北京餐饮源排放细粒子理化特征及其对有机颗粒物的贡献

调研了北京餐饮业发展现状,通过在线监测、采样分析等手段研究北京4家不同烹调方式的餐馆所排放颗粒物的质量浓度、粒径分布、形貌特征、化学组分,并初步估算餐饮源排放细粒子对北京细粒子中颗粒有机物的贡献.结果表明,餐馆的原料、烹饪过程、油烟去除装置以及客流量都会影响餐馆所排放颗粒物的物理、化学性质.样本餐馆营业期间排放颗粒物PM_{2 .5}质量浓度是当日环境大气PM_{2 .5}质量浓度的8～35倍,PM_{1 .0}在PM_{2 .5}的质量浓度中约占50%～85%.餐饮源排放颗粒物多以固态和液态颗粒物形貌存在,化学组分质量百分数由多到少依次是有机物、无机离子和元素碳,分别占到PM_{2 .5}质量浓度的70%左右、5%～11%和小于2%.初步估计结果表明,北京餐饮源排放细粒子对有机颗粒物的贡献和交通源的排放相当,成为北京细粒子有机颗粒物的主要来源之一.认识餐饮源排放颗粒物的理化性质,可以为改善北京空气质量和保证居民身体健康提供数据支持.     

Kinetics of selective catalytic reduction of NO by NH3 on Fe-Mo/ZSM-5 catalyst

The catalyst of Fe-Mo/ZSM-5 has been found to be more active than Fe-ZSM-5 and Mo/ZSM-5 separately for selective catalytic reduction (SCR) of nitric oxide (NO) with NH3. The kinetics of the SCR reaction in the presence of O2 was studied in this work. The results show that the observed reaction orders were 0.74-0.99, 0.01-0.13, and 0 for NO, O2 and NH3, respectively, at 350-450℃. And the apparent activation energy of the SCR was 65 kJ/mol on the Fe-Mo/ZSM-5 catalyst. The SCR mechanism was also deduced. Adsorbed NO species can react directly with adsorbed ammonia species on the active sites to form N2 and H2O. Gaseous O2 might serve as a reoxidizing agent for the active sites that have undergone reduction in the SCR process. It is also important to note that a certain amount of NO was decomposed directly over the Fe-Mo/ZSM-5 catalyst in the absence of NH3.     

以高岭土为原料合成高稳定性介孔分子筛

以廉价的高岭土和硅酸钠为硅源,用水热法合成了介孔分子筛。采用X射线粉末衍射、Fourier变换红外光谱、热分析、N2物理吸附、扫描电子显微镜和透射电子显微镜埘样品进行了表征,同时研究了样品的热稳定性和水热稳定性。结果表明：长程有序的介孔分子筛平均孔径约为2．75nm：经900℃焙烧3h或100℃水热处理6d,样品的介孔结构不被破坏,说明样品具有高的热稳定性和水热稳定性。     

镉对长江华溪蟹金属硫蛋白mRNA表达的诱导及低分子量壳聚糖的联合作用

采用实时荧光定量PCR法,研究了不同浓度镉（Cd2＋）对长江华溪蟹（Sinopotamon yangtsekiense）金属硫蛋白（metallothionein,简称MT）在肝胰腺、鳃、肌肉和心脏中mRNA表达的诱导作用及低分子量壳聚糖（lowmolecular weight chitosan,简称LMWC）的联合作...     

Ti/SnO2-Sb2O5/PbO2阳极电化学氧化降解苯甲酸研究

文章研究了TI/SnO2-Sb2O5/Pbo2在两室电解池中氧化降解苯甲酸的性能,主要考察了电流密度、初始pH值、初始苯甲酸浓度和支持电解质这四个参数对TOC去除效率的影响。实验表明在电流密度为30 mA/cm2,初始苯甲酸浓度为0.5 mmol/L,支持电解质(Na2SO4)为0.1mol/L的条件下,经过6 h反应...     

La-Co-Fe-Cu/HZSM-5在尾气碳颗粒燃烧中的催化性能

采用柠檬酸络合低温浸渍法制备分子筛负载钙钛矿型复合氧化物催化剂。采用XRD、SEM和H2-TPR等手段对催化剂性能进行表征,并在微型固定床反应器中对催化剂进行活性评价。结果表明,在钙钛矿型复合氧化物中进行B位离子掺杂,可以改善催化活性,碳颗粒燃烧温度降低。在20%LaCoO3/HZSM-5催化剂中用铁离子部分取代钴离子可以改善碳颗粒的燃烧性能,取代量增加碳颗粒燃烧温度降低,但是生成CO2的选择性也降低,以20%LaCo0.2Fe0.8O3/HZSM-5为催化剂,Tig、Tm和Tf分别为256℃、399℃和403℃,但生成CO2的选择性只有72.5%。在20%LaCo1-xFexO3/HZSM-5中的钙钛矿型复合氧化物B位离子中加入铜离子后,在碳颗粒燃烧反应中生成CO2的选择性得到明显改善,Sco2提高10个单位以上。以20%LaCo0.2Fe0.6Cu0.2O3/HZSM-5为催化剂,在碳颗粒燃烧反应中生成CO2的选择性可以达到94.7%,Tig、Tm和Tf分别为242℃、427℃和445℃。     

偶氮染料分子结构对其生物脱色影响的研究进展

偶氮染料是工业中染料用量最大的一类,不同的分子结构对其微生物脱色性能具有一定的影响作用。文章综述了偶氮染料分子结构中的取代基种类及其取代位置对染料的脱色规律,以及分子特征结构对微生物脱色的量化分析。对目前染料生物脱色规律研究中存在的问题进行了分析,提出相应的对策措施。     

稀释接种法测BOD5考核样品的一些注意点

用稀释接种法测定BOD5时,由于操作繁琐,全部实验时间需要5d,任一环节出现问题都会影响实验结果。在进行考核实验时,由于时间紧,样品量有限,因此每个实验操作步骤都要谨慎仔细。通过实践经验,就BOD,考核实验总结了一些注意点。     

液相高压放电降解RB5染料废水的试验研究

随着印染工艺不断更新,大量化学分子结构复杂的化工染料应用到印染行业,使得常规的水处理工艺难以降解印染废水中的染料。本文以活性黑（RB5）染料为研究对象,采用液相高压放电产生强氧化性自由基来降解染料废水,考察反应时间、初始浓度和气体流量对RB5降解的影响,研究结果表明：在外部功率相同的情况下,浓度高染料其降解率相对较低;通入氧气量增加,产生的活性自由基和活性物质数量也增加,RB5的降解率也增大,但气流量不宜过大;高压放电产生的各种活性物质容易破坏染料发色基团的分子链,使其脱色。     

Effects of metal and acidic sites on the reaction by-products of butyl acetate oxidation over palladium-based catalysts

Catalytic oxidation is widely used in pollution control technology to remove volatile organic compounds. In this study, Pd/ZSM-5 catalysts with different Pd contents and acidic sites were prepared via the impregnation method. All the catalysts were characterized by means of N2 adsorption- desorption, X-ray fluorescence （XRF）, HE temperature programmed reduction （H2-TPR）, and NH3 temperature programmed desorption （NH3-TPD）. Their catalytic performance was investigated in the oxidation of butyl acetate experiments. The by-products of the reaction were collected in thermal desorption tubes and identified by gas chromatography/mass spectrometry. It was found that the increase of Pd content slightly changed the catalytic activity of butyl acetate oxidation according to the yield of CO2 achieved at 90%, but decreased the cracking by-products, whereas the enhancement of strong acidity over Pd-based catalysts enriched the by-product species. The butyl acetate oxidation process involves a series of reaction steps including protolysis, dehydrogenation, dehydration, cracking, and isomerization. Generally, butyl acetate was cracked to acetic acid and 2- methylpropene and the latter was an intermediate of the other by-products, and the oxidation routes of typical by-products were proposed. Trace amounts of 3-methylpentane, hexane, 2-methylpentane, pentane, and 2-methylbutane originated from iso4merization and protolysis reactions.