β修正罗丹明B光度法测定工业废水中银

对β修正光度法测定废水中痕量银进行了研究，该方法能消除反应液中过量显色剂干扰，提高分析灵敏度和准确度。测定结果表明，银加标回收率９３．０－１０６．０％，精密度ＲＳＤ２．３％，银量低测定浓度０．０２ｍｇ／Ｌ。该方法适合于印相，电镀等行业废水银分析。     

铁铜双金属有机骨架MIL-101(Fe,Cu)活化双氧水降解染料性能

针对非均相芬顿传质效率低和Fe（Ⅲ）Fe（Ⅱ）转化慢导致活性低等问题,采用溶剂热法制备铁铜双金属有机骨架材料[MIL-101（Fe,Cu）],并研究了材料界面性质、催化降解染料（亚甲基蓝）性能以及活化催化机制.结果表明,MIL-101（Fe,Cu）晶体结构完整且呈三维八面体形状;比表面积和平均孔径分别为667.2 m² ·g^-1和1.9 nm,可充分暴露反应活性位点.MIL-101（Fe,Cu）在广谱pH范围可活化H₂ O₂高效降解亚甲基蓝.当pH=5、反应20 min,MIL-101（Fe,Cu）/H₂ O₂对20 mg ·L^-1亚甲基蓝的去除率为100%,较MIL-101（Fe）/H₂O₂和单独H₂ O₂分别提高43.1%和88.9%.自由基猝灭实验与反应前后铁和铜价态变化结果表明,羟基自由基（·OH）是MIL-101（Fe,Cu）/H₂ O₂催化降解亚甲基蓝的主要活性物种;Cu（Ⅱ）掺杂引入新的活性位点,且Cu（Ⅱ）/Cu（Ⅰ）循环和Fe（Ⅲ）/Fe（Ⅱ）循环可协同产生·OH,进而提高催化效率.MIL-101（Fe,Cu）作为新型非均相类芬顿催化剂,无需复杂pH调节即可获得良好催化效果,在工业废水处理上具有较好地应用前景.     

机动车轮胎磨损颗粒物化学组分特征研究

为研究机动车道路行驶过程中轮胎磨损排放的颗粒物理化特性,利用轮胎轮廓仿真磨耗仪,对国内主流17种轮胎胎面进行仿真磨耗实验,获得颗粒物样品,提取并检测其中18种元素和20种多环芳烃（PAHs）的含量.结果显示,元素和PAHs含量因轮胎品牌和速度等级的不同而差异显著.18种元素平均含量为（99.04±68.43）mg/g,占样品总重的9.90%,其中Si（88.97±67.85）mg/g、Zn（6.77±1.64）mg/g和Na（1.05±0.75）mg/g的平均含量均超过1mg/g,Cd的含量最低,为（0.43±0.31）μg/g.20种PAHs含量之和（∑20PAHs）在12.13~433.64 μg/g,平均为（94.13±110.18）μg/g,PY的平均含量最高（30.98±31.27）μg/g,其次是CHR、BaP、FA、PHE和BghiP,平均含量最低的是AC（0.58±0.2）μg/g;从环数看,以4环PAHs为主（占∑20PAHs的45.03%~67.93%）,其次为3环（平均含量为15.45%）和5环（平均含量为12.62%）.总体来说,国外品牌轮胎样品中元素和PAHs含量略高于国内品牌,而主要PAHs环数略低于国内品牌.     

苯醌对聚合硅酸铁多相UV-Fenton体系的增效机制

通过构建苯醌增效聚合硅酸铁多相UV-Fenton体系,讨论了体系中橙Ⅱ的脱色和降解途径.在研究苯醌浓度对聚合硅酸铁铁离子的释放、Fe²⁺与Fe³⁺之间的转化、H₂O₂分解和·OH生成影响的基础上,提出了苯醌对聚合硅酸铁多相UV-Fenton体系的增效机制.结果表明,随苯醌浓度的增加,其紫外光下光解还原聚合硅酸铁并释放Fe²⁺的程度增大、H₂O₂分解速度加快、产生·OH浓度峰值增高且出现的时间提前;苯醌增效体系释放于溶液中的Fe²⁺可以通过Fenton反应转化成Fe³⁺,反应结束后聚合硅酸铁能重新吸附Fe³⁺并使其浓度降低,避免了增效体系铁离子的二次污染.本研究将为多相催化剂催化过程的调控提供新的视角,为多相光助-芬顿反应在有机废水资源化中的应用提供理论依据和技术支持.     

Adsorption of 17β-estradiol from aqueous solution by raw and direct/pre/post-KOH treated lotus seedpod biochar

Five biochars derived from lotus seedpod(LSP) were applied to examine and compare the adsorption capacity of 17β-estradiol(E2) from aqueous solution.The effect of KOH activation and the order of activation steps on material properties were discussed.The effect of contact time,initial concentration,p H,ionic strength and humic acid on E2 adsorption were investigated in a batch adsorption process.Experimental results demonstrated that the pseudo second-order model fitted the experimental data best and that adsorption equilibrium was reached within 20 hr.The efficiency of E2 removal increased with increasing E2 concentration and decreased with the increase of ionic strength.E2 adsorption on LSP-derived biochar(BCs) was influenced little by humic acid,and slightly affected by the solution p H when its value ranged from 4.0 to 9.0,but considerably affected at p H 10.0.Low environmental temperature is favorable for E2 adsorption.Chemisorption,π–π interactions,monolayer adsorption and electrostatic interaction are the possible adsorption mechanisms.Comparative studies indicated that KOH activation and the order of activation steps had significant impacts on the material.Post-treated biochar exhibited better adsorption capacity for E2 than direct treated,pretreated,and raw LSP biochar.Pyrolyzed biochar at higher temperature improved E2 removal.The excellent performance of BCs in removing E2 suggested that BCs have potential in E2 treatment and that the biochar directly treated by KOH would be a good choice for the treatment of E2 in aqueous solution,with its advantages of good efficiency and simple technology.