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铜钴尖晶石复合氧化物催化剂的组成对二甲苯完全氧化反应催化性能的影响 总被引:5,自引:0,他引:5
具有特定结构的复合氧化物,如ABO3,A2BO4及AB2O4等对某些反应比单一氧化物具有更好的催化性能[1,2]. 然而,有关尖晶石型复合氧化物AB2O4对有机物燃烧反应催化性能的研究相对较少,且常用的模型反应大都是一氧化碳或甲烷的催化氧化反应[3]. 超微粒子由于具有大的比表面积和高的表面能等特性,在催化领域已日益引起人们的重视[4]. 低温固相合成是近十几年发展起来的一种新的超细粒子制备方法[5]; 它具有不使用溶剂,无废液排放,工艺过程简单,能耗低等优点,属于对环境友好的“绿色化学”. 目前,此法在合成多组分复合氧化物及催化化学中的应用仍不多见. 本文以含有结晶水的醋酸铜和醋酸钴为原料,采用低温固相合成法制备了单组分氧化铜和氧化钴,以及三种不同铜钴比的铜钴尖晶石型复合氧化物,并以二甲苯氧化为模型反应,采用XRD,BET及程序升温还原(TPR)等手段进行了研究. 相似文献
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低镍甲烷化催化剂中镍和氧化镧的分散研究 总被引:4,自引:0,他引:4
本文用X射线衍射法(XRD), 透射电镜(TEM), 配合电子衍射对Ni/Al2O3,Ni/γ-Al_2O_3-La_2O_3等催化剂中镍晶粒度和La_2O_3的分散状态进行了测量和讨论。用透射电镜测量了不同La_2O_3含量的催化剂中镍晶粒度分布, 其平均直径可与X射线宽化法测定值相比较。催化剂中随La_2O_3加入量的增加, Ni晶粒有细化趋势, 从而提高了甲烷化催化活性。对La_2O_3在γ-Al_2O_3表面作密置单层分散的模型提出了新的旁证, 并推断由于La_2O_3在γ-Al_2O_3表面高分散并产生较强相互作用, 使γ-Al_2O_3接近表层晶格发生畸变。 相似文献
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Combustion catalysts La0.8Sr0.2MnO3 supported on γ-Al2O3, α-Al2O3, cordierite (2MgO•2Al2O3•5SiO2) and ZrO2 were compared. Further investigation was focused on LSM/ γ-Al2O3 catalyst. It was observed that LSM/γ-Al2O3 catalyst loaded with 20% (mass fraction) LSM (La0.8Sr0.2MnO3 or corresponding oxides), heated at 750℃ or above, perovskite-type oxides were found by XRD examination, whereas, the same catalyst loaded with 10% or less LSM, perovskite oxides were absent, calcination temperature about 750℃ is necessary for the formation of perovskite structure in LSM/γ-Al2O3 catalysts. High activity of complete oxidation of xylen will be obtained when perovskite-type oxides.
Investigation of TPR showed that neat LSM or LSM/γ-Al2O3(20%) was reduced by H2-N2 mixed gas. Two degradation processes took place. In the first, reduced temperature peak was about 350 - 450℃. If reduction ended at 400℃, perovskite structure was retained, which may be due to the reduction of Mn3+to Mn2+ on the surface of LSM only. In the second process, perovskite structure was destroied, and La2O3, Mn2O3, Mn - Sr - O oxides could be obtained, which took place in the temperature range 685 - 750℃ and ended at 800℃. This was proved by TPR experiments (Fig. 3, 5) and XRD patterns (Fig. 4)
Catalysts LSM/γ-Al2O3(10% or 20%) heated at 500℃ have only one TPR peak, i. e. lower temperature peak. This is due to the absence of perovskite-type oxides in the catalysts. However, neat LSM or LSM/γ-Al2O3(20%) heated 750℃ or above, not only the first low temperature TPR peak but also the second peak, which is contributed by the perovskite-type oxides in these catalysts appeared. Therefore, the second TPR peak, i. e. the higher temperatue peak is a characteristic peak for perovskite-type oxides in the reduced process. When LSM/ γ-Al2O3 (10%) catalys is heated at 750℃, no perovskite-type oxides were detected by XRD, and the second reduction peak was absent also in TPR process. \
The order of the second reduction peak temperature(characteristic peak of perovskite - type ox- ides) is: neat LSM(750℃)> LSM/γ-Al2O3 20% (685-698℃) -deposited LSM/γ-Al2O3 (698℃) > LSM/γ-Al2O3 15% (677 - 680℃) >(LSM/γ-AL2O3 10% 620 - 630℃, for Mn - Al - O medium oxides on surface). It is correleted with the increasing of the effect of support sequentially.
When LSM/γ-Al2O3 catalysts were heated at 900℃, more stable phase, spinel MnAl2O4 appeared, which could be proved by TPR of model catalyst MnAl2O4/γ-Al2O3. 相似文献
Investigation of TPR showed that neat LSM or LSM/γ-Al2O3(20%) was reduced by H2-N2 mixed gas. Two degradation processes took place. In the first, reduced temperature peak was about 350 - 450℃. If reduction ended at 400℃, perovskite structure was retained, which may be due to the reduction of Mn3+to Mn2+ on the surface of LSM only. In the second process, perovskite structure was destroied, and La2O3, Mn2O3, Mn - Sr - O oxides could be obtained, which took place in the temperature range 685 - 750℃ and ended at 800℃. This was proved by TPR experiments (Fig. 3, 5) and XRD patterns (Fig. 4)
Catalysts LSM/γ-Al2O3(10% or 20%) heated at 500℃ have only one TPR peak, i. e. lower temperature peak. This is due to the absence of perovskite-type oxides in the catalysts. However, neat LSM or LSM/γ-Al2O3(20%) heated 750℃ or above, not only the first low temperature TPR peak but also the second peak, which is contributed by the perovskite-type oxides in these catalysts appeared. Therefore, the second TPR peak, i. e. the higher temperatue peak is a characteristic peak for perovskite-type oxides in the reduced process. When LSM/ γ-Al2O3 (10%) catalys is heated at 750℃, no perovskite-type oxides were detected by XRD, and the second reduction peak was absent also in TPR process. \
The order of the second reduction peak temperature(characteristic peak of perovskite - type ox- ides) is: neat LSM(750℃)> LSM/γ-Al2O3 20% (685-698℃) -deposited LSM/γ-Al2O3 (698℃) > LSM/γ-Al2O3 15% (677 - 680℃) >(LSM/γ-AL2O3 10% 620 - 630℃, for Mn - Al - O medium oxides on surface). It is correleted with the increasing of the effect of support sequentially.
When LSM/γ-Al2O3 catalysts were heated at 900℃, more stable phase, spinel MnAl2O4 appeared, which could be proved by TPR of model catalyst MnAl2O4/γ-Al2O3. 相似文献
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稀土氧化物特别是La2O3作为助催化剂,对CO甲烷化反应有促进作用,已为人们所知[‘j.研究焙烧温度对La。O。-NIO催化剂结构、导电性,特别是对其在不同类型反应中催化性能的影响,目前文献报道较少.本文通过多晶X射线衍射(XRD),差热一热重分析(DTA-TG),导电性测量,CO甲烷化及二甲苯完全氧化反应活性测定等手段,考察了所制备的La。Os-NIO催化剂经不同温度焙烧后,结构、热效应、导电性的变化,并研究了该体系催化剂在上述两种不同类型反应中的催化性能.用分析纯试剂La(NO3)·6H2O和La(NO3)3·6H2O(北京化工… 相似文献
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合成了两个稀土复合氧化物LaMnO3和La(0.927)φ(0.073)MnO3,并对其进行了结构、电阻率、XPS表面分析、水汽转化及二氧化碳甲烷化反应的催化性能测定。初步解释了结构与性能的关系。 相似文献
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