接种不同污泥启动厌氧氨氧化ASBR反应器研究

采用ASBR反应器,分别以好氧硝化污泥和厌氧颗粒污泥为种泥,通过对氨氮、亚硝酸盐氮等指标的监测和数据分析、污泥颜色的观察,研究2个厌氧氨氧化反应器启动的可行性及其差异.结果表明,2个厌氧氨氧化反应器均可成功启动;采用好氧硝化污泥启动厌氧氨氧化反应器耗时142 d,启动前后污泥颜色变化不大,亚硝酸盐氮浓度超过20 mmol/L会对厌氧氨氧化产生明显的抑制作用;采用厌氧颗粒污泥启动厌氧氨氧化反应器耗时249 d,启动前后污泥颜色变化很大,从黑色逐渐变为砖红色,亚硝酸盐氮浓度超过13.4 mmol/L会对厌氧氨氧化产生抑制作用;分别用以上2种污泥启动的厌氧氨氧化ASBR反应器中占优势地位的厌氧氨氧化菌不同.     

Experimental investigation of the e ect of flow turbulence and sediment transport patterns on the adsorption of cadmium ions onto sediment particles

The mechanism of flow turbulence,sediment supply conditions,and sediment transport patterns that affect the adsorption of cadmiumions onto sediment particles in natural waters are experimentally simulated and studied both in batch reactors and in a turbulencesimulation tank.By changing the agitation conditions,the sediment transport in batch reactors can be categorized into bottom sediment-dominated sediment and suspended sediment-dominated sediment.It is found that the adsorption rate of bottom sediment is much lessthan that of suspended sediment,but the sediment transport pattern does not affect the final(equilibrium)concentration of dissolvedcadmium.This result indicates that the parameters of an adsorption isotherm are the same regardless of the sediment transport pattern.Inthe turbulence simulation tank,the turbulence is generated by harmonic grid-stirred motions,and the turbulence intensity is quantifiedin terms of eddy diffusivity,which is equal to 9.84F(F is the harmonic vibration frequency)and is comparable to natural surfacewater conditions.When the turbulence intensity of flow is low and sediment particles stay as bottom sediment,the adsorption rateis significantly low,and the adsorption quantity compared with that of suspended sediment is negligible in the 6 h duration of theexperiment.This result greatly favors the simplification of the numerical modeling of heavy metal pollutant transformation in naturalrivers.When the turbulence intensity is high but bottom sediment persists,the rate and extent of descent of the dissolved cadmiumconcentration in the tank noticeably increase,and the time that is required to reach adsorption equilibrium also increases considerablydue to the continuous exchange that occurs between the suspended sediment and the bottom sediment.A comparison of the results ofthe experiments in the batch reactor and those in the turbulence simulation tank reveals that the adsorption ability of the sediment,andin particular the adsorption rate,is greatly over-estimated in the batch reactor.     

纳米材料对斑马鱼的氧化损伤及应激效应研究

以斑马鱼(Daniorerio)为受试动物,研究了纳米及常规TiO2、ZnO悬浮液对其鳃、消化道及肝脏的氧化损伤及应激效应,同时对纳米及常规TiO2、ZnO悬浮液中的颗粒形貌特征及·OH生成量进行了测定.结果发现,虽然纳米TiO2、ZnO颗粒与其常规颗粒在溶液中的粒径分布接近,但50mg/L纳米TiO2、ZnO悬浮液中·OH产生量(96h光照下,分别为2.17mmol/L、0.72mmol/L)远远高于50mg/L常规颗粒(未检测到).50mg/L纳米TiO2处理下,斑马鱼肝脏中超氧化物歧化酶(SOD)、过氧化氢酶(CAT)、还原型谷胱甘肽(GSH)、蛋白质羰基含量分别为对照的70.2%、65.4%、53%、178.1%;消化道中SOD活性及GSH、丙二醛(MDA)含量分别为对照的149.6%、212.9%、217.2%;鳃中MDA含量为对照的160.9%.而50mg/L常规TiO2悬浮液对斑马鱼没有产生毒理效应.5mg/L纳米及常规ZnO对斑马鱼肝脏的氧化伤害最强,其中5mg/L纳米ZnO处理组中SOD、CAT活性及GSH、MDA含量分别为对照的62.9%、53.1%、45.2%、204.2%,5mg/L常规ZnO处理组中SOD、CAT活性及GSH、MDA含量分别为对照组48.3%、51.8%、34.6%、289.6%;虽然斑马鱼鳃及消化道也受到明显氧化应激效应(p0.05),但并没有受到氧化损伤.研究表明,团聚作用对不同化学组成纳米颗粒的毒性影响程度不同;且不同化学组成纳米颗粒在生物体内可能通过不同机制产生了不同种类的ROS,从而对不同细胞组分产生的氧化损伤及应激效应是其重要的毒理机制.     

连续流膜生物反应器中好氧颗粒污泥的形成及机制探讨

为了探讨好氧颗粒污泥在连续流膜生物反应器(MBR)中的形成过程和机制,采用连续流试验的方法,研究了好氧颗粒污泥形成过程中膜反应器内污染物的去除效果和好氧颗粒污泥特性的变化,并对连续流MBR中好氧颗粒污泥的形成机制进行了探讨.结果显示,连续流MBR中好氧颗粒污泥的形成增强了MBR的运行稳定性和抗冲击能力.废水中微生物抑制...     

搅拌-序批式活性污泥反应器(WSBR)中好氧颗粒污泥的特性研究

为研究搅拌-序批式活性污泥反应器(WSBR)中好氧颗粒污泥的特性,利用WSBR反应器与传统SBR反应器对好氧活性污泥颗粒化的过程进行了比较.结果表明,在添加同量的聚炳烯酰胺(PAM)条件下,具有合理二次流场的WSBR反应器在4d就可见好氧颗粒污泥,而SBR反应器则在第10d才出现好氧颗粒污泥,且WSBR反应器中好氧颗粒...     

碳源变化对降解2,4-D的好氧颗粒污泥性能及形态的影响

在长期运行的序批式生物反应器(SBR)中,考察了以葡萄糖和2,4-二氯苯氧乙酸(2,4-D)为混合碳源培养的好氧颗粒污泥在转换为2,4-D唯一碳源废水后,其形态、结构及对目标污染物去除功能的变化.结果表明,基质转换为2,4-D单一碳源后,好氧颗粒污泥仍保持了对目标污染物高效的去除能力.当进水2,4-D浓度为361～564mg/L,其去除率为99.2%～100%,COD平均去除率达到85.6%.混合碳源向2,4-D单一碳源转换对原好氧颗粒结构产生一定破坏作用,使其发生部分解体,粒径由513μm下降到302μm.但好氧颗粒污泥良好的耐负荷冲击使其保持了颗粒主体,通过一段时间适应调整后能够重新聚集生长,最终获得能够利用2,4-D为唯一碳源生长并具有良好沉降性(SVI20～40mL/g)的好氧颗粒污泥,粒径为489μm.扫描电子显微镜(SEM)观察结果表明,混合碳源转向单一碳源使好氧颗粒生物相丰富度降低.     

Effect of platinum on the photocatalytic degradation of chlorinated organic compound

TiO2 nanoparticles, doped with di erent Pt contents, were prepared by a modified photodeposition method using Degussa P-25 TiO2, H2PtCl6 6H2O and methanol as the solvents. The physicochemical properties of Pt/TiO2 were investigated by the nitrogen adsorption and desorption isotherm measurement technique, X-ray di raction analysis and photoluminescence spectra, respectively. Reaction rates from photocatalytic removal of dichloromethane over Degussa P-25 TiO2 and Pt/TiO2 were evaluated. The average diameter and BET surface area of the TiO2 catalyst particles were 300 nm and 50 m2/g, respectively. The degradation e ciency was 99.0%, 82.7%, 55.2%, and 57.9% with TiO2 at inlet concentrations of 50, 100, 200, and 300 ppm, respectively. And the degradation e ciency was 99.3%, 79.7%, 76.5%, and 73.4% with a 0.005 wt.% Pt/TiO2 at inlet concentrations of 50, 100, 200, and 300 ppm, respectively. In addition, we found that the photoluminescence emission peak intensities decreased with increases in the doping amount of Pt, which indicates that the irradiative recombination was weakened. Furthermore, the results showed that the UV/0.005 wt.% Pt/TiO2 process was capable of e ciently decomposing gaseous DCM in air.     

内循环(IC)反应器运行规律研究

研究采用自制内循环(IC)反应器,以实验室模拟废水为进水,接种城市污水处理厂的剩余污泥,对反应器的启动及运行过程进行研究,在经过污泥驯化、颗粒培养、调整及稳定的不同阶段连续运行.结果表明:启动初期反应器pH过低,产甲烷菌生长受抑制,导致VFA累积,容易酸化.通过改变模拟废水中微量元素的浓度及添加缓冲溶液,酸化的反应器可...     

La-Co-Fe-Cu/HZSM-5在尾气碳颗粒燃烧中的催化性能

采用柠檬酸络合低温浸渍法制备分子筛负载钙钛矿型复合氧化物催化剂。采用XRD、SEM和H2-TPR等手段对催化剂性能进行表征,并在微型固定床反应器中对催化剂进行活性评价。结果表明,在钙钛矿型复合氧化物中进行B位离子掺杂,可以改善催化活性,碳颗粒燃烧温度降低。在20%LaCoO3/HZSM-5催化剂中用铁离子部分取代钴离子可以改善碳颗粒的燃烧性能,取代量增加碳颗粒燃烧温度降低,但是生成CO2的选择性也降低,以20%LaCo0.2Fe0.8O3/HZSM-5为催化剂,Tig、Tm和Tf分别为256℃、399℃和403℃,但生成CO2的选择性只有72.5%。在20%LaCo1-xFexO3/HZSM-5中的钙钛矿型复合氧化物B位离子中加入铜离子后,在碳颗粒燃烧反应中生成CO2的选择性得到明显改善,Sco2提高10个单位以上。以20%LaCo0.2Fe0.6Cu0.2O3/HZSM-5为催化剂,在碳颗粒燃烧反应中生成CO2的选择性可以达到94.7%,Tig、Tm和Tf分别为242℃、427℃和445℃。     

好氧颗粒污泥处理青霉素废水研究

青霉素在其生产过中产生大量的废水,其COD值较高,生化性较差,成分复杂,微生物难以降解,其处理技术是世界性难题。文章采用以葡萄糖模拟废水培养的好氧颗粒污泥为接种体,经青霉素废水逐步驯化后,使其完全处理青霉素废水。实验结果表明,应用好氧颗粒污泥技术,处理青霉素废水,COD,NH3_N,TP去除率较高,具有很好的处理效果。