Measuring water resource use efficiency of the Dong Nai River Basin (Vietnam): an application of the two-stage data envelopment analysis (DEA)

Environment, Development and Sustainability - The recent growth of agriculture, industry and urban areas in Vietnam requires a large amount of water consumption as a production factor. This paper...     

土地整治对工业区周边土壤微生物多样性和群落结构影响分析

为探究土地整治对重金属污染环境下土壤理化性质及其中微生物的影响,本文基于Illumina高通量测序技术,对比分析了工业区周边土地整治区内外的土壤微生物群落结构和多样性.结果表明:①从土壤性质来看,土地整治区重金属污染状况和土壤质量均优于非整治区.②从土壤微生物群落结构来看,水田土壤微生物群落主要的菌门为变形菌门、绿弯菌门、酸杆菌门,而土地整治可能降低了变形菌门相对丰度,提高了绿弯菌门和酸杆菌门的相对丰度,同时在属水平上也提高了鞘脂单胞菌属、地杆菌属的相对丰度.③从土壤微生物多样性来看,土地整治区中土壤微生物多样性和功能性明显得到改善,但随着重金属污染程度的升高,改善效果逐渐减弱.④Spearman相关性分析表明,Cd、Hg、Pb、pH、AP是影响微生物群落的主要环境因子,而硫杆菌属、芽孢杆菌属、鞘脂单胞菌属与多种重金属元素表现出显著的正相关关系.本研究证实了土地整治有助于改善土壤微生物多样性和功能性,并提升土壤质量.     

基于LOADEST和数字滤波的水源地基流氮素输出定量方法应用实例

地表直接径流和基流均是流域非点源氮/磷养分输出的重要水文途径.科学认识和定量模拟基流氮/磷养分输出对于准确解析水源地水体非点源污染来源至关重要.基于Load Estimator模型和数字滤波算法,建立了定量水源地基流氮素输出的方法体系.以浙江省珊溪水源地的玉泉溪流域为例,利用玉泉溪2010-01—2013-12期间逐月总氮(TN)水质监测数据和逐日流量数据,展示了该方法的计算过程.结果表明,本文建立的水源地基流氮素输出定量方法结果合理,模拟精度高,决定系数和纳什系数分别为0.83和0.80;玉泉溪流域2010—2013年TN负荷量为141.21～274.68 t·a~(-1),平均208.63 t·a~(-1),年基流TN负荷量为84.39～168.68 t·a~(-1),平均127.69 t·a~(-1);基流对玉泉溪年均TN负荷量贡献率高达60%以上,流域基流养分输出对地表水体的污染应引起足够重视.     

左炔诺孕酮对稀有鮈鲫脂质代谢的干扰效应

为探究孕激素左炔诺孕酮（LNG）对鱼类脂质代谢的影响,将刚孵化的稀有鮈鲫仔鱼置于0.8和6.5ng/L LNG暴露6个月至性成熟,考察其生长指标、肝脏组织病理学变化、脂质和脂蛋白含量及脂质代谢相关基因的表达情况.结果显示：（1）0.8,6.5ng/L LNG暴露显著降低70dph稀有鮈鲫的体重和肥满度,且6.5ng/L LNG暴露显著降低180dph雌、雄鱼的体长或体重;（2）0.8,6.5ng/L LNG暴露导致180dph成鱼肝脏出现细胞空泡、肝细胞肿胀等损伤;（3）0.8,6.5ng/L LNG暴露显著降低180dph雌鱼肝脏中甘油三酯、胆固醇的含量,且6.5ng/L LNG暴露显著降低雌鱼血浆中甘油三酯的含量,但对雄鱼肝脏及血浆的脂质含量无显著影响;（4）0.8,6.5ng/L LNG暴露显著降低180dph雌鱼肝脏中脂肪酸合成酶基因（fasn） mRNA的表达水平,且6.5ng/L LNG暴露显著降低180dph雄鱼肝脏中fasn及乙酰辅酶A羧化酶基因（acaca） mRNA的表达水平.由此可见,LNG长期低剂量暴露可抑制稀有鮈鲫的生长、诱导肝细胞损伤、引起肝脏和血浆脂质含量发生性别差异性变化,并影响肝脏中脂质代谢相关基因的表达,表明LNG在低浓度下可干扰稀有鮈鲫的脂质代谢,提示LNG对鱼类种群具有较高的潜在生态风险.     

海绵城市的地区分类建设范式

在系统分析我国城市的水文地质和气候条件等自然因素和新旧城区、功能区等社会因素的基础上,分类和总结现有海绵城市试点经验,提出了基于我国地域分类和社会属性分类的海绵城市建设策略和范式,以期为海绵城市建设的推广提供借鉴。     

石墨烯/聚苯胺修饰阴极对反硝化MFC性能影响

反硝化生物阴极微生物燃料电池（MFC）以电极为电子供体,在自养条件下完成硝酸盐去除过程.本研究以碳布（CC）为基底材料,分别制备获得还原氧化石墨烯修饰（rGO-CC）,聚苯胺修饰（PANI-CC）及二者复合修饰的CC电极（rGO/PANI-CC）,并考察其作为阴极材料对反硝化生物阴极MFC产电脱氮性能的影响.扫描电镜结果显示,rGO-CC和PANI-CC的碳纤维分别被片层状rGO和网状PANI覆盖,而rGO/PANI-CC表面呈现PANI在附着rGO的碳纤维上团聚的形貌,均增大了碳布的比表面积.循环伏安测试显示,rGO/PANI-CC具有最高的电化学活性.以rGO-CC,PANI-CC和rGO/PANI-CC为阴极构建MFC的产电能力分别提高了82%,24%和41%,其阴极对NO₃^--N的去除能力增强了23%,9%和13%.16S rDNA测序结果揭示修饰后电极表面微生物的多样性下降,Stappia和Pacacoccus属微生物的丰度增加.     

土壤环境中微塑料的污染现状及其影响研究进展

微塑料作为一种持久性污染物,对土壤生态系统具有严重影响,土壤中微塑料的污染已愈加受到国内外学者的广泛关注。当前关于土壤环境中微塑料的研究较少,针对当前土壤中微塑料的来源、分布、降解迁移、生态效应及污染防治等方面进行综述。主要包括以下几个方面:1）概括土壤生态系统中微塑料的来源、分布特点和迁移降解规律,确定了土壤环境中微塑料的赋存状态;2）总结土壤生态系统中微塑料与其他污染物的复合效应;3）分析了微塑料对土壤理化性质、动物、植物、微生物的影响,并揭示了微塑料对于土壤生态系统的影响;4）根据土壤微塑料的分布特点、降解迁移及生态效应提出污染防治措施。最后,对今后土壤微塑料的研究重点进行了展望。     

Tuning the fill percentage in the hydrothermal synthesis process to increase catalyst performance for ozone decomposition

The performance of Ce-OMS-2 catalysts was improved by tuning the fill percentage in the hydrothermal synthesis process to increase the oxygen vacancy density. The Ce-OMS-2 samples were prepared with different fill percentages by means of a hydrothermal approach (i.e. 80%, 70%, 50% and 30%). Ce-OMS-2 with 80% fill percentage (Ce-OMS-2-80%) showed ozone conversion of 97%, and a lifetime experiment carried out for more than 20?days showed that the activity of the catalyst still remained satisfactorily high (91%). For Ce-OMS-2-80%, Mn ions in the framework as well as K ions in the tunnel sites were replaced by Ce⁴⁺, while for the others only Mn ions were replaced. O₂-TPD and H₂-TPR measurements proved that the Ce-OMS-2-80% catalyst possessed the greatest number of mobile surface oxygen species. XPS and XAFS showed that increasing the fill percentage can reduce the AOS of Mn and augment the amount of oxygen vacancies. The active sites, which accelerate the elimination of O₃, can be enriched by increasing the oxygen vacancies. These findings indicate that increasing ozone removal can be achieved by tuning the fill percentage in the hydrothermal synthesis process.     

Effects of SO2 and H2O on low-temperature NO conversion over F-V2O5-WO3/TiO2 catalysts

F-V_2 O_5-WO3/Ti02 catalysts were prepared by the impregnation method.As the content of F ions increased from 0.00 to 0.35 wt.%,the NO conversion of F-V_2 O_5-WO_3/TiO_2 catalysts initially increased and then decreased.The 0.2 F-V_2 O_5-WO_3/TiO_2 catalyst(0.2 wt.% F ion)exhibited the best denitration(De-NOx) performance,with more than 95% NO conversion in the temperature range 160-360℃,and 99.0% N2 selectivity between 110 and 280℃.The addition of an appropriate amount of F ions eroded the surface morphology of the catalyst and reduced its grain size,thus enhancing the NO conversion at low temperature as well as the sulfur and water resistance of the V_2 O_5-WO3/Ti02 catalyst.After selective catalytic reduction(SCR) reaction in a gas flow containing SO_2 and H_2 O,the number of NH3 adsorption sites,active component content,specific surface area and pore volume decreased to different degrees.Ammonium sulfate species deposited on the catalyst surface,which blocked part of the active sites and reduced the NO conversion performance of the catalyst.On-line thermal regeneration could not completely recover the catalyst activity,although it prolonged the cumulative life of the catalyst.In addition,a mechanism for the effects of S02 and H_2 O on catalyst NO conversion was proposed.     

Recent advances in catalytic decomposition of ozone

Ozone (O₃), as a harmful air pollutant, has been of wide concern. Safe, efficient, and economical O₃ removal methods urgently need to be developed. Catalytic decomposition is the most promising method for O₃ removal, especially at room temperature or even subzero temperatures. Great efforts have been made to develop high-efficiency catalysts for O₃ decomposition that can operate at low temperatures, high space velocity and high humidity. First, this review describes the general reaction mechanism of O₃ decomposition on noble metal and transition metal oxide catalysts. Then, progress on the O₃ decomposition performance of various catalysts in the past 30 years is summarized in detail. The main focus is the O₃ decomposition performance of manganese oxides, which are divided into supported manganese oxides and non-supported manganese oxides. Methods to improve the activity, stability, and humidity resistance of manganese oxide catalysts for O₃ decomposition are also summarized. The deactivation mechanisms of manganese oxides under dry and humid conditions are discussed. The O₃ decomposition performance of monolithic catalysts is also summarized from the perspective of industrial applications. Finally, the future development directions and prospects of O₃ catalytic decomposition technology are put forward.