电场与MnxCey催化剂在苯氧化反应中的协同效应及机理探究

挥发性有机物（VOCs）大量排放已成为日益严重的环境问题,为了实现VOCs的高效去除,本文采用自蔓延燃烧合成法制备了一系列锰铈复合氧化物催化剂,将稳恒直流电场引入典型VOCs气体苯的催化氧化过程,并基于不同电场条件下催化剂的理化性质表征结果进行机理分析.实验结果表明,Mn_xCe_y催化剂对含苯废气的去除有良好的效果,稳恒直流电场显著促进了催化剂的活性,其中Mn₁Ce₃的催化性能最佳,电流为5 mA时,Mn₁Ce₃催化剂在155℃可达到50%的苯转化率,在202.4℃可达到90%的苯转化率,对应的转化温度T₅₀和T₉₀比传统方法分别降低了62.4℃和48.3℃,且电场中的反应活化能由52.32 kJ·mol^-1降低至32.31 kJ·mol^-1.根据实验现象及表征结果,发现协同效应与活性位点的快速持续再生及活性氧物种的转化有关,由此提出苯在Mn_xCe_y催化剂上的氧化机理及电场协同催化的反应模型.     

骆马湖表层水体中32种PPCPs类物质的污染水平、分布特征及风险评估

为评价骆马湖水体中药品和个人护理品(PPCPs)的污染水平、空间分布特征及生态风险,利用高效液相色谱-串联质谱测定了骆马湖水体中22个采样点的32种PPCPs.结果表明,骆马湖表层水体中共检出了23种PPCPs,总浓度范围为892~1 536 ng·L~(-1),其中浓度最高的为诺氟沙星(256~707 ng·L~(-1)),其次是酮洛芬(85~438 ng·L~(-1))、安赛蜜(101~290 ng·L~(-1))及萘普生(1.9~112 ng·L~(-1)).不同采样位点的PPCPs浓度存在一定的空间差异,呈现湖东北部地区较高,西南部地区较低的趋势.房亭河入湖口处PPCPs浓度较高,嶂山闸出湖口处浓度较低.对13种药物类PPCPs生态风险评价结果表明,诺氟沙星RQs为0.26~0.72,对于骆马湖水生生态系统表现为中风险,吉非罗齐在大部分采样点RQs0.01,表现为低风险,其余的化合物RQs0.01未表现出生态环境风险.采用简单叠加模型计算PPCPs的联合毒性风险熵范围为0.29~0.75,整体上看,骆马湖PPCPs对于水生生物表现出中风险.对6种PPCPs的人体健康风险结果表明,RQs均小于1,表明骆马湖PPCPs对人体健康无直接风险.     

污泥水磷和有机物同步混凝去除的多目标优化技术研究

通过引入多响应值的归一化评分法进行了污泥水磷和有机物同步混凝去除的多目标优化,并利用响应面(RSM)技术考察了Al/P比、聚丙烯酰胺(PAM)投加量和悬浮固体(SS)浓度对污染物去除的单独效应和联合效应.结果表明,复合投加聚合氯化铝和PAM能同步去除污泥水中磷和有机物,并改善沉降效果.归一化后单目标RSM优化显示,对污泥水中磷和有机物同步去除的贡献为Al/P比SS浓度PAM投加量.在最优条件Al/P比为3、PAM浓度为1.22 mg·L~(-1)、SS浓度为3.58 g·~(L-1)的条件下,正磷和总有机碳去除率分别为93.1%和53.9%.与多响应变量优化相比,引入归一化评分法有效解决了变量间数值量级差异的问题,使结果的分析计算变得简单方便.     

极端干旱水文年(2011年)夏季珠江口溶解氧的分布特征及影响因素研究

气候变化背景下,极端气候事件对河口生态环境的影响已引起许多研究者的关注.基于2011年夏季的调查资料,分析了珠江口在极端干旱情况下溶解氧的分布特征及其与海水稳定性、营养盐和浮游植物分解之间的关系,并对河口底层低氧区的成因进行初步探讨.调查结果发现,在珠江特低径流量的情况下,珠江口邻近海域底层明显出现低氧状态,DO的最低值仅为1.38 mg.L-1.相关性分析显示,表层水和底层水之间的ΔDO与ΔT、ΔS、ΔDIN、ΔSS和ΔPOC都达到显著相关的水平,其中ΔDO与ΔT和ΔPOC呈极显著的正相关,而与ΔS呈极显著的负相关关系.研究表明,与1999年和2009年夏季不同,2011年夏季珠江口底层低氧环境的形成主要与极端干旱气候下低径流导致河口水体滞留时间延长及颗粒态有机物质在沉降过程中的分解耗氧有关.另外,从最低DO值的角度分析,珠江口季节性缺氧程度在过去20 a间并未呈现显著的变化趋势.     

陶粒移动床处理低浓度生活污水的性能

采用填充率为30%的生物陶粒移动床(BCMBBR)处理东莞城镇低浓度、低碳高氨氮生活污水(COD约130～185 mg·L-1、C/N=3～7).同时,考察了BCMBBR在5种工况下的运行效果及相应的微生物相状况.结果表明,BCMBBR运行的最佳条件为:HRT为8 h,气水体积比为4:1.COD,BOD5、NH4+-N...     

Synthesis and kinetics investigation of meso-microporous Cu-SAPO-34 catalysts for the selective catalytic reduction of NO with ammonia

A series of meso-microporous Cu-SAPO-34 catalysts were successfully synthesized by a one-pot hydrothermal crystallization method, and these catalysts exhibited excellent NH_3-SCR performance at low temperature. Their structure and physic chemical properties were characterized by means of X-ray diffraction patterns(XRD), Scanning electron microscopy(SEM), Transmission electron microscopy(TEM), N_2 sorption-desorption, nuclear magnetic resonance(NMR), Inductively Coupled Plasma-Atomic Emission spectrometer(ICP-AES), X-ray absorption spectroscopy(XPS),Temperature-programmed desorption of ammonia(NH_3-TPD), Ultraviolet visible diffuse reflectance spectroscopy(UV-Vis DRS) and Temperature programmed reduction(TPR).The analysis results indicate that the high activities of Cu-SAPO-34 catalysts could be attributed to the enhancement of redox property, the formation of mesopores and the more acid sites. Furthermore, the kinetic results verify that the formation of mesopores remarkably reduces diffusion resistance and then improves the accessibility of reactants to catalytically active sites. The 1.0-Cu-SAPO-34 catalyst exhibited the high NO conversion( 90%) among the wide activity temperature window in the range of 150–425℃.     

油污染土壤重金属赋存形态和生物有效性研究

采用逐级提取法对江苏某油区5个已污染的碱性土壤中的Pb、Cd、As、Cr的金属赋存形态和在其上生长的植物的生物可给性进行了调查结果表明,除总Cd外,其他3种金属对土壤都有不同程度的污染污染类型不同,使莎草的生物有效性有较大差异,与对照点相比,除总Cr外,其它3种金属的生物富集系数明显降低金属赋存形态也有不同,其中Pb和Cr以铁锰结合态和残渣态为主,As以铁锰结合态、残渣态和有机质结合态为主,Cd以碳酸盐结合态和残渣态为主.     

农业废物好氧堆肥中氨氧化细菌的群落结构

应用聚合酶链式反应-变性梯度凝胶电泳（PCR-DGGE）技术对农业废物好氧堆肥过程中氨氧化细菌（ammonia-oxidizingbacteria,AOB）种群结构随时间的变化情况进行了研究,结果表明,AOB群落的Shannon-Weaver指数初始值为2.58,堆肥结束时为2.02,多样性整体呈下降趋势.通过对部分优...     

Removal kinetics of phosphorus from synthetic wastewater using basic oxygen furnace slag

Removal kinetics of phosphorus through use of basic oxygen furnace slag (BOF-slag) was investigated through batch experiments. Effects of several parameters such as initial phosphorus concentration, temperature, BOF-slag size, initial pH, and BOF-slag dosage on phosphorus removal kinetics were measured in detail. It was demonstrated that the removal process of phosphorus through BOF-slag followed pseudo-first-order reaction kinetics. The apparent rate constant (k_obs) significantly decreased with increasing initial phosphorus concentration, BOF-slag size, and initial pH, whereas it exhibited an opposite trend with increasing reaction temperature and BOF-slag dosage. A linear dependence of k_obs on total removed phosphorus (TRP) was established with k_obs = (3.51 ± 0.11) × 10^− 4 × TRP. Finally, it was suggested that the Langmuir–Rideal (L–R) or Langmuir–Hinshelwood (L–H) mechanism may be used to describe the removal process of phosphorus using BOF-slag.     

Removal kinetics of phosphorus from synthetic wastewater using basic oxygen furnace slag

Removal kinetics of phosphorus through use of basic oxygen furnace slag(BOF-slag)was investigated through batch experiments. Effects of several parameters such as initial phosphorus concentration, temperature, BOF-slag size, initial p H, and BOF-slag dosage on phosphorus removal kinetics were measured in detail. It was demonstrated that the removal process of phosphorus through BOF-slag followed pseudo-first-order reaction kinetics. The apparent rate constant(kobs) significantly decreased with increasing initial phosphorus concentration, BOF-slag size, and initial p H, whereas it exhibited an opposite trend with increasing reaction temperature and BOF-slag dosage.A linear dependence of kobson total removed phosphorus(TRP) was established with kobs=(3.51 ± 0.11) × 10- 4× TRP. Finally, it was suggested that the Langmuir–Rideal(L–R)or Langmuir–Hinshelwood(L–H) mechanism may be used to describe the removal process of phosphorus using BOF-slag.