Temperature and water pressure head effects on the degradation of the diketonitrile metabolite of isoxaflutole in a loamy soil under two tillage systems

Laboratory studies were conducted to evaluate the effects of temperature and water pressure head on the degradation of the diketonitrile metabolite (DKN) of isoxaflutole during 84 d in samples collected in a loamy soil under conventional (CT) and conservation (MT) tillage systems. Soil temperature was the major factor controlling DKN degradation in the two tillage systems. The shortest half-lives (T_1/2) were measured in the seedbed samples under MT at 25 °C and −33 cm water pressure head. We found that mouldboard ploughing under CT was responsible for the spatial variability of herbicide degradation properties, whereas under MT herbicide degradation was associated to the vertical distribution of organic matter.     

东北地区臭氧预氧化对常规净水工艺效果分析

为检验臭氧预氧化在北方地区的效果,结合东北地区某微污染水源做出了分析和探索,发现臭氧氧化对净水处理效果良好。并全面阐述了微污染水源采用臭氧预氧化技术后带来的效果,可用于脱色除臭、控制氯化消毒副产物、去除藻类和藻毒素、助凝和助滤、初步去除或转化污染物,为相关的工程设计奠定了基础。     

Water pressure head and temperature impact on isoxaflutole degradation in crop residues and loamy surface soil under conventional and conservation tillage management

Laboratory incubations were performed in order to evaluate the dissipation of the proherbicide isoxaflutole in seedbed layer soil samples from conventional and conservation tillage systems and in maize and oat residues left at the soil surface under conservation tillage. The effects of temperature and water pressure head on radiolabelled isoxaflutole degradation were studied for each sample for 21 d. Mineralisation of isoxaflutole was low for all samples and ranged from 0.0% to 0.9% of applied ¹⁴C in soil samples and from 0.0% to 2.4% of applied ¹⁴C in residue samples. In soil samples, degradation half-life of isoxaflutole ranged from 9 to 26 h, with significantly higher values under conservation tillage. In residue samples, degradation half-life ranged from 3 to 31 h, with significantly higher values in maize residues, despite a higher mineralisation and bound residue formation than in oat residues. Whatever the sample, most of the applied ¹⁴C remained extractable during the experiment and, after 21 d, less than 15% of applied ¹⁴C were unextractable. This extractable fraction was composed of diketonitrile, benzoic acid derivative and several unidentified metabolites, with one of them accounting for more than 17% of applied ¹⁴C. This study showed that tillage system design, including crop residues management, could help reducing the environmental impacts of isoxaflutole.     

Scenario Modeling Potential Eco-Efficiency Gains from a Transition to Organic Agriculture: Life Cycle Perspectives on Canadian Canola,Corn, Soy,and Wheat Production

We used Life Cycle Assessment to scenario model the potential reductions in cumulative energy demand (both fossil and renewable) and global warming, acidifying, and ozone-depleting emissions associated with a hypothetical national transition from conventional to organic production of four major field crops [canola (Brassica rapa), corn (Zea mays), soy (Glycine max), and wheat (Triticum aestivum)] in Canada. Models of these systems were constructed using a combination of census data, published values, and the requirements for organic production described in the Canadian National Organic Standards in order to be broadly representative of the similarities and differences that characterize these disparate production technologies. Our results indicate that organic crop production would consume, on average, 39% as much energy and generate 77% of the global warming emissions, 17% of the ozone-depleting emissions, and 96% of the acidifying emissions associated with current national production of these crops. These differences were almost exclusively due to the differences in fertilizers used in conventional and organic farming and were most strongly influenced by the higher cumulative energy demand and emissions associated with producing conventional nitrogen fertilizers compared to the green manure production used for biological nitrogen fixation in organic agriculture. Overall, we estimate that a total transition to organic production of these crops in Canada would reduce national energy consumption by 0.8%, global warming emissions by 0.6%, and acidifying emissions by 1.0% but have a negligible influence on reducing ozone-depleting emissions.     

关于企业环境保护审计的初探

从环保审计的现状入手，分析目前企业环保审计难以向纵深发展的主要原因，提出实施企业环保审计的最佳切入点，将环保审计融入常规审计之中，并对环保审计提出配套的措施，确保环保审计适应现代化企业的发展。     

大中型风机叶轮前盘的简易旋压成形

提出了一种适用于单件或小批量生产大中型风机叶轮前盘的新工艺——滚轮芯模简易旋压成形工艺,这种工艺经济实用,简便易行,可在一定范围内推广应用。     

普通活性污泥膜生物反应器处理洗车废水的应用研究

膜生物反应器是近年来发展起来的一种新型高效水处理设备。它将分离工程中的膜技术应用于好氧活性污泥处理系统，由膜组件取代传统生化处理技术中的二次沉淀池和砂滤池，由膜分离技术代替传统方法中的重力式沉淀泥水分离技术方式，具有简洁、高效等优点。采用普通活性污泥膜生物反应器工艺对天津某一洗车点洗车废水进行处理，并将处理出水回用于洗车。     

Economic analysis of conventional versus selective demolition—A case study

Studies on selective demolition (also named deconstruction) in the past few years have produced some high quality economic, material and environmental information. Economic data, however, varies considerably between regions since local conditions strongly influence labour costs, tipping fees and/or market prices for recovered materials. Regional financial and regulatory constraints will bind the economic viability of conventional and selective demolition choices, which are essentially economic in a free market. Given this, the present study evaluates the economic implications of the two demolition types by analyzing a case study in Portugal. A few scenarios are considered, based on possible waste management options, some of which favour selective demolition over the conventional type.     

Techno-economic characteristics of wastewater treatment plants retrofitted from the conventional activated sludge process to the membrane bioreactor process

• Retrofitting from CAS to MBR increased effluent quality and environmental benefits. • Retrofitting from CAS to MBR increased energy consumption but not operating cost. • Retrofitting from CAS to MBR increased the net profit and cost efficiency. • The advantage of MBR is related to the adopted effluent standard. • The techno-economy of MBR improves with stricter effluent standards. While a growing number of wastewater treatment plants (WWTPs) are being retrofitted from the conventional activated sludge (CAS) process to the membrane bioreactor (MBR) process, the debate on the techno-economy of MBR vs. CAS has continued and calls for a thorough assessment based on techno-economic valuation. In this study, we analyzed the operating data of 20 large-scale WWTPs (capacity≥10000 m³/d) and compared their techno-economy before and after the retrofitting from CAS to MBR. Through cost-benefit analysis, we evaluated the net profit by subtracting the operating cost from the environmental benefit (estimated by the shadow price of pollutant removal and water reclamation). After the retrofitting, the removal rate of pollutants increased (e.g., from 89.0% to 93.3% on average for NH₃-N), the average energy consumption increased from 0.40 to 0.57 kWh/m³, but the operating cost did not increase significantly. The average marginal environmental benefit increased remarkably (from 0.47 to 0.66 CNY/g for NH₃-N removal), leading to an increase in the average net profit from 19.4 to 24.4 CNY/m³. We further scored the technical efficiencies via data envelopment analysis based on non-radial directional distance functions. After the retrofitting, the relative cost efficiency increased from 0.70 to 0.73 (the theoretical maximum is 1), while the relative energy efficiency did not change significantly. The techno-economy is closely related to the effluent standard adopted, particularly when truncating the extra benefit of pollutant removal beyond the standard in economic modeling. The modeling results suggested that MBR is more profitable than CAS given stricter effluent standards.     

传统活性污泥法与膜生物反应器污泥沉降性能的比较

针对污泥沉降性能,在运行条件相同的情况下对膜生物反应器(MBR)与传统活性污泥法(CAS)进行比较。结果表明：CAS工艺污泥沉降性能优于MBR工艺;CAS工艺出水水质受污泥沉降性能影响大;MBR工艺污泥沉降性能主要由反应器中累积的高浓度胞外聚合物(EPS)含量所影响,当EPS浓度大于100mg／g时,污泥沉降性能开始恶化;CAS工艺曝气池中EPS浓度没有累积;MBR工艺污泥颗粒平均粒径小于CAS工艺中污泥颗粒。