obtained. Also discussed herein are case studies involving pollutants having a wide spectrum of K(ow)s, different types of dissolved organic matters, different pH values and ionic strengths. In most of the case studies, the sorption equilibrium coefficients initially increase with the-concentrations of dissolved organic matters and, then, decrease after reaching a maximum value. This study also addresses the relative errors of partition coefficients attributed to the negligence of the effect caused by the dissolved organic matter, the so-called third-phase effect.     

Mechanical Properties and Isothermal Crystallization Behaviour of Poly(lactide)/Poly(methyl methacrylate)/α-Cellulose Composites

Polylactide (PLA)/polymethylmethacrylate (PMMA)/α-cellulose composites were fabricated using a twin-screw extruder. During fabrication, α-cellulose short fibres were incorporated for improving the toughness of the brittle PLA and a chain extender was used for reducing PLA hydrolysis. Highly transparent PLA and PMMA were blended to obtain miscible and transparent blends. For evaluating the performance of the PLA/PMMA/α-cellulose composites, a series of measurements, including tensile and Izod impact tests, light transmission and haze measurements, thermomechanical analysis, and determination of isothermal crystallisation behaviour, was conducted. Adding the chain extender considerably reduced the occurrence of hydrolytic degradation. Both the chain extender and α-cellulose short fibres increased the elongation at break and Izod impact strength of the composites. Compared with the neat PLA, including 1.0 wt% α-cellulose short fibres increased the elongation at break and Izod impact strength of the composite PLA by approximately 211 and 219 %, respectively. According to the observed mechanical performance, the optimal blending ratios for PLA and PMMA were between 90:10 and 80:20. The total light transmittance of the composites was as high as 91 %, indicating that the PLA/PMMA blend was highly miscible. The haze value of the PLA/PMMA/α-cellulose composites was lower than 32 %. Incorporating cellulose short fibres increased the number of crystallisation sites and crystallinity of the PLA/PMMA/α-cellulose composites while reducing the spherulite dimensions.     

Agricultural pesticide residues in farm ditches of the Lower Fraser Valley, British Columbia, Canada

Transient and permanent farm ditches flowing to the Lower Fraser River tributary fish streams of British Columbia, Canada, were sampled at several locations in 2003-2004 to determine the occurrence and concentration of residues of selected pesticides, their transformation products, and soluble/extractable Cu++ ions. Of the 43 compounds analyzed, 28 and 22 pesticides were detected in transient farm ditch water and sediments, respectively. About 34% fewer pesticides, however, were found in both matrices of permanent farm ditches. Average concentrations (microg L(-1)) of those most frequently detected in permanent farm ditch water were atrazine (0.20), alpha -chlordane (0.06), desethylatrazine (0.13), diazinon (0.55), dieldrin (0.28), endosulfan sulfate (0.16), glyphosate (6), metalaxyl (0.27); and soluble Cu++ ions (25). Those most often found in ditch sediments (microg kg(-1)) were aminomethylphosphonic acid (AMPA) (2,300), 1,1,1-trichloro-2,2-bis-(4-chlorophenyl)ethane (DDT) (250), endosulfan sulfate (500), glyphosate (1,225); and extractable Cu++ ions (58,000). The risk potential of these pesticide residues to non-target aquatic organisms inhabiting Fraser River tributary fish streams contiguous to permanent farm ditches is evaluated and discussed.     

Degradation of carbofuran in water by solar photocatalysis in presence of photosensitizers

The effect of the presence of photosensitizers, methylene blue (MB) and rose Bengal (RB), on the degradation of carbofuran (2,3-dihydro-2,2-dimethylbenzofuran-7-yl methylcarbamate) in water in a solar photocatalytic system was investigated. It was found that as compared to MB, RB generally showed a stronger effect on the decomposition of carbofuran under comparable conditions. Among the conditions studied, adding 2 x 10(-6) M of RB, that corresponding to 2% of the initial concentration of carbofuran solution in the system, rendered the most effective degradation of carbofuran. As a result, a carbofuran removal percentage of 69.9%, a mineralization efficiency of 28.0%, and a microtoxicity reduction of 65.0% could be achieved. The degradation and mineralization of carbofuran was found to follow the pseudo-first order reaction kinetics. The decomposition mechanism of carbofuran was further investigated through identification of the intermediates to elaborate the influence of dye photosensitizer on the solar photocatalysis of carbofuran in water. On the basis of the intermediates identified, including carbofuran phenol, 3-hydroxy carbofuran phenol, and substituted alcohols (3-phenoxy 1-propanol, 2-ethyl 1-hexanol, 2-butoxyl ethanol), it appears that hydrolysis and hydroxylation were the two key mechanisms for decomposing carbofuran during the process of solar photocatalysis with the aid of dye photosensitizer.     

一、二次风配比对75t/h循环流化床的影响

本文利用FLUENT模拟软件对75t/h循环流化床进行数值模拟,研究了一、二次风配比(5∶5、5.5∶4.5和6∶4)对炉内温度场、速度场和CO2分布的影响,发现一、二次风配比为5.5∶4.5时,循环流化床运行较优,炉内温度场较均匀,且基本能达到规定运行温度,速度分布均匀,炉内烟气流速较高,出口烟气速度分别比1、3#工况要高33.42％和13.70％,炉内CO2分布较优,旋风分离器具有很高的工作效率.     

基于群决策和层次分析法的长江中游地区农村污水处理技术评价及优选

长江流域农村污水治理是实现长江大保护的重要环节,但现有处理技术存在工艺多样、难以选择和缺少评价等问题.因此,调研收集了长江中游地区农村污水处理工程案例资料,分析了不同收集方式和排放标准下各处理技术的应用情况,构建了农村污水处理技术评价指标体系,并基于群决策和层次分析法对各处理技术进行了分类评价.结果表明,长江中游地区农村污水的收集方式以单村或小规模联村收集为主,处理规模主要集中在200 m³·d^-1以下,处理技术以厌氧+生态工艺应用最多(28.05%),一体化设备的应用也较为广泛(22.47%).评价指标体系准则层中技术性能权重最大(0.503 9),其次分别为经济效益(0.247 4)、运行管理(0.155 9)和环境影响(0.092 8),指标层中TP去除率、吨水运行成本、氨氮去除率和维护管理难易的权重较高.评价和优选结果表明,强化生态及厌氧+生态处理技术适于在长江中游农村地区推广和应用.研究结果可为长江中游地区农村污水处理技术的评估选择提供科学依据和参考.     

华东区域PM2.5变化背景下浙江省人口经济暴露水平评估

利用1998~2012年卫星反演的细颗粒物(PM_(2.5))全球高精度产品数据集,精细化地给出了华东地区PM_(2.5)时空分布与变化特征,并分析了此背景下浙江省PM_(2.5)的人口经济暴露水平.结果表明1998~2012年期间,浙江省区域平均PM_(2.5)浓度整体变化呈现出先增加、后下降的特征,拐点出现在2007~2009年前后,与华东区域大背景的变化趋势一致.1998~2000年华东南部与山东东部的年平均PM_(2.5)浓度基本保持在50μg·m~(-3)以下,其余地区大多在50~75μg·m~(-3)左右,华东地区和浙江省PM_(2.5)浓度超过35μg·m~(-3)的地区分别占到51.8%和21.1%.1998~2009年PM_(2.5)浓度上升趋势非常明显,华东地区的平均变化趋势为2.58μg·(m~3·a)~(-1),浙江省的上升趋势较华东区域慢,为1.43μg·(m~3·a)~(-1).2007~2009年PM_(2.5)浓度达到最大,华东和浙江省超过35μg·m~(-3)的地区分别占到82.1%和65.9%.此后PM_(2.5)浓度呈现出下降的变化趋势,华东地区和浙江省的平均变化趋势分别为-1.75μg·(m~3·a)~(-1)和-1.58μg·(m~3·a)~(-1),PM_(2.5)浓度超过35μg·m~(-3)的地区比例均有所下降,说明政府颁布的一系列节能减排方针政策可能对华东地区的空气质量改善起到了一定的成效.2010年浙江地区PM_(2.5)暴露水平超过35μg·m~(-3)的人口比例和GDP比例分别为74.0%和70.8%,其中38.1%的人口生活的环境和38.9%的GDP产生的环境PM_(2.5)浓度年平均值在50μg·m~(-3)以上.