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221.
222.
The thermal hazards of dicumyl peroxide (DCP) and benzoyl peroxide (BPO), self-reactive chemicals are identified and characterized using high-pressuredifferential scanning calorimeter, and simultaneous thermogravimetric analyzer, a C80 micro-calorimeter is used. The apparent exothermic onset temperature of DCP is found to be between the range of 112–122 °C for different heating rates in DSC tests. There are two coupled peaks of BPO around 105 °C at both the heating rates of 4.0 and 8.0 °C/min while no endothermic peak showed at lower heating rates. Furthermore, another endothermic peak appears immediately after the exothermic peak at about 211 °C of DCP under high-pressure conditions. For BPO, the endothermic peak before the exothermic peak disappears as the pressure increases to 1.0 and 1.5 MPa. The average values of apparent activation energy calculated by Flynn-Wall-Ozawa and Kissinger-Akahira-Sunose methods during the conversion rate between 15 and 75% of DCP are 80.69 and 74.05 kJ/mol, and that of BPO are 119.96 and 112.93 kJ/mol, respectively. According to the isothermal tests, the thermal decomposition of DCP behaviors is an n-th order reaction while BPO conforms to the laws of autocatalytic reaction. 相似文献
223.
Microwave and Fenton's reagent oxidation of wastewater 总被引:16,自引:0,他引:16
J.?Sanz J.?I.?Lombra?aEmail author A.?M.?De Luis M.?Ortueta F.?Varona 《Environmental Chemistry Letters》2003,1(1):45-50
We compared two H2O2 oxidation methods for the treatment of industrial wastewater: oxidation using Fenton's reagent [H2O2/Fe(II)] and microwave irradiation. Both methods were applied to the treatment of synthetic phenol solutions (100 mg L−1) and of an industrial effluent containing a mixture of ionic and non-ionic surfactants at high load (20 g L−1 of COD). The effects of initial pH, initial H2O2 concentration, Fenton catalyst amount and irradiation time were assessed. According to the oxidation of phenol, it has been
found that the oxidation by Fenton's reagent is dependent on the pH, contrary to the microwave system, which is not influenced
by this parameter. For both systems, a limiting amount of oxidant has been found; above this point the oxidation of phenol
is not improved by a further addition of peroxide. The oxidation of the industrial surfactant effluent has only been successful
with the Fenton's reagent. In this case, large amounts of ferrous ions are necessary for the precipitation of the ionic surfactants
of the effluent, followed by the oxidation of the non-ionic constituents of the solution.
Electronic Publication 相似文献
224.
Trihalomethanes (THMs) the by-products of chlorination in water treatment are recognised as a threat to public health due
to their carcinogenicity. The photodegradation of THMs using hydrogen peroxide has been found to give increased removal efficiency
and the outcome of the study may find, its application in designing a unit process for water treatment. Batch experiments
were carried out using UV lamp of 83 W and 40% w/w Hydrogen peroxide (H2O2) in test waters between 2.5–10 pH range of chloroform, bromodichloromethane, dibromochloromethane and bromoform at 50–200
μg L−1 initial concentration. 92–100% removal of chloroform, bromodichloromethane, dibromochloromethane and bromoform were found
with 0.1% of H2O2 and 90 min of UV exposure. 相似文献
225.
采用化学浸渍法将Fe@Fe2O3纳米线负载在活性炭纤维/泡沫镍上组成Fe@Fe2O3/ACF/Ni复合阴极,以钛基铂(Pt/Ti)为阳极,考察载铁量、初始pH值和不同电化学体系对除藻效果的影响,探究无供氧条件下Pt/Ti-Fe@Fe2O3/ACF/Ni电化学体系除藻的效能;基于·OH间接检测、铁离子浓度、H2O2浓度及pH值的分析和·O2-的检测研究Pt/Ti-Fe@Fe2O3/ACF/Ni中性电化学体系反应机制.结果表明,当制备阴极阶段投加0.03g FeCl3×6H2O,初始藻浓度为0.7×109~0.8×109个/L,电流密度为75mA/cm2,初始pH6.2时,电解60min,该体系除藻率可达到92.3%.在Pt/Ti-Fe@Fe2O3/ACF/Ni电化学体系中,Fe@Fe2O3/ACF/Ni阴极可通过电化学反应产生大量·OH和·O2-,使藻细胞破裂死亡;该体系除藻的主要机理是非均相电Fenton反应. 相似文献
226.
活性炭纤维电极产生过氧化氢的影响因素与机制研究 总被引:3,自引:1,他引:2
以活性炭纤维为阴极、RuO2/Ti网为阳极、Na2SO4为支持电解质的电化学体系为研究对象,研究了电流强度、pH值和溶解氧含量等主要参数对电化学体系产生H2O2的影响.结果显示,在电流强度0.12~0.50 A范围内,H2O2的生成量随着电流强度增大而升高,反应60 min后,H2O2浓度可达稳定值;电化学体系具有较宽泛的pH范围,初始pH在2.0~6.0时活性炭纤维阴极产生的H2O2均高于500μmol.L-1,pH 2.0时H2O2生成量最大,可达575.8μmol.L-1;体系中溶解氧浓度影响H2O2的电化学生成量,溶解氧浓度越高H2O2生成量越大;无背景气体通入时,电化学体系自身产生的溶解氧可以支持活性炭纤维阴极产生高浓度的H2O2.研究结果表明具有高比表面积的活性炭纤维电极是一种高效的电-Fenton阴极. 相似文献
227.
Yingying You Shaobin Huang Xuesong Zhao Han Li Fangqin Cheng Jinhua Wu Yongqing Zhang Shaofeng Zhou 《环境科学学报(英文版)》2019,31(9):39-45
This study for the first time proposed an efficient microbial electrolyte/UV system for Methyl Orange decomposition. With an external applied voltage of 0.2 V and cathode aeration of20 mL/min, H_2O_2 could be in-situ generated from two-electron reduction of oxygen in cathode, reaching to 8.1 mg/L in 2 hr and continued to increase. The pollutant removal efficiency of approximate 94.7% was achieved at initial neutral pH, with the activation of ·OH in the presence of UV illumination. Although the nature of its guiding principles remain on the vista of practical exploration, this proof-of-concept study provides an alternative operation pattern of solar–microbial hybrid technology for future wastewater treatment from a basic but multidisciplinary view. 相似文献
228.
采用等体积浸渍法制备了一种新型Fe-Mn/AC催化剂,应用于催化湿式过氧化氢氧化(CWPO)间甲酚废水.通过SEM和XRF表征了其表面形态结构和元素组成,通过穆斯堡尔谱分析了催化剂中铁离子的存在形态,结果表明,新型Fe-Mn/AC催化剂中的铁以二价铁、三价铁以及四氧化三铁的形式存在.通过正交实验考察了CWPO降解间甲酚的影响因素,结果表明,各因素对间甲酚转化率影响的大小顺序依次为:底物初始p H值反应温度反应时间催化剂投加量.通过正交实验得到CWPO降解间甲酚的最佳反应条件.当间甲酚浓度为100 mg·L-1、反应温度为40℃、反应时间为40 min、催化剂投加量为0.6 g·L-1及底物初始p H值为3时,间甲酚转化率为99.8%,TOC去除率为28.3%.气相色谱/质谱联用没有检测到中间产物,气相色谱检测到CWPO降解间甲酚中间产物主要为乙酸和丙酸. 相似文献
229.
电芬顿反应原理研究进展 总被引:6,自引:0,他引:6
电芬顿法作为一种新型电化学氧化技术,因其强氧化能力以及环境友好的特性引起了国内外的广泛关注.电芬顿反应通过电极产生H2O2和(或)Fe2+,进行一系列反应生成具有强氧化能力的羟基自由基·OH.为了提高电子传递速度,产生更多芬顿试剂,国内外学者研发出不同类型的电芬顿反应器.通过分析电芬顿反应中·OH浓度与有机物浓度间的关系,大多数学者在准一级反应动力学基础上确定了反应常数,然而,目前其应用仍只停留在实验室阶段,电芬顿技术的效率及机理仍需要进一步研究改进. 相似文献
230.
To solve the problem of shortened backwashing intervals in groundwater plants, several disinfectants including ozone (O3), hydrogen peroxide (H2O2) and chlorine dioxide (ClO2) were examined to peel off the film from the quartz sand surface in four pilot-scale columns. An optimized oxidant dosage and oxidation time were determined by batch tests. Subsequently, the optimized conditions were tested in the four pilot-scale columns. The results demonstrated that the backwashing intervals increased from 35.17 to 54.33 (H2O2) and to 53.67 hr (ClO2) after the oxidation treatments, and the increase of backwashing interval after treatment by O3 was much less than for the other two treatments. Interestingly, the treatment efficiency of filters was not affected by O3 or H2O2 oxidation; but after oxidation by ClO2, the treatment efficiency was deteriorated, especially the ammonia removal (from 96.96% to 24.95%). The filter sands before and after the oxidation were characterized by scanning electron microscopy and X-ray photoelectron spectroscopy. Compared with the oxidation by O3 and H2O2, the structures on the surface of filter sands were seriously damaged after oxidation by ClO2. The chemical states of manganese on the surfaces of those treated sands were only changed by ClO2. The damage of the structures and the change of the chemical states of manganese might have a negative effect on the ammonia removal. In summary, H2O2 is a suitable agent for film peeling. 相似文献