粘胶基活性炭纤维用于低浓度SO2常温脱除的实验研究

活性炭纤维（ACF）是一种新型功能性炭材料。应用粘胶基活性炭纤维（cellulose-ACF）对低浓度SO2（571 mg/m3）进行吸附氧化实验,通过改变活性炭纤维量、SO2浓度、氧浓度,观察cellulose-ACF脱除低浓度SO2能力的变化规律。实验结果表明,随着活性炭纤维量、氧浓度的增加,cellulose-ACF对低浓度SO2的脱除能力增强。在此基础上展望活性炭纤维在大气环保领域的应用前景。     

Residual concentrations of micropollutants in benthic mussels in the coastal areas of Bohai Sea, North China

Studies of heavy metals and organic pollutants in different benthic mussel species from Bohai Sea show that concentrations of Cd in mussels commonly exceed national biological quality standards. In addition, a site located in Laizhou Bay exhibits higher average concentrations of As, Hg and Pb with respect to the other sites. Residual levels of petroleum hydrocarbons at several sites in Liaodong Bay also exceed quality guidelines. Contents and compositional characteristics of DDT and its metabolites in mussels suggest the probability of recent inputs and potential ecological risks to the local benthic environment.     

污泥淤砂分离器再分离溢流污泥

研究了污泥淤砂分离器对分离原污泥所得的溢流污泥进行再分离时,分离器的分离效果和分离分流污泥的性质。实验结果表明,污泥淤砂分离器对溢流污泥进行再分离时,分离器的除砂效率为34.5%,分离度为1.60,与分离原污泥时相比,分离器的分离性能降低;分离得到的溢流污泥MLVSS/MLSS比值为0.406,仅比进料污泥增加了2.2%,未能进一步提高溢流污泥MLVSS/MLSS比值;分离得到的底流污泥浓度MLSS为16.81 g/L,仅为原污泥浓度的1.4倍,底流污泥SVI、CST分别为45.7 mL/g和1.37 s·L/g SS,与原污泥相比仅分别减小了9.3%和2.7%,溢流污泥再分离,会降低底流污泥的浓缩效果,降低底流污泥沉降性能、脱水性能的提高幅度,不利于底流污泥的处理处置。     

硝化细菌对碘普罗胺的降解及作用机制

将富含硝化细菌的驯化污泥投放于培养基中,以碘普罗胺(IOPr)为处理对象,研究硝化细菌对IOPr的降解促进作用情况。结果表明,富集培养的硝化细菌能有效地促进IOPr的降解,最佳反应条件为:温度30℃,pH 8.0~8.5,初始投加浓度为10 mg/L,同时在硝化细菌存在条件下,IOPr的5 d降解率可达84.1%。IOPr的生物降解属于共代谢机制,向培养基中加入葡萄糖、可溶性淀粉和麦芽糖,可以显著提高IOPr的降解去除率;在投加500 mg/L葡萄糖作为外加碳源时,硝化细菌对IOPr的3 d降解率可达60.3%。     

不同挂膜方式生物滴滤塔处理含H2S恶臭气体

采用菌剂挂膜,活性污泥挂膜和自然挂膜3种不同方式形成生物滴滤塔,考察挂膜方式对生物滴滤塔去除H2s恶臭气体的影响。结果表明,当进气H2S浓度为5mg／m3时,菌剂挂膜、活性污泥挂膜、自然挂膜形成的生物滴滤塔出气H2s浓度分别为15．7～17．4、11．6～14．8和15．0～15．9μg／m3;塔内压降分别为3—4mm水柱、6mm水柱和4—5mm水柱;喷淋后滤出液中硫酸根的浓度分别为14、22和17mg／L,硫的转化率分别为45％、60％和50％。当进气H2S浓度增大至7mg／m3时,3个塔经过7d的调整后,均能达到稳定状态,稳定后3个塔中出气H2s浓度和压降基本没变,喷淋后滤出液中硫酸根浓度依次增大至25、31和30mg／L左右。采用活性污泥挂膜形成的生物滴滤塔处理H2s的能力比菌剂挂膜和自然挂膜的高。     

华北某油田石油降解菌的筛选及降解特性

以石油为唯一碳源,从华北某油田污染土壤中筛选出石油降解菌12株。其中5株菌有较强降解能力,分别编号为z-3、z-6、z-7、z-8和z-b,在30℃,160 r/min摇床培养10 d后,菌株对石油降解率分别为63.8%、34.2%、44.8%、50.5%和42.3%。通过生理生化和分子生物学鉴定,确定这5株菌分别属于假单胞菌属（Pseudomonas）、根瘤菌属（Rhizobium）、假黄单胞菌属（Pseudoxanthomonas）、假单胞菌属（Pseudomonas）、鞘氨醇单胞菌属（Sphingomonas）。通过对这5株菌生物量、脱氢酶及邻苯二酚 2,3-双加氧酶活性的监测,发现生物量及酶活性与石油降解能力具有直接关系。最后,对5株菌的生长条件进行优化,其中z-3、z-6、z-7和z-b菌株对石油降解率较优化前提高10%左右。     

广东省道路交通噪声预测统计模型

为了建立符合广东省的道路交通噪声预测模型,在国内学者相关研究成果的基础上,对FHWA模型进行了深入分析,并根据道路交通噪声预测模型原理,引入等效车流量等概念建立了理论噪声预测统计模型.在此基础上,对广东省市政路和高速路的交通噪声实测数据进行多元线性回归分析,确定广东省交通噪声预测统计模型.经验证,在广东省交通噪声预测评价中该模型预测精度非常高.该研究思路与方法值得在全国各地区处理交通噪声环境问题的工作中加以推广与应用.     

染料厂污染土壤中六氯苯的水淹法厌氧降解

以乙酸为碳源,采用正交实验的方法,探讨了水淹法厌氧降解某染料厂污染土壤中六氯苯的效果,研究考察了初始pH、反应温度和固液比3个环境因素对六氯苯降解率的影响,确定了六氯苯最佳的厌氧降解条件。结果表明,初始pH对土壤中六氯苯的降解率影响最大。在初始pH为5,反应温度为45℃,固液比为1∶1的最佳反应条件下,六氯苯的降解率最高达到52.56%。     

Process analysis of a regional air pollution episode over Pearl River Delta Region,China, using the MM5-CMAQ model

This study focuses on the influences of a warm high-pressure meteorological system on aerosol pollutants, employing the simulations by the Models-3/CMAQ system and the observations collected during October 10–12, 2004, over the Pearl River Delta (PRD) region. The results show that the spatial distributions of air pollutants are generally circular near Guangzhou and Foshan, which are cities with high emissions rates. The primary pollutant is particulate matter (PM) over the PRD. MM5 shows reasonable performance for major meteorological variables (i.e., temperature, relative humidity, wind direction) with normalized mean biases (NMB) of 4.5–38.8% and for their time series. CMAQ can capture one peak of all air pollutant concentrations on October 11, but misses other peaks. The CMAQ model systematically underpredicts the mass concentrations of all air pollutants. Compared with chemical observations, SO₂ and O₃ are predicted well with a correlation coefficient of 0.70 and 0.65. PM_2.5 and NO are significantly underpredicted with an NMB of 43% and 90%, respectively. The process analysis results show that the emission, dry deposition, horizontal transport, and vertical transport are four main processes affecting air pollutants. The contributions of each physical process are different for the various pollutants. The most important process for PM₁₀ is dry deposition, and for NO_x it is transport. The contributions of horizontal and vertical transport processes vary during the period, but these two processes mostly contribute to the removal of air pollutants at Guangzhou city, whose emissions are high. For this high-pressure case, the contributions of the various processes show high correlations in cities with the similar geographical attributes. According to the statistical results, cities in the PRD region are divided into four groups with different features. The contributions from local and nonlocal emission sources are discussed in different groups.

Implications: The characteristics of aerosol pollution episodes are intensively studied in this work using the high-resolution modeling system MM5/SMOKE/CMAQ, with special efforts on examining the contributions of different physical and chemical processes to air concentrations for each city over the PRD region by a process analysis method, so as to provide a scientific basis for understanding the formation mechanism of regional aerosol pollution under the high-pressure system over PRD.     

Treatment of a dyeing wastewater from a woolen mill using an A/O membrane bio-reactor

An anaerobic/oxic membrane bioreactor (A/O MBR) was used for treatment of dyeing wastewater from a woolen mill.COD and color of the wastewater were 54-473 mg/L and 40-400 dilution time (DT) respectively. The ratio of BOD5/COD was less than 0.13. By the A/O MBR process, the average removal of COD, BOD5, color and turbidity was 82％, 96％, 71％ and 99％, respectively. The average COD, BOD5, color and turbidity of effluent was 37 nag/L, 0.8 mg/L, 40 DT and 0.44 NUT respectively. The effluent COD met the local standard of reuse water in Beijing, China. The average COD volume load of the anaerobic biological tank was 0. 0483 kgCOD/(m3·d) and that of the aeration tank of the MBR was 0. 3589 kgCOD/(m3·d). The sludge load of the MBR was 0.19 kgCOD/(kg· MLSS· d) on average and the maximum of that was 0.4 kgCOD/( kg· MLSS· d).The flux of the A/O membrane bioreactor could be remained at larger than 50 L/(h· m2· 0.1MPa). The results indicated that A/O membrane bioreactor has technical feasibility for treatment of woolen mill wastewater.