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.     

农户分化、技术约束与耕地保护技术选择差异——基于不同约束条件下的农户技术采纳理论分析框架

在不完全要素市场和农户分化背景下,探索不同类型农户、耕地保护技术约束与技术选择之间内在行为逻辑,以期为保障我国耕地质量可持续发展提供参考。利用Probit和Logit方法,通过微观数据剖析不同类型农户技术选择意愿、行为逻辑及不同约束条件下的技术选择差异。研究表明：纯农户、I类兼业户和II类兼业户在耕地保护意愿方面具有统一性,但随着非农收入的增加农户耕地保护意愿逐渐降低;在行为逻辑方面,异质性农户耕地保护技术选择上差异显著,不同类型农户的禀赋特征与不同耕地保护技术间存在非对称性和偏差,主要受不同技术属性和风险偏好的约束。因此在耕地保护技术实施与推广应用时,应当更多地考虑不同农户禀赋优势与农户风险偏好程度。     

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.