基于稳定氢同位素的太原市大气单环芳烃来源

采集太原市城北和城南区域环境空气和5类污染源挥发性有机物样品,测定样品中典型单环芳烃稳定氢同位素（δD）组成,基于同位素质量平衡原理计算单环芳烃从源到环境空气受体的δD初始混合值,探讨单环芳烃来源.结果表明,柴油挥发源、溶剂挥发源、汽油挥发源（97^#）、汽油挥发源（95^#）、机动车尾气（97^#）、机动车尾气（95^#）和民用燃煤源中单环芳烃δD范围依次为：（-138.7‰~-115.5‰）、（-147.0‰~-121.0‰）、（-150.8‰~-117.6‰）、（-131.8‰~-113.8‰）、（-171.2‰~-120.0‰）、（-138.9‰~-102.7‰）和（-168.3‰~-142.3‰）,民用燃煤源中单环芳烃δD显著贫重氢同位素（D）组成,机动车尾气源与汽油挥发源中苯的δD相比显著贫D,可用于探索污染物转化过程;城北和城南环境空气中δD范围为（-131.7‰~-115.1‰）和（-131.9‰~-74.9‰）,δD初始混合值为-138.4‰和-173.9‰,体现了其来源差异.     

全球液化石油气运输网络贸易社区特征及其演化分析

液化石油气在全球清洁能源消耗市场中扮演着极为重要的角色,其通过船舶在不同港口之间进行运输,而港口之间通过局部密集的运输关系,形成了联系极为紧密的贸易社区。采用复杂网络社区探测方法,基于2013—2017年全球液化石油气船舶轨迹大数据构建运输网络,并对其贸易社区特征及其演化趋势开展分析。结果表明：（1）液化石油气（Liquefied Petroleum Gas,LPG）贸易社区内的港口之间的联系更加紧密,不同社区内的枢纽港口联系也日益紧密;（2）各个贸易社区的规模呈现出增长趋势,且同一社区内的港口在地理空间上变得更为集聚;（3）亚太地区、中东、西北欧和地中海地区形成的社区在全球LPG贸易中一直保持着重要地位,而随着时间推移,美洲社区已逐渐从一个相对孤立的社区发展成为与其他社区存在紧密联系的社区。     

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。     

科技创新投入对环境全要素生产率的影响机制

使用2004~2015年的中国280个地级市的面板数据,对科技创新投入与环境全要素生产率间的非线性关系、内部影响机理和空间异质性进行分析,结果显示：科技创新投入与环境全要素生产率之间呈现倒N型关系,两个拐点的位置分别为7.722（2257.47万元）和9.610（14913.17万元）;在外部资本进入、污染治理、市场规模效应3种影响路径中,科技创新投入影响下的外部资本进入对环境全要素生产率依然存在污染避难所的负向效应,科技创新投入与外部资本间效应为0.1363,外部资本与环境全要素生产率间效应为-0.0065;科技创新投入能够增强企业的污染治理技术并提高环境全要素生产率,三者间前后效应分别为-0.0277和-0.0311;科技创新的投入与高效益增强了市场规模效应,有效促进生产结构的转型进而提高环境全要素生产率,三者间前后效应为0.0186和0.4346.空间异质性中,外部资本进入与溢出效应带来的污染避难所负效应在中部地区显著,在西部和东北部地区不显著,而污染天堂正效应在东部地区存在但不显著;污染创新治理投入的技术正溢出效应在东部和西部地区效应显著,在中部和东北部不显著;科技创新投入与市场需求规模效应在空间区域无差异且显著为正.建议依据科技创新投入的不同影响路径来实施空间差异化策略.     

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.