Influence of osmotic distillation on membrane absorption for the treatment of high strength ammonia wastewater

Osmotic distillation (OD) was found to be a coupled process in membrane absorption (MA) for the treatment of high strength ammonia wastewater. As a result, ammonia could not be concentrated in absorption solution(AS) as expected. The inhibition of the coupled OD in MA process was investigated as well as various factors affecting the inhibition. The results indicated that the coupled OD can be effectively inhibited by heating concentrated solution and cooling dilute solution. It was also found that experimental minimum inhibition temperature difference(MITD) between concentrated and dilute solutions was different when using polyvinylidene fluoride(PVDF) and polypropylene(PP) membranes respectively, which could be ascribed to material properties, such as OD and membrane distillation (MD) coefficients of the membranes. Experimental MITDs were found to be higher than theoretical MITDs which were calculated using a simplified method.     

UV-catalytic treatment of spent caustic from ethene plant with hydrogen peroxide and ozone oxidation

The performance of UV/H2O2, UV/O3 and UV/H2O2/O3 oxidation systems for treating spent caustic from an ethylene plant was investigated, in UV/H2O2 system, with the increase of H202 dosage, removal efficiencies of COD and the ratio of biochemical oxygen demand(BOD) to chemical oxygen demand(COD) of the effluent were increased and a better performance was obtained than the H2O2 system alone. In UV/H2O2 system, removal efficiency of COD reach 68% under the optimum condition, and BOD/COD ratio was significantly increased from 0.22 to 0.52. In UV/O3 system, with the increase of O3 dosage, removal efficiency of COD and BOD/COD ratio were increased, and a better performance was obtained than the O3 system alone. Under the optimum condition, removal efficiency of COD was 54%, and BOD/COD ratio was significantly increased from 0.22 to 0.48. In UV/H2O2/O3 system, COD removal efficiency was found to be 22.0% higher than UV/O3 system.     

Dissimilatory reduction of FeIII (EDTA) with microorganisms in the system of nitric oxide removal from the flue gas by metal chelate absorption

In the system of nitric oxide removal from the flue gas by metal chelate absorption, it is an obstacle that ferrous absorbents are easily oxidized by oxygen in the flue gas to ferric counterparts, which are not capable of binding NO. By adding iron metal or electrochemical method, Fe^Ⅲ (EDTA) can be reduced to Fe^Ⅱ(EDTA).However, there are various drawbacks associated with these techniques. The dissimilatory reduction of Fe^Ⅲ(EDTA) with microorganisms in the system of nitric oxide removal by metal chelate absorption was investigated. Ammonium salt instead of nitrate was used as the nitrogen source, as nitrates inhibited the reduction of Fe^Ⅲ due to the competition between the two electron acceptors. Supplemental glucose and lactate stimulated the formation of Fe^Ⅱ more than ethanol as the carbon sources. The microorganisms cultured at 50~C were not very sensitive to the other experimental temperature, the reduction percentage of Fe^Ⅲ varied little with the temperature range of 30-50℃.Concentrated Na2 CO3 solution was added to adjust the solution pH to an optimal pH range of 6-7. The overall results revealed that the dissimilatory ferric reducing microorganisms present in the mix-culture are probably neutrophilic, moderately thermophiUc Fe^Ⅲ reducers.     

国家《大气污染防治行动计划》健康效益评估

为了提高空气质量改善进程,2013 年国家发布了《大气污染防治行动计划》。本文基于空气污染与健康效益评估模型(BenMAP),对人口分布资料、大气污染与人体健康影响的暴露反应关系等进行了本土化修正,采用“支付意愿法”与“疾病成本法”相结合的方法,系统评估了《大气污染防治行动计划》实施后,PM_2.5 污染变化引起的环境健康效益。研究结果表明,《大气污染防治行动计划》的实施将在一定程度上降低PM_2.5 环境浓度,改善环境空气质量。如果《大气污染防治行动计划》空气质量目标全面实现,可以避免城镇8.9 万居民的过早死亡,减少12 万人次住院治疗以及941 万人次的门诊和急诊病例,实现的全国健康效益约为867 亿元/ 年,说明了《大气污染防治行动计划》实施的健康有益性。本文对政府部门开展污染损失评估及制定环境健康政策具有重要的参考价值。     

新型复合材料处理氮磷废水的性能研究

采用阳离子表面活性剂十六烷基三甲基溴化铵（Hexadecyl Trimethyl Ammonium Bromide，HDTMA）和稀土溶液氯化镧（LaCl₃）对人造沸石进行改性，以增强其对水中氨氮和总磷的同步去除效果.结果表明，HDTMA和LaCl₃可有效负载于人造沸石表面，且在pH为7的条件下，改性沸石对氨氮和总磷的去除率分别由改性前的75%和1%提高到95.67%和91.96%.影响因素的实验表明，改性沸石对不同浓度废水的氨氮和总磷去除率均达到90%以上；氮、磷的去除率随改性沸石投加量的增加而上升；准二级动力学模型适合描述改性沸石对氨氮吸附的动力学过程，准一级动力学模型适合描述改性沸石对总磷吸附的动力学过程；吸附等温线说明改性沸石对水中氨氮的吸附属于离子交换，对水中磷酸盐的吸附包含离子交换和化学吸附两种过程.此外，通过再生性能、负载强度和离子竞争的试验证明改性沸石能应用于实际生化尾水的氮、磷去除.     

杭州市水源切换对饮用水中DBPs分布影响及其健康风险评价

千岛湖配水工程改善了杭州市的供水水质,水源由钱塘江为主转变为千岛湖外调水源为主.以供水管网末端龙头为调查对象,考察了水源切换前后饮用水中消毒副产物(disinfection by-products,DBPs)的构成特征,并对DBPs存在水平的致癌和非致癌风险进行了对比分析.结果表明供水管网终端龙头水在水源切换后水质明显...     

镉"加标"沉积物对泥鳅(Misgurnus anguillicaudatus)生物毒性研究

选择泥鳅(Misgurnus anguillicaudaus)作为受试生物,以泥鳅死亡率、血液红细胞数量、红细胞体积、红细胞微核率和核异常率作为测试指标,考察了沉积物中"加标"金属镉(Cd)的毒性状况,探讨了水体沉积物中重金属的生物毒性影响.结果表明:高有机质的粘土粉砂性沉积物能够有效吸附重金属镉;镉加标暴露组泥鳅的死...     

工程机械不同工况下PM_(2.5)排放及其碳质组分特征

我国工程机械排放控制起步较晚.为研究实际工况下工程机械的PM2.5排放特性及其碳质组分构成,采用便携式颗粒物稀释采样系统,对3台工程机械(2台挖掘机和1台装载机)在不同典型工况(行驶、作业和怠速)下的PM2.5及其碳质组分〔OC(有机碳)和EC(元素碳)〕的现场排放特征进行了测试.结果表明:沃尔沃挖掘机、山河智能挖掘机的PM2.5排放因子(基于燃油)分别为1.85~3.26和1.56~2.62 g/kg,厦工装载机的PM2.5排放因子为0.98~1.48 g/kg.不同工况对PM2.5排放因子影响较大,怠速工况下PM2.5排放因子是行驶工况下的1.49~1.76倍.工程机械排放的PM2.5中,碳质组分是最主要的成分,其质量分数高达71.0%~84.5%.其中,w(OC)为44.6%~72.0%,在怠速工况下最高;w(EC)则为8.6%~30.9%,在行驶工况下较高.测试工程机械的PM2.5排放水平较高,因此应尽快加强工程机械排放的污染防治.     

安全管理基础数据的统计分析

本文阐述了通过对安全管理基础数据的统计分析,研究企业在某一时期或阶段的安全生产状况,从中发现规律、认识问题,以此来制定相应的有针对性的安全管理措施,抑制事故和不安全现象的发生,推动企业的安全管理工作。     

两级序批式MBR膜污染特性研究

采用两级SBR与膜法相结合的两级序批式MBR工艺处理生活污水,考察两级序批式运行模式对膜污染特性的影响.对运行111 d后的平板膜污染阻力分布进行了测算,并对两级序批式MBR与连续流单级好氧MBR的平板膜污染速率进行对比试验.结果表明: 两级序批式MBR的平板膜污染阻力以凝胶极化阻力为主,占总阻力的43%,沉积阻力较低,仅占总阻力的10%;与连续流单级好氧MBR相比,两级序批式MBR可以在更高的膜通量下运行,保持更低的膜污染速率,在运行42 d后,过膜流量从100 L/h下降至85 L/h,过膜压差从1.52×10~4 Pa增加至2.22×10~4 Pa;而连续流好氧MBR系统,过膜流量从61 L/h降低至39 L/h,过膜压差却从1.01×10~4 Pa增加至2.63×10~4 Pa.研究表明,两级序批式MBR工艺可以改善膜过滤过程的水力条件,从而有效地减缓浓差极化,降低沉积污染及凝胶层污染,序批式、膜间歇运行与空曝的结合起到了关键性作用.