利用轨迹模式模拟近地层臭氧日变化

提出在多条轨迹上应用轨迹模式，以实现对固 区臭氧浓度日变化的模拟，应用该方法对北京燕山石化炼油厂地区的Ｏ３浓度日变化进行了模拟，结果表明模拟值和实测值十分吻和。进一步模拟了当地的臭氧生物特征，并讨论了当地的气象条件和源排放对Ｏ３生成浓度的影响。结果说明削减ＮＯｘ的排放量是控制该地区光化学烟雾形成的关键，而降低燃烃和芳香烃在排放物中所占的比例也是控制该地区光学烟雾的重要手段。     

高浓度甲基橙溶液的低压湿式催化氧化处理

以高浓度甲基橙溶液模拟偶氮染料废水,采用低压湿式催化氧化法(LPWCO)进行处理,考察了H2O2投量、温度、FeSO4投量、硫酸浓度、甲基橙浓度等因素对甲基橙脱色率的影响。结果表明,LPWCO法能有效地使高浓度(大于400mg/L)甲基橙溶液脱色,脱色率大于95%,而H2O2投量不到Fenton法的5%。     

水解酸化＋两级生物接触氧化处理高盐度水产品加工废水

介绍了“水解酸化＋两级生物接触氧化”处理水产品加工废水的运行效果和工程实例，结果表明：对C1^-浓度平均6000mg／L的高盐度水产品加工废水，系统对COD、SS、氨氮的去除率分别超过了88％、90％、85％，出水COD、SS、氨氮分别低于100mg／L、70mg／L、15mg／L，出水完全可以达到《污水综合排放标准》（GB8978—1996）一级排放标准。     

The spatial and temporal distribution of total ozone over China

In this paper the grid data of total ozone mapping spectrograph (TOMS) installed on Nimbus-7 satellite (1978 to 1994) was used and the spatial and temporal distribution of total ozone over China was analyzed. The research indicates that the Qinghai-Tibet Plateau destroyed the latitudinal distribution of total ozone of China and the low value closed center emerged over Qinghai-Tibet Plateau. Long time change trends of seasonal total ozone of Qinghai-Tibet plateau are provided. It shows that the most obvious decrease of total ozone occurs in winter (Jan.), then in summer (Jul.), the relevant slow change occurs in autumn (Oct.) and spring (Apr.).     

Efficient degradation of organic pollutants by S-NaTaO3/biochar under visible light and the photocatalytic performance of a permonosulfate-based dual-effect catalytic system

Removing large concentrations of organic pollutants from water efficiently and quickly under visible light is essential to developing photocatalytic technology and improving solar energy efficiency. This study used a simple hydrothermal method to prepare a non-metallic, S-doped NaTaO₃ (S-NTO) photocatalyst, which was then loaded onto biochar (BC) to form a S-NTO/BC composite photocatalyst. After uniform loading onto BC, the S-NTO particles transformed from cubic to spherical. The photogenerated electron-hole pair recombination probability of the composite photocatalyst was significantly lower than those of the NTO particles. The light absorption range of the catalyst was effectively widened from 310 nm UV region to visible region. In addition, a dual-effect catalytic system was constructed by introducing peroxymonosulfate (PMS) into the environment of the pollution to be degraded. The Rhodamine B, Methyl Orange, Acid Orange 7, tetracycline, and ciprofloxacin degradation efficiency at 40 mg/L reached 99.6%, 99.2%, 84.5%, 67.1%, and 70.7%, respectively, after irradiation by a 40 W lamps for 90 min. The high-efficiency visible-light catalytic activity of the dual-effect catalytic system was attributed to doping with non-metallic sulfur and loading of catalysts onto BC. The development of this dual-effect catalytic system provides new ideas for quickly and efficiently solving the problem of high-concentration organic pollution in aqueous environments, rationally and fully utilizing solar energy, and expanding the application of photocatalytic technology to practice.     

Decomplexation of Cu-1-hydroxyethylidene-1,1-diphosphonic acid by a three-dimensional electrolysis system with activated biochar as particle electrodes

The feasibility of decomplexation removal of typical contaminants in electroplating wastewater, complexed Cu(II) with 1-hydroxyethylidene-1,1-diphosphonic acid (Cu-HEDP), was first performed by a three-dimensional electric reactor with activated biochar as particle electrodes. For the case of 50 mg/L Cu-HEDP, Cu(II) removal (90.7%) and PO initial pH 7, acid-treated almond shell biochar (AASB) addition 20 g/L, and reaction time 180 min, with second-order rate constants of 1.10 × 10⁻³ and 1.94 × 10⁻⁵ min⁻¹respectively. The growing chelating effect between Cu(II) and HEDP and the comprehensive actions of adsorptive accumulation, direct and indirect oxidation given by particle electrodes accounted for the enhanced removal of Cu-HEDP, even though the mineralization of HEDP was mainly dependent on anode oxidation. The performance attenuation of AASB particle electrodes was ascribed to the excessive consumption of oxygen-containing functionalities during the reaction, especially acidic carboxylic groups and quinones on particle electrodes, which decreased from 446.74 to 291.48 µmol/g, and 377.55 to 247.71 µmol/g, respectively. Based on the determination of adsorption behavior and indirect electrochemical oxidation mediated by in situ electrogenerated H₂O₂ and reactive oxygen species (e.g., •OH), a possible removal mechanism of Cu-HEDP by three-dimensional electrolysis was further proposed.     

生物氧化塔的应用

介绍了生物氧化培处理含油污水的装置运行情况．大量数据说明该塔具有操作弹性大，适用范围广，能耗低，脱除率高，不外排过剩的活性污泥等特点，具有广阔的推广应用前景。     

Mn-Cu-O负载型催化剂上CO氧化性能的研究

研究了ＺｒＯ２或Ａｌ２Ｏ３负载Ｍｎ－Ｃｕ－Ｏ体系催化剂ＣＯ催化氧化活性，以及物相结构，表面氧性能与活性的关系。结果表明，锆基催化剂的氧化活性明显优于铝基催化剂，起燃温度Ｔ５０低达５０℃，ＺｒＯ２载 利于活性组份形成高活性物相，并促进表面吸附氧的脱附，表现出催化剂表面吸附氧的脱附温度高低次序与其氧化活性有一致的对应关系。     

混凝沉淀-水解酸化-生物吸附-UBF-接触氧化一氧化沟-吸附工艺处理聚醚多元醇废水

对聚醚多元醇废水采用混凝沉淀-水解酸化-生物吸附-UBF-接触氧化一氧化沟-吸附等进行连续处理。结果表明，该处理工艺具有废水处理效果好、出水水质稳定（出水水质达GB8978—1996中的一级标准）、操作管理方便等优点，是处理该类化工废水的有效方法之一。     

Fe3+催化氧化S(Ⅳ)反应机理初探

通过分析酸性条件下(pH为1～3),Fe3 催化氧化S(Ⅳ)过程中溶液吸光度变化的趋势,对Fe3 催化氧化S(Ⅳ)的反应机理进行了初步推导.实验证明,液相中该反应机理主要是催化氧化与自由基反应相结合,O2的存在对于反应有重要作用,O-2的生成是S(Ⅳ)被氧化的关键;当水中溶解氧接近耗尽时,反应进程发生改变.当Fe3 、S(Ⅳ)浓度增加,自由基生成量增加时,有利于反应进行;作为反应产物,Fe2 、S(Ⅵ)浓度增加,反应推动力减小,反应速率降低;同时Fe2 、SO24-可以与溶液中的其它物质形成配合物,影响了Fe3 -S(Ⅳ)配合物的生成与分解,不利于S(Ⅵ)的氧化.