SO2气氛下Cu-Ce-O催化剂氧化柴油车排气碳烟的性能

运用程序升温氧化(TPO)对共沉淀法合成的Cu-Ce-O催化剂进行了活性评价,考察了在不同浓度的S0,气氛下cu-Ce-O催化剂氧化模拟碳黑的性能,并用BET、XRD、TPR和FT-IR对催化剂进行了表征.BET和XRD测试显示,cu和ce的结合使催化剂比表面积增大,晶体结构发生变化,形成了复合氧化物;TPO活性测试结果表明,Cu-Ce-O复合催化剂比单一组分的CuO或CeO2具有更好的低温催化活性.复合氧化物cu-Ce-O中Cu原子含量越高,对应硫化后的催化剂氧化碳烟的能力越低,同时催化剂表面生成的硫酸盐越多,即催化剂抗硫中毒能力也降低.浓度低于0.03%的SO2对Cu-Ce-O的催化性能有一定的促进作用,但SO2的体积分数超过0.03%后碳黑燃烧速率变慢;FT-IR初步证实了高体积分数的SO2所产生的大量SO24-可能是抑制催化剂活性的原因.     

Size effect of Pt nanoparticles in acid-assisted soot oxidation in the presence of NO

Pt/Al₂O₃ catalysts with mean Pt particle size ranged from 2.7 to 7.1 nm were synthesized by chemical reduction method, and the sulfated counterparts were prepared by impregnation of sulfuric acid. The turnover frequency of platinum for soot oxidation under loose contact conditions in a feed flow containing NO and O₂ are positively correlated with the size of platinum. The sulfated Pt/Al₂O₃ exhibits higher catalytic activity for soot oxidation in the presence of NO despite their reduced ability for NO₂ production. Such a contradiction is more significant for those catalysts with smaller platinum particles. Herein, the catalysts were characterized by X-ray diffraction (XRD), Brunauer-Emmett-Teller (BET), transmission electron microscopy (TEM), inductive coupled plasma (ICP) emission spectrometry, CO chemisorption, thermogravimetric analysis (TGA), NH₃ temperature-programmed desorption (NH₃-TPD), NO temperature-programmed oxidation (TPO) and NO_x temperature-programmed desorption (TPD). Possible effect of Pt particle size for the catalytic oxidation of soot in the presence of NO was presented based primarily on the promoted NO₂ transfer efficiency onto the soot pushed by the acidic catalysts.     

Removal of formaldehyde over MnxCe1-xO2 catalysts: Thermal catalytic oxidation versus ozone catalytic oxidation

MnxCe1- xO2（x： 0.3–0.9） prepared by Pechini method was used as a catalyst for the thermal catalytic oxidation of formaldehyde（HCHO）. At x = 0.3 and 0.5, most of the manganese was incorporated in the fluorite structure of Ce O2 to form a solid solution. The catalytic activity was best at x = 0.5, at which the temperature of 100% removal rate is the lowest（270°C）. The temperature for 100% removal of HCHO oxidation is reduced by approximately 40°C by loading 5 wt.% Cu Oxinto Mn0.5Ce0.5O2. With ozone catalytic oxidation, HCHO（61 ppm） in gas stream was completely oxidized by adding 506 ppm O3 over Mn0.5Ce0.5O2 catalyst with a GHSV（gas hourly space velocity） of 10,000 hr-1at 25°C. The effect of the molar ratio of O3 to HCHO was also investigated. As O3/HCHO ratio was increased from 3 to 8, the removal efficiency of HCHO was increased from 83.3% to 100%. With O3/HCHO ratio of 8, the mineralization efficiency of HCHO to CO2 was 86.1%. At 25°C, the p-type oxide semiconductor（Mn0.5Ce0.5O2） exhibited an excellent ozone decomposition efficiency of 99.2%,which significantly exceeded that of n-type oxide semiconductors such as Ti O2, which had a low ozone decomposition efficiency（9.81%）. At a GHSV of 10,000 hr-1, [O3]/[HCHO] = 3 and temperature of 25°C, a high HCHO removal efficiency（≥ 81.2%） was maintained throughout the durability test of 80 hr, indicating the long-term stability of the catalyst for HCHO removal.     

Effect of pretreatment on Pd/Al2O3 catalyst for catalytic oxidation of o-xylene at low temperature

The effect of pretreatment on Pd/Al₂O₃ catalysts for the catalytic oxidation of o-xylene at low temperature was studied by changing the pretreatment and testing conditions. The fresh and pretreated Pd/Al₂O₃ catalysts were characterized by transmission electron microscopy (TEM), X-ray photoelectron spectroscopy (XPS) and X-ray diffraction (XRD). The results showed that the pretreatment dramatically changed the Pd/PdO ratio and then significantly affected the Pd/Al₂O₃ activity; while the pretreatment had not much influence on Pd particle size. The Pd/Al₂O₃ pre-reduced at 300℃/400℃, which has fully reduced Pd species, showed the highest activity; while the fresh Pd/Al₂O₃, which has fully oxidized Pd species, presented the worst performance, indicating the Pd chemical state plays an important role in the catalytic activity for the o-xylene oxidation. It is concluded that metallic Pd is the active species on the Pd/Al₂O₃ catalyst for the catalytic oxidation of o-xylene at low temperature.     

Effects of synthesis methods on the performance of Pt + Rh/Ce0.6Zr0.4O2 three-way catalysts

The 0.7 wt% Pt + 0.3 wt% Rh/Ce0.6Zr0.4O2 catalysts were fabricated via different methods, including ultrasonic-assisted membrane reduction(UAMR) co-precipitation, UAMR separation precipitation, co-impregnation, and sequential impregnation. The catalysts were physico-chemically characterized by N2 adsorption, XRD, TEM, and H2-TPR techniques, and evaluated for three-way catalytic activities with simulated automobile exhaust. UAMR co-precipitation- and UAMR separation precipitationprepared catalysts exhibited a high surface area and metal dispersion, wide λ window and excellent conversion for NOx reduction under lean conditions. Both fresh and aged catalysts from UAMRprecipitation showed the high surface areas of ca. 60–67 m2/g and 18–22 m2/g, respectively, high metal dispersion of 41%–55%, and small active particle diameters of 2.1–2.7 nm. When these catalysts were aged, the catalysts prepared by the UAMR method exhibited a wider working window(Δλ = 0.284–0.287) than impregnated ones(Δλ = 0.065–0.115) as well as excellent three-way catalytic performance, and showed lower T50(169.C) and T90(195.C) for NO reduction than the aged catalysts from impregnation processes, which were at 265 and 309.C, respectively. This implied that the UAMR-separation precipitation has important potential for industrial applications to improve catalytic performance and thermal stability. The fresh and aged 0.7 wt% Pt + 0.3 wt% Rh/Ce0:6Zr0:4O2 catalysts prepared by the UAMR-separation precipitation method exhibited better catalytic performance than the corresponding catalysts prepared by conventional impregnation routes.     

Effects of WOx modification on the activity, adsorption and redox properties of CeO2 catalyst for NOx reduction with ammonia

A series of WO₃/CeO₂ (WOx/CeO₂) catalysts were synthesized by wet impregnation of ammonium metatungstate on a CeO₂ support. The resulting solid acid catalysts were characterized by X-ray diffraction (XRD), UV-Vis spectroscopy (UV-Vis), Raman spectroscopy (Raman), in-situ Fourier transform infrared spectroscopy (in-situ FT-IR) of ammonia adsorption, NH₃-TPD, H₂ temperature-programmed reduction (H₂-TPR), NH₃/NO oxidation and activity measurements for NOx reduction by NH₃ (NH₃-SCR). The results show that polytungstate (WOx) species are the main species of tungsten oxide on the surface of ceria. The addition of tungsten oxide enhances the Brönsted acidity of ceria catalysts remarkably and decreases the amount of surface oxygen on ceria, with strong interaction between CeO₂ and WOx. As a result, the N₂ selectivity of NH₃ oxidation and NH₃-SCR at high temperatures (> 300℃) is enhanced. Therefore, a wide working temperature window in which NOx conversion exceeds 80% (NOx conversion > 80%) from 200 to 450℃, is achieved over 10 wt.% WOx/CeO₂ catalyst. A tentative model of the NH₃-SCR reaction route on WOx/CeO₂ catalysts is presented.     

Characterization and performance of Pt/SBA-15 for low-temperature SCR of NO by C3H6

Pt supported on mesoporous silica SBA-15 was investigated as a catalyst for low temperature selective catalytic reduction(SCR) of NO by C 3 H 6 in the presence of excess oxygen.The prepared catalysts were characterized by means of XRD,BET surface area,TEM,NO-TPD,NO/C 3 H 6-TPO,NH 3-TPD,XPS and 27 Al MAS NMR.The effects of Pt loading amount,O 2 /C 3 H 6 concentration,and incorporation of Al into SBA-15 have been studied.It was found that the removal efficiency increased significantly after Pt loading,but an optimal loading amount was observed.In particular,under an atmosphere of 150 ppm NO,150 ppm C 3 H 6,and 18 vol.% O 2,0.5% Pt/SBA-15 showed remarkably high catalytic performance giving 80.1% NOx reduction and 87.04% C 3 H 6 conversion simultaneously at 140°C.The enhanced SCR activity of Pt/SBA-15 is associated with its outstanding oxidation activities of NO to NO 2 and C 3 H 6 to CO 2 in low temperature range.The research results also suggested that higher concentration of O 2 and higher concentration of C 3 H 6 favored NO removal.The incorporation of Al into SBA-15 improved catalytic performance,which could be ascribed to the enhancement of catalyst surface acidity caused by tetrahedrally coordinated AlO 4.Moreover,the catalysts could be easily reused and possessed good stability.     

MO_x-CeO_2/HZSM-5催化剂催化氧化含氯挥发性有机物研究

采用浸渍法制备了不同过渡金属掺杂的MOx-CeO2/HZSM-5（M分别表示Cr、Mn、Fe、Co、Ni和Cu）催化剂,研究了各催化剂对1,2-二氯乙烷（DCE）的催化降解性能.结果表明,过渡金属掺杂后,MOx-12%CeO2/HZSM-5催化剂催化氧化1,2-二氯乙烷（DCE）的活性明显提高.各催化剂（记为M-CeO...     

Numerical evaluation of the effectiveness of NO2 and N2O5 generation during the NO ozonation process

Wet scrubbing combined with ozone oxidation has become a promising technology for simultaneous removal of SO₂ and NO_x in exhaust gas. In this paper, a new 20-species, 76-step detailed kinetic mechanism was proposed between O₃ and NO_x. The concentration of N₂O₅ was measured using an in-situ IR spectrometer. The numerical evaluation results kept good pace with both the public experiment results and our experiment results. Key reaction parameters for the generation of NO₂ and N₂O₅ during the NO ozonation process were investigated by a numerical simulation method. The effect of temperature on producing NO₂ was found to be negligible. To produce NO₂, the optimal residence time was 1.25 sec and the molar ratio of O₃/NO about 1. For the generation of N₂O₅, the residence time should be about 8 sec while the temperature of the exhaust gas should be strictly controlled and the molar ratio of O₃/NO about 1.75. This study provided detailed investigations on the reaction parameters of ozonation of NO_x by a numerical simulation method, and the results obtained should be helpful for the design and optimization of ozone oxidation combined with the wet flue gas desulfurization methods (WFGD) method for the removal of NO_x.     

铜铈复合氧化物上石化行业典型VOCs的氧化行为与动力学

采用共沉淀法和等体积浸渍法制备了CuCeO x复合催化剂,对材料的物化性质进行了XRD、低温N2吸脱附、H2-TPR和O2-TPD表征.以石化行业典型VOCs(苯、甲苯和正己烷)为探针污染物,研究了污染物组成与浓度、反应空速、O2浓度、H2O浓度和催化剂种类对其氧化行为的影响,并对反应动力学参数进行了模型拟合.共沉淀得到的催化剂具有均匀的活性相、好的低温可还原性能和较多的活性表面氧物种.甲苯氧化率随着污染物浓度升高而降低,高转化率下苯浓度与其氧化率无相关性,正己烷的氧化率与入口浓度呈正比.苯能够显著抑制甲苯的氧化,而甲苯加入有利于苯的氧化.正己烷对苯氧化的影响较小,但能够促进甲苯的转化,苯系物对正己烷氧化有明显的抑制作用.低空速和高氧浓度都有利于污染物的氧化,氧浓度的变化对正己烷和苯的氧化影响较小.水汽对甲苯的氧化有明显的抑制作用,而对苯和正己烷氧化有明显的促进作用.共沉淀催化剂具有更好的甲苯和苯氧化性能,而无水条件下浸渍催化剂具有更好的正己烷氧化性能.拟一级动力学模型能够很好地模拟不同条件下污染物的氧化行为.     

EGR率对农用单缸柴油机燃用生物柴油的NOx与PM排放特性影响分析

单缸柴油机作为小型农用机械不可或缺的动力源,在使用过程中会产生大量污染物.其中氮氧化合物（NO_x）和颗粒（PM）是气溶胶的主要组成部分,对大气环境造成了严重污染.为有效改善农用单缸柴油机NO_x和PM排放,本研究通过添加生物柴油对柴油进行改质以及采用机内EGR净化技术两种方案,测量了柴油机分别燃用柴油B0,生物柴油调合燃料B20、B50在不同EGR率下的NO_x和PM排放.结果表明,采用EGR技术能够明显改善柴油机的NO_x排放,但同时会引起碳烟排放的增加.通过在柴油中添加生物柴油能够在一定程度上降低碳烟排放,其中高负荷、大EGR率条件下的改善最为明显.在2000 r·min^-1、75%负荷,EGR率为30%时,燃用B50的碳烟排放与燃用B0相比降低了47.3%.总体上柴油中添加生物柴油与EGR技术共同作用能够有效降低柴油机高负荷工况时的颗粒排放总数量.     

SO2对MnOx/PG催化剂低温脱硝的影响机理研究

采用等体积浸渍法制备了锰氧化物负载凹凸棒石(MnO_x/PG)低温SCR催化剂,通过SO₂暂态响应、程序升温表面反应(TPSR)等实验技术研究了烟气中SO₂对催化剂SCR脱硝活性的影响行为.采用程序升温脱附(TPD)、BET比表面及孔径分布测定、XPS等表征技术对催化剂硫中毒的机理及化学本质进行了深入分析.结果表明,低温下烟气中SO₂对MnO_x/PG催化剂的SCR脱硝活性存在显著的抑制作用,催化剂中毒主要由烟气中SO₂的催化氧化引起.一方面SO₂氧化为SO₃后与NH₃及H₂O竞争反应形成复杂的硫酸铵盐堵塞催化剂孔道,另一方面与活性组分MnO₂结合形成MnSO₄使得部分活性组分形态发生变迁.其中硫酸铵盐的形成可通过适当的热处理得以去除,而MnSO₄则不可恢复,但催化剂SCR活性却显著增加,表明MnSO₄的形成不是催化剂失活的主要因素.吸附态的硫可显著增加催化剂表面酸性,因此对SCR活性有促进作用.催化剂失活主要机理为:由气相SO₂的连续氧化并与NH₃相结合形成硫酸铵盐,并且在低温下难以分解,以致堵塞催化剂活性中心.     

Effect of TiO2 calcination temperature on the photocatalytic oxidation of gaseous NH3

Carbon-modified titanium dioxide(TiO2) was prepared by a sol-gel method using tetrabutyl titanate as precursor, with calcination at various temperatures, and tested for the photocatalytic oxidation(PCO) of gaseous NH3 under visible and UV light. The test results showed that no samples had visible light activity, while the TiO2 calcined at 400℃ had the best UV light activity among the series of catalysts, and was even much better than the commercial catalyst P25. The catalysts were then characterized by X-ray diffractometry, Brunauer-Emmett-Teller adsorption analysis, Raman spectroscopy, thermogravimetry/differential scanning calorimetry coupled with mass spectrometry, ultraviolet-visible diffuse reflectance spectra, photoluminescence spectroscopy and in situ diffuse reflectance infrared Fourier transform spectroscopy. It was shown that the carbon species residuals on the catalyst surfaces induced the visible light adsorption of the samples calcined in the low temperature range( 300℃). However, the surface acid sites played a determining role in the PCO of NH3 under visible and UV light over the series of catalysts. Although the samples calcined at low temperatures had very high SSA, good crystallinity, strong visible light absorption and also low PL emission intensity, they showed very low PCO activity due to their very low number of acid sites for NH3 adsorption and activation. The TiO2 sample calcined at 400℃ contained the highest number of acid sites among the series of catalysts, therefore showing the highest performance for the PCO of NH3 under UV light.     

V2O5/TiO2与MoO3/TiO2催化剂表面结构形貌及其对催化氧化碳烟活性的影响

为研究纳米级V₂O₅与MoO₃催化剂表面结构对其催化氧化碳烟活性的影响,以TiO₂为载体,采用等体积浸渍法制备了不同负载率(5%、10%、20%、40%)的V₂O₅/TiO₂与MoO₃/TiO₂催化剂,通过扫描电镜(SEM)、X射线衍射仪(XRD)对比研究了2种催化剂在TiO₂载体上的分散状态及物相结构.以Printex-U碳黑为试验用碳烟,采用热重分析仪对V₂O₅与MoO₃催化剂催化碳烟氧化的活性进行了比较.结果表明:V₂O₅与MoO₃在TiO₂载体上均存在一个单层分散饱和阈值,分别为V20(负载率为20%,下同)、Mo10,在该阈值前后活性组分在载体上分别以单层分散状态和明显的晶态存在.对于V₂O₅催化剂,其最佳催化活性出现在负载率接近单层分散饱和阈值时,与无催化状态相比,T_i(起燃温度)、T_p(最大失重率温度)以及T_f(燃尽温度)分别下降了69.1、46.0、23.0 ℃,有明显的阈值效应.而对于MoO₃催化剂,因其自身低熔点性而表现出良好的表面迁移能力,再加上α-MoO₃晶体特有的层状结构,使其可释放出更多的晶格氧,随着负载率的增加,该催化剂催化氧化碳烟活性持续增加,并且未观察到明显的阈值效应.研究显示,在相同负载率下,MoO₃催化剂催化氧化碳烟活性均高于V₂O₅催化剂.      

Effect of chromium oxide as active site over TiO2-PILC for selective catalytic oxidation of NO

This study introduced TiO2-pillared clays （TiO2-PILC） as a support for the catalytic oxidation of NO and analyzed the performance of chromium oxides as the active site of the oxidation process. Cr-based catalysts were prepared by a wet impregnation method. It was found that the 10 wt.% chromium doping on the support achieved the best catalytic activity. At 350℃, the NO conversion was 61% under conditions of GHSV = 23600 hr^-l. The BET data showed that the support particles had a mesoporous structure. Hz-TPR showed that Cr（10）TiP （10 wt.% Cr doping on TiO2-PILC） clearly exhibited a smooth single peak. EPR and XPS were used to elucidate the oxidation process. During the NO ＋ O2 adsorption, the intensity of evolution of superoxide ions （O2^-） increased. The content of Cr^3＋ on the surface of the used catalyst was 40.37%, but when the used catalyst continued adsorbing NO, the Cr^3＋ increased to 50.28%. Additionally, Oα/Oβ increased markedly through the oxidation process. The NO conversion decreased when SO2 was added into the system, but when the SO2 was removed, the catalytic activity recovered almost up to the initial level. FT-IR spectra did not show a distinct characteristic peak of SO4^2-.     

Fe2O3 particles as superior catalysts for low temperature selective catalytic reduction of NO with NH3

Fe203 particle catalysts were experimentally studied in the low temperature selective catalytic reduction （SCR） of NO with NH3. The effects of reaction temperature, oxygen concentration, [NH3]/[NO] molar ratio and residence time on SCR activity were studied. It was found that Fe203 catalysts had high activity for the SCR of NO with NH3 in a broad temperature range of 150-270℃, and more than 95% NO conversion was obtained at 180℃ when the molar ratio [NH3]/[NO] = 1, the residence time was 0.48 seconds and 02 volume fraction was 3%. In addition, the effect of SO2 on SCR catalytic activity was also investigated at the temperature of 180℃. The results showed that deactivation of the Fe2O3 particles occurred due to the presence of SO2 and the NO conversion decreased from 99.2% to 58% in 240 min, since SO2 gradually decreased the catalytic activity of the catalysts. In addition, X-ray diffraction, Thermogravimetric analysis and Fourier transform infrared spectroscopy were used to characterize the fresh and deactivated Fe2O3 catalysts. The results showed that the deactivation caused by SO2 was due to the formation of metal sulfates and ammonium sulfates on the catalyst surface during the de-NO reaction, which could cause pore plugging and result in suppression of the catalytic activity.     

复合氧化物催化材料上碳颗粒物的催化燃烧

针对柴油车排放碳颗粒物的控制 ,研制可应用于柴油车排放碳颗粒物催化再生复合氧化物催化材料 .通过运用热分析仪 (TGA)和程序升温氧化反应装置 (TPO)对复合氧化物催化材料的活性进行评价 ,研究了催化材料的组成、原子配比、催化材料与碳颗粒物质量比、H₂O的加入、焙烧温度对催化活性的影响 .实验结果表明 :双组分金属氧化物催化剂中 ,Cu-Mo-O有较好的活性 ;多组分金属氧化物催化剂中 ,Cu-K-Mo-O在原子比Cu∶K∶Mo =1∶1∶2 ,催化剂与碳颗粒物质量比为 5∶1时活性最好 ,其碳颗粒物起燃温度为 32.7℃ ,同时H₂O和焙烧温度对该催化剂的影响较小 ,是能够应用于柴油车排放碳颗粒物控制催化再生的良好催化材料 .     

A comparative study of Mn/CeO2, Mn/ZrO2 and Mn/Ce-ZrO2 for low temperature selective catalytic reduction of NO with NH3 in the presence of SO2 and H2O

Ce-ZrO2 is a widely used three-way catalyst support.Because of the large surface area and excellent redox quality,Ce-ZrO2 may have potential application in selective catalytic reduction(SCR) systems.In the present work,Ce-ZrO2 was introduced into a low-temperature SCR system and CeO2 and ZrO2 supports were also introduced to make a contrastive study.Mn/CeO2,Mn/ZrO2 and Mn/Ce-ZrO2 were prepared by impregnating these supports with Mn(NO3)2 solution,and have been characterized by N2-BET,XRD,TPR,TPD,XPS,FT-IR and TG.The activity and resistance to SO2 and H2O of the catalysts were investigated.Mn/Ce-ZrO2 and Mn/CeO2 were proved to have better low-temperature activities than Mn/ZrO2,and yielded 98.6% and 96.8% NO conversion at 180°C,respectively.This is mainly because Mn/Ce-ZrO2 and Mn/CeO2 had higher dispersion of manganese oxides,better redox properties and more weakly adsorbed oxygen species than Mn/ZrO2.In addition,Mn/Ce-ZrO2 showed a good resistance to SO2 and H2O and presented 87.1% NO conversion,even under SO2 and H2O treatment for 6 hours,and the activity of Mn/Ce-ZrO2 was almost restored to its original level after cutting off the injection of SO2 and H2O.This was due to the weak water absorption and weak sulfation process on the surface of the catalyst.     

不同硅铝比Fe-ZSM-5催化剂对氧化亚氮催化分解性能的研究

以不同硅铝比的H-ZSM-5分子筛为载体,采用离子交换法和化学气相沉积法制备Fe-ZSM-5催化剂,并用XRD、BET、TEM、UV-vis和NH3-TPD等表征手段对催化剂进行分析,研究催化剂中铁的存在状态.结果表明,分子筛的硅铝比影响铁在分子筛中的分布形态,化学气相沉积法和热离子交换法制得硅铝比为25的Fe-ZSM-5-25分子筛催化剂上均匀地分布着粒径为8 nm左右的纳米氧化铁颗粒,并且Fe-ZSM-5-25分子筛催化剂比Fe-ZSM-5-300更容易形成Fe3+x O y团簇.制得的Fe-ZSM-5分子筛催化剂催化分解氧化亚氮(N2O),结果表明,相同的制备方法,硅铝比小的Fe-ZSM-5-25催化剂对N2O分解活性更好;相同硅铝比的Fe-ZSM-5催化剂,采用化学气相沉积法制得的对N2O分解活性最好.另外,O2的存在对Fe-ZSM-5上N2O催化分解活性有抑制作用,而NO对N2O催化分解活性展示了一定的正效应.最后,经过100 h的连续反应,Fe-ZSM-5催化剂依然能够保持催化活性.     

脉冲介质阻挡放电下MnOx-CeO2催化氧化碳烟的关键表面物种研究

采用柠檬酸络合法制备了Mn/(Mn+Ce)原子比为0.4的MnO_x-CeO_2复合氧化物,使其分别在有和无脉冲介质阻挡放电条件下,多次催化氧化碳烟.采用XRD、BET、Raman和XPS对新制备未反应过的和各次反应后的MnO_x-CeO_2进行表征.结果发现,在初次反应中,脉冲介质阻挡放电对反应具有强化作用,使MnO_x-CeO_2具备更好的活性.在放电和无放电2种条件下,催化剂第2次反应的活性均较第1次有所降低,且放电条件下降幅更大,而在第3次反应时催化剂活性在两种条件下均保持稳定状态.以上现象原因为,初次反应,两种条件下高温使MnO_x-CeO_2中Mn-Ce-O固溶体发生相分离,部分Mn析出生成了Mn_3O_4;未引入放电时催化剂表面发生不可逆还原的Mn~(4+)量更少,且拥有更多Ce~(3+)并产生了本征氧空位及更多的表面氧;放电的引入,加剧了初次反应时MnO_x-CeO_2表面Mn~(4+)向Mn~(3+)和Mn~(2+)的转化,使其具备更高的活性,但也抑制了Mn~(4+)的恢复,降低了催化剂的活性.在随后的反应中,有无放电催化剂均保持了稳定.脉冲介质阻挡放电对MnO_x-CeO_2反应的关键因素Mn~(4+)、本征氧空位和表面氧产生了重要影响,这种影响在初次反应时并不可逆,进而减弱了放电对反应的强化作用,该现象不可忽视,值得进一步研究.