对氯苯甲酸用于测量OH#方法探讨2.误差分析

对氯苯甲酸用于测量臭氧氧化过程中产生的OH.浓度时会产生误差.为了研究误差的大小,进行了臭氧的间歇实验,以测量臭氧分解速率常数k.通过对比乙二酸、甲苯和腐殖酸溶液中投加对氯苯甲酸前后k值的变化,判断投加的对氯苯甲酸是否能引起测量误差及误差大小.试验结果表明,含清除剂少的水样,对氯苯甲酸测量OH.浓度时会引起很大的误差.在对氯苯甲酸捕获率小于10%的水样中,对氯苯甲酸测量OH.时产生的误差小.在捕获率大于20%的水样中,采用对氯苯甲酸测量OH.会产生较大误差,不能用来测量OH.浓度.     

氯苯甲酸植物毒性实验中抗氧化酶变化的量化研究

为研究氯苯甲酸(CBA)的植物毒性,评估生物化学参数能否作为CBA植物毒性的指示因子,采用对CBA敏感的小白菜种子和大白菜种子进行暴露实验,在根伸长抑制率为10%～50%的质量浓度范围内,研究了CBA剂量-抗氧化酶活性的关系.结果表明:随着CBA质量浓度的升高,超氧化物歧化酶(SOD)活性总体上呈逐渐上升至峰值然后下降趋势,过氧化物酶(POD)活性逐渐降低,过氧化氢酶(CAT)活性与SOD活性近似,呈先升后降趋势,但幅度大于SOD活性.对CBA剂量-酶活性抑制率进行了回归分析,对拟合效果进行了显著性检验(P<0.05),并求出相应的半效应浓度(EC50),实验材料的SOD和CAT活性的EC50均在实验区间之外,POD活性的EC50则在实验区间之内,表明在实验区间内,SOD和CAT活性不敏感,POD活性为有效指标      

H_2O_2－O_3氧化法处理染料中间体H酸和1－氨基蒽醌生产废液的研究

研究采用羟基自由基氧化法处理难生物降解染料中间体Ｈ酸和１－氨基蒽醌生产废液提高其生物降解性。研究表明：羟基自由基是一种非常强的氧化剂，能迅速分解有机物，改善废水的生物降解性能；经羟基自由基氧化处理后，能提高废水的絮凝处理效率。本文还对羟基自由基氧化反应机理作了探讨。     

臭氧氧化水中壬基酚的反应机理研究

采用臭氧氧化浓度为20 mg/L的壬基酚溶液,研究了臭氧氧化去除壬基酚的效果及氧化过程中中间产物的变化情况,探讨了臭氧氧化壬基酚的反应机理.结果表明,臭氧氧化涉及2种氧化方式,臭氧分子的单独反应和臭氧/羟基自由基的联合氧化.2种氧化方式在18 min内均能完全去除壬基酚,联合氧化方式在4 min内即能达到96％的去除率,而单独臭氧分子氧化需要12 min.氧化过程中检测到甲醛的产生,单独臭氧氧化下甲醛产生量在8 min左右达到稳定,而混合氧化方式下甲醛量逐步增加.     

臭氧氧化产物甲醛的产生机理研究

对3类含不同碳链结构的有机物进行臭氧氧化,研究了氧化过程中的甲醛浓度变化情况,并对臭氧单独氧化、臭氧和羟基自由基混合氧化和羟基自由基氧化特性进行了分析.以丙烯酸为目标物,分别研究了不同进气流量、气态臭氧浓度和双氧水投加量对甲醛浓度的影响.结果表明:苯环上不同的取代基对甲醛产量有较大影响,单烯烃的α-C上连接的基团对甲醛浓度影响更大;在氧化过程中,甲醛浓度表现出先增后减的变化趋势,出现峰值.增大进气流量和进气臭氧浓度会使峰值减小,并使出峰时间缩短,但会提高初始产出速率;对不同有机物,羟基自由基氧化对甲醛产量的影响不同,氧化丙烯酸和反丁烯二酸时,甲醛积累量减小,而氧化壬基酚和水杨酸等芳香族化合物时,甲醛积累量提高.     

Ru负载促进GeZnNO固溶体光解水反应的机理研究

光催化水分解生成氢气和氧气是解决环境污染和能源危机的方法之一,但当前对光解水的反应机理研究较少.本文通过进一步研究反应路径,以期为合成高效率光解水反应光催化剂提供新思路.采用固态合成法制备了GeZnNO可见光催化剂,并对部分催化剂进行RuO₂改性.同时,通过XRD、BET、UV-vis-DRS、PL等方法对催化剂进行表征.在整个光催化水分解体系中加入可能的中间产物H₂O₂,分别观察·OH和O₂的变化,初步证明H₂O₂是水分解中间产物,并提出相应水分解反应机理.通过在整个光催化水分解体系中加入Fe³⁺,观察·OH和O₂的变化,进一步验证了前面的推测.最终结果表明,H₂O₂是光催化水分解反应体系中氧气生成的中间产物,对整个水分解起着重要作用.同时发现,RuO₂助催化剂不仅具有析氢位点的作用,还能够催化H₂O₂...     

利用电化学方法产生芬顿试剂的探讨与建议

利用电化学法产生Fe2+和H2O2作为芬顿试剂的持续来源,两者生成后立即生成具有高度活性的羟基自由基,使有机物氧化成CO2和H2O.在此,详细阐述了各种电芬顿法的运行机理及其影响因素,简要介绍了电芬顿法在国内外的研究现状,并对其今后的发展趋势进行了展望.     

水中羟基氧化铁催化臭氧分解和氧化痕量硝基苯的机理探讨

测定了木质颗粒活性炭(GAC)和负载在GAC上的羟基氧化铁(FeOOH)催化水中臭氧分解的速率常数并探讨了催化臭氧分解的途径.以水中几种氧化物表面羟基密度和表面零电荷pH值(pH_zpc)为表征氧化物表面性质的参数,考察了2个参数对催化臭氧氧化水中硝基苯的影响.GAC和负载在GAC上的FeOOH使水中臭氧一级分解速率常数分别提高了68%和108%,用叔丁醇捕获掉生成的羟基自由基后,前者的分解速率常数降低了9%,后者降低了20%.GAC在催化臭氧分解时主要起到吸附剂和还原剂的作用,FeOOH催化臭氧分解过程中促进了羟基自由基生成.氧化物表面羟基密度和催化臭氧氧化水中硝基苯的效果之间没有直接的关系,由氧化物的pH_zpc决定的表面电荷状态与催化氧化效果有关,表面接近电中性时对催化氧化硝基苯有利.高密度的表面羟基会使表面羟基之间形成较强的氢键,使催化作用减弱.     

ZnOOH/O3催化臭氧化体系去除水中痕量对氯硝基苯

以实验室制备的羟基化锌(ZnOOH)为催化剂,考察了其催化臭氧化去除水中痕量对氯硝基苯(pCNB)的效能,通过研究自由基抑制试剂叔丁醇对催化效果的影响,推断了催化反应机理,并研究了催化性能的影响因素.结果表明,ZnOOH具有较强的催化臭氧化去除pCNB能力.本实验条件下,蒸馏水中反应20 min时,催化臭氧化比单独臭氧化对pCNB的去除率提高了51.3个百分点;催化过程遵循自由基反应机理,催化剂表面结合的羟基基团有利于催化反应;pCNB的去除效果随催化剂投量的增加而更佳,催化剂重复使用3次后,催化效果基本没有变化,水中的重碳酸盐以及缓冲溶液中的磷酸盐可以明显降低催化活性,中性条件下,催化作用最佳.     

ZnOOH/O3催化臭氧化体系去除水中痕量对氯硝基苯

以实验室制备的羟基化锌（ZnOOH）为催化剂,考察了其催化臭氧化去除水中痕量对氯硝基苯（ppCNB能力.本实验条件下,蒸馏水中反应20　min时,催化臭氧化比单独臭氧化对pCNB的去除率提高了51 .3个百分点;催化过程遵循自由基反应机理,催化剂表面结合的羟基基团有利于催化反应;pCNB的去除效果随催化剂投量的增加而更佳,催化剂重复使用3次后,催化效果基本没有变化,水中的重碳酸盐以及缓冲溶液中的磷酸盐可以明显降低催化活性,中性条件下,催化作用最佳.     

臭氧氧化水中2,4,6-三氯酚的反应机理研究

研究了臭氧氧化对2,4,6-三氯酚的去除效果,以及氧化过程中过氧化氢、氯离子、甲酸和乙二酸的变化情况,探讨了臭氧氧化2,4,6-三氯酚的反应机理和反应途径.实验结果表明,如果溶液中没有自由基清除剂,在臭氧投加量为24mg·L~(-1)时,0·1mmol·L~(-1)的2,4,6-三氯酚在6min内,去除率可达99%.臭氧分子氧化2,4,6-三氯酚的过程中产生过氧化氢,检测到的过氧化氢的最大摩尔浓度为初始2,4,6-三氯酚摩尔浓度的22·5%.中间产物过氧化氢随后和臭氧反应生成大量的羟基自由基,此时2,4,6-三氯酚是被臭氧和羟基自由基联合氧化,生成甲酸和乙二酸.当溶液中含有大量的自由基清除剂时,2,4,6-三氯酚首先被臭氧分子氧化成黄色的氯代对苯醌,然后氧化成甲酸和乙二酸.臭氧氧化2,4,6-三氯酚存在臭氧分子氧化以及O3/OH·联合氧化两种反应途径.     

Pathway of the ozonation of 2,4,6-trichlorophenol in aqueous solution

The reaction mechanism and pathway of the ozonation of 2,4,6-trichlorophenol (2,4,6-TCP) in aqueous solution were investigated. The removal efficiency and the variation of H₂O₂, Cl⁻ formic acid, and oxalic acid were studied during the semi-batch ozonation experiments (continuous for ozone gas supply, fixed volume of water sample). The results showed that when there was no scavenger, the removal efficiency of 0.1 mmol/L 2,4,6-TCP could reach 99% within 6 min by adding 24 mg/L ozone. The reaction of molecular ozone with 2,4,6-TCP resulted in the formation of H₂O₂. The maximal concentration of H₂O₂ detected during the ozonation could reach 22.5% of the original concentration of 2,4,6-TCP. The reaction of ozone with H₂O₂ resulted in the generation of a lot of OH• radicals. Therefore, 2,4,6-TCP was degraded to formic acid and oxalic acid by ozone and OH• radicals together. With the inhibition of OH• radicals, ozone molecule firstly degraded 2,4,6-TCP to form chlorinated quinone, which was subsequently oxidized to formic acid and oxalic acid. Two reaction pathways of the degradation of 2,4,6-TCP by ozone and O₃/OH• were proposed in this study. Translated from Acta Scientiae Circumstantiae, 2005, 25(12): 1619–1623 [译自: 环境科学学报]     

Degradation kinetics and mechanism of trace nitrobenzene by granular activated carbon enhanced microwave/hydrogen peroxide system

The kinetics of the degradation of trace nitrobenzene (NB) by a granular activated carbon (GAC) enhanced microwave (MW)/hydrogen peroxide (H₂O₂) system was studied. Effects of pH, NB initial concentration and tert-butyl alcohol on the removal efficiency were examined. It was found that the reaction rate fits well to first-order reaction kinetics in the MW/GAC/H₂O₂ process. Moreover, GAC greatly enhanced the degradation rate of NB in water. Under a given condition (MW power 300 W, H₂O₂ dosage 10 mg/L, pH 6.85 and temperature (60±5)℃), the degradation rate of NB was 0.05214 min^-1 when 4 g/L GAC was added. In general, alkaline pH was better for NB degradation; however, the optimum pH was 8.0 in the tested pH value range of 4.0-12.0. At H₂O₂ dosage of 10 mg/L and GAC dosage of 4 g/L, the removal of NB was decreased with increasing initial concentrations of NB, indicating that a low initial concentration was beneficial for the degradation of NB. These results indicated that the MW/GAC/H₂O₂ process was effective for trace NB degradation in water. Gas chromatography-mass spectrometry analysis indicated that a hydroxyl radical addition reaction and dehydrogenation reaction enhanced NB degradation.     

Formation mechanisms of nitrous acid (HONO) during the haze and non-haze periods in Beijing, China

As an important precursor of hydroxyl radical (OH), nitrous acid (HONO) plays a significant role in atmospheric chemistry. Here, an observation of HONO and relevant air pollutants in an urban site of Beijing from 14 to 28 April, 2017 was performed. Two distinct peaks of HONO concentrations occurred during the observation. In contrast, the concentration of particulate matter in the first period (period Ⅰ) was significantly higher than that in the second period (period Ⅱ). Comparing to HONO sources in the two periods, we found that the direct vehicle emission was an essential source of the ambient HONO during both periods at night, especially in period Ⅱ. The heterogeneous reaction of NO₂ was the dominant source in period Ⅰ, while the homogeneous reaction of NO with OH was more critical source at night in period Ⅱ. In the daytime, the heterogeneous reaction of NO₂ was a significant source and was confirmed by the good correlation coefficients (R²) between the unknown sources (P_unknown) with NO₂, PM_2.5, NO₂ × PM_2.5 in period Ⅰ. Moreover, when solar radiation and OH radicals were considered to explore unknown sources in the daytime, the enhanced correlation of P_unknown with photolysis rate of NO₂ and OH ($J_{{\mathrm{NO}}_2}$ × OH) were 0.93 in period Ⅰ, 0.95 in period Ⅱ. These excellent correlation coefficients suggested that the unknown sources released HONO highly related to the solar radiation and the variation of OH radicals.     

Formation control of bromate and trihalomethanes during ozonation of bromide-containing water with chemical addition: Hydrogen peroxide or ammonia?

To ensure the safety of drinking water, ozone (O₃) has been extensively applied in drinking water treatment plants to further remove natural organic matter (NOM). However, the surface water and groundwater near the coastal areas often contain high concentrations of bromide ion (Br^?). Considering the risk of bromate (BrO₃^?) formation in ozonation of the sand-filtered water, the inhibitory efficiencies of hydrogen peroxide (H₂O₂) and ammonia (NH₃) on BrO₃^? formation during ozonation process were compared. The addition of H₂O₂ effectively inhibited BrO₃^? formation at an initial Br^? concentration amended to 350 µg/L. The inhibition efficiencies reached 59.6 and 100% when the mass ratio of H₂O₂/O₃ was 0.25 and > 0.5, respectively. The UV₂₅₄ and total organic carbon (TOC) also decreased after adding H₂O₂, while the formation potential of trihalomethanes (THMsFP) increased especially in subsequent chlorination process at a low dose of H₂O₂. To control the formation of both BrO₃^? and THMs, a relatively large dose of O₃ and a high ratio of H₂O₂/O₃were generally needed. NH₃ addition inhibited BrO₃^? formation when the background ammonia nitrogen (NH₃N) concentration was low. There was no significant correlation between BrO₃^? inhibition efficiency and NH₃ dose, and a small amount of NH₃N (0.2 mg/L) could obviously inhibit BrO₃^? formation. The oxidation of NOM seemed unaffected by NH₃ addition, and the structure of NOM reflected by synchronous fluorescence (SF) scanning remained almost unchanged before and after adding NH₃. Considering the formation of BrO₃^? and THMs, the optimal dose of NH₃ was suggested to be 0.5 mg/L.     

Degradation of 2,4-dichlorophenoxyacetic acid in water by ozone-hydrogen peroxide process

IntroductionAt present, several types of organic pollutantsreferred to as environmental endocrine disruptors(ED) have been suggested to be associated withabnormal sexual development (Hu, 2000). It wasreported that the ED led to the decline of reproductive…     

催化臭氧化降解磺基水杨酸

选用3种固体催化剂催化臭氧化降解磺基水杨酸.结果表明,MnO₂和V₂O₅催化活性并不明显,而自制的钒氧化物(VO)催化剂具有较好的催化臭氧化性能.在本实验条件下与单独臭氧化相比,30min后VO/O₃体系的COD和TOC去除率由原来的58%和25%提高到86%和61%.VO催化剂的作用机理是催化臭氧分解产生了高活性氧化剂(如羟基自由基等).     

H2O2湿式氧化处理含酸性红B染料模拟废水的研究

用H2 O2 作氧化剂 ,在连续式的压力反应器内探索了WPO(过氧化氢湿式氧化法 )、CWPO(催化过氧化氢湿式氧化法 )氧化降解含酸性红B染料模拟废水的过程 ,分别考察温度、压力、氧化剂量及催化剂对反应过程与对象污染物降解的影响规律 .结果表明 ,与常规湿式氧化法相比 ,WPO能在较低的温度和压力下降解结构稳定的有机物 ,在 2 2 0℃、8min、0 1MPa时 ,含1 5 0 0mg·L-1 酸性红B染料模拟废水的COD和色度的去除率分别达到 6 0 5 0 %和 96 80 % .同时发现 ,通过升温和增加过氧化氢的投加量不能够使废水COD和色度的去除率进一步提高 ,故引入Cu2 作催化剂来实现CWPO过程 ,在 2 2 0℃、8min、0 1MPa条件下 ,CWPO对同一废水的COD和色度的去除率分别达到 82 5 0 %和 99 71 % .通过计算得出CWPO与WPO相比基于COD的表观活化能降低了 6 5 93 % .