2,4-二氯苯氧乙酸臭氧氧化动力学研究

研究了臭氧氧化条件下2,4-二氯苯氧乙酸在鼓泡反应器内的去除动力学,考察了pH、温度、气体流量、初始浓度等因素对反应的影响,得到反应动力学速率常数与温度和pH的关系。     

臭氧深度氧化法处理2,4-二氯苯氧乙酸农药废水

对臭氧深度氧化法降解农药2,4-二氯苯氧乙酸(2,4-D)废水进行了研究。实验结果表明,紫外光催化臭氧化降解2,4-D成效显著,臭氧/紫外(UV)深度氧化法是最好的臭氧化处理方法。2,4-D200mg/L的水样,反应30min,2,4-D降解完全,75min时矿化率达75%以上。碱性反应氛围有利于臭氧化反应进行。自由基抑制剂(叔丁醇)的加入,显著降低臭氧化反应去除2,4-D的效果,自由基参与的反应历程对于2,4-D的降解十分重要。双氧水的引入对2,4-D降解无明显促进作用,这是因为双氧水分解消耗OH-,没有缓冲的反应体系pH降低,限制了双氧水的分解和.OH自由基链反应。总之,单独臭氧化对2,4-D降解有一定的反应效率,在有利于.OH产生的体系中,2,4-D降解效率进一步提高。     

Fe-MCM-41催化氧化2,4-二氯苯氧乙酸

采用水热法合成了Fe-MCM-41中孔分子筛,紫外、红外及XRD表征显示铁离子已进入中孔分子筛骨架。以H2O2为氧化剂形成类Fenton试剂,实验结果表明,在催化剂加入量为1 g/L、H2O2体积分数为6%、pH为4、反应时间为10h、反应温度为35℃的条件下,处理质量浓度为50 mg/L的2,4-D废水的降解率达94.95%。宏观动力学研究显示,该反应近似为一级反应,反应速率常数、表观活化能分别为0.21667 min-1和26.65 kJ/mol。     

Mn的氧化价态对Mn／γ-Al2O3催化剂催化臭氧氧化气相低浓度甲苯的影响

采用共沉淀法,以Al2O3为载体制备Mn／γ-Al2O3和Mn—Ce／Mn／γ-Al2O3催化剂,并分别在N2气氛和O2气氛下焙烧。采用固定床连续流动反应器,研究所制备催化剂在室温条件下催化臭氧氧化甲苯的性能。通过XRD、XPS和FTIR等手段对催化剂的结构和组成进行表征。结果表明,Mn／Mn／γ-Al2O3催化剂具有良好的催化臭氧氧化甲苯和催化臭氧自身分解的性能,共沉淀法制备催化剂的最佳Mn负载量为20％。O2气氛焙烧和Ce的加入,可以有效提高催化剂的活性和寿命。原因是O2气氛焙烧和Ce的加入可以提高Mn的氧化价态。催化剂失活的主要原因是有机副产物在催化剂表面吸附堆积,失活催化剂在550℃、空气气氛下焙烧可恢复催化性能。     

Mn3O4催化臭氧化钻井废水的作用机理

通过静态实验,探讨了Mn3O4对钻井废水臭氧化过程的催化作用机理,考察了Mn3O4及Cl-对臭氧分解、水体湍动程度、羟基自由基抑制剂碳酸氢根和叔丁醇的加入对COD去除率的影响,分析了反应过程中TOC和pH的变化。结果表明,催化剂加量为100 mg/L时,臭氧分解率由单独臭氧时的38.2%增加到81.4%,Mn3O4对钻井废水中有机物的吸附去除率仅为2%,O3/活性炭体系对COD去除率与单独臭氧效果接近,说明臭氧在催化剂表面存在吸附作用,促进臭氧分解;水体不搅拌与搅拌速度增加为900 r/min时,COD去除率由52%增加到58%,搅拌程度对钻井废水COD去除效果影响不大;HCO3-浓度为100 mg/L时,COD去除率降低到41.2%,说明了体系中有羟基自由基产生;氯离子浓度为1 000 mg/L,臭氧的分解率降低了9.2%,证明了臭氧在催化剂表面的吸附作用;羟基自由基抑制剂叔丁醇的加入,使得COD去除率由54.3%降低为40.8%,证实了反应体系中存在羟基自由基。同时在反应过程中,体系的TOC 由191.9 mg/L降低至37.6 mg/L;pH由原来的11.2降低到6.3。实验现象说明,臭氧吸附在Mn3O4催化剂表面,分解产生羟基自由基,进而氧化去除钻井废水中有机物,这在某种程度上证明了Mn3O4催化臭氧化对有机物的降解遵循羟基自由基机理。     

臭氧催化氧化降解苯胺的机理

对臭氧单独氧化和臭氧催化氧化下的苯胺降解效率进行了比较,并通过液质联机分析了氧化过程中产物变化情况。实验结果表明,催化剂MnO2-CuO-CeO2/沸石的添加能有效地提高臭氧氧化苯胺的降解率,当苯胺初始浓度为200mg/L,反应20 min后,苯胺的去除率由原来的75%提高到89%;通过LC-MS分析,臭氧催化氧化苯胺降解过程中代谢产物依次为对亚胺醌、对苯醌、马来酸和草酸,并由此推断出了臭氧催化氧化降解苯胺的途径。     

γ-Al2O3负载Mn基催化剂低温催化臭氧氧化NO

利用等体积浸渍法制备γ-Al2O3负载Mn基催化剂,考察了掺杂元素种类,掺杂元素与Mn元素摩尔比以及煅烧温度对NO低温（100 ℃）催化氧化活性的影响,并对催化剂在有SO2或H2O的烟气中的稳定性进行了探究。结果表明,掺杂元素为Ce,Ce/Mn=0.4,煅烧温度为500 ℃条件下制备的催化剂NO催化活性最佳,在NO体积浓度为500×10-6,臭氧浓度为20.9 mg·L-1,n(O3)/n(NO)=0.2,反应温度为100 ℃,模拟烟气总流量为1.0 L·min-1,模拟烟气相对湿度为4%的条件下,NO的转化率最高可达70%。此外,还对催化剂在不同条件下的稳定性和活性恢复情况进行了探究。实验最终实现了在低O3浓度条件下达到较高NO转化率的目的,为烟气脱硝提供了一种具有应用潜力的新技术。     

催化臭氧氧化降解糖蜜酒精废水的研究

以SnO2为催化剂,研究糖蜜酒精废水在臭氧条件下的氧化降解反应,为糖蜜酒精废水的治理提供一种新的处理方法.研究表明,SnO2加速了臭氧氧化反应,使糖蜜酒精废水的氧化降解加快.影响糖蜜酒精废水氧化降解的主要因素有臭氧流量、废水的初始pH和催化剂用量等.加大臭氧流量及增加催化剂用量,均有利于糖蜜酒精废水的降解.适宜的反应条件是:糖蜜酒精废水的稀释倍数为10倍,臭氧流量为130 mg/h,催化剂用量为2.500 g/L,废水的初始pH为4.25,温度为30 ℃.在该条件下反应60 min,废水的脱色率为60.2%,COD去除率为44.5%.动力学分析表明,单独臭氧氧化降解糖蜜酒精废水和SnO2催化臭氧氧化降解糖蜜酒精废水均为拟一级反应.     

2-甲基-4-氯苯氧乙酸及其脱氯产物的光化学降解

紫外消毒工艺作为废水/给水处理的重要步骤,不仅可以有效控制水中的病原体,而且可使废水或水源水中存在的一些污染物发生化学降解作用,但目前对这一作用过程的研究尚不完善。本文针对一种典型的除草剂——2-甲基-4-氯苯氧乙酸（MCPA）及其脱氯产物二甲基苯氧乙酸（MPA）,研究了两者在紫外灯照射下的光化学行为,并进一步考察了波长、初始pH值、H2O2及水中其他共存物质对MCPA和MPA光降解效率的影响。研究结果表明,不同光源对MCPA的光降解速率大小为：254 nm波长紫外灯 > 365 nm波长紫外灯 > 可见光灯;低pH值不利于MCPA的光降解,但对MPA光降解的影响不大;在溶液中加入H2O2,会增大MCPA和MPA的光降解速率;MCPA的光降解过程符合一级动力学方程;腐殖酸（HA）会降低MCPA的光降解速率;MPA与MCPA呈现相似的光降解效应,但反应速率比MCPA略快,且在两者共存状态下会降低MCPA的光降解速率。     

Adsorption characteristics of 2,4-dichlorophenoxyacetic acid (2,4-D) from aqueous solution on powdered activated carbon

The removal of 2,4-dichlorophenoxyacetic acid (2,4-D), one of the most commonly used phenoxy acid herbicides, from aqueous solution was studied by using acid-washed powdered activated carbon (PAC) as an adsorbent in a batch system. Adsorption equilibrium, kinetics, and thermodynamics were investigated as a function of initial pH, temperature, and initial 2,4-D concentration. Powdered activated carbon exhibited the highest 2,4-D uptake capacity of 333.3 mg g(-1) at 25 degrees C and an initial pH value of 2.0. Freundlich, Langmuir, and Redlich-Peterson isotherm models were used to express the equilibrium data of 2,4-D depending on temperature. Equilibrium data fitted very well to the Freundlich equilibrium model in the studied concentration range of 2,4-D at all the temperatures studied. Three simplified models including pseudo-first-order, pseudo-second-order, and saturation-type kinetic models were used to test the adsorption kinetics. It was shown that the adsorption of 2,4-D on PAC at 25, 35, and 45 degrees C could be best fitted by the saturation-type kinetic model with film and intraparticle diffusions being the essential rate-controlling steps. The activation energy of adsorption (EA) was determined as--1.69 kJ mole(-1). Using the thermodynamic equilibrium coefficients obtained at different temperatures, the thermodynamic constants of adsorption (deltaG degrees, deltaH degrees, and deltaS degrees) were also evaluated.     

Synergy of ozonation and photocatalysis to mineralize low concentration 2,4-dichlorophenoxyacetic acid in aqueous solution

Concentration of 2,4-dichlorophenoxyacetic acid (2,4-D) may affect its degradation kinetics in advanced oxidation systems, and combinations of two or more systems can be more effective for its mineralization at low concentration levels. Degradations and mineralizations of 0.045mM 2,4-D using O(3), O(3)/UV, UV/TiO(2) and O(3)/UV/TiO(2) systems were compared, and influence of reaction temperature on the mineralization in O(3)/UV/TiO(2) system was investigated. 2,4-D degradations by O(3), O(3)/UV and UV/TiO(2) systems were similar to the results of earlier investigations with higher 2,4-D concentrations. The degradations and total organic carbon (TOC) removals in the four systems were well described by the first-order reaction kinetics. The degradation and removal were greatly enhanced in O(3)/UV/TiO(2) system, and further enhancements were observed with larger O(3) supplies. The enhancements were attributed to hydroxyl radical (()OH) generation from more than one reaction pathway. The degradation and removal in O(3)/UV/TiO(2) system were very efficient with reaction temperature fixed at 20 degrees C. It was suspected that reaction temperature might have influenced ()OH generation in the system, which needs further attention.     

An unconventional approach to studying the reaction kinetics of the Fenton's oxidation of 2,4-dichlorophenoxyacetic acid

The Fenton's oxidation kinetics of herbicide 2,4-D at various [Fe(II)] and [H(2)O(2)] combinations was investigated and modelled through an unconventional approach. The reaction kinetics of 2,4-D degradation demonstrated a two-stage pattern of decay, where a very fast reactive stage was followed by a retardation stage due to the depletion of oxidants and to the competitive side-reactions of the intermediates (including 2,4-dichlorophenol, chlorohydroquinone and 2,6-dichlororesorcinol). A model characterized by two newly established constants, the initial decay rate and the maximum oxidative capacity, was proposed and proven capable of describing the two-stage process, which cannot easily be described by conventional first- or second-order kinetics approaches.     

Evaluation and comparison of advanced oxidation processes for the degradation of 2,4-dichlorophenoxyacetic acid (2,4-D): a review

Environmental Science and Pollution Research - Organochlorine pesticides have generated public concern worldwide because of their toxicity to human health and the environment, even at low...     

Fungal bioconversion of 2,4-dichlorophenoxyacetic acid (2,4-D) and 2,4-dichlorophenol (2,4-DCP)

Ninety strains of fungi from the collection of our mycology laboratory were tested in Galzy and Slonimski (GS) synthetic liquid medium for their ability to degrade the herbicide 2,4-dichlorophenoxyacetic acid (2,4-D) and its by-product, 2,4-dichlorophenol (2,4-DCP) at 100 mg l(-1), each. Evolution of the amounts of each chemical in the culture media was monitored by HPLC. After 5 days of cultivation, the best results were obtained with Aspergillus penicilloides and Mortierella isabellina for 2,4-D and with Chrysosporium pannorum and Mucor genevensis for 2,4-DCP. The data collected seemed to prove, on one hand, that the strains responses varied with the taxonomic groups and the chemicals tested, and, on the other hand, that 2,4-D was less accessible to fungal degradation than 2,4-DCP. In each case, kinetics studies with the two most efficient strains revealed that there was a lag phase of 1 day before the onset of 2,4-D degradation, whereas there was none during 2,4-DCP degradation. Moreover, 2,4-DCP was detected transiently during 2,4-D degradation. Finally, M. isabellina improved its degradation potential in Tartaric Acid (TA) medium relative to GS and Malt Extract (ME) media.     

Exposure of homeowners and bystanders to 2,4-dichlorophenoxyacetic acid (2,4-D).

Total body dose received in home gardeners applying 2,4-D and bystanders living within the household, but not applying the pesticide was measured. Levels of 2,4-D were monitored in air samples both inside the home and downwind of the application site. Homeowners were divided into protective and non-protective apparel groups and applied both a granular and liquid formulation of 2,4-D on two separate dates. Analyses of urine collected from homeowners for 96 hours following applications found total body doses ranging from non-detectable to 0.0071 mg/kg of body weight. The highest exposures occurred in the non-protected group and were consistently associated with spills of the liquid concentrate or excessive contact with the dilute mixture on the hands or forearms. Residues of 2,4-D were not detected in urine samples supplied by bystanders to home applicators. Residues of 2,4-D were detected in five of the 76 air samples taken during the home applications. Two of these air samples coincided with measurable applicator exposure but it is unlikely that this was a major route of exposure.     

Fine route for an efficient removal of 2,4-dichlorophenoxyacetic acid (2,4-D) by zeolite-supported TiO2

Zeolites HY, Hbeta and HZSM-5 with different physico-chemical properties were chosen as support for TiO2 to illustrate their adsorption, dispersion and electronic structure in photocatalysis. The extent of TiO2 loading was monitored by XRD and BET surface area measurements. The adsorption capacity of HY zeolite was found to be high and hence chosen for further modification to continue the investigation. Photodegradation kinetics were carried out with 2,4-dichlorophenoxyacetic acid (2,4-D) in aqueous solution. The extent of 2,4-D degradation on TiO2/HY loading revealed the importance of adsorption in photocatalysis. Mineralisation studies on all three zeolites with 1 wt.% TiO2 loading demonstrated the good dispersion properties of TiO2/HY. Its photocatalytic activity was found to be excellent with formulated 2,4-D. Comparison of relative photonic efficiencies demonstrated that supported photocatalysts exhibited higher activity than some of the commercial photocatalysts. The high activity of supported TiO2 is due to synergistic effects of improved adsorption of 2,4-D and efficient delocalisation of photogenerated electrons by zeolite support.     

Adsorption of 2,4-dichlorophenoxyacetic acid and 4-chloro-2-metylphenoxyacetic acid onto activated carbons derived from various lignocellulosic materials

Adsorption of 2,4-dichlorophenoxyacetic acid (2,4-D) and 4-chloro-2-metylphenoxyacetic acid (MCPA) from aqueous solution onto activated carbons derived from various lignocellulosic materials including willow, miscanthus, flax, and hemp shives was investigated. The adsorption kinetic data were analyzed using two kinetic models: the pseudo-first order and pseudo-second order equations. The adsorption kinetics of both herbicides was better represented by the pseudo-second order model. The adsorption isotherms of 2,4-D and MCPA on the activated carbons were analyzed using the Freundlich and Langmuir isotherm models. The equilibrium data followed the Langmuir isotherm. The effect of pH on the adsorption was also studied. The results showed that the activated carbons prepared from the lignocellulosic materials are efficient adsorbents for the removal of 2,4-D and MCPA from aqueous solutions.     

Green preparation of a novel red mud@carbon composite and its application for adsorption of 2,4-dichlorophenoxyacetic acid from aqueous solution

This study reports the eco-friendly preparation of a novel composite material consisting of red mud and carbon spheres, denoted as red mud@C composite, and its application for the removal of 2,4-dichlorophenoxyacetic acid herbicide (2,4-D) from aqueous solution. The preparation route has a green approach because it follows the low-energy consuming one-step hydrothermal process by using starch as a renewable carbon precursor and red mud as a waste from aluminum production industry. Characterization of the red mud@C composite was performed by FT-IR, TGA, SEM, TEM, BET, XRD, and Raman microscopy analyses. The batch adsorption studies revealed that the red mud@C composite has higher 2,4-D adsorption efficiency than those of the red mud and the naked carbon spheres. The maximum removal at initial pH of 3.0 is explained by considering the pKa of 2,4-D and pH of point of zero charge (pH_pzc) of the composite material. The adsorption equilibrium time was 60 min, which followed the pseudo-second-order kinetic model together with intra-particle diffusion model. The isotherm analysis indicated that Freundlich isotherm model better represented the adsorption data, with isotherm parameters of k [15.849 (mg/g) (mg/L)^?1/n] and n (2.985). The prepared composite is reusable at least 5 cycles of adsorption-desorption with no significant decrease in the adsorption capacity.