淄博市夏季城区与背景点VOCs污染特征比较

为研究城区及背景点夏季挥发性有机物(VOCs)污染特征的差异,于2020年7月在淄博市城区站点和背景站点在线监测环境VOCs,分析其污染特征和化学反应活性,运用正交矩阵因子分析模型(PMF)解析VOCs的来源.结果表明,城区点ρ(TVOC)和ρ(NOx)高于背景点,但ρ(O3)较低;城区点ρ(TVOC)和ρ(NOx)呈...     

紫外活化过硫酸钠灭活水中噬菌体MS2的特性及机制

水环境中的病毒对常见的消毒技术有较强的抵抗力.为了开发水中病毒的高效灭活技术,以噬菌体MS2为对象,研究紫外活化过硫酸钠（UV/PS）体系灭活病毒的特性和机制.采用双层平板法对噬菌体MS2进行定量检测,研究UV/PS对水样中噬菌体MS2的灭活率和动力学特征,并考察PS用量、pH值和噬菌体初始浓度等因素对灭活效果的影响.利用透射扫描电镜观察UV/PS处理前后噬菌体的形貌,利用电子顺磁共振波谱法确认反应体系中存在的自由基种类.在自由基淬灭实验的基础上,分析计算UV/PS体系中各因素对噬菌体灭活的贡献率.结果表明,当紫外辐照强度为160 μW·cm^-2时,UV/PS处理4 min即可去除4.39 lg的噬菌体MS2,较单独使用同样辐照剂量的UV消毒灭活率高1.44 lg.UV/PS体系对噬菌体MS2的灭活动力学过程符合一级反应动力学模型.增加体系中的PS初始浓度能明显提高对噬菌体的灭活率和灭活速率,而pH和噬菌体初始浓度对UV/PS灭活噬菌体的影响较小.UV/PS处理可导致噬菌体的衣壳破损,促进了噬菌体颗粒团聚.UV/PS体系中存在SO₄^-·和·OH,是噬菌体MS2灭活的重要因素.·OH比SO₄^-·对噬菌体MS2灭活的贡献更大.     

Unique products from the reaction of naphthalene with the hydroxyl radical

Many of the products of the reaction of naphthalene (Naph) with the OH radical in a reaction chamber were identified. Previously unidentified products included 1,2-naphthoquinone (NQ), oxygenated indenes and benzopyrones. Possible pathways for the formation of 1,2-NQ and 1,4-NQ are proposed. In the chamber reactions, more 1,2-NQ than 1,4-NQ partitioned to the particle phase. From this result we infer that, in the atmosphere, the percentage of 1,2-NQ in the particle phase should be greater than that for the 1,4-NQ. Because both of these compounds are considered to be toxic, and since they appear in both the gas and particle phases in the reaction chamber, and by implication in the atmosphere, it is considered important that both the gas and particle phases of these two compounds should be measured to assess their impact on human health.     

蒽醌-2-磺酸钠有机体系光引发自由基降解染料

采用蒽醌-2-磺酸钠有机体系光引发自由基降解废水中的染料。分析了蒽醌-2-磺酸钠有机体系光引发自由基降解的机理,考察了曝气、光照强度和初始染料质量浓度等因素对降解效果的影响。实验结果表明：曝气有利于蒽醌-2-磺酸钠有机体系光引发自由基降解染料;在光照强度1 000 W、初始染料质量浓度50 mg/L的条件下,反应60 min后酸性蓝80溶液的脱色率可达100%;在酸性红249、酸性黄42、酸性蓝80、活性艳红KD-8B、活性黄K-6G和活性翠蓝K-NG 6种商用酸性和活性染料中,蒽醌-2-磺酸钠有机体系对活性黄K-6G和活性艳红KD-8B的脱色率最高,对酸性蓝80和活性翠蓝K-NG的脱色率最低。     

盐酸羟胺和酒石酸强化Fe2+/Na2S2O8体系降解双酚A

Fe2+/Na2S2O8（persulfate,PS）体系中存在Fe2+易发生沉淀且Fe3+无法还原的问题,以典型的持久性有机污染物双酚A（bisphenol A,BPA）为研究对象,分别考察络合剂酒石酸（tartaric acid,TA）和还原剂盐酸羟胺（hydroxylamine,HA）强化Fe2+/PS体系对双酚A降解过程的影响。在Fe2+/TA/PS体系、Fe2+/HA /PS体系及Fe2+/TA/HA/PS体系中分别考察了盐酸羟胺投加量、酒石酸投加量、体系pH作用范围等因素的影响,同时对氧化作用机理加以分析。研究表明：酒石酸和盐酸羟胺均能提高双酚A在Fe2+/PS体系中的去除率,且均具有最优值;络合剂酒石酸起到长期促进作用,而还原剂盐酸羟胺起到短期促进作用。探针实验表明络合剂和还原剂共同强化的体系中·OH和SO4·-仍然是主要的氧化物种。当PS投加量均为2.64 mmol·L-1时,30 min内Fe2+/TA/HA/PS体系中SO4·-的生成量为11.3 μmol·L-1,而Fe2+/PS体系中SO4·-的生成量为1.4 μmol·L-1,表明体系通过加速了自由基生成速率从而加快了双酚A的降解。研究结果表明Fe2+/TA/HA/PS体系在中性条件下实现了对双酚A的强化降解,显著优于Fe2+/PS体系。     

Determination of photochemically-generated reactive oxygen species (ROS) in natural water

Reactive oxygen species (ROS) can be produced by interactions between sunlight and light-absorbing substances in natural water environment. ROS may participate in the indirect photolysis of trace organic pollutants, therefore resulting in the changing of their environmental fates and ecological risks in natural water system. Bisphenol A (BPA), an endocrine-disrupting chemical, exits widely in natural water. The photodegradation of BPA promoted by ROS (·OH, 1O2, HO2·/O2·-) which were produced on the excitation of ubiquitous constituents (such as nitrate ion, humic substances and Fe(III)-oxalate complexes) in natural water under simulated solar radiation was investigated. Both molecular probe method and electron spin resonance (ESR) test were used for the determine the characterization of generated ROS. It was found that ·OH was photochemically produced with the presence of nitrate ion, humic substances and Fe(III)-oxalate complexes and 1O2 was produced with the presence of humic substances. The steady-state concentrations of ·OH was 1.27×10-14 mol/L in nitrate ion, and the second-order rate constant of BPA with ·OH was 1.01×1010L/( mol·s).     

Mechanism for the destruction of carbon tetrachloride and chloroform DNAPLs by modified Fenton's reagent

The destruction of a carbon tetrachloride DNAPL and a chloroform DNAPL was investigated in reactions containing 0.5 mL of DNAPL and a solution of modified Fenton's reagent (2M H2O2 and 5mM iron(III)-chelate). Carbon tetrachloride and chloroform masses were followed in the DNAPLs, the aqueous phases, and the off gasses. In addition, the rate of DNAPL destruction was compared to the rate of gas-purge dissolution. Carbon tetrachloride DNAPLs were rapidly destroyed by modified Fenton's reagent at 6.5 times the rate of gas purge dissolution, with 74% of the DNAPL destroyed within 24h. Use of reactions in which a single reactive oxygen species (hydroxyl radical, hydroperoxide anion, or superoxide radical anion) was generated showed that superoxide is the reactive species in modified Fenton's reagent responsible for carbon tetrachloride DNAPL destruction. Chloroform DNAPLs were also destroyed by modified Fenton's reagent, but at a rate slower than the rate of gas purge dissolution. Reactions generating a single reactive oxygen species demonstrated that chloroform destruction was the result of both superoxide and hydroxyl radical activity. Such a mechanism of chloroform DNAPL destruction is in agreement with the slow but relatively equal reactivity of chloroform with both superoxide and hydroxyl radical. The results of this research demonstrate that modified Fenton's reagent can rapidly and effectively destroy DNAPLs of contaminants characterized by minimal reactivity with hydroxyl radical, and should receive more consideration as a DNAPL cleanup technology.     

PVDF ultrafiltration membranes of controlled performance via blending PVDF-g-PEGMA copolymer synthesized under different reaction times

PVDF blended different graft ratio of PVDF-g-PEGMA were systematically studied. Tuning the amphiphilic copolymer synthesis time to control membrane performance. The PVDF membrane with PVDF-g-PEGMA at 19 h possesses most surface oxygen content. The synthesis time of PVDF-g-PEGMA at 9 h is good for high flux UF membrane. Polyvinylidene fluoride grafted with poly(ethylene glycol) methyl ether methacrylate (PVDF-g-PEGMA) was synthesized using atomic transfer radical polymerization (ATRP) at different reaction times (9 h, 19 h, and 29 h). The corresponding conversion rates were 10%, 20% and 30%, respectively. PVDF was blended with the copolymer mixture containing PVDF-g-PEGMA, solvent and residual PEGMA under different reaction times. In this study, we explored the effect of the copolymer mixture additives with different synthesis times on cast membrane performance. Increasing the reaction time of PVDF-g-PEGMA causes more PVDF-g-PEGMA and less residual PEGMA to be found in the casting solution. Incremental PVDF-g-PEGMA can dramatically increase the viscosity of the casting solution. An overly high viscosity led to a delayed phase inversion, thus hindering PEGMA segments in PVDF-g-PEGMA from migrating to the membrane surface. However, more residual PEGMA contributed to helping more PEGMA segments migrate to the membrane surface. The pure water fluxes of the blended membrane with reaction times of 9 h, 19 h, and 29 h are 5445 L·m⁻²·h⁻¹, 1068 L·m⁻²·h⁻¹and 1179 L·m⁻²·h⁻¹, respectively, at 0.07 MPa. Delayed phase inversion can form smaller surface pore size distributions, thus decreasing the water flux for the membranes with PVDF-g-PEGMA at 19 h and 29 h. Therefore, we can control the membrane pore size distribution by decreasing the reaction time of PVDF-g-PEGMA to obtain a better flux performance. The membrane with PVDF-g-PEGMA at 19 h exhibits the best foulant rejection and cleaning recovery due to its narrow pore size distribution and high surface oxygen content.     

A pulsed switching peroxi-coagulation process to control hydroxyl radical production and to enhance 2,4-Dichlorophenoxyacetic acid degradation

• A new pulsed switching peroxi-coagulation (PSPC) system was developed. • The EC_T for 2,4-D removal in the PSPC was lower than that in the EF. • The iron consumption for 2,4-D removal in the PSPC was lower than that in the PC. The aim of this study was to develop a new pulsed switching peroxi-coagulation system to control hydroxyl radical (?OH) production and to enhance 2,4-Dichlorophenoxyacetic acid (2,4-D) degradation. The system was constructed with a sacrifice iron anode, a Pt anode, and a gas diffusion cathode. Production of H₂O₂ and Fe²⁺ was controlled separately by time delayers with different pulsed switching frequencies. Under current densities of 5.0 mA/cm² (H₂O₂) and 0.5 mA/cm² (Fe²⁺), the ?OH production was optimized with the pulsed switching frequency of 1.0 s (H₂O₂):0.3 s (Fe²⁺) and the ratio of H₂O₂ to Fe²⁺ molar concentrations of 6.6. Under the optimal condition, 2,4-D with an initial concentration of 500 mg/L was completely removed in the system within 240 min. The energy consumption for the 2,4-D removal in the system was much lower than that in the electro-Fenton process (68±6 vs. 136±10 kWh/kg TOC). The iron consumption in the system was ~20 times as low as that in the peroxi-coagulation process (196±20 vs. 3940±400 mg/L) within 240 min. The system should be a promising peroxi-coagulation method for organic pollutants removal in wastewater.