阴-阳离子有机膨润土吸附水中苊的性能及机理研究

用溴化十二烷基三甲铵（DTMAB）、十二烷基硫酸钠（SDS）、十二烷基苯磺酸钠（SDBS）按不同配比制得一系列阴一阳离子有机膨润土,研究了有机膨润土吸附水中苊的性能及机理。结果表明,阴一阳离子有机膨润土对水中苊的吸附去除能力大于单阳离子有机膨润土,且与改性时所用阴离子表面活性剂的种类、浓度有关;阴一阳离子有机膨润土对苊的吸附等温线呈线性,吸附机理主要是分配作用。     

改性膨润土联合混凝剂处理微污染水中有机物

采用十二烷基多糖苷季铵盐作为改性剂制备改性膨润土,研究了改性膨润土联合混凝剂去除有机物的效果,考察了有机改性剂用量、微波辐射功率、辐射时间、膨润土投加量、pH值对有机物去除效果的影响,探讨了改性膨润土的改性和去除机理。结果表明,经微波改性后,实现了十二烷基多糖苷季铵盐阳离子对膨润土的插层,增大了层间距,提高了膨润土的吸附性能。联合混凝剂投加改性膨润土能够改善絮凝性能,显著提高有机物的去除效果。在最佳条件下,改性膨润土与PAC联合后的强化混凝,对初始浓度15.3 mg/L的微污染水中有机物的去除率达到95%以上,吸附符合Freundlich吸附等温方程。     

改性膨润土颗粒对微污染水中有机物和氨氮的吸附

采用粘结剂聚乙烯醇(PVA)、造孔剂碳酸氢钠(NaHCO3)和微波强化Al改性膨润土(以下简称M-Al-Bt)制备改性膨润土颗粒(以下简称MBG),研究MBG对微污染水中有机物和氨氮(NH4-N)的吸附效果,考察了不同投加量、反应时间、pH值对腐殖酸(HA)和NH4-N的去除效果影响.结果表明,投加量3 g/L,反应时间20 min,pH=7时,MBG对微污染水中20 mg/L HA和5mg/L NH4-N的去除率分别可达98%和20%以上.HA和NH4-N共存时,存在竞争吸附,HA影响了MBG对NH4-N的去除.     

改性钙铝LDH对水中硝基苯和萘的吸附

为了解经十二烷基硫酸钠（SDS）改性的钙铝LDH作为吸附剂吸附水体中硝基苯和萘的吸附性能,结合有机钙铝LDH的结构特征和有机质含量,对有机改性前后钙铝LDH分别对硝基苯、萘的动力学和等温吸附线进行了研究。探讨了其吸附机理。结果表明,有机钙铝LDH层间距为3．25nm,有机质含量约为45％。提出了有机改性后的钙铝LDH对硝基苯和萘的吸附率增强,且萘的吸附效率高于硝基苯;有机钙铝LDH对非离子型有机污染物的吸附作用机理主要为分配作用。     

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。     

Simultaneous removal of organic compounds and heavy metals from soils by electrokinetic remediation with a modified cyclodextrin

Thousands of sites are contaminated with both heavy metals and organic compounds and these sites pose a major threat to public health and the environment. Previous studies have shown that electrokinetic remediation has potential to remove heavy metals and organic compounds when they exist individually in low permeability soils. This paper presents the feasibility of using cyclodextrins in electrokinetic remediation for the simultaneous removal of heavy metals and polycyclic aromatic hydrocarbons (PAHs) from low permeability soils. Kaolin was selected as a model low permeability soil and it was spiked with phenanthrene as well as nickel at concentrations of 500 mg kg-1 each to simulate typical mixed field contamination. Bench-scale electrokinetic experiments were conducted using hydroxypropyl beta-cyclodextrin (HPCD) at low (1%) and high (10%) concentrations and using deionized water in control test. A periodic voltage gradient of 2VDC cm-1 (with 5 d on and 2 d off) was applied to all the tests, and 0.01 M NaOH was added during the experiments to maintain neutral pH conditions at anode. In all tests, nickel migrated as Ni2+ ions towards the cathode and most of it was precipitated as Ni(OH)2 within the soil close to the cathode due to high pH condition generated by electrolysis reaction. The solubility of phenanthrene in the flushing solution and the amount of electroosmotic flow controlled the migration and removal of phenanthrene in all the tests. Even though high flow was generated in tests using deionized water and 1% HPCD, migration and removal of phenanthrene was low due to low solubility of phenanthrene in these solutions. The test with 10% HPCD solution showed higher solubility of phenanthrene which caused it migrate towards the cathode, but further migration and removal was retarded due to reduced electric current and electroosmotic flow. Approximately one pore volume of flushing resulted in approximately 50% removal of phenanthrene from the soil near the anode. Sustained higher electroosmotic flow with higher concentration cyclodextrin and maintaining low soil pH near cathode should be investigated to increase removal efficiency of both phenanthrene and nickel.     

Simultaneous removal of cyanobacterial blooms and production of clean water by coupling flocculation with a rotary drum filter

Environmental Science and Pollution Research - A mechanical harvesting technology based on coupling flocculation with a rotary drum filter (RDF, 35-μm) was applied to remove cyanobacterial...     

Development,validation and application of a method to analyze phenols in water samples by solid phase micro extraction-gas chromatography-flame ionization detector

In this work the development, validation and application of method using Solid Phase Microexctration (SPME) for the analyses of five pollutants (phenol, 2-nitrophenol, 2,4-dimethylphenol, 2,4-dichlorophenol and 4-chloro, 3-methyl phenol) in supplying water, using gas chromatography (GC) with flame ionization detector (FID) is described. The optimal conditions obtained for SPME were: fiber type: Poliacrylate (PA); extraction time: 40 minutes; extraction temperature: 70°C; amount of salt added to sample (NaCl): 15%; desorption temperature: 8 minutes. The parameters studied in the method validation were: limit of detection (0.3 and 3.5 μ g.L^{? 1}); precision, measured by the variation coefficient (between 2.1 and 8.8%); calibration curve and linearity, by using the external standardization method (between 1 and 50 50 μ g.L^{? 1}). After the methodology development, samples of water collected in Atibaia River (São Paulo - Brazil) were analyzed, using the optimized methodology. Three water samples collected in the rain season showed a peak with retention time close to 4-chloro, 3 methyl phenol further analyzed by Gas Chromatography-Mass Spectrometry for the identity confirmation. In spite of the fact that none target compounds were found in the river water samples analyzed, the presence of two phenols different from those investigated (p-terc butyl phenol; butylated hydroxytoluene) were detected. These results together with the results of the limit of detection (that showed to be lower than the maximum concentration of phenols demanded by different environment control agencies), and the results of the validation, indicate the applicability of this method for the analysis of selected phenols in river water samples.     

竹制填料生物接触氧化工艺处理污染河水简

针对受污染的湖溪河水质特征,以传统弹性塑料填料做对比,研究以竹球和竹丝为填料的生物接触氧化工艺,考察填料的挂膜时间、生物量和污水处理效果;确定连续曝气和间歇曝气时反应器的最优运行工况：连续曝气时为HRT=7.5 h,DO=3 mg/L;间歇曝气时为厌氧1.2 h、好氧6.3 h交替运行。实验结果表明,与弹性塑料填料相比,竹制填料挂膜速度快,竹球填料的水处理效果最好;连续曝气最优工况下竹球填料反应器中COD、TN、NH₃-N和TP的平均去除率分别为66.7%、47.9%、57.1%和30.6%;间歇曝气最优工况下竹球填料反应器中COD、TN、NH₃-N和TP的平均去除率分别64.08%、39.95%、60.7%和54.68%;竹制填料可替代传统的塑料填料作为生物接触氧化工艺的载体填料。     

氮掺杂多孔碳电极CDI技术对水中四环素和硬度离子的高效去除

为解决水体中过剩四环素 (tetracycline, TC)与水硬度离子(Ca²⁺和Mg²⁺)等共存带来的复杂环境污染问题,采用分散聚合法将含氮单体聚合成手风琴状碳前驱体并将其碳化后,制备得到氮掺杂多孔碳材料 (nitrogen-doped porous carbon, NPC),采用电容去离子技术考察了NPC电极同步去除不同水体、pH、初始浓度中TC和水硬度离子的能力。结果表明：Langmuir,Freundlich和Temkin模型对NPC样品电吸附TC的吸附等温线分别进行拟合,发现电吸附过程包含了化学吸附、强静电吸附和物理吸附等机制,吸附过程较为复杂;NPC独特的手风琴状层次结构,使得TC的电吸附容量高达854.3 mg·g⁻¹,是传统自吸附的2.4倍 (350.6 mg·g⁻¹);稳定的层次结构与高导电碳网络结构,协同增强了NPC电极的吸附稳定性、再生性和循环稳定性,使其在自然水体中经过200次吸-脱附后吸附容量仍可保持在78%以上。由此可知,基于CDI技术的氮掺杂多孔碳电极能够有效地同步去除水体中的四环素和硬度离子。该研究结果可为复杂水体污染处理提供参考。     

宽叶香蒲表面流人工湿地脱氮除磷效果研究

以运行A/O工艺的生化反应器出水为处理对象,在中试规模上研究了宽叶香蒲表面流人工湿地的脱氮除磷效果及影响因素.结果表明,在工况Ⅰ条件下,COD去除率为43.2%,COD面积负荷去除率为4.79 g/(m2·d),COD面积负荷去除率常数为0.18 m/d,SS、NH4+-N和NO-3-N的去除率分别为41.2%、9.4%、3.4%,TN去除率为11.8%,TN面积负荷去除率为1.36g/(m2·d),TN面积负荷去除率常数为0.04 m/d,TP去除率为30.1%,TP面积负荷去除率为0.29 g/(m2·d),TP面积负荷去除率常数为0.13 m/d;在工况Ⅱ条件下,COD去除率为18.7%,COD面积负荷去除率为1.19 g/(m2·d),COD面积负荷去除率常数为0.06 m/d,SS、NH4+-N、NO2--N、NO3--N的去除率分别为31.6%、29.8%、65.0%,29.2%.TN去除率为31.4%,TN面积负荷去除率为2.33 g/(m2·d),TN面积负荷去除率常数为0.12 m/d,TP去除率为29.4%,TP面积负荷去除率为0.22 g/(m2·d),TP面积负荷去除率常数为0.11 m/d.在COD面积负荷去除率,TN面积负荷去除率、TP面积负荷去除率分别为4.90～9.80、2.76～8.83、0.57～1.39 g/(m2·d),水力停留时间(HRT)为0.4～1.1 d条件下,随HRT,水温、(NO2+-N+NO3--N)/TN的增加,表面流人工湿地的TN面积负荷去除率线性增加.     

应用自动识别和定量系统评价两种污水再生工艺对微量有机污染物的去除效果

采用气质联用分析,并结合自动识别与定量系统(AIQS-DB)考察2种再生水厂采用的深度处理工艺对微量有机污染物的去除效果。结果表明,以污水为原水的膜生物反应器(MBR)+臭氧氧化+生物活性炭滤池(BAC)工艺用于再生水生产,MBR工艺对有机污染物的去除起主要作用;城市污水厂二级出水为原水的混凝沉降+浸没式超滤(SMF)/连续微滤(CMF)+部分反渗透(RO)+臭氧氧化工艺用于再生水生产,其SMF和CMF工艺段的膜截留作用均可有效消减有机污染物含量,SMF的效果优于CMF;2种工艺中采用的臭氧技术都能进一步加强部分物质的去除效果。气质联用结合AIQS-DB可用于再生水中污染物的筛查和不同污水再生工艺对微污染物消减效果的评价。     

Comparison of calculated evaporation rates of water droplets with those of pesticide droplets measured in a wind tunnel by Dennison and Wedding (1984)

Abstract

Calculations, based on Fuchs’ (1959) formula, of evaporation rates of water droplets freely falling through air are compared with those of water‐based pesticide droplets measured by Dennison and Wedding (1984) in a wind tunnel. Results indicate that calculations of evaporation rates of water droplets, are not significantly different from measurements of that of water‐based pesticide droplets under conditions of 20 °C and 20% relative humidity, but different under other measurement conditions.