Effects of SO2 and H2O on low-temperature NO conversion over F-V2O5-WO3/TiO2 catalysts

F-V_2 O_5-WO3/Ti02 catalysts were prepared by the impregnation method.As the content of F ions increased from 0.00 to 0.35 wt.%,the NO conversion of F-V_2 O_5-WO_3/TiO_2 catalysts initially increased and then decreased.The 0.2 F-V_2 O_5-WO_3/TiO_2 catalyst(0.2 wt.% F ion)exhibited the best denitration(De-NOx) performance,with more than 95% NO conversion in the temperature range 160-360℃,and 99.0% N2 selectivity between 110 and 280℃.The addition of an appropriate amount of F ions eroded the surface morphology of the catalyst and reduced its grain size,thus enhancing the NO conversion at low temperature as well as the sulfur and water resistance of the V_2 O_5-WO3/Ti02 catalyst.After selective catalytic reduction(SCR) reaction in a gas flow containing SO_2 and H_2 O,the number of NH3 adsorption sites,active component content,specific surface area and pore volume decreased to different degrees.Ammonium sulfate species deposited on the catalyst surface,which blocked part of the active sites and reduced the NO conversion performance of the catalyst.On-line thermal regeneration could not completely recover the catalyst activity,although it prolonged the cumulative life of the catalyst.In addition,a mechanism for the effects of S02 and H_2 O on catalyst NO conversion was proposed.     

Density functional theory (DFT) studies of vanadium-titanium based selective catalytic reduction (SCR) catalysts

Based on density functional theory (DFT) and basic structure models, the chemical reactions on the surface of vanadium-titanium based selective catalytic reduction (SCR) denitrification catalysts were summarized. Reasonable structural models (non-periodic and periodic structural models) are the basis of density functional calculations. A periodic structure model was more appropriate to represent the catalyst surface, and its theoretical calculation results were more comparable with the experimental results than a non-periodic model. It is generally believed that the SCR mechanism where NH₃ and NO react to produce N₂ and H₂O follows an Eley-Rideal type mechanism. NH₂NO was found to be an important intermediate in the SCR reaction, with multiple production routes. Simultaneously, the effects of H₂O, SO₂ and metal on SCR catalysts were also summarized.     

Coupling mechanism of activated carbon mixed with dust for flue gas desulfurization and denitrification

To clarify the effect of coking dust, sintering dust and fly ash on the activity of activated carbon for various industrial flue gas desulfurization and denitrification, the coupling mechanism of the mixed activated carbon and dust was investigated to provide theoretical reference for the stable operation. The results show that coking dust had 34% desulfurization efficiency and 10% denitrification efficiency; correspondingly, sintering dust and fly ash had no obvious desulfurization and denitrification activities. For the mixture of activated carbon and dust, the coking dust reduced the desulfurization and denitrification efficiencies by blocking the pores of activated carbon, and its inhibiting effect on activated carbon was larger than its own desulfurization and denitrification activity. The sintering dust also reduced the desulfurization efficiency on the activated carbon while enhancing the denitrification efficiency. Fly ash blocked the pores of activated carbon and reduced its reaction activity. The reaction activity of coking dust mainly came from the surface functional groups, similar to that of activated carbon. The reaction activity of sintering dust mainly came from the oxidative property of Fe₂O₃, which oxidized NO to NO₂ and promoted the fast selectively catalytic reduction (SCR) of NO to form N₂. Sintering dust was activated by the joint action of activated carbon, and both had a coupling function. Sintering dust enhanced the adsorption and oxidation of NO, and activated carbon further promoted the reduction of NO_x by NH₃; thus, the denitrification efficiency increased by 5%-7% on the activated carbon.     

基于风险矩阵和五元减法集对势的湖泊水生态健康动态诊断评估

为判断湖泊水生态健康子系统发展趋势、诊断病态因子,引进了五元减法集对势,建立生态子系统与物理化学子系统的合成矩阵得到湖泊水生态健康状态,从而提出了基于风险矩阵和五元减法集对势的湖泊水生态健康动态诊断评估方法,并应用于安徽省瓦埠湖。结果表明:瓦埠湖水生态健康状态1980—2015年呈变差趋势,2012年为微病态,2015年略有好转。五元减法集对势识别出瓦埠湖水生态健康的病态因子主要有底栖动物、浮游动物、叶绿素、COD、TN、TP和透明度,为改善瓦埠湖水生态健康的重要指标。上述风险矩阵和五元减法集对势耦合的动态诊断评估方法可为湖泊水生态健康评估提供新的思路。     

水动力对沉积物-水界面氧通量产生机制的影响

选取三峡库区支流御临河为研究对象,测量了5个水动力条件（平均流速为0.00,0.03,0.07,0.12,0.20m/s）下沉积物-水界面（SWI）氧通量的变化及水动力条件对SWI氧通量产生机制的影响.结果表明,随着平均流速的升高,SWI氧通量增加,由0.00m/s时的1.197mmol/（m²·h）增加为0.20m/s时的43.981mmol/（m²·h）,溶解氧穿透深度增加,氧进入沉积物更深处并被微生物和还原性物质所利用,沉积物耗氧量上升;当平均流速较低时,沉积物耗氧量以生物耗氧量为主,在0.00m/s与0.03m/s时生物耗氧量为氧通量的85.3%与57.7%;当水体平均流速较高,化学耗氧量与其他耗氧量中的化学过程耗氧量在氧通量中的比重逐步提高.     

利用HYSPLIT模型研究珠三角地区VOCs时空分布特征

于2016年在中国广东大气超级监测站,开展4个季节的VOCs长时间观测,共获得2142组有效数据,并利用HYSPLIT模型分析珠三角地区VOCs时空分布特征.结果表明,各类VOCs混合比和化学反应活性具有明显的季节变化特点.观测期间,VOCs平均浓度为（18.523±20.978）×10^-9,其中,低碳烯烃和苯系物二者混合比之和仅占46%,但贡献了85%的·OH消耗速率（L_OH）、82%的臭氧生成潜势（OFP）和97%的二次气溶胶生成潜势（SOAFP）.观测站点主要受来自北部内陆地区气团（1#）、西部内陆地区气团（2#）、台湾海峡南端气团（3#）以及南部海洋地区气团（4#）的影响.1#气团中炔烃和苯系物的混合比占比最高,分别达到10%、37%,而3#气团中低碳烷烃的浓度水平最高,达到（8.437±5.561）×10^-9.通过估算气团中VOCs的化学反应活性,可以发现,1#气团的VOCs化学反应活性最强,其对O₃和SOA的生成贡献最高.1#、2#、3#和4#气团中VOCs的化学反应活性主要由苯系物和低碳烯烃贡献.     

CeO2形貌结构对催化湿式空气氧化苯酚性能的影响

采用水热法、沉淀法和溶胶凝胶法制备了3种不同形貌的CeO₂催化材料,并将其用于湿式空气氧化苯酚水溶液过程中,探讨了CeO₂形貌结构对催化湿式氧化苯酚水溶液性能的影响.采用扫描电子显微镜（SEM）、透射电子显微镜（TEM）、X射线衍射（XRD）、程序升温还原（TPR）等手段对CeO₂催化材料进行了表征.结果表明,水热法制备的CeO₂催化材料表现出较好催化性能,主要原因是水热法合成的CeO₂呈现交错的纳米棒状结构,主要暴露（220）晶面,且沿着（220）晶向生长.在反应温度为200℃、空气压力为2MPa、苯酚初始浓度500mg/L的条件下,最终（240min）COD的去除率为95.5%.     

洪泽湖不同入湖河流沉积物磷形态特征及生物有效性

为揭示洪泽湖入湖河流沉积物磷形态空间差异性及影响因素,分析了洪泽湖自西北向西南7条入湖河流65个表层沉积物中不同磷（P）形态,并探讨了磷形态空间赋存特征的影响因素及环境意义.研究表明：沉积物总磷（TP）含量为488.90mg/kg~960.22mg/kg,无机磷（Pi）为主要形态,相对含量为65.81%~76.16%.西部入湖流域沉积物有机磷（Po）以非活性有机磷（NLOP）为主,汴河最高,相对含量约占Po的50.41%,生物有效态无机磷（BAP）相对含量最高,占Pi的66.84%,污染程度最高;西南和西北入湖流域Po则以中活性有机磷（MLOP）为主,Pi以钙结合态无机磷（HCl-Pi）为主.西北入湖流域由于受当地地质背景的影响,HCl-Pi所占Pi相对含量最高（43.02%）,从而减缓了磷的移动能力,污染程度最低.随着沉积物污染程度的增加,生物有效态Po含量增加,但所占Po相对含量降低;HCl-Pi含量增加,所占Pi相对含量降低,这一现象和我国其它典型地区沉积物磷形态空间分布类似.西部和西南入湖流域主要受水土流失、有机面源污染及藻类生长的影响,有机质环境较高,水交换能力弱,可被有机质降解的Po组分高于可被矿化的Po组分,大部分难降解Po组分易沉积,导致西部和西南入湖流域较高的BAP和NLOP含量,富营养化程度较高.沉积物OM是各形态磷之间相互转化的关键因素,和沉积物内源磷地球生物化学循环密切相关.洪泽湖入湖流域沉积物磷形态空间差异性主要由农业面源污染物的输入而导致内源磷负荷加剧.洪泽湖西部和西南入湖流域应重点控制农田水土流失及养殖业面源污染,建设滨岸修复带,遵循少量多次增施有机肥原则,减少农用地水土流失.健全农村养殖业废水废渣处理;划定科学养殖区;提倡铜围网箱,增加水体交换率.而对于洪泽湖西北入湖流域则应重点防止过度城镇化带来的水土流失及对生态功能保护区过高的污染负荷.     

融合Lamb-Jenkinson分型法和LSTM神经网络的PM2.5预测研究

文章采用NCEP/NCAR逐日海平面气压场资料,利用Lamb-Jenkinson环流分型法对张家口大气环流进行分型,分析环流型与PM_(2.5)质量浓度之间的关系,并针对PM_(2.5)浓度的预测,提出一种融合Lamb-Jenkinson环流分型和LSTM神经网络混合模型的方法,即以环流指数为预测因子基于LSTM方法搭建PM_(2.5)质量浓度的预测模型。结果表明:影响张家口地区的主要环流型有反气旋型、气旋型、偏北平直型、西南平直型、偏西平直型、东北平直型等、西北平直型、偏东平直型。PM_(2.5)污染日出现的主要环流型为南气旋平直型、东南平直型、偏南平直型、偏东气旋型、西南气旋平直型、偏东平直型、气旋型等,而反气旋型和反气旋式平直环流型不利于污染出现。张家口地区的PM_(2.5)污染与地面环流有着密切的联系,当存在PM_(2.5)污染时,张家口地区处于日本海高压后部的均压场区域,污染越严重,日本海高压中心强度越强。模型预测结果的均方根误差为9.88、平均绝对误差为5.84、拟合优度达0.80,表明该模型具有一定的预报能力。     

Cr(Ⅵ)踪迹指标现场测定用于铬污染地下水源解析

根据研究区地下水样品测试结果,该文选定与Cr(Ⅵ)极强相关,且物理化学性质较稳定的钠离子作为研究地下水中Cr(Ⅵ)迁移规律的踪迹指标,并采用钠离子复合电极建立了踪迹指标现场检测方法。实验结果表明,钠离子浓度在5～500 mg/L线性范围内的电极响应斜率为-61.09 mV/pNa(103%),方法检出限为0.69 mg/L,加标回收率为92.8%～103.4%,现场测试结果与实验室测试结果一致。该研究根据踪迹指标钠离子与污染物现场检测数据,构建了钠离子与Cr(Ⅵ)浓度比值的对数函数,并有效识别出主污染源、次级污染源、污染物迁移主路径、潜在污染区、潜在影响区及背景区,为铬渣类污染场地土壤和地下水环境风险评价及污染修复提供了技术支撑和参考依据。