Morphology-dependent interfacial interactions of Fe2O3 with Ag nanoparticles for determining the catalytic reduction of p-nitrophenol

In this work,we fabricated three kinds of Ag/Fe_2O_3 model catalysts with different morphologies to study the interfacial interactions between Ag and Fe_2O_3,and how they affected the catalytic activity in hydrogenation of p-nitrophenol was explored.The hydrothermal method was used to synthesize the metal oxide supported silver catalyst,with various morphologies including nanoplates(NPs),nanospheres(NSs),and nanocubes(NCs).The crystal structure,morphology and surface elements of the composite were investigated by various measurements,such as X-ray diffraction(XRD),scanning electron microscopy(SEM),transmission electron microscopy(TEM) and X-ray photoelectron spectroscopy(XPS).The catalytic activity was also evaluated by the reduction of p-nitrophenol to p-aminophenol.It was found that the activities of the above catalysts varied with the morphology of the support.Among them,Ag/Fe_2O_3 NPs promoted the highest performance,Ag/Fe_2O_3 NSs were slightly inferior,and Ag/Fe_2O_3 NCs were the worst.At last,we ascribed the remarkable activity of Ag/Fe_2O_3 NPs to the strong metal-support interactions between Ag and Fe_2O_3.     

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.     

达里诺尔湖水体DOM荧光特征及其来源解析

达里诺尔湖（简称“达里湖”）是内蒙古自治区高原地区重要的生态屏障,探究达里湖水质状况及污染来源,对加强流域水环境治理、改善水环境质量具有十分重要的意义.于2018年9月及2019年6月对湖水进行采样,并通过三维荧光光谱结合PARAFAC（平行因子分析）模型,探究达里湖水体DOM（溶解性有机质）来源及其与水质的关系.结果表明:①达里湖水体中pH较高,ρ（DOC）（DOC为溶解性有机碳）、ρ（NH₄+-N）、ρ（TP）相对较高,均超过GB 3838—2002《地表水环境质量标准》Ⅴ类水质标准限值.②水体中DOM含4种荧光组分.夏季水体DOM主要分布于河流入湖口附近,其中,类腐殖质荧光组分（紫外区类富里酸和可见区类富里酸）占总组分的62.93%,类蛋白类荧光组分（类色氨酸和类酪氨酸）占总组分的36.07%;秋季水体DOM主要分布于东南侧,其中,类腐殖质荧光组分占总组分的40.52%,类蛋白类荧光组分占总组分的59.48%.③达里湖采样点荧光参数表明,达里湖DOM自生源特征较强,腐殖化程度较低.类腐殖质荧光组分与ρ（DOC）、ρ（Chla）均呈正相关,类色氨酸荧光组分与pH呈正相关,类络氨酸与ρ（DTN）、ρ（NH4+-N）、ρ（DTP）均呈正相关.研究显示,达里湖DOM具有陆源与生物源双重特性,DOM的形成与微生物、细菌、浮游生物的生命活动密切相关.      

洱海北部入湖河流水质特征及其对北部湖区的影响

基于2016—2018年罗时江、弥苴河、永安江及洱海北部湖区监测数据分析,探讨洱海北部入湖河流污染变化特征及对北部湖区的影响。结果表明:1）"北三江"监测断面总磷、COD、氨氮浓度整体稳定在GB 3838—2002《地表水环境质量标准》Ⅱ—Ⅲ类标准限值内,年内污染物浓度变化表现出典型的农业面源污染特征,且受流域内产业模式等的综合影响;2）研究期间,河流首要污染物为TN,旱季次要污染物为COD,雨季为TP。雨季入湖负荷高于旱季,弥苴河污染负荷大于罗时江、永安江。"北三江"入湖TN和TP污染负荷分别占洱海允许负荷的50.1%和59.7%;3）入湖河流的磷元素输入是洱海北部湖区磷污染的重要来源。北部湖区污染物浓度对氮、磷入湖污染负荷相关性次月强于当月,响应存在延迟。筛选环境友好型种植模式,控制"北三江"氮磷入湖负荷,有利于保护洱海水环境。     

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%.     

大气沉降向华中丘陵区稻田输入硫通量的观测

选取我国华中丘陵区的湖南省长沙县一个典型水稻种植区,对2015与2016年2年雨水样中的SO₄²-S和大气SO₂的沉降量进行监测,分析雨水中SO₄^2-、NO₃^-的关系,解析大气硫沉降的主要来源.结果表明,研究区大气中SO₂-S和雨水中SO₄^2--S的年均浓度分别为8.5 μg/m³和1.1mg/L,大气硫沉降年均总量为26.8kgS/（hm²·a）,其中年均降雨混合沉降量18.2kgS/（hm²·a）,年均干沉降量为8.6kgS/（hm²·a）.研究区域硫素干、混合沉降量存在明显的季节差异,硫素混合沉降春季高于夏、秋、冬季,而硫素干沉降冬季高于春、夏、秋季.雨水中NO₃^-/SO₄^2-的质量比大多小于1,表明研究区大气硫素主要来自固定污染源（燃煤）.华中丘陵区稻田具有较高的硫沉降,但硫沉降量已较21世纪初出现了较大幅度下降,农业生产中需要根据农田硫素收支状况酌情补充硫肥来保证作物高产稳产.     

3种重金属对蛋白核小球藻的联合毒性及机理

重金属污染日益严重,对人类具有潜在威胁。该文以绿藻蛋白核小球藻(Chlorella pyrenoidosa)为受试生物,3种典型重金属污染物镉(Cd)、铜(Cu)和铬(Cr)为研究对象,采用均匀设计射线法设计重金属三元混合物体系(Cd-Cu-Cr),应用时间毒性微板分析法系统考察3种重金属对蛋白核小球藻的单一毒性及联合毒性,并通过分析绿藻中叶绿素和蛋白质含量探讨3种重金属及其混合物的可能的毒性作用机理。结果表明:3种重金属对蛋白核小球藻的毒性均随着暴露时间的延长逐渐增强,呈现明显的时间依赖性;重金属处理后的蛋白核小球藻中叶绿素含量随暴露时间的延长不断减少,如在24～72 h时,Cd处理的蛋白核小球藻中的叶绿素减少率增长较快,后趋于稳定,而Cr和Cu处理后的绿藻在整个暴露时间内叶绿素减少率均增加;Cd和Cr处理后绿藻的蛋白质含量减少率随着暴露时间的延长快速增加,而Cu处理后的绿藻中蛋白质减少率在24～72 h趋于平缓,之后减少率迅速增加;5条混合物射线的毒性均为加和作用,即组分间没有发生明显的毒性相互作用;三元混合物在低浓度时对蛋白核小球藻具有促进生长作用,在高浓度时抑制其生长,即Hormesis现象;三元混合体系处理后的绿藻中叶绿素及蛋白质的含量与单一Cu处理后的变化规律相似,这表明混合物的毒性机制受单一组分的影响。     

氮掺杂二氧化钛负载钒磷氧催化氧化NO的实验研究

以VPO为活性组分,N掺杂TiO 2为载体,采用浸渍法制备了VPO/TiN催化剂,基于单因素实验研究了其对NO的选择性催化氧化(SCO)性能以及抗硫抗水性能。研究表明:当P/V为1/5、N/Ti为1、活性组分负载量为10%、焙烧温度为350℃时,催化剂的SCO活性最好,NO氧化率达到61%;光致发光光谱(PL)表征显示N掺杂TiO 2在催化剂表面形成的氧空位可增强催化剂对O 2的吸附;VPO/TiN催化剂抗硫抗水性能较强,反应后的催化剂表面未发现硫酸根的特征峰,水蒸气主要通过与NO竞争吸附占据活性位点来抑制催化剂的SCO活性。     

Evaluating national hydrogen refueling infrastructure requirement and economic competitiveness of fuel cell electric long-haul trucks

This study explored the national hydrogen refueling infrastructure requirement along major United States (US) interstate highway corridors to support the deployment of fuel cell electric trucks (FCETs) for the national long-haul trucking fleet. Given the long-haul trucking shipment demand in 2025 projected by the Freight Analysis Framework, locations and capacities of hydrogen stations were identified for inter-zone freight flows, and the total daily refueling demand was estimated for intra-zone flows for each FAF zone. Based on the infrastructure deployment results, we conducted an economic feasibility analysis of FCETs by evaluating the total ownership cost. We found that when the FCET penetration is relatively high (e.g., 10% penetration), FCETs become more competitive in terms of fuel cost and idling cost and could be economic viable if the incremental vehicle cost is reduced to meet the near-term FCET technology cost targets and the liquefaction cost is reduced to an optimal case. We also observed that the station cost depends on regional factors, particularly regional demand, which is used to determine station capacity. Thus, one possible strategy for station roll-out is to have early investment in target regions where station costs are expected to be relatively low such as the Pacific and West South Central regions.