氧化亚铜和氢氧化铜对苦草抗氧化酶活性和叶绿素含量的影响

研究了不同浓度氧化亚铜和氢氧化铜可湿性粉剂染毒对苦草叶片抗氧化酶〔超氧化物歧化酶(SOD)、抗坏血酸过氧化物酶(APX)和过氧化物酶(POD)〕比活力、丙二醛(MDA)含量和叶绿素含量的影响。结果表明,以0.15～1.5 mg.L-1氧化亚铜可湿性粉剂对苦草染毒7 d,其叶片SOD、APX和POD活性明显升高,1.5 mg.L-1处理组3种抗氧化酶比活力分别比助剂对照组升高49.0%、77.0%和39.0%,MDA含量极显著上升46.9%,总叶绿素含量显著下降42.6%。染毒14 d后3种抗氧化酶比活力均有不同程度回落,MDA含量恢复至正常水平,总叶绿素含量也有所回升。以0.1～1.0 mg.L-1氢氧化铜对苦草染毒7 d,1.0 mg.L-1处理组3种抗氧化酶比活力和MDA含量也呈显著上升趋势,总叶绿素含量显著下降。染毒14 d时3种抗氧化酶比活力和MDA含量恢复到正常水平,总叶绿素含量回升。上述结果显示,在氧化亚铜和氢氧化铜引起的铜胁迫早期,苦草叶片抗氧化酶因过氧化应激响应而上升,膜脂出现一定程度过氧化损伤,叶绿素含量下降,但随着暴露时间的延长,苦草对铜胁迫产生适应性,过氧化损伤得以缓解,叶绿素含量回升。     

锰氧化物负载施氏矿物去除酸性矿山废水中As(III)的性能及机理

施氏矿物是天然的砷吸附剂,但其存在酸性条件下对As(III)吸附性能较弱且无法对As(III)氧化降毒的缺陷. 采用液相沉淀法成功制备出锰氧化物负载施氏矿物(MnO_x@Sch),研究锰负载量、初始pH值和共存离子对MnO_x@Sch去除As(III)的影响,并采用吸附动力学结合XPS、FTIR及TEM等表征探究该过程的机理. 结果表明:在初始pH=3、投加量为0.5 g·L^-1、As(III)初始浓度为1 mg·L^-1的条件下,As(III)与MnO_x@Sch反应后的剩余浓度仅为2.42~3.38 μg·L^-1.MnO_x@Sch去除As(III)受初始pH影响较小,H₂PO₄^-共存时As(III)去除存在明显的抑制作用. MnO_x@Sch 去除As(III)的过程符合准二级动力学方程和颗粒内扩散方程. 液相化学组分和固相产物表征分析显示MnO_x@Sch对As(III)的去除机理可概括为As(III)氧化、静电吸附和络合配位及配体交换. 研究结果可为施氏矿物及其改性材料应用于酸性矿山废水砷污染治理提供理论依据.     

不同硅铝比Fe-ZSM-5催化剂对氧化亚氮催化分解性能的研究

以不同硅铝比的H-ZSM-5分子筛为载体,采用离子交换法和化学气相沉积法制备Fe-ZSM-5催化剂,并用XRD、BET、TEM、UV-vis和NH3-TPD等表征手段对催化剂进行分析,研究催化剂中铁的存在状态.结果表明,分子筛的硅铝比影响铁在分子筛中的分布形态,化学气相沉积法和热离子交换法制得硅铝比为25的Fe-ZSM-5-25分子筛催化剂上均匀地分布着粒径为8 nm左右的纳米氧化铁颗粒,并且Fe-ZSM-5-25分子筛催化剂比Fe-ZSM-5-300更容易形成Fe3+x O y团簇.制得的Fe-ZSM-5分子筛催化剂催化分解氧化亚氮(N2O),结果表明,相同的制备方法,硅铝比小的Fe-ZSM-5-25催化剂对N2O分解活性更好;相同硅铝比的Fe-ZSM-5催化剂,采用化学气相沉积法制得的对N2O分解活性最好.另外,O2的存在对Fe-ZSM-5上N2O催化分解活性有抑制作用,而NO对N2O催化分解活性展示了一定的正效应.最后,经过100 h的连续反应,Fe-ZSM-5催化剂依然能够保持催化活性.     

生物碳的物理结构与化学成分对土壤氧化亚氮排放的影响

为探究生物碳对土壤中重要温室气体氧化亚氮(N2O)排放的影响机制,将生物碳的可溶性化学成分和稳定的物理结构分离后得到浸提液和碳骨架,设置了4种不同的实验处理方式:土壤(对照)、土壤+生物碳、土壤+浸提液、土壤+碳骨架,进行了为期90 d的室内培养试验.实验结果显示,在培养前期(前7 d),添加生物碳和碳骨架的处理都显著抑制了土壤N2O的释放,且抑制程度相似,最高均可达80%,而添加浸提液的处理却显著促进了土壤N2O的释放.因此,土壤添加生物碳后对N2O排放的抑制作用主要归因于生物碳的物理结构,生物碳的物理结构可以有效地提高土壤的pH值、吸附土壤及其自身含有的可能促进N2O释放的化学物质,从而减少土壤中N2O的产生和排放.     

N2O emission from nitrogen removal via nitrite in oxic-anoxic granular sludge sequencing batch reactor

Bionitrification is considered to be a potential source of nitrous oxide （N2O） emissions, which are produced as a by-product during the nitrogen removal process. To investigate the production of N2O during the process of nitrogen removal via nitrite, a granular sludge was studied using a labscale sequence batch reactor operated with real-time control. The total production of N2O generated during the nitrification and denitrification processes were 1.724 mg/L and 0.125 mg/L, respectively, demonstrating that N2O is produced during both processes, with the nitrification phase generating larger amount. In addition, due to the NEO-N mass/oxidized ammonia mass ratio, it can be concluded that nitrite accumulation has a positive influence on N2O emissions. Results obtained from PCRDGGE analysis demonstrate that a specific Nitrosomonas microorganism is related to N2O emission.     

Characteristics of greenhouse gas emission in three full-scale wastewater treatment processes

Three full-scale wastewater treatment processes, Orbal oxidation ditch, anoxic/anaerobic/aerobic （reversed A^2O） and anaerobic/anoxic/aerobic （A^2O）, were selected to investigate the emission characteristics of greenhouse gases （GHG）, including carbon dioxide （CO2）, methane （CH4） and nitrous oxide （N2O）. Results showed that although the processes were different, the units presenting high GHG emission fluxes were remarkably similar, namely the highest CO2 and N2O emission fluxes occurred in the aerobic areas, and the highest CH4 emission fluxes occurred in the grit tanks. The GHG emission amount of each unit can be calculated from its area and GHG emission flux. The calculation results revealed that the maximum emission amounts of CO2, CH4 and N2O in the three wastewater treatment processes appeared in the aerobic areas in all cases. Theoretically, CH4 should be produced in anaerobic conditions, rather than aerobic conditions. However, results in this study showed that the CH4 emission fluxes in the forepart of the aerobic area were distinctly higher than in the anaerobic area. The situation for N2O was similar to that of CH4： the N2O emission flux in the aerobic area was also higher than that in the anoxic area. Through analysis of the GHG mass balance, it was found that the flow of dissolved GHG in the wastewater treatment processes and aerators may be the main reason for this phenomenon. Based on the monitoring and calculation results, GHG emission factors for the three wastewater treatment processes were determined. The A^2O process had the highest CO2 emission factor of 319.3 g CO2/kg CODremoved, and the highest CH4 and N2O emission factors of 3.3 g CH4/kg CODremoved and 3.6 g N2O/kg TNremoved were observed in the Orbal oxidation ditch process.     

基于EPR技术的5种纳米金属氧化物光生活性物种的形成研究

纳米金属氧化物的光化学性质使其成为新的催化剂和杀菌剂,而活性氧化物种(Reactive Oxygen Species,ROS)作为其具有催化杀菌性能的主要原因受到广泛关注.本研究通过电子顺磁共振(EPR)自旋捕捉和自旋标记技术,研究了5种纳米金属氧化物(n Al_2O_3、n CuO、n Ti O_2、n Fe_2O_3和n ZnO)在不同光照条件下形成光生电子、羟基自由基(·OH)、超氧阴离子(O_2~-·)和单线态氧(~1O_2)的能力.结果表明,在光照过程中,n Al_2O_3、n CuO、n Ti O_2和n ZnO能够生成·OH和~1O_2,n Fe_2O_3只生成了~1O_2.其中,n Ti O_2生成的光生电子和·OH最多,n CuO仅次于n Ti O_2,n Al_2O_3和n ZnO能够生成·OH,但生成量很少.本实验结果可为预测和评价纳米金属氧化物的光催化性能及环境风险提供一定的理论支持.     

新型Ag(I)选择性吸附材料的制备及吸附性能研究

将壳聚糖（CTS）、氧化石墨烯（GO）、3-巯基丙基三甲氧基硅烷（MPTMS）交联制得巯基改性壳聚糖-氧化石墨复合材料（SFCG）.采用傅里叶变换红外光谱仪、扫描电子显微镜、元素分析仪对改性前后和吸附前后的材料进行表征.研究吸附剂投加量、温度、时间、初始浓度对吸附效果的影响.实验结果表明,SFCG与CTS相比结构发生很大变化,呈现薄层状结构,表面有褶皱.SFCG能够在短时间内选择性高效吸附Ag（I）,最大吸附量为578.41 mg·g^-1.通过吸附等温线、吸附动力学、吸附热力学的研究发现,其吸附等温线符合Langumir吸附模型,为单层吸附;吸附过程符合准二级动力学模型,以化学吸附为主,同时吸附过程是自发的、放热的.另外,银是一种贵金属,因此,SFCG将在废水处理和回收贵金属等方面均表现出良好的应用前景.