多中心治理下公众参与大气污染防治路径探析

动员全社会力量保护环境,积极推动公众参与环保工作,是解决环境保护问题的根本途径。运用多中心治理理论分析,发现政府治污理念陈旧、制度不健全、公众责任意识淡漠、环保社会组织弱小等,是我国大气污染治理中公众参与度低的主要原因,因此提出转变观念、完善机制、加强教育、支持和引导环保社会组织,促进公众参与的多元治理模式的形成,真正推动大气环境质量的改善。     

TS-1分子筛催化O_3/H_2O_2氧化乙酸

研究了酸性条件下TS-1分子筛催化O3/H2O2体系（O3/H2O2/TS-1）对降解水中乙酸效率的影响,优化了相关工艺参数,并对其作用机理进行了分析。结果表明,在pH为2.8时,TS-1的加入能显著提高臭氧化的降解效率。优化工艺参数表明,当过氧化氢投加量为3 g/L,TS-1投加量为5 g/L时,O3/H2O2/TS-1体系对乙酸具有较高的降解率,60 min后O3/H2 O2/TS-1体系对乙酸（初始浓度为100 mg/L）的去除率达到了58.7%。当pH为0.8时,O3/H2 O2/TS-1体系对乙酸的去除率仅为19.8%,降解效果较差。定量化计算表明,O3/H2O2和O3/H2O2/TS-1的Rct分别为1.62×10-8和8.67×10-7。通过测定乙酸降解过程水样中过氧化氢和液相臭氧的浓度变化,推测了具体反应机理。由于此体系在酸性条件下对乙酸有较好的降解效果,拓宽了现有O3/H2O2体系的应用范围。     

TS-1分子筛催化O3/H2O2氧化乙酸

研究了酸性条件下TS-1分子筛催化O3/H2O2体系(O3/H2O2/TS-1)对降解水中乙酸效率的影响,优化了相关工艺参数,并对其作用机理进行了分析。结果表明,在pH为2.8时,TS-1的加入能显著提高臭氧化的降解效率。优化工艺参数表明,当过氧化氢投加量为3 g/L,TS-1投加量为5 g/L时,O3/H2O2/TS-1体系对乙酸具有较高的降解率,60 min后O3/H2 O2/TS-1体系对乙酸(初始浓度为100 mg/L)的去除率达到了58.7%。当pH为0.8时,O3/H2 O2/TS-1体系对乙酸的去除率仅为19.8%,降解效果较差。定量化计算表明,O3/H2O2和O3/H2O2/TS-1的Rct分别为1.62×10-8和8.67×10-7。通过测定乙酸降解过程水样中过氧化氢和液相臭氧的浓度变化,推测了具体反应机理。由于此体系在酸性条件下对乙酸有较好的降解效果,拓宽了现有O3/H2O2体系的应用范围。     

乳化液膜体系去除电解锰废水中的Mn2+

采用乳化液膜法处理电解锰废水,考察制乳条件和提取条件对去除效果的影响。研究结果表明最佳制乳条件为:4%(V/V)span-80做表面活性剂,3%二(2-乙基己基)磷酸酯做载体,柴油做膜溶剂,用NaOH调节内水相pH为12,制乳时间为10 min,油内比2∶1;最佳提取条件:外水相pH为6～7、乳水比1∶10、提取时间10 min。制得的乳化液膜对电解锰废水中的Mn2+去除率可高达99.99%,出水Mn2+浓度低于2mg/L,实现水质达标排放。     

National Park Development in China: Conservation or Commercialization?

The rapid development of parks and ecotourism in China has attracted worldwide attention, not only for the beauty of the landscape that the parks are protecting but also for their abundant and often unique biodiversity. However, in some areas, the development of ecotourism has actually led to the degradation of local ecological, economic, and social systems. Using National Forest Parks for demonstration, this article analyzes the current political, institutional, legal, environmental, and economic issues concerning National Parks in China, and examines their potential future development. Although the intention of National Park systems in China is to raise environmental quality, and to protect biodiversity and social livelihoods, their success has varied. Future success will be measured by their capacity to reduce poverty, to promote long-term rehabilitation of wildlife habitats, and to simultaneously protect Chinese culture and biodiversity.     

卡鲁塞尔氧化沟反应器两相流PIV图像处理研究及实验分析

在单相数字粒子图像测速度(PIV)技术的基础上,研究了PIV两相流动的测试及图像处理方法.利用数学形态学的原理以及互相关法,对两相粒子图像进行标定、识别、区分和流场分析,编辑了相应的软件.并采用此技术对卡鲁塞尔氧化沟模型直道及弯道段二维液固两相流速进行测量,克服了传统点测量方法无法获取全场流动同步信息的缺陷,较好地反映了不同位置处固液流动分布的基本特性.结果表明,沟内径向流速远小于轴向,流速大小相差约一个数量级;同一断面上轴向流动分布是决定水力特性的主要因素;径向流速和水体动能是决定污泥沉积位置的主要因数,固相总体流速小于液相.     

Characteristics of an aerobic denitrifier that utilizes ammonium and nitrate simultaneously under the oligotrophic niche

Introduction

An aerobic denitrifier was isolated from the Hua-Jia-Chi pond in China and identified as Pseudomonas mendocina 3-7 (Genbank No. HQ285879). This isolated strain could express periplasmic nitrate reductase which is essential for aerobic denitrification occurred when the dissolved oxygen (DO) level maintains at 3?C10?mg?L^?1.

Methods

To determine whether the ability of isolated strain is exhibited in the bioremediation of polluted drinking source water, the heterotrophic nitrification and aerobic denitrification characteristics of P. mendocina 3-7 under different cultural conditions such as oxygen level, nitrate and organic concentrations were studied from the nitrogenous balance in the paper.

Results and conclusions

By measuring the nitrogen balance in all experiments under different culture conditions, the removal of total organic carbon and ammonium was positively correlated with total nitrogen removal, especially under high substrate level. With substrate concentration decreasing, ammonium and nitrate removal occurred separately, and ammonium was completely utilized first under low substrate concentration. Compared to that under high substrate level, the specific growth rate of P. mendocina 3-7 was not low under the low substrate level and the pollutant removal efficiencies remained high, which implies the stronger nitrogen removal and acclimatization capacities of the strain in oligotrophic niches.     

The characteristics of waste Saccharomyces cerevisiae biosorption of arsenic(III)

Purpose

The potential of using waste Saccharomyces cerevisiae as adsorbent for the adsorption of As(III) from aqueous solution was assessed.

Methods

The biosorbent was characterized by Fourier transform infrared (FTIR) spectroscopy analysis. Various parameters including pH, biosorbent dosage, contact time, and temperature were systematically investigated.

Results and conclusions

The FTIR results of S. cerevisiae biomass showed that biomass has different functional groups, and these functional groups are able to react with metal ion in aqueous solution. Several biosorption isotherms were used to fit the equilibrium data, showing sorption to be monolayer on the heterogeneous surface of the biosorbent. The maximum biosorption capacity calculated using Langmuir model was found to be 62.908???g/g at pH?5.0, biosorbent dosage 5?g/L, contact time 240?min, and temperature 35?°C. The kinetic studies indicated that the biosorption process of the As(III) followed well the pseudo-second-order equation. The intraparticle diffusion and Richenberg models were applied to the data, and we found that the biosorption of As(III) was governed by film diffusion followed by intraparticle diffusion. The thermodynamics constants indicated that the biosorption of As(III) onto S. cerevisiae was spontaneous and endothermic under examined conditions. Biosorbent could be regenerated using 0.5?M NaOH solution, with up to 75?% recovery.     

混合硫酸盐还原菌代谢过程的影响因素

采用间歇实验,研究不同初始pH、Fe2+投加量、COD/SO24-及NO3-/SO24-比值等因素对SRB还原硫酸盐效果与速率的影响。实验结果表明:中性条件下(pH=7),硫酸盐的去除效果最佳,去除率达到84.66%,还原速率为15.07 mg/(L.h),在初始pH为4～9的范围内,体系具有较好的缓冲能力;当COD/SO24-比值为3时,反应209 h,硫酸盐去除率为85.33%,还原速率为8.16 mg/(L.h),随着反应的进行,体系的pH趋于中性;当溶液中有亚铁离子存在,且浓度为0～200 mg/L时可促进硫酸盐还原菌的生长,提高其对硫酸盐的去除率;NO3-对硫酸盐的还原有明显的抑制作用。     

可降解餐盒去除地下水硝酸盐的砂槽模拟实验研究

采用室内砂槽实验装置,研究了以可降解餐盒(BMB)为反硝化碳源的生物反应器对于模拟污水中硝酸盐的去除效果及其影响因素。结果表明,以BMB为反硝化碳源的反应器启动时间短。当进水硝酸盐浓度为50 mg/L,水温为25℃,水力停留时间为1.15 d时,硝酸盐的去除率可达92.6%以上,实验过程中出现亚硝酸盐积累,出水TOC浓度上升,但反应稳定后亚硝酸盐浓度均低于0.1 mg/L,且TOC浓度有下降趋势;水力停留时间减小或者进水硝酸盐浓度增加均能使得脱氮效率降低,但当水力停留时间在0.57~1.15 d,进水硝酸盐浓度在50~80 mg/L范围变化时,反应器硝酸盐去除效率仍能达到80%以上;温度对反硝化作用影响较大,当温度为(20±1)℃时,硝酸盐的去除效率仅为62.0%、74.4%和97.5%。