拟除虫菊酯类农药的降解与代谢研究进展

拟除虫菊酯类农药残留引发各种环境污染和食品安全问题,文章主要综述了该农药的生物降解、光降解和生物代谢三个方面的国内外研究现状。生物降解是其分解代谢的重要环境过程之一,微生物、哺乳动物、水生生物、昆虫及植物等对拟除虫菊酯的代谢都具有不可替代的作用,其中微生物降解菌的分离、微生物的酶促降解及其衍生的基因工程菌技术迅速发展,为通过基因克隆高效表达拟除虫菊酯降解酶提供依据。合理利用光能可有效去除拟除虫菊酯,光敏化降解与光猝灭降解研究可有助于农药混配的效果分析。通过拟除虫菊酯在生物体内的代谢分析可为治疗人体农药中毒提供有效方法。文章还讨论了吸附作用、氧化作用对拟除虫菊酯的降解效果。     

Arsenate biotransformation by Microcystis aeruginosa under different nitrogen and phosphorus levels

The arsenate(As(V)) biotransformation by Microcystis aeruginosa in a medium with different concentrations of nitrogen(N) and phosphorus(P) has been studied under laboratory conditions. When 15 μg/L As(V) was added, N and P in the medium showed effective regulation on arsenic(As) metabolism in M. aeruginosa, resulting in significant differences in the algal growth among different N and P treatments. Under 0.2 mg/L P treatment, increases in N concentration(4–20 mg/L) significantly stimulated the cell growth and therefore indirectly enhanced the production of dimethylarsinic acid(DMA), the main As metabolite, accounting for 71%–79% of the total As in the medium. Meanwhile, 10–20 mg/L N treatments accelerated the ability of As metabolization by M. aeruginosa, leading to higher contents of DMA per cell.However, As(V) uptake by M. aeruginosa was significantly impeded by 0.5–1.0 mg/L P treatment,resulting in smaller rates of As transformation in M. aeruginosa as well as lower contents of As metabolites in the medium. Our data demonstrated that As(V) transformation by M. aeruginosa was significantly accelerated by increasing N levels, while it was inhibited by increasing P levels. Overall, both P and N play key roles in As(V) biotransformation processes.     

物质流分析视角下北京市物质代谢研究

作为"重大国家战略"的"京津冀一体化"日益引起社会各界的高度重视,推动其进程的加快,首先要解决的就是该区域的资源环境问题,而北京作为该经济圈的核心,其资源环境问题的解决更是起着关键性的作用.在提高城市环境质量、改善人们生存环境方面,北京市仍任重而道远.运用物质流分析方法(EW-MFA)可以深入探讨社会经济发展与资源消耗及环境污染之间的关系,从而为社会经济发展过程中资源环境问题的解决提供科学依据.因此,本文采用欧盟物质流核算框架(EW-MFA)建立了北京市"吞吐"状态的物质代谢模型.结果表明:1992—2014年北京市的物质输入与输出总体呈上升趋势,矿物和化石燃料是北京市物质输入的主要组成部分;受社会经济发展水平的影响,北京市的物质投入强度表现出先上升后下降的趋势;研究期间内物质代谢效率不断提高.针对北京市的资源环境问题,应转变传统发展理念,不能一味地追求物质财富的增加而忽略生态环境的影响,且不断推动技术的革新和产业结构的调整应成为实现社会经济可持续发展的有效路径.     

氮素在人工湿地基质中分布研究

介绍了一种改进的人工湿地，该湿地在传统潜流湿地的基础上，提高水流曲折性，改用渡形方式的流态，使污水反复多次地经过土壤基质．狄而增强了吸附、沉淀的效果，更为有效地提高污染物的去除效果。通过实验将传统湿地和渡式湿地进行比较，发现波式湿地出水COD和NH4^＋-N明显低于传统湿地；波式湿地的除氮效果也明显优于传统湿地。     

人工湿地在农业面源污染控制方面的应用

简述了人工湿地的类型及去除氮，磷，有机物的主要机理，人工湿地内植物的作用及其它一些问题，从而说明了人工湿地作为一种造价低，运行简单及管理方便的农业面源污染控制系统在我国尤其是广大城镇和农村地区具有良好的应用前景。     

大气自动监测校准中气体流量对仪器示值误差的影响及控制

研究了大气自动监测系统中标准气、校准气以及零空气的流量大小引起仪器示值误差及时校准曲线质量的影响,提出了重点控制标气流量是减小仪器示值误差的关键,从而解决了低浓度校准点仪器示值偏低、误差大及校准曲线截距大的技术难点,提高了大气自动监测中多点校准质量和监测结果的准确性.     

Regional water flows – Assessing opportunities for sustainable management

Sustainable water management may strongly benefit from an integrated approach. Additionally, an integrated urban water management policy considering the various urban water flows and the possible interactions between the water sector and the remaining urban activities can benefit if based on an urban metabolism based analysis. This article assesses water flows of Lisbon Metropolitan Area considering the conventional water supply system and wastewater treatment system flows and also the hydrological cycle flows, and proposes a global set of indicators to perform a benchmarking analysis of the 18 municipalities of the region. Results highlighted the heterogeneous nature of the Metropolitan area in terms of water management – either in terms of management entities (predominantly public or municipalized), water consumption (varying from 227.4 l/hab.day in Palmela to 402.7 l/hab.day in Seixal), wastewater treatment (10 out of 18 municipalities already undergo secondary or tertiary wastewater treatments), runoff indices (depending on the municipality's level of urbanization), among other. Through the output volumes it was also assessed the potential of the municipalities to reuse wastewater for potable or non-potable urban uses, as well as the potential to harvest and harness rainwater. The main constraints to an integrated water management were identified and some potential solutions were measured and proposed even though they need further assessment, particularly in a cost-benefit perspective.     

光质对小球藻(Chlorella sorokiniana)生长和代谢机制的调控

为研究光质对小球藻(Chlorella sorokiniana)生长和代谢机制的影响,分析了不同光质下C. sorokiniana的生长情况,利用Illumina平台进行转录组测序.结果表明:红､蓝光是C. sorokiniana生长的有效光质,红､蓝光培养7d后藻细胞密度分别比白光对照组的高52.96%和61.11%.C. sorokiniana在不同光质下具有独特的生理特性,蓝光组Chl a､Chl b和Car最高,分别为(17.84±0.26), (8.39±0.19), (6.04±0.08) mg/L;红光培养7d后微藻的碳水化合物和脂质含量最高,分别达到了(115.60±1.81)μg/mg和(18.64±0.54)%.通过转录组测序分析,不同光质下C. sorokiniana的基因表达存在差异,红光下碳酸酐酶､乙酰辅酶A羧化酶和脂肪酸合成酶的基因表达量较高,差异表达的基因大部分参与了脂肪酸合成和碳固定过程;蓝光下RubisCO酶的基因表达量最高且光合系统中富集的差异基因均上调表达,光合速率和碳固定速率最快;绿光下微藻大部分的基因表达量较低,新陈代谢潜能较差;白光下C. sorokiniana的TCA循环活跃,不利于储存碳水化合物和脂质.     

Precise regulation of acid pretreatment for red mud SCR catalyst: Targeting on optimizing the acidity and reducibility

• The optimum SCR activity was realized by tuning the acid pretreatment. • Optimized catalysts showed NO_x conversion above 90%. • The NH₃ and NO adsorption capacity of Al-O₃-Fe is stronger than Fe-O₃-Fe. • The formation of almandine consumes Fe³⁺ and Al³⁺ and weakens their interaction. Red mud (RM), as an alkaline waste, was recently proved to be a promising substitute for the SCR catalyst. Dealkalization could improve the acidity and reducibility of red mud, which were critical for SCR reaction. However, the dealkalization effect depended on the reaction between acid solution and red mud. In this study, we realized the directional control of the chemical state of active sites through tuning the acid pretreatment (dealkalization) process. The pretreatment endpoint was controlled at pH values of 3–5 with diluted nitric acid. When the pH values of red mud were 3 and 5 (CRM-3 and CRM-5), activated catalysts showed NO_x conversion above 90% at 275°C–475°C. The high initial reaction rate, Ce³⁺/(Ce³⁺ + Ce⁴⁺) ratio, and surface acidity accounted for the excellent SCR performance of CRM-5 catalyst. Meanwhile, more Fe³⁺ on the CRM-3 surface improved the NH₃ adsorption. There was a strong interaction between Al and Fe in both CRM-5 and CRM-3 catalysts. DFT results showed that the adsorption capacity of the Al-O₃-Fe for NH₃ and NO is stronger than that of Fe-O₃-Fe, which enhanced the NO_x conversion of the catalyst. However, the almandine was formed in CRM-4, consumed part of Fe³⁺ and Al³⁺, and the interaction between Al and Fe was weakened. Also, deposited almandine on the catalyst surface covered the active sites, thus leading to lower NH₃-SCR activity.     

A comparison of on-site nutrient and energy recycling technologies in algal oil production

Research on biofuel production pathways from algae continues because among other potential advantages they avoid key consequential effects of terrestrial oil crops, such as competition for cropland. However, the economics, energetic balance, and climate change emissions from algal biofuels pathways do not always show great potential, due in part to high fertilizer demand. Nutrient recycling from algal biomass residue is likely to be essential for reducing the environmental impacts and cost associated with algae-derived fuels. After a review of available technologies, anaerobic digestion (AD) and hydrothermal liquefaction (HTL) were selected and compared on their nutrient recycling and energy recovery potential for lipid-extracted algal biomass using the microalgae strain Scenedesmus dimorphus. For 1 kg (dry weight) of algae cultivated in an open raceway pond, 40.7 g N and 3.8 g P can be recycled through AD, while 26.0 g N and 6.8 g P can be recycled through HTL. In terms of energy production, 2.49 MJ heat and 2.61 MJ electricity are generated from AD biogas combustion to meet production system demands, while 3.30 MJ heat and 0.95 MJ electricity from HTL products are generated and used within the production system.Assuming recycled nutrient products from AD or HTL technologies displace demand for synthetic fertilizers, and energy products displace natural gas and electricity, the life cycle greenhouse gas reduction achieved by adding AD to the simulated algal oil production system is between 622 and 808 g carbon dioxide equivalent (CO₂e)/kg biomass depending on substitution assumptions, while the life cycle GHG reduction achieved by HTL is between 513 and 535 g CO₂e/kg biomass depending on substitution assumptions. Based on the effectiveness of nutrient recycling and energy recovery, as well as technology maturity, AD appears to perform better than HTL as a nutrient and energy recycling technology in algae oil production systems.