公众参与环境保护制度属性及制度模块构建

民主政治是公众参与制度的出发点和归宿,通过公众的有效参与,环境执法权得到监督;有序是公众参与制度的自然属性,有序才能使参与变得顺畅;利益均衡是公众参与制度的价值准则,环境矛盾最终体现为环境利益和经济利益之争,解决环境纠纷的最佳手段是寻找利益均衡点;政府居于环境执法的主导地位,同时发挥指导、引导、疏导公众和企业的作用;多重沟通平台是公众参与制度的效率保证,政府、企业、公众在执法前后的多重沟通,才能达到参与的最终目标。与公众参与环境执法制度属性相对应的是制度模块建设,如监督制度、程序制度、纠纷调处制度、润性执法制度以及沟通制度等。这些制度既能准确反映公众参与环境执法制度属性,又能完成制度赋予的使命。     

Closing the water cycle for industrial laundries: An operational performance and techno-economic evaluation of a full-scale membrane bioreactor system

To reduce the consumption of freshwater in the laundry industry, a new trend of closing the water cycle has resulted in the reuse/recycling of water. In this study, the performance of a full-scale submerged aerobic membrane bioreactor (9 m³) used to treat/reuse industrial laundry wastewater was examined over a period of 288 days. The turbidity and total solids (TS) were reduced by 99%, and the chemical oxygen demand (COD) effluent removal efficiencies were between 70% and 99%. The levels of COD removed by the membrane were significantly greater than the levels of biodegraded COD. This enabled the bioreactor to sustain COD levels that were below 100 mg/L, even during periods of low wastewater biodegradation due to bioreactor sludge. An economic evaluation of the membrane bioreactor (MBR) system showed a savings of 1.13 € per 1 m³ of water. The payback period for this system is approximately 6 years. The energy and maintenance costs represent only 5% of the total cost of the MBR system.     

集成膜法水处理工艺的研究与应用

集成膜法除盐系统具有连续产水、出水质量好、易控制、占地少、不需酸碱、利于环保等优点。文章通过对集成膜法水处理技术进行研究与应用,将原有的化学除盐水处理方式改为集成膜法水处理工艺,该方法产水水质高且水质稳定,每年可节约酸碱200 t,阴、阳离子交换树脂10 t,切实解决电厂所面临的产水水质不稳定、酸碱废液排放等问题,有力推动了清洁生产。     

道南膜技术测定Ca(NO3)2溶液体系中汞的化学形态

虽然道南膜技术(DMT)已经成功用于土壤/溶液中多种重金属自由态离子浓度的测定,但DMT技术测定Hg的形态尚未解决.采用DMT测定Ca(NO3)2溶液体系中Hg化学形态.实验结果表明,Hg在阳离子交换膜内的吸附除静电吸附外还存在结合力更强的化学吸附,Hg在阳离子交换膜内扩散成为Hg跨膜传输受阻的主要因素,限制道南膜技术用于Hg形态测定.Hg2+和Hg(OH)2都表现出在阳离子交换膜上的强烈吸附,供端(Donor)Hg损失达50%以上.缩短试验时间至8h以内,可在一定程度上降低Hg吸附.计算结果表明,由于大量的Hg滞留在阳离子交换膜内,在计算受端(Acceptor)Hg浓度时引入滞留系数补偿供端Hg的损失,较好地预测了Ca(NO3)2溶液体系中Hg的化学形态.     

聚合物/表面活性剂二元体系对油水界面性质的影响

文章应用界面张力仪、Zeta电位仪和表面黏弹性仪测定了聚合物、表面活性剂及其二元复合体系的质量浓度对油水界面性质的影响,并应用透射电镜观察了采出液的液膜结构。结果表明,随着聚合物质量浓度的增加,油水界面的界面剪切黏度值和界面张力值增大,颗粒表面Zeta电位的绝对值增大;随着表面活性剂质量浓度的增加,油水界面的界面剪切黏度变化幅度很小,但界面张力显著减小,颗粒表面Zeta电位绝对值增大;聚合物与表面活性剂复合能够形成稳定的聚合体,具有较大的界面剪切黏度值,较小的界面张力和较高的Zeta电位值;体系中聚合物、表面活性剂及水中悬浮物形成了类似"晶体"结构。     

厌氧微网反应器处理生活污水膜污染物研究

采用涤纶网加工的微网膜组件与厌氧反应器结合构成厌氧微网生物反应器用于处理城市生活污水。在不同反应器形式和水力停留时间条件下反应器稳定运行了144 d。研究结果表明完全搅拌反应器在膜通量12 L/(m2.h)条件下跨膜压差变化较小,整体出水水质高于无搅拌式反应器。通过膜面SS含量测定、粒径和三维荧光光谱分析等方法对膜面污染物进行了系统分析。无搅拌式AnFBR随着停留时间的延长,膜面污染物的SS减少,粒径减小;完全搅拌式AnFBR膜面污染物的SS最少,粒径最小。三位荧光分析表明SMP主要有2个类蛋白质荧光峰A和B,中心位置(Ex/Em)分别位于230~235/335~350 nm及280~290/330~355 nm,EPS样品中除了峰A和峰B外还有2个峰,峰C位置(Ex/Em)在340~350/435~445 nm,与类富里酸物质有关,峰D位于420~440/465~515 nm,与类腐殖酸物质有关。     

生物滴滤塔处理制革恶臭气体微生物特性研究

在生物滴滤塔处理制革恶臭气体中,采用SBR法对活性污泥进行驯化,考查生物滴滤塔处理制革恶臭气体中微生物的特性。研究了微生物对氨氮和硫化物的去除效率以及驯化过程中污泥容积指数(SVI)的变化,并对挂膜后填料表面的微生物相进行扫描电镜观察。结果表明:经过19 d的驯化,微生物对氨氮和硫化物的去除率分别可以达到98.29%和94.16%,驯化期间污泥容积指数均保持在正常的范围之中。挂膜14 d的扫描电镜显示,填料表面有均匀的生物膜分布,说明微生物在填料上已经挂膜成功,驯化的微生物可以达到去除制革恶臭气体的要求。     

Fe-NaA分子筛膜的制备及催化湿式H2O2氧化甲基橙溶液

采用湿法造纸、二次生长和湿法浸渍法合成了一种新型微纤复合Fe-NaA分子筛膜催化剂,并将其用于催化湿式H_2O_2氧化甲基橙溶液.首先通过湿法造纸和烧结工艺制备纸状烧结不锈钢微纤(PSSF)载体,然后采用二次生长法在PSSF上合成NaA分子筛膜,最后以九水硝酸铁(Fe(NO_3)_3·9H_2O)和微纤复合NaA分子筛膜为原料,利用湿法浸渍法制备微纤复合Fe-NaA分子筛膜催化剂.考察了连续固定床反应器中温度、床层高度、进料液流量和甲基橙入口浓度对甲基橙降解性能的影响,并测定了催化剂重复使用3次后的稳定性.结果表明,随温度及床层高度增加,甲基橙转化率先增加然后趋于稳定;随进料液流量增加,甲基橙转化率均大于95%,但COD脱除率略有降低,当流量分别为2、3和4 mL·min~(-1),固定床连续运转5 h时COD脱除率分别为81.9%、76.4%和69.8%;随甲基橙入口浓度增加,其转化率变化幅度很小.在pH=2、催化剂床层高度2.0 cm、温度70℃、进料液流量4 mL·min~(-1)、甲基橙浓度50～200 mg·L~(-1)、固定床连续运转5 h的条件下,甲基橙转化率超过96%,COD转化率大于67%,铁浸出浓度低于4 mg·L~(-1).催化剂被重复使用3次后,甲基橙转化率基本保持不变.     

Recent advances in thin film composites membranes for brackish groundwater treatment with critical focus on Saskatchewan water sources

Drinking water scarcity is an ever-increasing global concern. This issue appears as a greater threat to the countries with no access to sea water resources or rivers, since their potential water resources are only limited to ground waters only. There are serious concerns with the treatment of ground water resources, including landfill leachates, agricultural contaminations (pesticides, herbicides, and fertilizers), and rural contaminations. Membrane separation has been proved to be the governing technology in water and wastewater treatment plants, as these methods are responsible for more than half of the market share of the world's desalination capacity. This study intends to offer a holistic view of the groundwater contamination with specific focus on Saskatchewan province in Canada, and the recent efforts in the groundwater treatment using thin film composite membrane technology. This study begins with an introduction of the general aspects of ground water and membrane separation, polluting agents, and their sources. It is followed by a discussion of Saskatchewan's groundwater status and various issues. Furthermore, the recent research that became available since 2010 is reviewed in details and the results are summarized with respect to purification efficiency. Different affecting parameters in a groundwater-thin film composite system are synthesized and an in-depth overview is presented.     

高有机负荷冲击对填料型MBR运行性能的影响

针对分散式农村生活污水有机负荷变化明显的特点,研究了填料型厌氧-缺氧-好氧膜生物反应器（A²O-MBR）抗高有机负荷的能力,考察了高有机负荷冲击对污染物去除效果、悬浮和附着污泥性质以及膜污染的影响.结果表明,高负荷冲击期间污染物去除稳定,氨氮去除率在冲击第3d从99.1%下降到78.5%,出水氨氮浓度高于5mg/L,随后去除率恢复至97.6%;悬浮和附着微生物的三磷酸腺苷（ATP）含量增加;附着生物量显著增加;细胞外聚合物（EPS）增加;高有机负荷冲击期间膜污染更严重,膜面污染层EPS含量显著增加;太阳能微动力A²O-MBR系统能减少10%的碳排放.