好氧颗粒污泥自生动态膜生物反应器处理碱减量印染废水

自生动态膜生物反应器(SFDMBR)接种颗粒污泥启动,研究溶解氧浓度和水力停留时间对该反应器处理碱减量印染废水的影响。自生动态膜生物反应器形成稳定的动态膜后,出水浊度小于10 NTU,系统对浊度的去除率在90%以上,溶解氧和水力停留时间对反应器出水浊度基本无影响。系统对废水色度的去除率随着溶解氧浓度的提高和水力停留时间的延长而增加,但是系统对色度的去除效率一般不超过40%。溶解氧浓度由0.3 mg/L逐渐增大至2.4 mg/L,COD的去除率由40%提升至80%,而当溶解氧浓度大于1.0 mg/L后,UV254的去除率达到95%。水力停留时间在8~48 h时,COD去除效率由65%逐渐上升至85%左右;水力停留时间在8~32 h,UV254去除效率为68%~93%,超过32 h后水力停留时间对UV254去除效率的影响已不明显。     

纳滤工艺去除水中微量内分泌干扰物

主要研究了DL1210型纳滤膜去除水中邻苯二甲酸二丁酯(DBP)、邻苯二甲酸二(2-乙基己基)酯(DEHP)、乐果和莠去津的影响因素,考察了温度、pH值、初始浓度、跨膜压力(TMP)和运行时间对膜通量和截留率的影响。结果表明,纳滤工艺是去除水中微量DBP、DEHP、乐果和莠去津的有效方法,初始pH值和温度的升高会导致纳滤膜对DBP、DEHP、乐果和莠去津的截留率的降低,膜对DBP和DEHP的截留率随初始浓度的升高而降低,TMP和运行时间不会对膜通量和目标污染物的截留率造成显著影响。当初始pH为5、初始浓度为5μg/L、温度为5℃、TMP为0.4 MPa时,纳滤工艺对DBP、DEHP、乐果和莠去津的截留率达到最佳,分别为91.8%、89.8%、98.02%和77.6%,出水中DBP、DEHP、乐果和莠去津浓度分别为0.41、0.49、0.099和1.12μg/L。     

Characterization of polychlorinated biphenyls and brominated flame retardants in surface soils from Surabaya, Indonesia

In this study, soil contamination by PCBs, PBDEs, HBCDs and two novel BFRs such as 1,2-bis-(2,4,6-tribromopenoxy) ethane (BTBPE) and decabromodiphenyl ethane (DBDPE) in various locations such as industrial, urban, rural, dumping site and agricultural areas of Surabaya, Indonesia has been characterized in order to evaluate their contamination status, profiles, potential sources, fate and behavior. Range and median concentrations of PCBs, PBDEs, HBCDs, BTBPE and DBDPE were ND - 9.6 (1.2), 0.069 - 24 (7.4), ND - 1.8 (0.48), ND - 1.7 (0.14) and ND - 7.6 (2.2) ng g⁻¹ dw, respectively. Industrial, urban and dumping areas were inventoried as the main sources of these pollutants. Decreasing gradient levels were observed for these contaminants from industrial district, urban, dumping site, rural and agricultural areas, in that order. Furthermore, organic carbon contents and proximity to the point sources were found as the major controlling factors. Contaminant profiles were characterized by the predominance of hexa-, hepta- and penta-homologues for PCBs; deca-, nona- and octa- for PBDEs and α-isomer for HBCDs. Product mixtures such as Ar1260/KC600 and Ar1254/KC500 for PCBs, deca- and octa-BDEs for PBDEs were the possible common formulations used in study area. To our knowledge, this is a first comprehensive study on characterization of soil contamination by PCBs, PBDEs and HBCDs together with two novel BFRs in a highly industrialized city located in tropical region. This study provides baseline information for establishing national monitoring programs in Indonesia.     

冬季菹草对悬浮泥沙的影响

利用冬季沉水植物菹草构建由浅水到深水的串联系统,含沙水依次流经浅水区和深水区,测定各级菹草对水体悬浮泥沙含量和沉降量的影响.结果显示,菹草系统可以降低水体中悬浮泥沙含量,并随水力停留时间延长而降低程度加大.各运行条件下,菹草系统悬浮泥沙平均沉降量65.7 g·m-2,比对照组高39.4%.菹草表面泥沙的吸附是一个"吸附-沉降-再吸附" 的动态过程,吸附量为3.26～5.69 g·kg-1.菹草对冬季水生态系统的自净功能起着十分重要的作用.     

Imazaquin degradation and metabolism in a sandy loam soil amended with farm litters

Irnazaquin applied in legume crops has a long residual time in soil, which often impacts safety of the susceptible crops. To increase safety of imazaquin application, two composted litters, bovine manure （BM） and chicken manure （CM）, were used to determine their effects on imazaquin environmental behavior by incorporating each kind of manure into the tested sandy loam soil at 10% （w/w）. The degradation of imazaquin in BM- and CM-amended soil was about 2.4 and 1.5 times, respectively, faster than that in unamended soil. The half-lives of imazaquin in BM-amended soil varied between 6.7 and 15.4 d over the temperature range of 20 to 40℃, and the degradation rate constant （k） increased by a factor of about 1.5 for every 10℃ change. Higher mix ratio did not significantly increase the degradation, and the optimal active degradation of imazaquin was observed approximately at the mix ratio of 10：1 of soil to BM. The different moisture levels had negligible effect on imazaquin degradation. In both unamended and BM-amended treatments, two metabolites were observed at 5, 10 and 30 d after treatment. One metabolite at retention time （RT） of 8.4 rain was identified as 2-（4- hydroxyl-5-oxo-2-imidazolin-2-yl） quinoline acid, originating from the loss of isopropyl group and hydroxylation at the 4-position of imidazolinone ring. The other at RT of 12.9 rain was identified as quinoline-2,3-dicarboxylic anhydride, resulting from detachment of imidazolinone ring and the forming of dicarboxylic anhydride. This finding suggested that the addition of farm litters into soil might be a good management option since it can not only increase soil fertility but also contribute to increase safety of imazaquin application to the following susceptible crops.     

基于热带海洋大气环境下机载PCB板的环境适应性对比研究

目的 通过机载PCB板(Printed Circuit Board,PCB)在热带海洋大气环境下的腐蚀老化特征和电气性能退化规律分析,研究其在热带海洋大气环境下的环境适应性。方法 根据热带海洋大气环境中PCB板的实际使用环境大多为舱室内部封闭或半封闭的情况,分别设计并开展海南万宁海洋平台棚下暴露场和某海域环境户外简易遮蔽玻璃框下3 a的自然环境试验。结果 PCB板的焊点、焊盘、印制导线以及引线头等部位在2种试验环境中均出现了不同程度的腐蚀破坏,试验后期,所有部位的腐蚀程度全部达到了4级,导通电阻从几十毫欧增大至几十兆欧,绝缘电阻从10 GΩ以上降低至几兆欧。结论 在万宁站试验2 a和某海域试验3 a后,PCB板均不满足耐电压的技术要求(500 V交流电压60 s),万宁海洋平台棚下暴露场对PCB板的环境适应性更为严酷。     

A~2/O-曝气生物滤池工艺处理低C/N比生活污水脱氮除磷

以低C/N比实际生活污水为研究对象,重点考查了A2/O-曝气生物滤池生化系统的脱氮除磷特性.同时,考虑到A2/O工艺的主要功能是除磷及反硝化,而曝气生物滤池则以硝化为目的.因此,通过缩短A2/O的泥龄,可将硝化过程从A2/O中分离出去,让曝气生物滤池完成硝化,实现硝化菌和聚磷菌的分离,并解决了硝化菌和聚磷菌泥龄之间的矛盾.试验结果表明,该生化系统可实现有机物、氮和磷的同步去除.在平均C/N比为4.2,内回流比R为250%的条件下,平均进水COD、TN、TP分别为239.9、57.3和5.1mg·L-1,平均最终出水COD、TN、TP分别为34.1、13.3和0.1mg·L-1,去除率分别为85.8%、76.9%和98.3%.曝气生物滤池对氨氮几乎保持了100%的去除率.序批试验表明,反硝化聚磷菌占聚磷菌的比例为40.5%.     

印刷线路板的超临界流体分离实验

目前印刷线路板(Printed Circuit Board, PCB)的资源化循环利用方法存在材料回收率低和环境污染的不足,采用一种新的超临界流体技术对PCB中的金属及其它成分进行分离处理,在采用丙酮、CO2及Lewis-酸的混合介质及优化的温度和压力反应条件下,获得了90%的金属回收率,高于目前的机械破碎分选实验结果.该方法为线路板的资源化循环再利用提供了一个新的有效选择.     

多氯联苯的气相色谱/质谱/质谱(GC/MS/MS)法测定

采用气相色谱/质谱/质谱(GC/MS/MS)法测定多氯联苯(PCB),具有良好的灵敏度和选择性,在地表水样品检测时,样品只须进行简单的液液萃取-浓缩,不须任何净化过程即可上机分析,方法检出限低于ng/L级。     

Environmental impact assessment (EIA): Equilibrium fugacity calculations and worst case approach

A mathematical model UNITRISK which can be used for screening purposes and risk ranking was set up to calculate relative risk values of single chemicals and mixtures of chemicals towards single or mixtures of organisms via contamination of air, water, soil and food dose. The concentration values are calculated by applying the fugacity concept or a dose must be defined. The dose-response is assumed to be linear versus concentration and degradative processes are not considered which is the worst case. The assumption that equilibria between the environmental phases exist is simplifying the model and is also representing the worst case. A mean risk factor is calculated which is 1 if the endpoint values (LC₅₀, LD₅₀, ADI, etc.) are exceeded for the investigated organisms and man.