生物柴油吸收VOCs的特性及热力学

采用具有高沸点、低粘度特性的生物柴油作为非极性挥发性有机废气（VOCs）的吸收剂,以甲苯为典型VOCs代表,通过吸收实验考察了生物柴油的甲苯吸收特性.结果发现,在同一浓度下生物柴油吸收甲苯容量优于矿物油,且比水提高1个数量级,并且随着初始浓度升高,吸收容量等比例上升.温度是吸收敏感因素,温度上升会导致吸收容量大幅下降.采用UNIFAC模型计算溶解度数据与实验数据吻合较好,平均相对误差为3.37%,可有效预测生物柴油吸收VOCs特性.在此基础上论文也考察了生物柴油对四氯乙烯、苯乙烯、氯苯的吸收特性,并计算了4种VOCs在生物柴油中的无限稀释活度系数、亨利系数及吸收过程的ΔG、ΔH和ΔS.结果表明生物柴油对这4种VOCs的吸收性能排序为：苯乙烯>氯苯>四氯乙烯>甲苯,饱和吸收容量分别为55.17,27.75,20.46,11.93mg/g.     

中国典型背景站夏季VOCs污染特征及来源解析

选取庞泉沟、神农架、武夷山和长岛4个代表性大气背景站,使用SUMMA罐采样及GC-FID/MS方法分析了4个背景站夏季环境空气中57种挥发性有机污染物浓度水平、物种组成以及日变化特征,并利用PMF模型对背景站VOCs进行来源解析和臭氧生成潜势（OFP）分析.结果表明,采样期间庞泉沟、神农架、武夷山和长岛的VOCs平均浓度分别为（23.06±8.14）×10^-9,（8.25±4.27）×10^-9,（7.95±11.31）×10^-9和（11.98±8.80）×10^-9.除庞泉沟外,背景点烷烃、芳香烃、烯烃和炔烃浓度均明显低于城市地区.背景点烷烃、芳香烃、烯烃占比与城市地区差异不显著,但背景点炔烃占比显著小于城市地区.烷烃和芳香烃的日变化呈现出白天消减,夜间累积的特点,烯烃浓度则在09：00~15：00点出现峰值.PMF源解析及成分分析结果表明,人为排放源对背景站VOCs构成和臭氧生成潜势有重要贡献.汽油挥发、溶剂及涂料使用、机动车尾气等排放源对4个背景站点的VOCs浓度贡献占比在39%~58%之间,对OFP贡献占比在35%~58%之间.燃烧源对4个背景站点的VOCs浓度贡献占比在18%~21%之间,对OFP贡献占比在约为13%..植物源对4个背景站点的VOCs浓度贡献占比在7%~17%之间,对OFP贡献占比在8%~33%之间,植物源贡献占比高于城市地区.     

过硫酸钠缓释胶囊反应带修复苯胺污染地下水

针对有机污染地下水原位化学氧化修复中普遍存在的氧化剂过量使用、污染物反弹和二次污染问题,以苯胺（AN）为特征污染物,以活化过硫酸盐为氧化剂,采用硬脂酸为胶结剂,制备过硫酸钠（PS）和硫酸亚铁（FeSO₄）缓释胶囊,构建基于PS和FeSO₄缓释胶囊的可渗透反应屏障（PS-FeSO₄-PRB）,考查了缓释胶囊组分、地下水流速对PRB中活性物质释放和AN去除的影响.结果表明,当缓释胶囊中活性物质/硬脂酸为1/2,地下水流速为0.1mL/min时,48h后PRB中PS和Fe²⁺累计释放率分别为43.18%和14.98%.当PRB中FeSO₄/PS为1/9时,AN累计去除率达到95.37%,TOC累计去除率为57.07%.采用砂柱模拟AN污染地下水,比较了直接注射PS和FeSO₄与PS-FeSO₄-PRB两种处理方式的修复性能,4d内两者的AN累计去除率分别为35.22%和69.74%,TOC累计去除率分别为15.83%与14.88%.PS-FeSO₄-PRB修复效果明显高于直接注射处理.GC/MS分析表明,处理后产生了对苯醌、偶氮苯以及长链烷烃等产物,导致AN矿化率不高.pH值和Eh连续记录结果表明,PS-FeSO₄-PRB处理能够保持反应体系氧化还原电位和酸碱性的相对稳定.相比直接注射氧化剂,基于PS和FeSO₄-缓释胶囊的PRB处理中地下水的急性毒性更低,二次污染风险更小.     

BPA和EE2在PA微塑料上竞争吸附的位点能量

为研究微塑料上雌激素共存的吸附行为,以17α-乙炔基雌二醇（EE2）和双酚A （BPA）为目标污染物,微塑料聚酰胺（PA）为吸附剂,通过等温吸附实验研究二者在单溶质和双溶质体系下的吸附性能,基于位点能量分布理论进一步剖析二者在PA微塑料上的的吸附特性.同时,采用X射线光谱（XPS）以及傅里叶变换红外光谱（FTIR）对吸附前后的PA微塑料进行表征,探究其可能存在的吸附机理.等温吸附拟合结果及XPS、FTIR的表征结果表明BPA和EE2及二者混合溶液在PA上的吸附属于非均质吸附,疏水分配及氢键作用为主要的吸附机制.位点能量分布分析结果表明,相同浓度（1～4mg/L）条件下,BPA吸附位点主要分布于高能量区;单溶质体系的EE2吸附位点主要集中于低能量区.双溶质体系下,相同浓度的两种物质位点分布函数均随着位点能量的增大而呈指数降低,BPA下降趋势较为平缓,吸附位点分布更集中.两种体系相比较,BPA平均位点能量和位点能量非均质性分别增加了0.749%和2.483%,吸附位点数量减少了10.852%;双溶质体系下EE2平均位点能量降低0.813%,位点能量非均质性增加1.870%,吸附位点数量增加42.429%.双酚A和EE2在PA微塑料上的竞争吸附中,EE2占优势.     

Identification of close relationship between atmospheric oxidation and ozone formation regimes in a photochemically active region

Understanding ozone (O₃) formation regime is a prerequisite in formulating an effective O₃ pollution control strategy. Photochemical indicator is a simple and direct method in identifying O₃ formation regimes. Most used indicators are derived from observations, whereas the role of atmospheric oxidation is not in consideration, which is the core driver of O₃ formation. Thus, it may impact accuracy in signaling O₃ formation regimes. In this study, an advanced three-dimensional numerical modeling system was used to investigate the relationship between atmospheric oxidation and O₃ formation regimes during a long-lasting O₃ exceedance event in September 2017 over the Pearl River Delta (PRD) of China. We discovered a clear relationship between atmospheric oxidative capacity and O₃ formation regime. Over eastern PRD, O₃ formation was mainly in a NO_x-limited regime when HO₂/OH ratio was higher than 11, while in a VOC-limited regime when the ratio was lower than 9.5. Over central and western PRD, an HO₂/OH ratio higher than 5 and lower than 2 was indicative of NO_x-limited and VOC-limited regime, respectively. Physical contribution, including horizontal transport and vertical transport, may pose uncertainties on the indication of O₃ formation regime by HO₂/OH ratio. In comparison with other commonly used photochemical indicators, HO₂/OH ratio had the best performance in differentiating O₃ formation regimes. This study highlighted the necessities in using an atmospheric oxidative capacity-based indicator to infer O₃ formation regime, and underscored the importance of characterizing behaviors of radicals to gain insight in atmospheric processes leading to O₃ pollution over a photochemically active region.     

Preparation and characterization of boron-doped corn straw biochar: Fe (Ⅱ) removal equilibrium and kinetics

Nowadays, iron ions as a ubiquitous heavy metal pollutant are gradually concerned and the convenient and quick removal of excessive iron ions in groundwater has become a major challenge for the safety of drinking water. In this study, boron-doped biochar (B-BC) was successfully prepared at various preparation conditions with the addition of boric acid. The as-prepared material has a more developed pore structure and a larger specific surface area (up to 897.97 m²/g). A series of characterization results shows that boric acid effectively activates biochar, and boron atoms are successfully doped on biochar. Compared with the ratio of raw materials, the pyrolysis temperature has a greater influence on the amount of boron doping. Based on Langmuir model, the maximum adsorption capacity of 800B-BC_1:2 at 25 °C, 40 °C, 55 °C are 50.02 mg/g, 95.09 mg/g, 132.78 mg/g, respectively. Pseudo-second-order kinetic model can better describe the adsorption process, the adsorption process is mainly chemical adsorption. Chemical complexation, ions exchange, and co-precipitation may be the main mechanisms for Fe²⁺ removal.     

Removal of unburned carbon from municipal solid waste fly ash by column flotation

Unburned carbon (UC) is the major source of organic contaminants in municipal solid waste (MSW) fly ash. So most organic contaminants can be removed by the removal of the UC from the MSW fly ash. In this paper, we first used a technique of column flotation to remove UC from MSW fly ash. The influences of column flotation parameters on the recovery efficiency of UC were systematically studied. It was found that the UC recovery efficiency was greatly influenced by the gas flow rate, pH value, collector kerosene's concentration and the types of fly ash. By optimizing the above parameters, we have successfully removed 61.2% of the UC from MSW fly ash having 5.24% UC content. The removal mechanism was well accounted for the kinetic theory of column flotation and surface-chemistry theory. The results indicate that the column flotation technique is effective in removing the UC from MSW fly ash, and show that there is a strong possibility for practical application of this technique in removing the organic contaminants from MSW fly ash.     

可见光助三维电极/电Fenton处理罗丹明B废水的研究

提出了以多孔TiO2薄膜(Porous-TiO2)板为阳极,活性炭负载Fe-Ni共掺P25颗粒(Fe-Ni-P25/AC)为粒子电极的可见光助三维电极/电Fenton(Vis-3D/EF)降解有机废水的新方法.同时,考察了该体系对罗丹明B溶液的去除效果和影响因素,探讨了降解过程的反应动力学,并与常规阳极和粒子电极组成的体系处理能耗进行了对比,探讨了Vis-3D/EF体系各个作用对去除率的贡献及对罗丹明B的降解机理.实验结果表明,在电源电压20 V、溶液pH=3、Fe2+离子投加量0.5 mmol·L-1、曝气量1.5 L·min-1、反应时间60 min时,20 mg·L-1罗丹明B的降解率为96.84%,处理过程更符合二级反应动力学.在此条件下,Porous-TiO2阳极板和Fe-Ni-P25/AC粒子电极组成的体系,降解过程具有明显的协同催化特点,协同因子达1.22,且处理能耗仅为常规石墨(Gr)阳极、活性炭(AC)粒子电极组成体系的1/85.5.Vis-3D/EF降解过程中电催化氧化作用、Fenton氧化作用、可见光催化作用及可见光下的协同作用对去除率的贡献分别为43.88%、20.21%、15.26%和17.49%.同时,通过叔丁醇捕获实验发现,·OH对去除率的贡献为75.58%,表明·OH是该体系中产生的主要活性物质.     

我国硝基苯的海水水质基准及生态风险评估研究

以一种重要的化工原料硝基苯为研究对象,通过收集、筛选我国本土物种的硝基苯海水生物毒性数据,同时针对我国海区生物特点补充8种典型海洋受试生物的毒理学实验,应用物种敏感度分布(SSD)方法推导了用于保护水生生物的我国硝基苯海水水质基准值。在此基础上,尝试应用2种概率生态风险评估方法初步评估了硝基苯在我国东海椒江口水体中的生态风险。研究结果表明,用于保护我国海水生物的硝基苯水质基准高值为1.42 mg·L-1,低值为0.037 mg·L-1,与应用SSD方法推导的硝基苯淡水水质基准差异不大。商值概率分布法和联合概率曲线法的风险表征结果表明,硝基苯对椒江口中的水生生物存在潜在的生态风险,需要管理部门采取一定的风险管控措施。研究结果有望为我国水质基准、生态风险研究及硝基苯的海水水质标准制定提供参考。