Cu-Ag/海泡石催化还原NO的研究

以天然海泡石为原料,对其进行酸改性并与活性氧化铝混合后作为催化剂载体,采用浸渍法制备了用于CO还原NO的Cu-Ag复合金属催化剂.对不同Ag负载量催化剂催化还原NO的活性进行了评价,考察了载体对催化剂催化活性的影响,用BET、XRD、SEM等对催化剂进行了表征.结果表明,当Ag负载量不超过5%时,复合金属催化剂性能好于单一金属催化剂;Ag负载量为2%时催化剂性能最好;采用海泡石-氧化铝混合物为载体的催化剂的孔径分布得到改善,对NO催化还原反应有更高的活性.     

不同波段下黄海中二甲基硫光氧化动力学研究

采集黄海表层海水样品,在模拟太阳光照射条件下研究二甲基硫(DMS)在UVB(280、295和305nm)、UVA(320、345和395nm)和可见光(435和495nm)8个不同波段下的光化学氧化动力学行为,并探讨其对二甲亚砜(DMSO)生成的贡献率.研究结果表明,DMS光氧化过程均符合一级反应动力学方程,在UVB、UVA和可见光波段的光氧化速率常数分别为2.71~5.52、2.23~4.09和1.5~2.65d^-1.同一样品UVB波段下DMS的氧化速率明显大于UVA和可见光波段下的速率,且在280nm下最大.随着光照时间的增长,海水样品中DMS浓度与有色溶解有机物(CDOM)的光谱吸收系数(α(355))表现出明显的负相关性,表明CDOM吸光特性对DMS的光氧化过程有明显影响.此外,8个不同波段下DMS光氧化向DMSO的转化率在20.0%-31.9%范围之间,其中在280nm下达到最大值.     

降低汽油机冷起动阶段有害排放的技术措施

在汽油机的一个测试循环中,约占排放污染物总量70%～80%的非甲烷碳氢化合物是在汽油机冷起动阶段没有经催化转化而直接排入大气中,造成严重污染。研究探讨了使用高效汽油添加剂、催化器减少汽油机冷起动排放污染物的机理和实况,进而提出了一些可行的实用方案。     

水介质中催化剂Raney Ni催化2-氯酚加氢脱氯

选择水作为反应介质,以氢气为氢源,研究了Raney Ni催化下、水溶液中2-氯酚的加氢脱氯,调查了溶剂、碱助剂和碱金属或碱土金属氯化物对加氢脱氯反应的影响.发现在水体系中,2-氯酚更容易被加氢脱氯,水作为反应介质时显著改善了加氢脱氯的反应环境,消除了无机氯化物在催化剂表面的吸附和累积,使催化剂保持了高活性.     

Modelling of Air Quality with CAMx: A Case Study in Switzerland

The three-dimensional Eulerian model CAMx (Comprehensive Air QualityModel with Extensions) was applied for the first time to simulate bothgaseous and particulate photochemical air pollution in Switzerland during July 28–30, 1993. The meteorological input data were prepared using the Systems Applications International Mesoscale Model (SAIMM). The CAMx model results were compared with the measurements carried out at ground level andfrom airborne measuring platforms within the frame of the Swiss POLLUMET research programme. In general, the CAMx performance for gaseous species wasfound to be better than that of the previously used Urban Airshed Model (UAM)and the Variable Grid Urban Airshed Model (UAM-V). The most significant improvement for the gaseous species is in the prediction of HNO₃ concentrations, due to the inclusion of aerosol chemistry. Aerosol species such as NO₃ ^-, NH₄ ⁺, SO₄ ^2-, and secondary organic aerosols were calculated in one particle size range (0.04–2.5 m) and compared with a few measurements available. Although July 29 was reasonably well simulated, overestimated wind speeds by SAIMM for July 30 caused a too fast transport of pollutants. Similarly to measurements, significant spatial correlation of the secondarily formed aerosols with ozone and formaldehyde is found in the afternoon.     

北京市城区大气羰基化合物的季节变化

2006年8月19～22日（夏季）、 10月24～30日（秋季）和2007年1月20～23日（冬季）,利用被动式扩散采样器(DSD-DNPH)对北京市城区5个地点C₁～C₁₀羰基化合物进行了采样.通过高效液相色谱(high performance liquid chromatography, HPLC)分析, 20种羰基化合物被检测出,在夏季、秋季和冬季其总浓度分别为(89.1±23.6)、(85.2±17.5)和(40.0±9.8) μg/m³.其中,甲醛、乙醛和丙酮是浓度最高的3种羰基化合物,它们的浓度从冬季的(7.1±2.1)、(10.3±3.1)、(9.5±1.8) μg/m³增长到夏季的(15.3±9.2)、(12.9±4.9)、(13.3±3.5) μg/m³和秋季的(13.2±4.0)、(13±4.4)、(15.3±4.0) μg/m³.定性分析表明,羰基化合物的污染来源,冬季主要是机动车污染,而夏季和秋季则是来自光化学反应、机动车和餐馆油烟的综合污染.此外,在风速较大、扩散条件较好的条件下,甲醛、乙醛和丙酮等主要污染物浓度明显降低,表明扩散条件对羰基化合物浓度的影响较明显.     

固体催化改良Fenton法处理苯酚废水的研究

针对目前常规Fenton法存在的H2O2耗量大的问题,提出了以活性炭作为催化剂载体的改良Fenton法。采用常规Fenton法以及改良Fenton法对苯酚废水的处理效果进行了对比实验研究,从H2O2投加量、接触反应时间和pH值影响因子出发分析比较了常规及改良Fenton法的COD及苯酚去除率。通过比较,改良Fenton法达到了优于常规Fenton法的处理效果,H2O2投加量20 mL/L,接触反应时间100 min,pH值为3是最佳的反应条件。降低了处理成本,提高了回收利用。     

常见金属及金属氧化物催化超声降解间苯二酚

探索了以常见金属铜、锌、铝单质及其氧化物为催化剂,提高超声降解间苯二酚速率的可行性。在超声/零价金属以及超声/金属氧化物同时存在的条件下,以间苯二酚为目标污染物,对间苯二酚的去除效果、溶液pH的变化及金属离子的溶出等进行考察,并对超声波与金属以及金属氧化物协同催化降解有机物的作用机理进行了初步的探讨。实验结果表明,铜、锌、氧化铜均可以有效地催化间苯二酚的超声降解,其过程均符合假一级动力学反应。各类金属和金属氧化物的催化能力排序为铜、锌混合物>氧化铜、锌混合物>锌>铜≈氧化铜。当间苯二酚初始浓度为0.05 mmol/L,初始pH=5,超声频率25 kHz,功率为200 W,铜、锌比例为1:1,投量为1 g/L时,US/Cu-Zn去除间苯二酚的速率常数为1.53×10-2min-1,是单独超声作用时的9倍。     

活性炭催化过二硫酸盐降解水中AO7

过二硫酸盐（persulfate,PS）活化技术是基于硫酸根自由基（SO 4^-.）的一种新型高级氧化技术.用颗粒状活性炭（GAC）常温常压下直接非均相催化PS来降解水中难生化偶氮染料AO7（acid orange 7）.结果表明,GAC/PS体系对AO7不但能够快速脱色,而且有较高的矿化率.n（PS）∶n（AO7）为...     

Conversion of the refractory ammonia and acetic acid in catalytic wet air oxidation of animal byproducts

Wet air oxidation (WAO) and catalytic wet air oxidation (CWAO) of slaughtered animal byproducts (ABPs) were investigated. Two step experiment was carried out consisting of a non-catalysedWAO run followed by a CWAO run at 170–275°C , 20 MPa, and reaction time 180 min. TheWAO (1st step) of sample (5 g/L total organic carbon (TOC)) yielded (82.0 4)% TOC removal and (78.4 13.2)% conversion of the initial organic-N into NH4 +-N. Four metal catalysts (Pd, Pt, Rh, Ru) supported over alumina have been tested in catalytic WAO (2nd step) at elevated pH to enhance ammonia conversion and organic matter removal, particularly acetic acid. It was found that the catalysts Ru, Pt, and Rh had significant e ects on the TOC removal (95.1%, 99.5% and 96.7%, respectively) and on the abatement of ammonia (93.4%, 96.7% and 96.3%, respectively) with high nitrogen selectivity. The catalyst Pd was found to have the less activity while Pt had the best performance. The X-Ray di raction analysis showed that the support of catalyst was not stable under the experimental conditions since it reacted with phosphate present in solution. Nitrite and nitrate ions were monitored during the oxidation reaction and it was concluded that CWAO of ammonia in real waste treatment framework was in good agreement with the results obtained from the literature for ideal solutions of ammonia.