2,4-二氯酚废水处理的试验研究

研究了活性炭吸附法处理2，4-二氯酚废水的工艺过程。研究结果表明。活性炭对该废水具有良好的吸附效果。此外，还对吸附过程的动力学进行了研究，结果表明吸附过程遵循Lagergren一级动力学模型，并得出25℃和35℃时速率常数分别为k298=0．0072min^-1、k308=0．0118min，吸附活化能Ea=38．5kj／mol。     

两种假单孢菌中二氯酚降解酶活性及其定域研究

对两种有降解二氯酚能力的假单孢菌Ｐｓｅｕｄｏｍｏｎａｓ ｓｐ．ＤＣＰ－１和Ｐｓｅｕｄｏｍｏｎａｓ ｓｐ．ＤＣＰ－２中二氯酚降解酶活性及定域进行了测定，结果表明该酶的活力与菌种、培养等因素有关，与诱导物的关系不显；酶主要定域在膜周及膜内；酶的活力在两种菌中的水平相当；酶的比活力在ＤＣＰ－１的膜周处表现出相当高的水平。     

Kinetic of carbonaceous substrate in an upflow anaerobic sludge sludge blanket (UASB) reactor treating 2,4 dichlorophenol (2,4 DCP)

The performance of an upflow anaerobic sludge blanket (UASB) reactor treating 2,4 dichlorophenol (2,4 DCP) was evaluated at different hydraulic retention times (HRTs) using synthetic wastewater in order to obtain the growth substrate (glucose-COD) and 2,4 DCP removal kinetics. Treatment efficiencies of the UASB reactor were investigated at different hydraulic retention times (2-20 h) corresponding to a food to mass (F/M) ratio of 1.2-1.92 g-COD g(-1) VSS day(-1). A total of 65-83% COD removal efficiencies were obtained at HRTs of 2-20 h. In all, 83% and 99% 2,4 DCP removals were achieved at the same HRTs in the UASB reactor. Conventional Monod, Grau Second-order and Modified Stover-Kincannon models were applied to determine the substrate removal kinetics of the UASB reactor. The experimental data obtained from the kinetic models showed that the Monod kinetic model is more appropriate for correlating the substrate removals compared to the other models for the UASB reactor. The maximum specific substrate utilization rate (k) (mg-COD mg(-1) SS day(-1)), half-velocity concentration (K(s)) (mg COD l(-1)), growth yield coefficient (Y) (mg mg(-1)) and bacterial decay coefficient (b) (day(-1)) were 0.954 mg-COD mg(-1) SS day(-1), 560.29 mg-COD l(-1), 0.78 mg-SS g(-1)-COD, 0.093 day(-1) in the Conventional Monod kinetic model. The second-order kinetic coefficient (k(2)) was calculated as 0.26 day(-1) in the Grau reaction kinetic model. The maximum COD removal rate constant (U(max)) and saturation value (K(B)) were calculated as 7.502 mg CODl(-1)day(-1) and 34.56 mg l(-1)day(-1) in the Modified Stover-Kincannon Model. The (k)(mg-2,4 DCP mg(-1) SS day(-1)), (K(s)) (mg 2,4 DCPl(-1)), (Y) (mg SS mg(-1) 2,4 DCP) and (k(d)) (day(-1)) were 0.0041 mg-2,4 DCP mg(-1) SS day(-1), 2.06 mg-COD l(-1), 0.0017 mg-SS mg(-1) 2,4 DCP and 3.1 x 10(-5) day(-1) in the Conventional Monod kinetic model for 2,4 DCP degradation. The second-order kinetic coefficient (k(2)) was calculated as 0.30 day(-1) in the Grau reaction kinetic model. The maximum 2,4 DCP removal rate constant (U(max)) and saturation value (K(B)) were calculated as 0.01 mg COD l(-1) day(-1) and 9.8 x 10(-3) mg l(-1) day(-1) in the Modified Stover-Kincannon model.     

Modeling of organic pollutant destruction in a stirred-tank reactor by ozonation

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竹炭对2,4-二氯苯酚的吸附特性及影响因素研究

研究了水溶液中竹炭对 2 ,4-二氯苯酚的吸附特性及其影响因素。结果表明 ,竹炭对 2 ,4-二氯苯酚具有较强的吸附性能 ,吸附效果与竹炭粒径、用量、污染物浓度以及吸附平衡时间和平衡方式有关。     

Removal of substituted phenols onto iron‐treated Nostoc sp. biomass

This study explored the possibility of removing 4‐nitrophenol (4‐NP) and 2,4‐dichlorophenol (2,4‐DCP) from water by using a dead blue‐green algae, Nostoc sp., dried and untreated and dried and treated with iron (Fe‐treated with 0.1 M ferric chloride solution for 1 day). The Nostoc sp. untreated and Fe‐treated biomass were used to study the sorption and desorption of 4‐NP and 2,4‐DCP. The effects of solute concentration, ionic strength, and temperature on sorption and desorption in the presence of untreated and treated Nostoc sp. biomass were investigated. The Fe‐treated Nostoc sp. biomass sorbed higher amounts of both 4‐NP and 2,4‐DCP than the untreated biomass. The percent cumulative desorption decreased from 6.41% to 0.28% and 1.84% to 0.19%, respectively, for 4‐NP and 2,4‐DCP for the Fe‐treated biomass. Biosorption of 4‐NP and 2,4‐DCP onto untreated and Fe‐treated Nostoc sp. biomass conformed to Freundlich isotherms. Iron treatment of Nostoc sp. biomass increased the value of ln K from 8.07 to 8.59 for 4‐NP and from 8.04 to 8.51 for 2,4‐DCP but decreased their desorption. An increase in ionic strength (0.003–0.03) increased the biosorption of both substituted phenols and decreased their percent desorption. An increase in temperature in the range of 15–35°C decreased the sorption of 4‐NP and 2,4‐DCP onto both untreated and Fe‐treated Nostoc sp. biomass and increased their desorption, indicating that the biosorption of both substituted phenols onto untreated and Fe‐treated Nostoc sp. biomass was principally a physical process. The results of this study suggest that Fe‐treated dried Nostoc sp. biomass could be explored as an inexpensive and eco‐friendly material for the effective removal of these phenols and, potentially, other chemicals from industrial wastewater and contaminated groundwater.     

纳米TiO2薄膜光催化降解2,4-二氯酚的动力学研究

以主波长为365nm的紫外光灯为光源，纳米TiO2薄膜为光催化剂，研究了2，4-二氯酚光催化降解的产物及Cl^-对2，4-二氯酚光催化反应动力学的影响，并进一步探讨了Cl对2，4-二氯酚光解影响的机理，2，4-二氯酚可以经光催化氧化被彻底矿化，结合外加Cl^-对2，4-二氯酚光催化降解的影响和L-H反应动力学分析，可以认为Cl^-对2，4-二氯酚光催化降解的抑制作用，是由于Cl^-与2，4-二氯酚在TiO2表面竞争同一活性位点所致。因此，当光催化反应进行到Cl^-在TiO2表面竞争性吸附较强时，在反应动力学方程中必须考虑Cl^-的竞争性作用。     

金属离子和氧化剂对3,5-二氯酚光化学降解的影响

在实验条件下 ,Fe2 +、KCl O3、KCl O4 、KBr O3、KIO4 对 3 ,5 -二氯酚光化学降解起加速作用 ,且随其浓度增大 ,加速作用也在增强。KIO4 的加速作用比较强。光照时 ,KIO4 +Mn2 +对 3 ,5 -二氯酚光化学降解的加速作用非常显著。无光照时 ,当 KMn O4 浓度增加时 ,3 ,5 -二氯酚被迅速氧化 ;KIO4 +Mn2 + /Fe2 + 能够使 3 ,5 -二氯酚发生化学降解 ,尤其是 KIO4 +Mn2 + 的作用。     

钛基氧化物阳极氧化降解水中2,4-二氯酚

采用热氧化法制备了具有TiO2、RuO2和IrO2涂层的钛基氧化物电极(Ti/TiO2/RuO2/IrO2),并以其为工作电极考察了:①水中2,4-二氯酚(DCP)的循环伏安特性;②pH值、阳极电位和反应时间对阳极氧化降解DCP的影响;③阳极氧化对DCP水溶液可生化性的影响.结果表明,电极的氧化物负载量显著影响DCP的循环伏安特性.较高的介质pH值利于DCP的电化学氧化降解,而低pH值更易导致DCP挥发.低阳极电位下,DCP主要通过阳极直接氧化降解,因受电流密度过低的限制其降解效果较差;高阳极电位下,DCP主要通过阳极间接氧化降解,当阳极电位为1.8V,反应时间为360min时,DCP去除率可达100%,COD的去除超过50%,但能耗较高.COD的检测与紫外-可视光谱曲线表明,DCP的电化学氧化降解过程产生了有机中间体.Ti/TiO2/RuO2/IrO2阳极氧化可显著提高DCP水溶液的可生化性,表明其在氯酚废水预处理或脱毒领域有一定应用潜力.