较高负荷条件下活性污泥-生物膜联合系统对氮磷的去除

中试试验条件下,考察了较高的有机负荷对活性污泥-悬浮载体生物膜联合系统对氮磷去除效果的影响。试验表明,水温为20~33℃时,在联合系统污泥龄为4~9d,有机负荷达到0.18~0.55kg/kg.d条件下,对磷的去除效果稳定在90%左右,氨氮的去除率达到80%以上,出水总氮平均为11mg/L,达到《城镇污水处理厂污染物排放标准》(GB18918-2002)中一级排放标准。同时,试验过程中也发现了联合系统的好氧池中存在明显的同步硝化反硝化现象,并初步分析了其原因与影响因素。     

镉试剂2B固相萃取光度法测定水中微量银

研究了镉试剂2B固相萃取测定银的方法。在pH为9.5的硼砂-氢氧化钠缓冲介质中,乳化剂-OP存在下,镉试剂2B与银反应生成2∶1稳定络合物,该络合物可用pH使用范围为1~12的W atersX terraTMRP18固相萃取小柱富集,小柱上富集的络合物用乙醇(内含0.01 mol/L、pH为9.5的四氢吡咯-醋酸缓冲溶液)洗脱后用光度法测定,在洗脱剂介质中最大吸收波长为555 nm,摩尔吸光系数为1.04×105L/(mol.cm)。银质量浓度在0.01~1.0μg/mL内符合比尔定律,方法用于环境水样中银含量的测定,结果令人满意。     

构建循环经济体系的系统经济学分析

本文首先从经济系统与循环经济体系之间的关系出发,论述了大力建设循环经济体系的关键点;接着描述传统经济系统中存在的主要问题,分析现有循环经济研究框架的不足;最后从系统经济学角度提出了一些完善中国循环经济体系建设的对策。     

典型航空印刷电路板盐雾环境腐蚀损伤规律研究

针对盐雾环境对航空电子产品腐蚀的突出作用,研究了典型航空印刷电路板在盐雾环境中的腐蚀（损伤）特征,并与印刷电路板的海洋大气环境效应进行了对比分析,获取了典型航空印刷电路板盐雾环境腐蚀（损伤）机理,建立了航空印刷电路板腐蚀（损伤）随盐雾环境作用时间的演变规律。     

浙东四明山红色旅游目的地的开发与建设

通过四明山红色旅游目的地开发建设的优势、机遇及劣势与挑战的分析,提出了开发与建设四明山红色旅游目的地的六大策略,即政府主导与市场运作相结合的开发策略、社会效益和经济效益兼顾的开发策略、红色旅游目的地品牌策略、"红绿结合"的开发策略、区域合作策略、基于和谐旅游发展的开发策略。     

生态系统健康与生态恢复及工程相应关系初探

自然生态系统健康的评价因素有组织结构、活力、恢复力、生态系统服务功能的维护、管理选择、对相邻系统的影响、减少投入、对人类健康的影响等,其类型有健康、较健康、亚健康、不健康、患病五级;其相应的生态恢复类型为生态预防、自然恢复、生态修复、生态重建;相应的生态工程有建立自然保护区、封育、补播与放流、人工林、人工草场、人工湿地等.     

Distribution characteristics of nonylphenolic chemicals in Masan Bay environments, Korea

To understand the distribution characteristics of nonylphenolics and sterols, samples such as in creek water, sea surface water, waste water treatment plant (WWTP) effluent water, sediment and mussel were collected and analyzed. The principal analytes are nonylphenol (NP), nonylphenol monoethoxylate (NP1EO), nonylphenol diethoxylate (NP2EO), coprostanol (5beta) and cholestanol (5alpha). All these target pollutants showed 100% detection frequency in all of the samples analyzed. Total concentration of nonylphenolic compounds ranged from 334 to 3628ngl(-1) (average: 1331ngl(-1)) in creek water, from 15 to 36400ngl(-1) (average: 1013ngl(-1)) in sea surface water, from 131 to 2811ngg(-1) dry weight (average: 581ngg(-1) dry weight) in sediment and from 50.5 to 289ngg(-1) dry weight (average: 139ngg(-1) dry weight) in mussel. For water samples, levels of nonylphenolics determined in summer season were higher than those in spring season. Among them, nonylphenol and NP1EO was dominant in creek water and seawater, respectively. The highest concentration was recorded in sediment near a WWTP effluent outlet. And high levels of nonylphenolics and sterols were found in about 3km area surrounding WWTP effluent outlet. Coefficient of linear regression (R(2)) for NP in mussel and in sediment was 0.90. Similarly good correlation (R(2)=0.98) was obtained between concentration in water and in mussel indicating that a steady state has been reached in this bay. The calculated bio concentration factor (BCF=2990) for NP in Masan Bay agrees well with reported values in the literature.     

Oxidation of elemental mercury using atmospheric pressure non-thermal plasma

The oxidation of gas phase elemental mercury (Hg0) by atmospheric pressure non-thermal plasma has been investigated at room temperature, employing both dielectric barrier discharge (DBD) of the gas mixture of Hg0 and injection of ozone (O3) into the gas mixture of Hg0. Results have shown that the oxidative efficiencies of Hg0 by DBD and the injection of O3 are 59% and 93%, respectively, with energy consumption of 23.7 J L(-1). This combined approach has indicated that O3 plays a decisive role in the oxidation of gas phase Hg0. Also the oxidation of Hg0 by injecting O3 into the gas mixture of Hg0 proceeds with better efficiency than DBD of the gas mixture of Hg0. These results have been explained by the incorporation of the competitive reaction pathways between the formation of HgO by O3 and the decomposition of HgO back to Hg0 in the plasma environment.     

Evaluation of municipal sewage treatment systems for pollutant removal efficiency by measuring levels of micropollutants

In order to evaluate the municipal sewage treatment systems used at Harbin municipal sewage treatment plant for their pollutant removal efficiency, raw sewage and effluent samples at different treatment stages from the sewage treatment systems were taken, priority pollutants (PPs) were identified and quantified using gas chromatography-mass spectrometry (GC-MS) and inductively coupled plasma-atomic emission spectrograph (ICP-AES). The test results indicated that there were one hundred and fifty species of organic pollutants identified in the raw sewage sample, and only ten species of PPs in all the sewage samples. The levels of dimethyl phthalate (DMP), diethyl phthalate (DEP), dibutyl phthalate (DBP), di-n-octyl phthalate (DnOP) in the sewage samples were 0.779-0.111 microg l(-1), 1.977-0.022 microg l(-1), 6.411-2.194 microg l(-1) and 7.152-2.953microg l(-1), respectively, and most of these phthalate esters (PAEs) were removed through anaerobic/aerobic (A/O) process; The levels of alachlor, acetochlor, atrazine were 0.074-0.021 microg l(-1), 0.160-0.096 microg l(-1) and 0.238-0.184 microg l(-1), respectively, and the total removal efficiency of atrazine was poorest through the sewage treatment systems. The levels of Cu, Cr, Se, Hg, Ni and Zn were 0.0030-0.2327 mg l(-1). It is therefore concluded from these results that the sewage treatment systems were efficient in removing most of the organic and inorganic compounds in this study, and so, the discharged effluent could cause little of the secondary pollution of the aquatic environment.     

Performance of an electrochemical COD (chemical oxygen demand) sensor with an electrode-surface grinding unit

An electrochemical COD (chemical oxygen demand) sensor using an electrode-surface grinding unit was investigated. The electrolyzing (oxidizing) action of copper on an organic species was used as the basis of the COD measuring sensor. Using a simple three-electrode cell and a surface grinding unit, the organic species is activated by the catalytic action of copper and oxidized at a working electrode, poised at a positive potential. When synthetic wastewater was fed into the system, the measured Coulombic yields were found to be dependent on the COD of the synthetic wastewater. A linear correlation between the Coulombic yields and the COD of the synthetic wastewater was established (10-1000 mg L(-1)) when the electrode-surface grinding procedure was activated briefly at 8 h intervals. When various kinds of wastewater samples obtained from various sewage treatment plants were measured, linear correlations (r(2)> or = 0.92) between the measured EOD (electrochemical oxygen demand) value and COD of the samples were observed. At a practical wastewater treatment plant, the measurement system was successfully operated with high accuracy and good stability over 3 months. These experimental results show that the application of the measurement system would be a rapid and practical method for the determination of COD in water industries.