选择性非催化还原法烟气脱硝工业试验

以氨水作为还原剂，在日产5kt的新型干法水泥生产线分解炉上进行选择性非催化还原脱硝工艺的工业性试验研究。在氨水质量分数为13.0%、喷入点温度为894℃、n（NH₃）∶n（NO_x）为1.2、雾化压力为0.35MPa的条件下，NO_x去除率最高，为72.8%，剩余NO_x质量浓度为196mg/m³，剩余NH₃质量浓度小于0.9mg/m³，远低于《水泥工业大气污染物排放标准》征求意见稿中限定的NO_x和NH₃质量浓度。     

Leaching,mobility and persistence of tebufenozide in columns packed with forest litter and soil

Abstract

Leaching, downward mobility and persistence of tebufenozide was investigated under laboratory conditions in columns packed with forest litter and soil, after fortification with the analytical grade material (purity > 99.6%) and with two commercial formulations, RH‐5992 2F (aqueous flowable) and RH‐5992 ES (emulsion suspension). Two types of litter and soil were used: one type with relatively high amounts of sand and the other with high amounts of clay.

The concentrations eluted in the leachates were lower when the analytical material (dissolved in acetone) was used for fortification, than when the two formulations (diluted with water) were used. The amount leached was higher for RH‐5992 2F than for RH‐5992 ES. The type of substrate, i.e., sandy or clay type, had only marginal influence on the amounts eluted in the leachates. Downward movement of tebufenozide from the top 2‐cm layer to the untreated middle and bottom layers (3‐cm segments) was consistently lower when the analytical material was used for fortification, than when the two formulations were used. Downward movement was higher for RH‐5992 2F than for RH‐5992 ES. Persistence of tebufenozide in substrates, maintained under submerged conditions for 70 days after leaching, indicated an initial 2‐week lag period prior to the onset of degradation. Formulation‐related differences were observed in the half‐life (DT₅₀) values. When the analytical material was used for fortification, the DT₅₀ ranged from ca 54 to 59 d. However, when the formulations were used for fortification, the DT₅₀ showed a higher range, i.e., from ca 62 to 67 d for RH‐5992 2F and ca 70 to 80 d for RH‐5992 ES. Formulation ingredients appear to have caused enhanced adsorption of tebufenozide onto the substrates, thus delaying degradation.     

Photolysis of the herbicide bispyribac sodium in aqueous medium under the influence of UV and sunlight in presence or absence of sensitizers

The photolysis of a rice herbicide Bispyribac sodium (Sodium 2, 6-bis [(4, 6-dimethoxypyrimidin-2-yl) oxy] benzoate) has been studied in different aqueous medium (distilled water, pond water and Irrigation water) under the influence of UV (λ max ≥ 250 nm) and sunlight in presence or absence of sensitizers (TiO₂ and KNO₃). The study was conducted under laboratory simulated condition which made it possible to evaluate the contribution of different factors viz. source of irradiation, solvent and sensitizers towards the photolysis of bispyribac sodium. The photodegradation proceeds via first order reaction Kinetics in all the cases. Five photo metabolites (M₁-M₅) were isolated in pure form by column chromatographic method from the irradiation system under UV influenced and TiO₂ as sensitizer. From the different spectral data (IR, NMR, UV-VIS, Mass) the structure of these five metabolites were assigned as M₁ (Phenol), M₂ [2, 6-Dihydroxy benzoic acid], M₃ [2, 6-bis [(4, 6 dimethoxypyrimidin-2yl) oxy] benzoic acid], M₄ [2-(3-Hydroxy-phenoxy)-pyrimidine-4, 6-diol] and M₅ as [2,4-Dihydroxy-3, 5-dimethoxy-6-(4-methoxy pyrimidine-2-yloxy)-benzoic acid]. Moreover, another six photometabolites (M₆-M₁₁) were identified from the different irradiation system on the basis of Micromass analysis. On the basis of MS/MS data analysis, the structure of these six photometabolites were assigned as M₆ [2-(4, 6-Dimethoxy-pyrimidin-2-yloxy)-6-hydroxy-benzoic acid], M₇ [2-Hydroxy-6-(4-hydroxy-6-methoxy-pyrimidin-2-yloxy)-benzoic acid], M₈ [4, 6-Dimethoxy-pyrimidin-2-ol], M₉ [6-Methoxy-pyrimidine-2, 4-diol], M₁₀ [2-Hydroxy-6-(pyrimidin-2-yloxy)-benzoic acid] and M₁₁ [2, 4, 6-Trimethoxy-pyrimidine]. The plausible Photodegradation pathways of bispyribac sodium in the present investigation were portrayed which proceeds via hydrolysis, hydrolytic cleavage, O-dealkylation, decarboxylation, dehydroxylation, O-alkylation and hydroxylation.     

The structure of the fire fighting foam surfactant Forafac®1157 and its biological and photolytic transformation products

For several decades, perfluorooctane sulfonate (PFOS) has widely been used as a fluorinated surfactant in aqueous film forming foams used as hydrocarbon fuel fire extinguishers. Due to concerns regarding its environmental persistence and toxicological effects, PFOS has recently been replaced by novel fluorinated surfactants such as Forafac®1157, developed by the DuPont company. The major component of Forafac®1157 is a 6:2 fluorotelomer sulfonamide alkylbetaine (6:2 FTAB), and a link between the trade name and the exact chemical structure is presented here to the scientific community for the first time. In the present work, the structure of the 6:2 FTAB was elucidated by ¹H, ¹³C and ¹⁹F nuclear magnetic resonance spectroscopy and high-resolution mass spectrometry. Moreover, its major metabolites from blue mussel (Mytilus edulis) and turbot (Scophthalmus maximus) and its photolytic transformation products were identified. Contrary to what has earlier been observed for PFOS, the 6:2 FTAB was extensively metabolized by blue mussel and turbot exposed to Forafac®1157. The major metabolite was a deacetylated betaine species, from which mono- and di-demethylated metabolites also were formed. Another abundant metabolite was the 6:2 fluorotelomer sulfonamide. In another experiment, Forafac®1157 was subjected to UV-light induced photolysis. The experimental conditions aimed to simulate Arctic conditions and the deacetylated species was again the primary transformation product of 6:2 FTAB. A 6:2 fluorotelomer sulfonamide was also formed along with a non-identified transformation product. The environmental presence of most of the metabolites and transformation products was qualitatively demonstrated by analysis of soil samples taken in close proximity to an airport fire training facility.     

Removal of humic substances by biosorption

Fungal pellets of Aspergillus niger 405,Aspergillus ustus 326,and Stachybotrys sp.1103 were used for the removal of humic substances from aqueous solutions.Batchwise biosorption,carried out at pH 6 and 25°C,was monitored spectrophotometrically and the process described with Freundlich’s model.Calculated sorption coeffcients Kf and n showed that A.niger exhibited the highest effciency.A good match between the model and experimental data and a high correlation coeffcient(R2)pointed out to judicious choice of ...     

对硝基苯胺的光化学降解研究

系统研究了氙灯和高压汞灯照射下对硝基苯胺(PNA)在蒸馏水、人工海水和天然海水中的光化学降解情况.结果表明,PNA光降解速率会受到光源、溶液介质、温度、起始浓度、重金属离子、甲醇及过氧化氢浓度的影响.随着光源强度的增强、起始浓度的增大、温度的增高和过氧化氢量的增加,PNA在海水中光降解速率相应加快;然而甲醇的加入可有效...     

冰中和水中四环素光降解动力学及其影响因素的比较

冰雪是一类重要且普遍的环境介质,而冰雪环境光化学是一门新兴的学科.在相同光照条件下比较冰中和水中有机污染物的光化学行为,有助于揭示冰雪光化学与水环境光化学之间的异同.本文以四环素（TC）为模型化合物,比较了模拟日光（λ>290 nm）照射下不同水体冰相和水相中TC的光降解动力学,研究了不同相中溶解性物质（腐殖酸（HA）、Cl^-、NO₃^-和Fe（III））对光降解的影响及作用机制,以揭示冰雪环境光化学和水环境光化学的异同.结果表明,冰中和水中TC光解遵循准一级反应动力学,纯水冰中表观光解量子产率为4.76×10^-3,高于纯水中表观光解量子产率（3.85×10^-3）.在不同水体中,冰相TC的光解快慢顺序为海水冰中 > 淡水冰中 > 纯水冰中,而在水相中光解快慢顺序与冰相不同,为淡水中 > 海水中 > 纯水中.通过考察主要溶解性物质对冰/水中TC光降解动力学的影响发现,无论是在冰相还是水相,Cl^-、HA、NO₃^-和Fe（III）均加快了TC的光降解,且促进作用随浓度的升高而增强.但在水相与冰相中每个因素促进的程度却存在差异,相对于水环境,冰中HA、NO₃^-、Fe（III）敏化作用较大,对TC光降解的促进作用较强;而冰中Cl^-对TC光解的促进作用较水相中弱.这些溶解性物质对TC光解的促进作用能够解释海水冰、淡水冰与海水、淡水中TC相对于纯水冰相/水相具有较强的光降解能力.进一步地,将实验数据外推到实际环境,在35°~50°N地区的仲冬季,冰雪表面和水体表层TC光化学降解的半减期分别为15.4~38.9 min和19.0~48.0 min,其不仅依赖于光解发生的纬度与季节,还受到反应基质（冰/水）的影响.以上结果揭示了冰中和水中TC光化学转化行为的异同,这对于准确评价寒冷环境中此类新型污染物的归趋具有重要意义.     

影响大气汞化学过程的敏感因子分析

为了分析汞在大气中的化学行为,在一个化学模式中加入汞的气相、气液平衡和液相反应,模拟大气汞及其化合物的演变规律,并分析了气象因子(云、光解率、温度)和化学因子(气态O3、H2O2、HO2、OH和气态零价汞Hg0(g))的初始体积分数对各形态汞及其化合物浓度和Hg0(g)转化率的影响.模拟结果表明,在中等大气污染条件下,Hg0(g)的每小时平均转化率为2.91%.敏感性试验结果表明,云量、光解率、温度、O3和Hg0(g)的初始体积分数对不同形态汞的影响较为显著.云量的增加、光解率的增加、臭氧初始体积分数的升高,各形态汞的平衡时间缩短,除气态氧化汞和一价汞离子外,其他形态汞的平衡浓度均会降低,Hg0(g)的转化率增加.温度增加将抑制Hg0(g)的转化.Hg0(g)的初始体积分数增加,各形态汞的浓度升高,但其平均转化率没有显著变化.不同因子对汞化学过程的相对作用对区域或全球大气汞的环境模拟具有指导意义.     

Semi-closed synthesis of nitrogen and oxygen Co-doped mesoporous carbon for selective aqueous oxidation

Heteroatom-doped meso/micro-porous carbon materials are conventionally produced by harsh carbonization under an inert atmosphere involving specific precursors, hard/soft templates, and heteroatom-containing agents. Herein, we report a facile synthesis of N and O co-doped meso/micro-porous carbon (NOMC) by template-free carbonization of a small-molecule precursor in a semi-closed system. The semi-closed carbonizaiton process yields hydrophilic NOMCs with large surface area in a high yield. The porous structure as well as the elemental composition of NOMCs can be modulated by changing the holding time at a particular temperature. NOMCs as metal-free heterogeneous catalysts can selectively oxidize benzyl alcohol and its derivatives into aldehydes/ketones with>85％conversion in aqueous solution, which is much higher than that of the control sample obtained in tube furnace (21％conversion), mainly due to their high N content, high percentage of pyridinic N, and large surface area. The presence of O-containing moieties also helps to improve the hydrophilicity and dispersion ability of catalysts and thus facilitates the mass transfer process during aqueous oxidation. The NOMC catalysts also dispayed excellent activity for a wide range of substrates with a selectivity of>99％.     

两种生物炭的制备及其对水溶液中四环素去除的影响因素

以中药材三桠苦药渣和玉米秸秆为原料,分别在400、600和800℃下热解制备生物炭,并研究其对水溶液中四环素的去除及其影响因素.利用元素分析、傅里叶红外光谱(FT-IR)、比表面积分析(BET)、X射线衍射(XRD)、扫描电子显微镜(SEM)等方法对制备的生物炭进行表征;并探究热解温度、生物炭添加量、初始溶液浓度、吸附时间、溶液pH、离子强度、环境温度等因素对生物炭去除水溶液中四环素的影响;通过吸附动力学和等温吸附平衡探究两种原料制备的生物炭对溶液中四环素的吸附行为.结果表明,生物炭对四环素的吸附性能随制备温度的升高而增加,800℃制备的三桠苦药渣生物炭(EIBC800)具有最佳吸附性能.生物炭添加量、溶液pH、离子强度、吸附时间对800℃制备的三桠苦药渣生物炭(EIBC800)和玉米秸秆生物炭(CSBC800)吸附水溶液中四环素影响较大,吸附时环境温度对吸附的影响大小依赖于抗生素质量浓度.EIBC800和CSBC800对四环素的吸附行为均符合准二级动力学方程(R~2分别为0. 954 0和0. 835 5),等温吸附符合Freundlich方程(R~2分别在0. 899 1～0. 957 9和0. 973 6～0. 994 6之间),主要吸附过程为化学吸附,且吸附过程均是自发吸热的过程.通过以两种原料所制备的生物炭吸附性能对比,EIBC800吸附抗生素的能力比CSBC800更强,说明中药渣在制备生物炭去除水环境中的抗生素具有较好的应用前景.