复合氧化物汽车尾气净化催化剂抗SO2中毒机理研究

复合氧化物催化剂(ASC)具有较高的活性和良好的抗SO_2中毒性能.用IR、XPS、TPD等技术研究了该催化剂抗SO_2中毒机理,结果表明,与易失活催化剂相比,ASC经500h反应(反应气含SO_2约20ppm),其活性组分价态无显著变化,仅表面发生SO_2的化学吸附,经与约500ppm的SO_2作用20h后,发现仅有少量SO_4~(2-)形成.这是由于在ASC催化剂中添加了特殊助剂,而使催化剂活性组分得到保护的缘故.     

深井曝气法处理环氧丙烷皂化废水

对深井曝气工艺处理高盐，高ｐＨ、高温的环氧丙烷皂化废水进行了主研究，结果表明，ＣＯＤｃｒ的去除率可达８０％，ＢＯＤ５的去除率可达９５％以上。     

以工业废物制备高效氧化铁系脱硫剂的研究

研究了以硫酸烧渣、转炉赤泥、平炉尘为主要原料制备氧化铁系 (SW型 )脱硫剂的方法及制备工艺。结果表明 :脱硫剂最佳配方为粘结剂 5 %～ 8% ,制孔剂 0 0 8%～ 0 1% ,木屑 8%～ 12 % ,工业废渣 (硫酸烧渣、转炉赤泥、平炉尘等 ) 78%～ 88% ;成型的最佳温度为 15 0℃ ,活化方法应根据主要原料的不同有所差异 ,活化条件以成型活化优于成型前活化     

废水中有机物对铁盐除磷的影响

通过批次实验探究了不同有机物对铁盐化学除磷的影响.结果显示，有机物对铁盐化学除磷的不利影响由强到弱依次为柠檬酸、黄腐酸、聚山梨酯-80、牛血清蛋白、葡萄糖、淀粉，柠檬酸的影响程度为其他五种有机物的5~20倍.较之含羟基有机物，含羧基有机物对铁盐除磷的不利影响更大.研究表明：铁盐化学除磷的实质是通过形成铁羟基氧化物（HFO）来除磷.含羧基有机物，如柠檬酸，可与磷酸根竞争HFO，有机物"抢占"HFO表面结合位点导致磷酸盐与HFO结合减少，从而使铁盐除磷效果下降.在所试柠檬酸浓度范围内，铁盐除磷率最高下降了90.70%.     

次级燃料还原燃烧产物内NOx的动力学特性研究

提出了在燃煤电站锅炉炉膛内添加次级燃料建立ＮＯｘ的还原区，以控制ＮＯｘ的排放，建立了描述ＮＯｘ还原动态过程的数学模型和化学动力学模型，对计算值和实测值作了比较分析。     

Experimental and theoretical studies on NO selective catalytic oxidation over α-MnO2

Based on the experimental and theoretical methods, the NO selective catalytic oxidation process was proposed. The experimental results indicated that lattice oxygen was the active site for NO oxide over the $\mathrm{\alpha }$-MnO₂(110) surface. In the theoretical study, DFT (density functional theory) and periodic slab modeling were performed on an $\mathrm{\alpha }$-MnO₂(110) surface, and two possible NO oxidation mechanisms over the surface were proposed. The non-defect $\mathrm{\alpha }$-MnO₂(110) surface showed the highest stability, and the surface O_s (the second layer oxygen atoms) position was the most active and stable site. O₂ molecule enhanced the joint adsorption process of two NO molecules. The reaction process, including O₂ dissociation and O=N-O-O-N=O formation, was calculated to carry out the NO catalytic oxidation mechanism over $\mathrm{\alpha }$-MnO₂(110). The results showed that NO oxidation over the $\mathrm{\alpha }$-MnO₂(110) surface exhibited the greatest possibility following the route of O=N-O-O-N=O formation. Meanwhile, the formation of O=N-O-O-N=O was the rate-determining step.     

利用粉煤灰制备高纯超细氧化铝粉体的研究

利用粉煤灰为原料制备高纯超细氧化铝粉体。给出了采用硅酸二钙晶相转变自粉化、高效分散剂———碳化法从粉煤灰中制备氧化铝方法的工艺路线 ,确定了从粉煤灰制备高纯超细氧化铝粉体的最佳工艺条件 ,为粉煤灰的高价值利用开辟了一条新途径     

利用XPS研究复合氧化物催化剂在汽车尾气净化中硫中毒及抗硫中毒机理

运用ＸＰＳ分析方法研究一系列复合氧化物催化剂中毒前后硫在其表面的各种形态及催化剂活性组分中毒前后的组成，价态，化学机理及其变化。结果表明，ＳＯ２在催化剂活性中心进行化学吸附，然后一部分ＳＯ２与活性组分生成相应的亚硫酸盐和硫酸盐，从而使催化剂失活。     

Promotional effect of cobalt doping on catalytic performance of cryptomelane-type manganese oxide in toluene oxidation

The cryptomelane-type manganese oxide (OMS-2)-supported Co (xCo/OMS-2; x = 5, 10, and 15 wt.%) catalysts were prepared via a pre-incorporation route. The as-prepared materials were used as catalysts for catalytic oxidation of toluene (2000 ppmV). Physical and chemical properties of the catalysts were measured using the X-ray diffraction (XRD), Fourier transform infrared spectroscopic (FT-IR), scanning electron microscopic (SEM), X-ray photoelectron spectroscopy (XPS), and hydrogen temperature-programmed reduction (H₂-TPR) techniques. Among all of the catalysts, 10Co/OMS-2 performed the best, with the T_90%, specific reaction rate at 245°C, and turnover frequency at 245°C (TOF_Co) being 245°C, 1.23 × 10⁻³ mol_toluene/(g_cat·sec), and 11.58 × 10⁻³ sec⁻¹ for toluene oxidation at a space velocity of 60,000 mL/(g·hr), respectively. The excellent catalytic performance of 10Co/OMS-2 were due to more oxygen vacancies, enhanced redox ability and oxygen mobility, and strong synergistic effect between Co species and OMS-2 support. Moreover, in the presence of poisoning gases CO₂, SO₂ or NH₃, the activity of 10Co/OMS-2 decreased for the carbonate, sulfate and ammonia species covered the active sites and oxygen vacancies, respectively. After the activation treatment, the catalytic activity was partly recovered. The good low-temperature reducibility of 10Co/OMS-2 could also facilitate the redox process accompanied by the consecutive electron transfer between the adsorbed O₂ and the cobalt or manganese ions. In the oxidation process of toluene, the benzoic and aldehydic intermediates were first generated, which were further oxidized to the benzoate intermediate that were eventually converted into H₂O and CO₂.     

Greenhouse impacts of anthropogenic CH4 and N2O emissions in Finland

The Finnish anthropogenic CH₄ emissions in 1990 are estimated to be about 250 Gg, with an uncertainty range extending from 160 to 440 Gg. The most important sources are landfills and animal husbandry. The N₂O emissions, which come mainly from agriculture and the nitric acid industry are about 20 Gg in 1990 (uncertainty range 10–30 Gg). The development of the emissions to the year 2010 is reviewed in two scenarios: the base and the reduction scenarios.According to the base scenario, the Finnish CH₄ emissions will decrease in the near future. Emissions from landfills, energy production, and transportation will decrease because of already decided and partly realized volume and technical changes in these sectors. The average reduction potential of 50%, as assumed in the reduction scenario, is considered achievable.N₂O emissions, on the other hand, are expected to increase as emissions from energy production and transportation will grow due to an increasing use of fluidized bed boilers and catalytic converters in cars. The average reduction potential of 50%, as assumed in the reduction scenario, is optimistic.Anthropogenic CH₄ and N₂O emissions presently cause about 30% of the direct radiative forcing due to Finnish anthropogenic greenhouse gas emissions. This share would be even larger if the indirect impacts of CH₄ were included. The contribution of CH₄ can be controlled due to its relatively short atmospheric lifetime and due to the existing emission reduction potential. Nitrous oxide has a long atmospheric lifetime and its emission control possiblities are limited consequently, the greenhouse impact of N₂O seems to be increasing even if the emissions were limited somehow.