首页|多金属掺杂尖晶石型催化剂制备及催化臭氧降解苯酚

多金属掺杂尖晶石型催化剂制备及催化臭氧降解苯酚

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采用水热合成法制备尖晶石型铁氧体,并对其M位掺杂多种金属离子以改性得到一系列催化剂,筛选后用于催化臭氧氧化降解苯酚。结果显示:与其他催化剂相比,Mn0。5Co0。5Fe2O4催化剂催化性能最佳,在苯酚质量浓度为30 mg/L,催化剂投加质量浓度为1 g/L,臭氧质量浓度为6 mg/L,流速为1 L/min并反应75 min时,化学需氧量(Chemical Oxygen Demand,COD)和苯酚的去除率分别可以达到90。11%和89。36%,较相同条件下单独臭氧氧化对COD和苯酚的去除率分别提高了31。16百分点和30。51百分点。利用X射线衍射(X-ray Diffraction,XRD)、X射线光电子能谱(X-ray Photoelectron Spectroscopy,XPS)、电子顺磁共振(Electron Paramagnetic Resonance,EPR)等多种手段对该催化剂进行了表征,发现催化剂纯度较高,晶化程度好。此外,通过猝灭和自由基捕获试验表明体系中·OH和1O2参与了苯酚降解反应。催化剂循环试验表明,Mn0。5Co0。5Fe2O4催化剂具有优异的催化稳定性和重复利用性。
Preparation of multimetal-doped spinel-type catalysts and their application in ozone degradation of phenol
Spinel-shaped ferrite was synthesized using the hydrothermal method,with various metal ions employed to modify the catalyst through doping at the M site.A total of seven catalysts were prepared and screened for their effectiveness in the catalytic ozonation degradation of phenol.The results indicated that the catalytic efficiency of these seven catalysts in the ozonation process was consistent with the observed trends in Chemical Oxygen Demand(COD)removal.When the mass concentration of phenol was set at 30 mg/L,the catalyst concentration at 1 g/L,and the ozone concentration at 6 mg/L,with a flow rate of 1 L/min and a reaction time of 75 minutes,the catalytic efficiency for phenol ozonation was highest for Mn0.5Cu0.5Fe2O4.The efficiency of the other catalysts,in descending order,was as follows:Mn0.5Co0.5Fe2O4,Ni0.5Cu0.5Fe2O4,Zn0.5Cu0.5Fe2O4,Co0.5Cu0.5Fe2O4,Ni0.5Co0.5Fe2O4,and Zn0.5Co0.5Fe2O4.All these catalysts demonstrated higher catalytic efficiency compared to ozone oxidation alone.Considering cost and safety,the Mn0.5Co0.5Fe2O4 catalyst was selected for subsequent experiments.To further investigate its catalytic performance,single metal catalysts MnFe2O4 and CoFe2O4 were also prepared.Under conditions where the mass concentration of phenol was 30 mg/L,the catalyst concentration was 1 g/L,the ozone concentration was 6 mg/L,the flow rate was 1 L/min,and the reaction time was 75 minutes,the removal rates of COD and phenol reached 90.11%and 89.36%,respectively.Compared to other catalysts under the same conditions,the removal rates of COD achieved by ozone oxidation alone,MnFe2O4,and CoFe2O4 increased by 31.16 percentage points,17.41 percentage points,and 4.31 percentage points,respectively.Similarly,the removal rates of phenol improved by 30.51 percentage points,22.23 percentage points,and 8.13 percentage points,respectively.The catalyst was characterized using several methods,including X-ray Diffraction(XRD)and X-ray Photoelectron Spectroscopy(XPS).The results indicated high purity of the catalyst,a favorable degree of crystallization,and successful loading of manganese(Mn)and cobalt(Co)elements.A catalyst cycling test was performed,demonstrating that the Mn0.5Co0.5Fe2O4 catalyst exhibits excellent catalytic stability and reusability.Quenching experiments were conducted,and Electron Paramagnetic Resonance(EPR)was employed to detect free radicals,confirming the involvement of·OH and 1O2 in the phenol degradation reaction within the system.Based on the experimental results,the formation process of free radicals during the Mn0.5Co0.5Fe2O4-catalyzed ozonation degradation of phenol was inferred.

environmental engineeringcatalytic ozonationphenolhydroxyl radicalssinglet oxygen

刘艳芳、张妙雨、刘文佳、杨梦鑫、孔兴华、任少勃、王崇璞、李欢欢、李贵霞

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河北科技大学环境科学与工程学院,石家庄 050018

河北科技大学建筑工程学院,石家庄 050018

河北协同水处理技术有限公司,石家庄 050000

环境工程学 催化臭氧氧化 苯酚 羟基自由基 单线态氧

河北省重点研发计划项目

21373602D

2024

安全与环境学报
北京理工大学 中国环境科学学会 中国职业安全健康协会

安全与环境学报

CSTPCD北大核心
影响因子:0.943
ISSN:1009-6094
年,卷(期):2024.24(10)
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