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1.
Using a laboratory-scale mixed reactor, the performance of alumina in degrading 2,4-Dichlorophenoxyacetic acid with ozone in the presence of tert-butyl alcohol radical scavenger was studied. The operating variables investigated were the dose of alumina catalyst and solution pH. Results showed that using ozone and alumina leads to a significant increase in 2,4-D removal in comparison to non-catalytic ozonation and adsorption processes. The observed reaction rate constants (k(obs)) for 2,4-D during ozonation were found to increase linearly with increasing catalyst dose. At pH 5, the k(obs) value increased from 19.3 to 26 M(-1) s(-1) and 67 M(-1) s(-1) when varying the alumina dose from 1 to 2 and 4 g L(-1), respectively. As pH was increased, higher reaction rates were observed for both non-catalytic ozonation and catalytic ozonation processes. Thus, at pH 3 and using a catalyst dose of 8 g L(-1), the k(obs) values for non-catalytic ozonation and catalytic ozonation processes were 3.4 and 58.9 M(-1) s(-1), respectively, whereas at pH 5 reaction rate constants of 6.5 and 128.5 M(-1) s(-1) were observed, respectively. Analysis of total organic carbon suggested that catalytic ozonation with alumina achieved a considerable level of mineralization of 2,4-D. Adsorption of 2,4-D on alumina was found to play an important role in the catalytic ozonation process.  相似文献   

2.
臭氧催化氧化工艺深度处理印染废水   总被引:1,自引:1,他引:1  
采用正交实验对催化剂NiO/γ-A12O3的制备条件进行优化,并探讨臭氧催化氧化法对于印染废水的深度处理效能.结果表明,最优的催化剂制备条件为:浸渍液浓度为3%、浸渍时间为4h、灼烧温度为450℃、灼烧时间为3h.臭氧催化氧化反应15 min时,COD浓度由84.22 mg/L降低至50.00 mg/L以下;氨氮浓度由10.88 mg/L降低至5.01 mg/L;色度去除率达到69%,明显高于单纯臭氧氧化的反应效率.  相似文献   

3.
活性炭负载金属氧化物催化臭氧氧化甲硝唑   总被引:1,自引:0,他引:1  
采用浸渍法制备了Fe、Ni、Ag、Ce 4种金属氧化物负载活性炭(MeOx/AC)催化剂,并用于甲硝唑(MNZ)的催化臭氧氧化降解,以考察其催化活性.在20 mg/h的臭氧投加量下,催化剂的加入(0.5 g)对MNZ(C0=5 mg/L;pH=5.5)的氧化和矿化有明显改善,其中NiOX/AC催化剂表现出较好的催化活性...  相似文献   

4.
垃圾焚烧发电厂渗滤液生化出水是一种高盐,且含腐殖酸类和水溶性小分子有机物的复杂废水。本研究提出了采用Ca(OH)2预处理,并催化臭氧氧化处理的新工艺路线,对工艺参数和催化过程机理进行了分析。结果表明,Ca(OH)2可以有效地预处理去除生化出水中的腐殖酸类大分子有机物,当其用量为12 g/L时,可使COD的去除率达到70%~75%。Ca(OH)2可强化催化臭氧氧化处理预处理废水中剩余的难降解小分子有机物,其机理可能是及时去除了反应体系中生成的碳酸根离子,其适宜用量为2 g/L废水。当搅拌转速小于600 r/min,进口气相中臭氧浓度小于66.24 mg/L时,增大反应体系搅拌强度和进口臭氧浓度可以强化废水COD的去除速率。该工艺在深度处理垃圾渗滤液生化出水中难降解有机物领域具有较大的应用前景。  相似文献   

5.
羟基氧化铁催化臭氧氧化去除水中阿特拉津   总被引:2,自引:0,他引:2  
以实验室制备的羟基氧化铁(FeOOH)为催化剂,研究了其催化臭氧氧化去除水中痕量阿特拉津的效能,并对影响催化效果因素及降解机理进行了探讨。在本实验条件下,反应8 min时催化氧化阿特拉津的去除率比单独臭氧氧化高出63.2%,而FeOOH对阿特拉津的吸附量很小,结果表明,FeOOH对臭氧氧化水中的痕量阿特拉津具有明显的催化活性。探讨了催化剂投量、pH、阿特拉津初始浓度和重碳酸盐碱度对催化氧化阿特拉津的影响。催化剂最佳投量为150 mg/L,去除率随pH和阿特拉津初始浓度的增加而升高,重碳酸盐浓度为200 mg/L时催化作用受到明显抑制。通过研究叔丁醇对催化反应的影响间接推断了催化反应的机理,叔丁醇作为羟基自由基抑制剂有效地抑制了水中羟基自由基的生成和它对阿特拉津的氧化反应,间接证明这种催化作用遵循羟基自由基的反应机理。  相似文献   

6.
Abstract

In the present work, dispersive micro-solid phase extraction (D-μ-SPE) method using magnetic graphene oxide tert-butylamine (GO/Fe3O4/TBA) nanocomposite, as an efficient sorbent, was applied for determining 2,4-dichlorophenoxyacetic acid (2,4-D) in water and food samples. Detection was carried out using high-performance liquid chromatography (HPLC) instrument. Influential parameters of D-μ-SPE such as sorbent and its amount, elution solvent and its volume, adsorption and desorption times and pH of sample solution were investigated and optimized. Under the optimized conditions, limit of detection and quantitation values were 0.007 and 0.02?μg/mL, respectively. Recovery data for several real samples were obtained within the range of 88.0–94.0% with a relative standard deviation (RSD) less than 7.5%. The proposed method was successfully applied to quantitative determination of 2,4-D in several vegetables and water samples.  相似文献   

7.
NiO/AC催化臭氧氧化去除水中的苯酚   总被引:1,自引:0,他引:1  
采用低温湿式浸渍法制备了负载氧化镍/活性炭(简称NiO/AC)催化剂。在不同pH、叔丁醇浓度等条件下,对NiO/AC与臭氧联合催化臭氧氧化苯酚的降解效果等进行了研究。用XRD、SEM及BET技术分析了活性炭与催化剂的组成、形貌及结构变化。结果表明,镍以棒状氧化镍的形式负载在活性炭表面,与AC相比,NiO/AC比表面积减少了47.9%。在O3/NiO/AC与苯酚的反应体系中,反应遵循羟基自由基(HO.)机理,苯酚的去除率比单独臭氧氧化提高了29%,且与溶液pH呈正相关。NiO/AC催化性能较稳定,镍离子最大析出浓度仅为7 mg/L,可重复使用。  相似文献   

8.
吴悦  吴纯德 《环境工程学报》2016,10(11):6446-6450
采用Nano-TiO2/O3和Nano-TiO2/UV/O3进行小试实验。通过对DOC、UV254、BrO3-和甲醛进行检测分析,研究了不同体系去除腐殖酸(HA)并控制臭氧副产物生成的效果。结果表明,当HA浓度为10 mg·L-1时,Nano-TiO2/O3体系对DOC的去除主要在反应进行20 min内完成,去除率仅达12.0%左右,对UV254的去除主要发生在2 min内,去除率仅达14.5%左右;而Nano-TiO2/UV/O3体系DOC和UV254的去除率分别达32.8%和53.3%。HA的存在显著减少了Nano-TiO2/O3体系BrO3-的生成量,出水BrO3-浓度为29.00 μg·L-1,而Nano-TiO2/UV/O3体系出水BrO3-浓度为5.00 μg·L-1。研究表明,相比Nano-TiO2/O3体系,Nano-TiO2/UV/O3体系能更好地控制BrO3-生成,同时能提高对HA的去除效果,且无甲醛生成的风险。  相似文献   

9.
以市售活性炭、硅藻土和氧化铝小球为载体,考察了负载铁基活性组分对催化臭氧化过程中溴酸盐的控制情况,其中,铁基复合氧化铝小球体现出更好的溴酸盐还原特性和催化剂稳定性,证实催化剂中铁氧化物是溴酸盐得到有效控制的主要活性组分。进一步考察了铁基复合氧化铝小球催化臭氧化处理实际原水过程中对溴酸盐的生成控制,以及反应过程中溶解性有机碳(DOC)的去除情况。结果表明,与单独臭氧化相比,该催化剂既能有效去除水中的溶解性有机物,又能明显抑制溴酸盐的生成,反应50h,其活性并没有明显下降。催化剂失活主要归因于吸附位点数量的下降,可以通过负载铁氧化物来实现催化剂的再生。  相似文献   

10.
为了提高有机物的臭氧化降解效率,工作中利用浸渍法制备了一种新型的三组分催化剂(记为V2O5-TiO2-AlF3/Al2O3)。催化臭氧化降解2,4-滴丙酸的实验结果表明,该催化剂能有效提高臭氧化的效率,体系可能遵循羟基自由基的作用机理。利用相对法计算结果表明,与单独臭氧化相比,V2O5-TiO2-AlF3/Al2O3催化臭氧化体系具有更大的Rct值。重复实验结果表明,该催化剂具有相对较好的稳定性。以上研究结果对推广催化臭氧化技术在实际废水处理中的应用具有重要的实际意义。  相似文献   

11.
采用自蔓延溶胶凝胶法分别制备了铁氧化物和铁铜复合氧化物催化剂,以酸性红B为降解对象,对比了单独臭氧氧化、铁氧化物和铁铜复合氧化物催化臭氧氧化对酸性红B的降解效果,考察了磁力搅拌速度(500~1 640 r/min)、溶液pH(3~11)、臭氧投加速率(3.55~28.4 mg/min)对铁铜复合氧化物催化性能的影响。结果表明,与单独臭氧氧化比较,铁氧化物和铁铜复合氧化物均能加速酸性红B的降解,促进色度和COD的去除,结合催化剂的表征结果,推断催化剂表面羟基促进臭氧分解产生.OH是其氧化性能较好的主要原因,另外,催化剂的吸附能力对催化性能也有一定影响。随着磁力搅拌速度、溶液pH、臭氧投加速率的增大,铁铜复合氧化物催化臭氧氧化酸性红B的效果越好。  相似文献   

12.
Tong SP  Liu WP  Leng WH  Zhang QQ 《Chemosphere》2003,50(10):1359-1364
The characteristics of different types of MnO2 catalytic ozonation of sulfosalicylic acid (SSal) and propionic acid (PPA) have been investigated in this paper. The experimental results show the dependence of catalytic activity of MnO2 on organic compounds and the pH of solutions, but it is independent on the type of MnO2. For example, three types of MnO2 have not any catalytic activity when ozonation of PPA under the condition of this experiment. All MnO2 catalytic ozonation of SSal at pH=1.0 have a greater total organic carbon removal than ozonation alone has, however, at pH=6.8 and 8.5, catalytic efficiency is not observed. Furthermore, the batch experimental results indicate that there are no direct relationship between the activity of metal oxide catalytic decomposition of ozone and that of its catalytic degradation of organic compounds.  相似文献   

13.
Degradation of atrazine by catalytic ozonation in the presence of iron scraps (ZVI/O3) was carried out. The key operational parameters (i.e., initial pH, ZVI dosage, and ozone dosage) were optimized by the batch experiments, respectively. This ZVI/O3 system exhibited much higher degradation efficiency of atrazine than the single ozonation, ZVI, and traditional ZVI/O2 systems. The result shows that the pseudo-first-order constant (0.0927?min?1) and TOC removal rate (86.6%) obtained by the ZVI/O3 process were much higher than those of the three control experiments. In addition, X-ray diffraction (XRD) analysis indicates that slight of γ-FeOOH and Fe2O3 were formed on the surface of iron scrap after ZVI/O3 treatment. These corrosion products exhibit high catalytic ability for ozone decomposition, which could generate more hydroxyl radical (HO?) to degrade atrazine. Six transformation intermediates were identified by liquid chromatography-mass spectrometry (LC-MS) analysis in ZVI/O3 system, and the degradation pathway of atrazine was proposed. Toxicity tests based on the inhibition of the luminescence emitted by Photobacterium phosphoreum and Vibrio fischeri indicate the detoxification of atrazine by ZVI/O3 system. Finally, reused experiments indicate the approving recyclability of iron scraps. Consequently, the ZVI/O3 system could be as an effective and promising technology for pesticide wastewater treatment.  相似文献   

14.
采用不同的表面改性方法(去矿化处理、氧化改性、碱改性和还原改性)对污泥基活性炭(SCAC)进行处理,分别获得了表面金属含量低、碱位低、碱性官能团含量高及Lewis碱含量高的4种改性SCAC(SCAC-D、SCAC-S、SCAC-OH和SCAC-N),对比考察了改性前后SCAC催化臭氧氧化去除布洛芬(IBP)的效能,并探讨了SCAC催化臭氧氧化反应的主要活性位点。结果表明,5种SCAC催化活性顺序为:SCAC-N > SCAC-OH > SCAC > SCAC-S > SCAC-D;金属组分减少会直接影响SCAC的催化活性,碱位减少对其催化活性的影响相对较弱,说明SCAC表面较为丰富的金属组分是其催化臭氧氧化反应的主要活性位点;增加SCAC表面碱位(Lewis碱和碱性官能团),减少表面酸性官能团有助于提高其催化活性。  相似文献   

15.
为研究不同阴离子条件下纳米TiO2催化臭氧化(nano-TiO2/O3)过程对溴酸盐(BrO3-)生成的影响,本研究通过小试实验分别考察了不同浓度溴离子(Br-)、氯离子(Cl-)、碳酸氢根离子(HCO3-)、硫酸根离子(SO42-)和亚硝酸根离子(NO2-)对纳米TiO2催化臭氧化过程BrO3-生成的影响,并对不同阴离子条件下单独臭氧化(O3)过程和nano-TiO2/O3过程BrO3-生成情况进行对比。结果表明,不同Br-初始浓度下,相对于O3过程,纳米TiO2对BrO3-生成的抑制效果规律不明显;Cl-浓度从0增至150 mg·L-1时,纳米TiO2抑制率呈现先增加后下降的趋势;HCO3-存在的水体,投加纳米TiO2对BrO3-生成的抑制效能大大减弱;当SO42-初始浓度为0~90 mg·L-1时,相对于O3过程,nano-TiO2/O3过程BrO3-生成量减少了22.50%~68.77%;当NO2-初始浓度为0~1 mg·L-1时,相对于O3过程,nano-TiO2/O3过程BrO3-生成量减少了2.22%~68.77%。  相似文献   

16.
以纯石英砂或煤矸石酸浸提铝废渣为原料,采用低温(850℃)纯碱烧结法制备水玻璃,考察了杂质Al2O3含量对原料中SiO2溶出率以及产品水玻璃模数的影响,通过电感耦合等离子发射光谱(ICP)、傅里叶红外光谱仪(FTIR)、X射线衍射仪(XRD)和热重分析(TGA)手段对原料和产物进行了分析和表征。结果表明,与纯石英砂为原料制备水玻璃相比,杂质Al2O3的存在降低了SiO2-Na2O体系的反应温度,但由于Al2O3会与反应体系中的SiO2和Na2O反应生成水不溶性的铝硅酸钠盐,导致实际可溶性SiO2的含量减少,降低了SiO2的溶出率和硅酸钠的模数。通过添加石英砂可控制提铝废渣中的A12O3含量低于5%,使提铝废渣中SiO2的溶出率达到90%以上,制得水玻璃模数达2.15。  相似文献   

17.
以市售活性炭、硅藻土和氧化铝小球为载体,考察了负载铁基活性组分对催化臭氧化过程中溴酸盐的控制情况,其中,铁基复合氧化铝小球体现出更好的溴酸盐还原特性和催化剂稳定性,证实催化剂中铁氧化物是溴酸盐得到有效控制的主要活性组分。进一步考察了铁基复合氧化铝小球催化臭氧化处理实际原水过程中对溴酸盐的生成控制,以及反应过程中溶解性有机碳(DOC)的去除情况。结果表明,与单独臭氧化相比,该催化剂既能有效去除水中的溶解性有机物,又能明显抑制溴酸盐的生成,反应50 h,其活性并没有明显下降。催化剂失活主要归因于吸附位点数量的下降,可以通过负载铁氧化物来实现催化剂的再生。  相似文献   

18.
In this study, we used primary cultures of fish hepatic cells as a tool for evaluating the effects of environmental contamination. Primary hepatic cell cultures derived from the subtropical fish Metynnis roosevelti were exposed to different concentrations (0.275, 2.75 and 27.5 μg L?1) of the herbicides 2,4-dichlorophenoxyacetic acid (2,4-D) and 4-chloro-2-methylphenoxyacetic acid (MCPA). Cellular respiratory activity was evaluated by polarography using three substrates: 0.5 M glucose, 0.5 M succinate and 0.5 M α-ketoglutarate. Significant changes were observed in cellular oxygen consumption with 0.5 M α-ketoglutarate. Even at low concentrations, 2,4-D and MCPA were potent uncouplers of oxidative phosphorylation. Primary cultures of M. roosevelti liver cells may provide a useful tool for the evaluation of environmental contaminant effects. A review of regulations regarding permitted concentrations of these herbicides is needed.  相似文献   

19.
采用柠檬酸络合分解法合成了四方晶点、K2NiF4型结构的稀土复合氧人LaSrMO4(M=Mn,Fe,Co,Ni)。实验结果,该类氧化物催化剂对恶臭和有毒的有机胺类化合物具有较好的催化降解作用,有机胺的氧降解可达100%,而氮氧化物的产生率低于10%,其含量可大大低于排放标准。  相似文献   

20.
Azo dye ozonation was carried in a semi-batch reactor to evaluate both the molecular and radical contributions of ozone on the dye decay. From two mass balance equations, the simultaneous determination of mass transfer, self-decomposition and solubility parameters of ozone were determinated; thus establishing the steady state conditions in the experimental system. The results of kinetic studies showed that the decay of azo dye was a pseudo-first-order reaction with respect to dye concentration and the overall rate constant increased with an increase in the pH, however declined with an increase in the dye concentration. Furthermore, from the overall rate constants obtained at various pH values a mathematical analysis of dye decay was performed, which provides a practical new method to quantify the radical and molecular contributions in the ozonation of azo dyes.  相似文献   

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