银柱吸附,离子色谱法测定海水中的NO3--N

利用银柱吸附海水中的Cl-离子,然后通过电导法离子色谱测定海水中的NO3-_N。研究结果表明,使用该方法测定海水中的NO3-_N,分析方法简单,测试结果准确,同一样品多次测定结果的相对标准偏差低于2.0%,检测结果不受干扰,检出限为0.008mgL,是监控海水中NO3-_N的有效方法。     

贫燃条件下汽车尾气中NOx催化净化研究进展

汽车尾气排放的NOx(主要是NO)是城市大气的主要污染源之一。本综述了近l0年来贫燃条件下NOx催化转化为N2的催化剂研究进展。这些方法包括HC-SCR、NO直接催化分解、NOx吸附-还原等。讨论了不同催化剂的性能影响因素。新的负载材料MFI、MCM-41、SAPO-34的应用增强了催化剂的性能。双功能催化剂由于两种活性位的协同作用表现出较高的活性和选择性。新的纳米结构概念催化剂NOx吸附还原中发现有广泛应用。介绍了上述催化脱除NOx的各种机理并指出了今后研究的方向。     

厌氧条件下砂壤水稻土N2、N2O、NO、CO2和CH4排放特征

了解厌氧条件土壤反硝化气体(N2、N2O和NO)、CO2和CH4排放特征,是认识反硝化过程机制的基础,并有助于制定合理的温室气体减排措施.定量反硝化产物组成,可为氮转化过程模型研发制定正确的关键过程参数选取方法或参数化方案.本研究选取质地相同(砂壤土)的两个水稻土为研究对象,通过添加KNO3和葡萄糖的混合溶液,将培养土壤的初始NO-3和DOC含量分别调节到50 mg·kg-1和300 mg·kg-1,采用氦环境培养-气体及碳氮底物直接同步测定方法,研究完全厌氧条件下土壤N2、N2O、NO、CO2和CH4的排放特征,并获得反硝化气态产物中各组分的比率.结果表明,在整个培养过程中,两个供试土壤的N2、N2O和NO累积排放量分别为6~8、20和15~18 mg·kg-1,这些气体排放量测定结果可回收土壤NO-3变化量的95%~98%,反硝化气态产物以N2O和NO为主,其中3种组分的比率分别为15%~19%(N2)、47%~49%(N2O)和34%~36%(NO);但反硝化气体产物组成的逐日动态均显现为从以NO为主逐渐过渡到以N2O为主,最后才发展到以N2为主.以上结果说明,反硝化气体产物组成是随反硝化进程而变化的,在以气体产物组成比率作为关键参数计算各种反硝化气体产生率或排放率的模型中,很有必要重视这一点.     

港口罢工对周边空气质量的影响

港口污染物的排放浓度极大地影响着周边的空气质量,以2013年3月28日香港国际集装箱码头发生的罢工事件为契机来探究港口运作短暂的瘫痪对周边空气质量的影响。首先,进行污染物之间的相关性分析确定影响本次罢工事件的污染物主要为NO_2、NO_x、SO_2以及O_3。其次,基于罢工前、罢工期间以及罢工后污染物排放的浓度变化,进行横向对比发现罢工期间的污染物确实有一定程度的减少。再次,利用纵向对比排除四季带来的影响探究不同年份同一阶段污染物浓度的变化情况评估罢工期间的空气质量。最后,以NO_2为例建立预测模型对罢工期间的NO_2浓度进行预测,根据实际值与预测值之间的差异来说明罢工影响了NO_2的预测趋势。这项研究主要强调港口空气质量对整个环境的影响,在一定程度上说明政府实施政策的有效性,为政府提供了决策支持,同时也要注重污染物之间的相互转化作用对环境的影响。     

NO参与铝诱导蚕豆保卫细胞死亡的调控

铝(Al)是地壳中含量最丰富的金属元素,是酸性土壤中导致植物生长抑制和作物产量下降的一个主要因素,但铝毒性作用机制尚不清楚.本文以蚕豆叶表皮为材料,研究铝胁迫对气孔保卫细胞活性的影响,探讨NO在铝诱导细胞死亡中的作用.结果表明,一定浓度的A1Cl3可诱导气孔保卫细胞活性降低,部分细胞死亡,且随着铝浓度的增高细胞死亡率增高.死细胞呈现核固缩、核崩解、凋亡小体等典型凋亡特征,且凋亡抑制剂Z-Asp-CH2-DCB能阻止AlCl3诱发的细胞死亡.用NO清除剂c-PTIO、NO合酶抑制剂L-NAME或硝酸还原酶抑制剂NaN3降低铝处理组胞内NO后,细胞死亡率显著降低,胞内ROS、Ca2+水平同期降低;NaN3还能降低铝处理组中具有程序性死亡特征的细胞比率.用ROS清除剂AsA清除铝处理组胞内ROS后,细胞死亡率显著降低,胞内Ca2+和NO水平亦显著降低;铝处理液中加入Ca2+通道抑制剂LaCl3后,细胞死亡率低于铝单独处理组,胞内ROS和NO水平无明显改变.研究结果表明,铝胁迫引起的胞内NO合成增加通过Ca2+信号途径介导了保卫细胞的程序性死亡.     

Fe2O3 particles as superior catalysts for low temperature selective catalytic reduction of NO with NH3

Fe203 particle catalysts were experimentally studied in the low temperature selective catalytic reduction （SCR） of NO with NH3. The effects of reaction temperature, oxygen concentration, [NH3]/[NO] molar ratio and residence time on SCR activity were studied. It was found that Fe203 catalysts had high activity for the SCR of NO with NH3 in a broad temperature range of 150-270℃, and more than 95% NO conversion was obtained at 180℃ when the molar ratio [NH3]/[NO] = 1, the residence time was 0.48 seconds and 02 volume fraction was 3%. In addition, the effect of SO2 on SCR catalytic activity was also investigated at the temperature of 180℃. The results showed that deactivation of the Fe2O3 particles occurred due to the presence of SO2 and the NO conversion decreased from 99.2% to 58% in 240 min, since SO2 gradually decreased the catalytic activity of the catalysts. In addition, X-ray diffraction, Thermogravimetric analysis and Fourier transform infrared spectroscopy were used to characterize the fresh and deactivated Fe2O3 catalysts. The results showed that the deactivation caused by SO2 was due to the formation of metal sulfates and ammonium sulfates on the catalyst surface during the de-NO reaction, which could cause pore plugging and result in suppression of the catalytic activity.     

FeⅡ(EDTA)络合协同RDB去除NO废气效能及过程分析

为进一步提高一氧化氮(NO)的去除效率,在新型生物转鼓反应器(rotating drum biofilter,RDB)中,以FeⅡ(EDTA)络合协同RDB生物转鼓的耦合技术强化难水溶性NO的气液传质速率,提高生物还原效能为目标进行了研究.结果表明,适量FeⅡ(EDTA)被添加到RDB底部营养液后,能迅速吸收气相中的NO并生成FeⅡ(EDTA)-NO络合物,进而可通过反硝化实现同步脱氮和络合剂再生.在转速0.5 r.min-1、空床停留时间(EBRT)57.7 s、温度30℃、pH 7～8的实验条件下,RDB的净化效能随络合剂的投加而显著改善;FeⅡ(EDTA)质量浓度从0增至500 mg.L-1后,NO去除率从61.1%提高到97.6%,去除负荷从16.2 g.(m3.h)-1上升到26.7 g.(m3.h)-1.分析了FeⅡ(EDTA)络合协同净化NO的反应过程,建立了NO净化效率与FeⅡ(EDTA)添加浓度的关联方程,可较好地拟合实验数据.     

胶州湾及邻近海域表层海水中一氧化氮浓度分布及其影响因素探讨

2011年2～3月利用化学发光法对胶州湾及邻近海域表层海水中一氧化氮(NO)浓度进行了监测.结合水文、化学和生物等要素的同步观测资料,对该海域NO浓度分布及其影响因素进行了探讨.结果表明,胶州湾内表层海水中NO浓度为0.080～0.493 nmol.L-1,平均值为(0.292±0.146)nmol.L-1,胶州湾外NO浓度为未检出～0.435 nmol.L-1,平均值为(0.160±0.130)nmol.L-1.总体来说,胶州湾表层海水中NO浓度呈现出自湾内向湾外递降的分布趋势,陆地径流和人为活动可能对NO浓度的分布造成一定程度的影响.胶州湾及邻近海域表层海水中NO浓度比开阔大洋高1个数量级.周日变化研究表明,NO浓度具有一定的变化特征,最大值出现在15:00,这可能主要受光照的影响.影响NO浓度分布的因素比较复杂,可能主要受亚硝酸盐、光强和pH等因素的影响.结果表明,2011年春季胶州湾及邻近海域表层海水是大气NO的源,通量约为1.09×10-15 mol.(cm2.s)-1.     

Emissions of SO2, NO and N2O in a circulating fluidized bed combustor during co-firing coal and biomass

This paper presents the experimental investigations of the emissions of SO2, NO and N2O in a bench scale circulating fluidized bed combustor for coal combustion and co-firing coal and biomass. The thermal capacity of the combustor is 30 kW. The setup is electrically heated during startup. The influence of the excess air, the degree of the air staging, the biomass share and the feeding position of the fuels on the emissions of SO2, NO and N2O were studied. The results showed that an increase in the biomass shares resulted in an increase of the CO concentration in the flue gas, probably due to the high volatile content of the biomass. In co-firing, the emission of SO2 increased with increasing biomass share slightly, however, non-linear increase relationship between SO2 emission and fuel sulfur content was observed. Air staging significantly decreased the NO emission without raising the SO2 level. Although the change of the fuel feeding position from riser to downer resulted in a decrease in the NO emission level, no obvious change was observed for the SO2 level. Taking the coal feeding position R as a reference, the relative NO emission could significantly decrease during co-firing coal and biomass when feeding fuel at position D and keeping the first stage stoichiometry greater than 0.95. The possible mechanisms of the sulfur and nitrogen chemistry at these conditions were discussed and the ways of simultaneous reduction of SO2, NO and N2O were proposed.     

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.