Entrainment mortality of Ichthyoplankton: Detectability and precision of estimates

The ability to detect and to develop a precise and accurate estimate of the entrainment mortality fraction is an important step in projecting power plant impacts on future fish population levels. Recent work indicates that these mortailities may be considerably less than 100% for some fish species in the early life stages. Point estimates of the entrainment mortality fraction have been developed based on probabilistic arguments, but the precision of these estimates has not been studied beyond the simple statistical test of the null hypothesis that no entrainment mortaility exists.The ability to detect entrainment mortality is explored as a function of the sample sizes (numbers of organisms collected) at the intake and discharge sampling stations of a power plant and of the proportion of organisms found alive in the intake samples (intake survival). Minimum detectable entrainment mortality, confidence interval width, and type II error (probability of accepting the null hypothesis of no entrainment mortality when there is mortality) are considered. Increasing sample size and/or decreasing sampling mortality will decrease the minimum detectable entrainment mortality, confidence interval width, and type II error for a given level of type I error.The results of this study are considered in the context of designing useful monitoring programs for determining the entrainment mortality fraction. Preliminary estimates of intake survival and the entrainment mortality fraction can be used to obtain estimates of the sample size needed for a specified level of confidence interval width or type II error. Final estimates of the intake survival and the entrainment mortality fraction can be used to determine the minimum detectable entrainment mortality and the type II error.     

Fe3O4活化过硫酸盐体系同步去除诺氟沙星和铅

采用Fe₃O₄活化过硫酸盐（PS）同步去除水中的NOR （诺氟沙星）和Pb （II）.探讨了Fe₃O₄投加量、PS浓度、初始pH值和Pb （II）浓度对NOR降解的影响.结果表明,NOR的降解符合伪一级反应动力学,在温度为30℃、NOR初始浓度为5.0mg/L、Pb （II）浓度为1.0mg/L、Fe₃O₄投加量为2.0g/L、PS浓度为1.5mmol/L、初始pH值为7.0的条件下,反应120min后,NOR降解率达90.2%,Pb （II）去除率为99.5%.自由基淬灭实验证实,硫酸根自由基（SO₄^-·）是NOR降解的主要自由基.通过LC-MS分析结果推测了NOR可能的降解路径和中间产物.Fe₃O₄活化PS高级氧化工艺可作为一种同步去除有机污染物和重金属的工艺.     

介质阻挡放电等离子体老化微塑料及对Zn (II)吸附的影响

为了在实验中缩短微塑料的老化时间,更真实地模拟自然老化条件,采用介质阻挡放电（DBD）等离子体老化聚乙烯微塑料（PE-MP）和聚丙烯微塑料（PP-MP）,同时研究了老化前后PE-MP和PP-MP对Zn （II）的吸附过程和机理.随着放电时间延长和输入电压升高,微塑料表面出现微小裂纹或孔洞,形成含氧官能团.老化后PE-MP和PP-MP对Zn （II）的吸附容量分别提高了22.7%和14.8%.老化前后微塑料对Zn （II）的吸附均符合准二级动力学模型.颗粒内扩散模型表明,Zn （II）在微塑料上的吸附过程可分为快速吸附,慢速吸附和吸附平衡3个阶段.同时,老化前后微塑料对Zn （II）的吸附均符合Langmuir吸附等温线模型.热力学结果表明,微塑料对Zn （II）的吸附是自发的吸热过程.Ca²⁺、腐殖酸和低pH值不利于微塑料对Zn （II）的吸附.     

PERCOLATION OF LEAD(II) AND CADMIUM(II) THROUGH TWO BENTONITES USED AS LANDFILL LINER

In order to prevent contamination of subsoil and groundwater by leachates containing heavy metals, montmorillonite linings are used on landfill bottoms. It is therefore important to understand ion uptake by this clay. In this study we have performed percolation of lead(II) and cadmium(II) through columns filled firstly with a technical bentonite and then with a reference bentonite. Elution curves provide an evaluation of metals retention. After the percolation step, columns are cut and metal ions are extracted to evaluate influence of side effects and soil depth on metal uptake. Moreover retentions of lead(II) and cadmium(II) are compared.     

Rapid decolorization of Acid Orange II aqueous solution by amorphous zero-valent iron

Some problems including low treatment capacity, agglomeration and clogging phenomena, and short working life, limit the application of pre-treatment methods involving zero-valent iron (ZVI). In this article, ZVI was frozen in an amorphous state through a melt-spinning technique, and the decolorization effect of amorphous ZVI on Acid Orange II solution was investigated under varied conditions of experimental variables such as reaction temperature, ribbon dosage, and initial pH. Batch experiments suggested that the decolorization rate was enhanced with the increase of reaction temperature and ribbon dosage, but decreased with increasing initial solution pH. Kinetic analyses indicated that the decolorization process followed a first order exponential kinetic model, and the surface-normalized decolorization rate could reach 2.09 L/(m². min) at room temperature, which was about ten times larger than any previously reported under similar conditions. Recycling experiments also proved that the ribbons could be reused at least four times without obvious decay of decolorization rate and efficiency. This study suggests a tremendous application potential for amorphous ZVI in remediation of groundwater or wastewater contaminated with azo dyes.     

邻菲罗啉对蒙脱石吸附镍离子性能影响

利用镍离子能与邻菲罗啉反应生成螯合物的性质,研究了加与未加邻菲罗啉条件下,蒙脱石对金属镍离子的吸附行为,考察了镍离子浓度、吸附时间、温度和溶液pH值等因素对吸附性能的影响.结果表明:加入邻菲罗啉后,蒙脱石对镍的螯合离子的吸附量明显增大;吸附平衡时间约为120min;蒙脱石对[Ni(phen)n]2+的吸附性基本不受pH值的影响.动力学研究表明该吸附过程符合准二级反应动力学模型,吸附量随温度升高而增大.二级动力学参数证明加入邻菲罗啉可显著提高蒙脱石对Ni2+的吸附性.蒙脱石对简单Ni2+的吸附符合Langmuir的单层吸附等温式;而蒙脱石对镍的螯合离子的吸附则符合Freundlich等温式.蒙脱石对Ni2+和[Ni(phen)n]2+的吸附均为自发、吸热和更无序的;XRD及FTIR研究表明,蒙脱石对[Ni(phen)n]2+的吸附以层间的物理吸附为主.     

Safety I–II,resilience and antifragility engineering: a debate explained through an accident occurring on a mobile elevating work platform

Occupational health and safety (OHS) represents an important field of exploration for the research community: in spite of the growth of technological innovations, the increasing complexity of systems involves critical issues in terms of degradation of the safety levels. In such a situation, new safety management approaches are now mandatory in order to face the safety implications of the current technological evolutions. Along these lines, performing risk-based analysis alone seems not to be enough anymore. The evaluation of robustness, antifragility and resilience of a socio-technical system is now indispensable in order to face unforeseen events. This article will briefly introduce the topics of Safety I and Safety II, resilience engineering and antifragility engineering, explaining correlations, overlapping aspects and synergies. Secondly, the article will discuss the applications of those paradigms to a real accident, highlighting how they can challenge, stimulate and inspire research for improving OHS conditions.     

活性炭吸附水中铅离子的动态研究

本文采用两种煤质活性炭，研究了其对不同浓度二价铅离子溶液的吸附，应用固定床吸附动力学模型，Ｍａｒｑａｄｔ方法非线性回归固定床吸附流出曲线，获得了铅离子在活性炭上的扩散传质系数。结果发现，孔扩散系数Ｄｐ强裂地依赖于铅离子入口浓度，随着入口浓度的升高，孔扩散系数变小，随后用上述扩攻系数理论预测了其它操作条件下的流出曲线，结果表明实验曲线与理论预测曲线能很好地相符，动态法能可靠地获取固吸附过程的吸附及扩     

Treatment of azo dye Orange II in a sequential anaerobic and aerobic-sequencing batch ractor system

We studied the biodegradation of Orange II in a sequential anaerobic and aerobic-sequencing batch reactor system. Granular activated carbon was used either packed into a column or added directly into the anaerobic reactor to investigate the treatment performance between the two operation conditions. We found that the circulation of mixed liquor between the anaerobic reactor and the carbon-packed column enhanced the chemical oxygen demand from 28 to 52% and Orange II removal efficiencies from 88 to 96%, under simultaneous adsorption and biodegradation process. The morphology of microbes was observed under an electron-scanning microscope.     

Chlorination of dibenzofuran and dibenzo-p-dioxin vapor by copper (II) chloride

Dibenzofuran (DF) is formed from phenol and benzene in combustion gas exhaust streams prior to particle collection equipment. Subsequent chlorination at lower temperatures on particle surfaces is a potential source of chlorinated dibenzofuran (CDF). Gas streams containing 8% O₂ and approximately 0.1% DF vapor were passed through particle beds containing copper (II) chloride (0.5% Cu, mass) at temperatures ranging from 200 to 400 °C to investigate the potential for CDF formation during particle collection. Experiment duration was sufficient to provide an excess amount of DF (DF/Cu=3). The efficiency of DF chlorination by CuCl₂ and the distribution of CDF products were measured, with effects of temperature, gas velocity, and experiment duration assessed. Results of a more limited investigation of dibenzo-p-dioxin (DD) chlorination by CuCl₂ to form chlorinated DD (CDD) products are also presented.

The efficiency of DF/DD chlorination by CuCl₂ was high, both in terms of CuCl₂ utilization and DF/DD conversion. Total yields of Cl on CDF/CDD products of up to 0.5 mole Cl per mole CuCl₂ were observed between 200 and 300 °C; this suggests that nearly 100% CuCl₂ was utilized, assuming a conversion of two moles of CuCl₂ to CuCl per mole Cl added to DD/DF. In a short duration experiment (DF/Cu=0.3), nearly 100% DF adsorption and conversion to CDF was achieved. The degree of CDF chlorination was strongly dependent on gas velocity. At high gas velocity, corresponding to a gas–particle contact time of 0.3 s, mono-CDF (MCDF) yield was largest, with yields decreasing with increasing CDF chlorination. At low gas velocity, corresponding to a gas–particle contact time of 5 s, octa-CDF yield was largest. DF/DD chlorination was strongly favored at lateral sites, with the predominant CDF/CDD isomers within each homologue group those containing Cl substituents at only the 2,3,7,8 positions. At the higher temperatures and lower gas velocities studied, however, broader isomer distributions, particularly of the less CDD/CDF products, were observed, likely due to preferential destruction of the 2,3,7,8 congeners.