Ozonation of azo dye Acid Red 14 in a microporous tube-in-tube microchannel reactor: decolorization and mechanism

Despite the great success of time-weighted average passive sampling of hydrophobic contaminants, such as PCBs and PAHs, the sampling of polar organic compounds still presents a challenge because the equilibrium between water and most sampling phases is attained in a relatively short time. In this study, we proposed a new time-integrative sampler using in situ solvent extraction (TISIS) for polar organic chemicals. The sampler was composed of a 15 cm poly(dimethylsiloxane) (PDMS) tubing, with an internal diameter of 0.5 mm and wall thickness of 0.5 mm, through which an extraction solvent (acetonitrile) was passed. Four polar organic contaminants, caffeine, atrazine, diuron and 17α-ethynylestradiol, were chosen for the evaluation of the performance of the sampler. Without the use of in situ solvent extraction, the PDMS tubing when exposed to a constant aqueous concentration of the four model compounds was able to linearly accumulate those compounds for less than 12 h and equilibrium between the PDMS tubing and water was attained in 2 d under our laboratory conditions. However, TISIS when exposed to a constant aqueous concentration was able to linearly accumulate all the model compounds without any exposure time limitation. The measured sampling rates at three different extraction flow rates (0.2, 0.5, 1.5 mL min⁻¹) were similar, regardless of the chemicals, indicating that the overall mass transfer from aqueous solution to the extraction solvent was most likely dominated by partitioning to the PDMS tubing and the internal diffusion within PDMS. In addition, a pulsed exposure experiment confirmed that TISIS operated in a time-integrative mode when the environmental concentration was highly fluctuated.     

旋转填充床中Fenton＋O3氧化降解模拟阿莫西林废水

以旋转填充床（RPB）作为反应装置,研究了Fenton工艺与Fenton＋O3工艺处理模拟阿莫西林废水的效果,考察了FeSO4·7H2O的投加量、温度、旋转床转速、液体流量及pH对C0D去除率的影响。实验表明,Fenton＋O3工艺的COD脱除率及BOD5／COD相对于Fenton工艺分别提升26．7％和140％。该工艺在pH为3、温度为25℃、液体流量30L／h、气体流量2．5L／h、转速800r／min、H2O2的投加量为1mmol／L及Fe2＋投加量为0．4mm01／L的条件下,100mg／L的模拟阿莫西林废水中COD的去除率达到57．9％,BOD5/COD从0增加到0．36,满足后续生化处理要求。     

A method for removing persulfate interference in the analysis of the chemical oxygen demand in wastewater

Environmental Chemistry Letters - In recent years, sulfate radical-based advanced oxidation has received increasing attention for the treatment of water and wastewater....     

TY型燃油添加剂在降低隧道空气污染中的应用

应用TY型燃油添加剂促进柴油燃烧更充分,降低采用无轨运输方式进行施工的隧道中空气污染.结果表明洞内 CO、Nox浓度及尾气烟度均值降低46%、55%、42%.测定值经统计学方差柱验,有极显著差异(P＜0.001).     

某地戈壁与普通环境辐射剂量率对比及差异分析研究

利用NaI(Tl)便携式x-γ剂量率仪对西北某地戈壁砾石地带及普通环境地表的辐射剂量率进行对比测量,对可能的影响因素进行分析,并使用统计检验的方法分析测量结果,发现戈壁砾石地带结果高于普通环境,均值高约14.5%.基于实验室HPGeγ谱测量土壤样品及理论分析,得到导致此结果的原因主要是土壤中天然放射性核素含量及地表氡析出率的差异.结论提示需重视人员稀少地带的辐射环境水平,为中国在某些戈壁地区从事核技术利用开发项目的环境影响评价提供经验.     

HpGe γ谱仪本底变化对环境样品放射性测量结果的影响

在环境样品测量过程中,本底涨落对天然核素测量结果的影响应根据其在谱仪中计数率的高低具体分析.用γ谱仪测量介质中天然放射性核素的活度浓度时,必然要进行本底谱的扣除,由此会带来一定的误差.对一台N型HpGe γ谱仪在8年间的23个本底谱进行了研究,并分析了本底涨落对测量结果的影响.研究发现,被测介质中天然放射性核素的活度浓度越低,本底涨落越大,由扣除本底引入的误差就越大.     

旋转填充床中Fenton+O_3氧化降解模拟阿莫西林废水

以旋转填充床(RPB)作为反应装置,研究了Fenton工艺与Fenton+O3工艺处理模拟阿莫西林废水的效果,考察了FeSO4·7H2O的投加量、温度、旋转床转速、液体流量及pH对COD去除率的影响。实验表明,Fenton+O3工艺的COD脱除率及BOD5/COD相对于Fenton工艺分别提升26.7%和140%。该工艺在pH为3、温度为25℃、液体流量30 L/h、气体流量2.5 L/h、转速800 r/min、H2O2的投加量为1 mmol/L及Fe2+投加量为0.4 mmol/L的条件下,100 mg/L的模拟阿莫西林废水中COD的去除率达到57.9%,BOD5/COD从0增加到0.36,满足后续生化处理要求。