内循环厌氧反应器多相流流场的三维数值分析简

利用数值模拟的方法,引入欧拉双流体多相流模型及标准k-ε紊流模型,模拟计算内循环厌氧反应器的三相流三维流场,并通过改变污泥颗粒密度及进水流量,针对固相流速及固含率的变化情况,分析条件的改变对流场的影响。研究结果表明,应用数值模拟方法可以获得内循环厌氧反应器内的流场特征;污泥颗粒密度及进水流量的改变对于反应器内污泥颗粒的流速及分布的均匀性有较为明显的影响。模拟结果对反应器的应用及优化设计具有一定的参考价值。     

催化铁与生物法耦合除磷工艺特性简

为了研究催化铁与生物耦合后对生物除磷特性的影响,实验采用人工配水用厌氧/好氧间歇流式富集培养聚磷微生物。对比发现,催化铁与生物耦合组中厌氧末段ORP降低了约60 mV,pH值小幅度的上升（≤0.3）,整个培养过程中铁离子的浓度开始快速增加,之后趋于稳定（约40 mg Fe/g MLSS）。对好氧末段污泥SVI值比较发现,耦合工艺污泥沉降性能得到改善。除磷曲线比较发现,耦合组中厌氧末段磷的释放量下降,而好氧阶段磷的吸收速率增加;胞内聚合物提取表明,耦合组厌氧末段聚磷菌细胞内PHA含量有提高,好氧末段糖原含量有下降。磷形态提取分析表明,耦合组好氧末段污泥中无机态PO^3-₄-P含量更高。低浓度铁离子可以起到与生物耦合同步除磷的目的,本工艺长期运行未发现耦合体系中催化铁对除磷的抑制作用。     

响应曲面法优化电化学氧化技术处理染料废水

采用IR和XRD等手段对自制磷钼酸铁(FePMo12)杂多酸进行表征,表明杂多阴离子具有Keggin结构。将FePMo12负载于修饰后的分子筛上制备FePMo12/APTES-4A催化剂填充于电化学反应器中,考察电化学氧化体系对酸性大红3R染料废水的脱色效果,其脱色率高于二维电化学反应器。利用Box-Behnken中心组合实验设计及响应面(RSM)分析,以pH值,板间距,槽电压,曝气量为实验因素,建立了以酸性大红3R的脱色率为响应值的二次多项式回归模型。研究表明,当电解时间为60 min时,曝气量0.05 m3/h、pH为2、板间距3.0 cm、槽电压11.0 V,在此条件下色度去除率可达69.4%,模型预测值与实验值能很好地吻合。方差分析结果表明,槽电压和pH、pH和曝气量的交互作用对响应值具有显著性影响。     

Toxicity of TiO2, ZrO2, Fe,Fe2O3, and Mn2O3 nanoparticles to the yeast, Saccharomyces cerevisiae

The growing application of engineered nanomaterials is leading to an increased occurrence of nanoparticles (NPs) in the environment. Thus, there is a need to better understand their potential impact on the environment. This study evaluated the toxicity of nanosized TiO₂, ZrO₂, Fe⁰, Fe₂O₃, and Mn₂O₃ towards the yeast Saccharomyces cerevisiae based on O₂ consumption and cell membrane integrity. In addition, the state of dispersion of the nanoparticles in the bioassay medium was characterized.     

Pseudomonas fluorescens Dynamics in the Soil Surface to Subsurface Transect

Microbial displacement in the soil is an important process for bioremediation and dispersal of wastewater pathogens. We evaluated cell movement in surface and subsurface red-yellow podzolic soil driven by advection and microbial motility and also survival of a microbial population at high pressure as is prevalent in deep soil layers. Pseudomonas fluorescens Br 12, resistant to rifampycin and kanamycin, was used as a model organism traceable in non-sterile soil. Our results showed that more than 40% of the P. fluorescens population survived under high pressure, and that microbial motility was not a major factor for its displacement in the soil. Cells were adsorbed in similar amounts to surface and subsurface soils, but more viable cells were present in the leachate of surface than in subsurface soils. The nature of this unexpected cell binding to the subsurface soil was studied by EPR, Mossbauer, NMR, and infrared techniques, suggesting iron had a weak interaction with microbes in soil. P. fluorescens movement in soil resulted mainly from convection forces rather than microbial motility. The transport of this bacterium along the transept toward groundwater encountered restricted viability, although it survived under high pressure conditions simulating those in deep soil layers.     

火焰原子吸收分光光度法测定饮用水中铁和锰的不确定度评定

分析了测试过程中不确定度影响因素,其主要来源为标准溶液、标准曲线拟合、样品重复测定、分光光度计4部分。本次测量结果为:铁(0.232±0.012)mg/L;锰(0.092±0.004)mg/L,k=2(约95%置信水平)。     

测定水中铁、锰、汞时前处理问题探讨

基于大量实测数据统计,比较了测定水中铁、锰、汞3种重金属时,样品是否过滤、加酸保存等前处理方式对测定结果的影响,提出铁、锰水样需过滤检测,汞水样不能过滤检测,且3种金属的水样均需加酸保存,这样测定的结果才能根据现行水环境质量标准进行评价。     

Bio-SR工艺去除硫化氢气体的研究

采用Bio-SR工艺,利用铁盐吸收与氧化亚铁硫杆菌的联合作用对H2S进行脱除实验。通过改进微生物的培养条件,减少了83.9%的沉淀量,一定程度上解决了挂膜后生物填料塔易堵塞的问题,保证了填料塔的连续运行。在实验选取工况下,硫化氢脱除率可达到98.4%以上,当吸收液中Fe3+浓度为5.5～6 g/L、H2S进气浓度为1 g/m3、通气量为0.08～0.12 m3/h时效果最佳,反应器可持续高效地运行。此外,对进气浓度、通气量与硫化氢去除率之间的相关性进行了进一步研究,其结果有利于反应器及运行参数的优化设计。     

基于AHP的POPs污染控制技术评价方法研究

POPs污染控制技术的引进和推广是削减POPs排放的重要手段,对最大限度地控制我国POPs污染,提升国家履行《斯德哥尔摩公约》的能力具有重要意义。为了筛选出适合我国发展需求与经济水平的技术,在对POPs污染控制技术进行分类研究的基础上,基于层次分析法(AHP)建立了POPs污染控制技术综合评价指标体系和评价方法。同时,选择钢铁行业的两种烟气POPs控制技术进行案例分析,证明了建立的评价方法具有较好的可行性。此外,评价结果表明,高炉煤气干式除尘余压压差发电技术优于转炉煤气干法烟气除尘及尘泥压块技术,应优先考虑在钢铁行业进行应用与推广,以提升行业POPs污染控制能力。