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511.
以硫酸钛为原料,用水热法制备了Fe3+掺杂锐钛矿型TiO2(Fe3+ - TiO2)粉末,用扫描电子显微镜测定了试样的形貌.研究了自制的Fe3+ - TiO,光催化剂对孔雀石绿的光催化降解作用.实验结果表明,在孔雀石绿溶液质量浓度为2 mg/L、Fe3+ - TiO2加入量为1.616 g/L、Fe3+-TiO2中Fe... 相似文献
512.
513.
The fate and transport of antibiotics in natural water systems is controlled in part by interactions with nanometer (10−9 m) metal oxide particles. Experiments were performed by mixing solutions of ampicillin (AMP), a common, penicillin-class human and veterinary antibiotic, with 25 nm-TiO2 (anatase) nanoparticles at different pH conditions. Both sorption and degradation of AMP were observed in the AMP-nanoparticle solutions. For AMP concentrations from ∼3 μM to 2.9 mM the overall AMP removal from solution can be described by linear isotherms with removal coefficients (Kr) of 3028 (±267) L kg−1 at pH 2, 11,533 (±823) L kg−1 at pH 4, 12,712 (±672) L kg−1 at pH 6, and 1941 (±342) L kg−1 at pH 8. Mass spectral analysis of AMP solutions after removal of the solid nanoparticles yielded ions that indicate the presence of peniclloic acid, penilloic acid and related de-ammoniated by-products as possible compounds resulting from the degradation of AMP at the TiO2 surface. 相似文献
514.
The behaviors and fate of polycyclic aromatic hydrocarbons (PAHs) in a coking wastewater treatment plant 总被引:4,自引:0,他引:4
The occurrence, behaviors and fate of 18 PAHs were investigated in a coking wastewater treatment plant in Songshan coking plant, located in Shaoguan, Guangdong Province of China. It was found that the target compounds occurred widely in raw coking wastewater, treated effluent, sludge and gas samples. In raw coking wastewater, high molecular weight (MW) PAHs were the dominant compounds, while 3-6 ring PAHs predominated in the final effluent. The dominant compounds in gas samples were phenathrene, fluoranthene and pyrene, while they were fluoranthene, pyrene, chrysene and benzo[k]fluoranthene for sludge. The process achieved over 97% removal for all the PAHs, 47-92% of eliminations of these target compounds in liquid phase were achieved in biological stage. Different behaviors of PAHs were observed in the primary tank, anaerobic tank, aerobic tank, hydrolytic tank and coagulation tank units, while heavier and lower ones were mainly removed in anaerobic tank and aerobic tanks, respectively. Regarding the fate of PAHs, calculated fractions of mass losses for low MW PAHs due to transformation and adsorption to sludge accounted for 15-50% and 24-49%, respectively, while the rest was less than 1%. For high MW PAHs, the mass losses were mainly due to adsorption to sludge and separation with tar (contributing 56-76% and 22-39%, respectively), and the removal through transformation was less. 相似文献
515.
TiO2光催化-微滤膜分离深度净化亚甲基蓝印染废水 总被引:1,自引:1,他引:0
采用悬浮式TiO2光催化膜反应器深度净化纺织工业园区含亚甲基蓝印染废水经生物处理二级出水,利用中空纤维微滤膜进行催化剂截留分离,研究催化剂投加量、运行时间、溶解氧、搅拌方式对出水水质及膜通量的影响。结果表明:光催化会消耗体系溶解氧,鼓风曝气搅拌可同时为系统供氧,优于机械搅拌;该耦合体系的催化剂最佳投加量为1 g/L,经光催化氧化-膜组合工艺处理后水质优于GB 4287-1992《纺织染整工业污染物排放标准》的I级标准,符合建设部颁布的《生活杂用水水质标准》(CJ/T 48-1999)。 相似文献
516.
《Journal of environmental science and health. Part. B》2013,48(4):603-612
Abstract The fumigant 1,3-dichloropropene (1,3-D) is considered a major replacement to methyl bromide, which is to be phased out of use in the United States by 2005. The main purpose of this study was to evaluate soil–water partitioning of 1,3-D in two California agricultural soils (Salinas clay loam and Arlington sandy loam). The partition coefficients (K d and K f ) were determined by directly measuring the concentration of 1,3-D in the solid phase (C s ) and aqueous phase (C w ) after batch equilibration. In the Salinas clay loam, the K f of cis-1,3-D in adsorption and desorption isotherms was 0.47 and 0.54, respectively, with respective values of 0.39 and 0.49 for trans-1,3-D. This slight hysteric effect suggests that a different range of forces are involved in the adsorption and desorption process. Since n was near unity in the Freundlich equation, the Freundlich isotherms can also be approximated using the liner isotherm. At 25°C, the K d of the 1,3-D isomers in both soils ranged from 0.46 to 0.56, and the K oc (organic matter partition coefficient) ranged from 58 to 70. The relatively low K d values and a K oc that falls within the range of 50–150, suggests that 1,3-D is weakly sorbed and highly mobile in these soils. Understanding the sorption behavior of 1,3-D in soil is important when developing fumigation practices to reduce the movement of 1,3-D to the air and groundwater. 相似文献
517.
Rubem S. Oliveira Jr. Diego G. Alonso William C. Koskinen Sharon K. Papiernik 《Journal of environmental science and health. Part. B》2013,48(12):1049-1057
Sorption and desorption of aminocyclopyrachlor (6-amino-5-chloro-2-cyclopropylpyrimidine-4-carboxylic acid) were compared to that of the structurally similar herbicide picloram (4-amino-3,5,6-trichloro-2-pyridinecarboxylic acid) in three soils of differing origin and composition to determine if picloram data is representative of aminocyclopyrachlor behavior in soil. Aminocyclopyrachlor and picloram batch sorption data fit the Freundlich equation and was independent of concentration for aminocyclopyrachlor (1/n = 1), but not for picloram (1/n = 0.80–0.90). Freundlich sorption coefficients (K f) for aminocyclopyrachlor were lowest in the eroded and depositional Minnesota soils (0.04 and 0.12 μmol (1–1/n) L1/n kg?1) and the highest in Molokai soil (0.31 μmol (1–1/n) L1/n kg?1). For picloram, K f was lower in the eroded (0.28 μmol (1–1/n) L1/n kg?1) as compared to the depositional Minnesota soil (0.75 μmol (1–1/n) L1/n kg?1). Comparing soil to soil, K f for picloram was consistently higher than those found for aminocyclopyrachlor. Desorption of aminocyclopyrachlor and picloram was hysteretic on all three soils. With regard to the theoretical leaching potential based on groundwater ubiquity score (GUS), leaching potential of both herbicides was considered to be similar. Aminocyclopyrachlor would be ranked as leacher in all three soils if t1/2 was > 12.7 days. To be ranked as non-leacher in all three soils, aminocyclopyrachlor t1/2 would have to be <3.3 days. Calculated half-life that would rank picloram as leacher was calculated to be ~15.6 d. Using the current information for aminocycloprachlor, or using picloram data as representative of aminocycloprachlor behavior, scientists can now more accurately predict the potential for offsite transport of aminocycloprachlor. 相似文献
518.
Abhishek Mandal 《Journal of environmental science and health. Part. B》2016,51(3):192-203
The aim of this study was to establish the bark of Eucalyptus tereticornis L. (EB) as a low cost bio-adsorbent for the removal of imidacloprid and atrazine from aqueous medium. The pseudo-first-order (PFO), pseudo-second-order (PSO), Elovich and intra-particle diffusion (IPD) models were used to describe the kinetic data and rate constants were evaluated. Adsorption data was analysed using ten 2-, 3- and 4-parameter models viz. Freundlich, Jovanovic, Langmuir, Temkin, Koble–Corrigan, Redlich–Peterson, Sips, Toth, Radke–Prausnitz, and Fritz-Schluender isotherms. Six error functions were used to compute the best fit single component isotherm parameters by nonlinear regression analysis. The results showed that the sorption of atrazine was better explained by PSO model, whereas the sorption of imidacloprid followed the PFO kinetic model. Isotherm model optimization analysis suggested that the Freundlich along with Koble–Corrigan, Toth and Fritz-Schluender were the best models to predict atrazine and imidacloprid adsorption onto EB. Error analysis suggested that minimization of chi-square (χ2) error function provided the best determination of optimum parameter sets for all the isotherms. 相似文献
519.
污泥和谷壳为原料制备了污泥-谷壳吸附剂(SCA)。采用SCA处理酸性大红和碱性嫩黄模拟混合染料废水。通过动力学分析、FTIR表征和SEM表征对SCA吸附混合染料的机理进行了研究。实验结果表明:在吸附温度25 ℃、混合溶液中酸性大红和碱性嫩黄的质量浓度均为100 mg/L、SCA加入量0.5 g/L、吸附时间400 min的条件下,酸性大红的吸附量为125 mg/g,碱性嫩黄的吸附量为170 mg/g;SCA对混合染料的吸附行为符合拟二级反应动力学方程,液膜扩散为吸附的主要控制过程。表征结果显示:SCA孔隙发达且丰富,以中孔和细密的微孔为主,说明SCA具有较高的吸附能力; SCA中包含C—H,C—OH,C—C,CC等主要官能团,SCA对混合染料的吸附为物理吸附。 相似文献
520.
Fenton法制备污泥基活性炭及其性能表征 总被引:1,自引:0,他引:1
污泥基活性炭孔隙率低下是污泥资源化利用的主要制约因素,而Fenton法预处理污泥,可有效改善活性炭性质。通过考察H2O2投加量、H2O2/Fe2+、活化pH以及炭化条件等参数,确定了最佳污泥基活性炭制备条件:H2O2投加量为5%(质量分数),H2O2/Fe2+为5∶1(质量比),活化pH为3,活化时间为2.0h,污泥含固率为1.0%(质量分数),炭化温度为600℃,炭化时间为2.0h,炭化升温速率为10℃/min。此时,得到的污泥基活性炭吸附碘值为340mg/g,比表面积为353.563m2/g,孔容积为0.238cm3/g,微孔容积为0.095cm3/g。该活性炭对阳离子和阴离子染料(亚甲基蓝和甲基橙)具有良好的吸附性能,结果表明,对亚甲基蓝和甲基橙的吸附更符合Langmuir方程,且其饱和吸附量分别为71.53、57.73mg/g。对吸附动力学的拟合结果表明,该吸附更符合二级动力学方程。 相似文献