首页 | 本学科首页   官方微博 | 高级检索  
相似文献
 共查询到19条相似文献,搜索用时 171 毫秒
1.
用柠檬酸溶胶-凝胶法制备钙钛矿型La0.6Sr0.4MnO3氧化物,并用Ag对其进行修饰,制得Ag/La0.6Sr0.4MnO3系列催化剂。结果表明,6%Ag/La0.6Sr0.4MnO3催化剂上甲烷或甲醇氧化转化95%时的反应温度T95可低至735K(对CH4)或421K(对CH3OH);适量Ag的负载修饰并不改变催化剂基质氧化物La0.6Sr0.4MnO3的纳米级钙钛矿型结构;Ag的掺杂诱使催  相似文献   

2.
负载型La0.8Sr0.2CoO3燃烧催化剂的载体效应   总被引:6,自引:1,他引:5  
贾美林  沈岳年 《分子催化》2000,14(4):265-269
负载型La0.8Sr0.2CoO3/β-A)催化剂,由于钴离子在不太高的温度下易和载体γ-AI2O3作用形成CoAl2O4尖晶石或在尖晶石,因而不能有效地成为CO、HC化合物完全氧化的催化剂,采用XRD、BET、DTA、TG和二甲苯完全氧化催化活性测试等手段,研究了CoAl2O4的形成过程,可以认为这是一个放热、释氧而失重的过程,并伴有晶胞的稍微增大,若在γ-AI2O3表面涂数一层以MgAl2O4  相似文献   

3.
负载型La0.8Sr0.2MnO3燃烧催化剂的载体效应   总被引:7,自引:0,他引:7  
用浸渍法制备负载型La_(0.8)Sr_(0.2)Mno_3燃烧催化剂,比较了γ-AI_2O_3、α-AI_2O_3、堇青石(2MgO·2Al_2O_3、5SiO_2)和ZrO_2四种载体的负载效果.用XRD,DPR着重研究了γ-Al_2O_3载体上由于负载量不同、焙烧温度不同引起的催化剂物相变化和二甲苯完全氧化的催化活性变化.  相似文献   

4.
本文运用TPR、TPD-MS、XRD等技术研究了Mn-Ag/γ-Al_2O_3催化剂的还原性能和再氧化能力.结果表明,Mn-Ag/γ-Al_2O_3中银物相由Ag ̄0和Ag_2O组成,锰物相由β-MnO_2和Mn2O_3组成.Mn/γ-Al_2O_3催化剂的TPR有二个还原峰,分别是MnO_2和Mn_2O_3的还原.Ag促使MnO_2和Mn_2O_3的还原明显向低温方向移动,而且MnO_2和Mn_2O_3的还原峰融合成一个还原峰.Mn-Ag/γ-Al_2O_3的TPD有三个脱氧峰,随着Ag含量增加,峰Ⅰ向高温方向移动,Mn ̄(4+)2p3/2的电子结合能增加,并且催化剂的再氧化能力增强.催化剂CO的氧化活性与催化剂的再氧化能力有很好的对应关系.  相似文献   

5.
La0.8Sr0.2MnO3和La0.8Sr0.2CoO3在γ—Al2O3上的载体效应研究   总被引:7,自引:1,他引:7  
薛屏  沈岳年 《分子催化》1998,12(6):424-428
一般认为La0.8Sr0.2MnO3和La0.8Sr0.2CoO3两种钱钛矿型复合氧化物是CO氧化、碳氢(HC)化合物完全氧化和NO,还原的良好氧化物催化剂,用复合硝酸功体,制取此类负载型催化剂,负载量15%,用二甲苯完全氧化反应作为“探针反应”,配合XRD分析、BETG只测定,发现resume  相似文献   

6.
Cu-Ag-Mn-Ce-O/γ-Al_2O_3催化剂对CH_3OH及CO深度氧化时各元素的相互作用王金安,许勇,汪仁(华东理工大学工业催化研究所,上海200237)关键词Cu-Ag-Mn-Ce-O/γ-Al_2O_3催化剂,深度氧化,甲醇,一氧化碳,相互?..  相似文献   

7.
Mn—Ag/r—Al2O3催化剂中氧的性能   总被引:1,自引:0,他引:1  
罗孟飞  周烈华 《分子催化》1995,9(4):285-290
本文运用TPR、TPD-MS、XRD等技术研究了Mn-Ag/r-Al2O3催化剂的还原性能和再氧化能力。结果表明,Mn-Ag/r-Al2O3中银物相由Ag^0和Ag2O组成,锰物相由β-MnO2和Mn2O3组成。Mn/r-Al2O3催化剂的TPR有二个还原峰,分别是MnO2和Mn2O3的还原。Ag促使MnO2和Mn2O3的朱明显向低温方向移动,而且MnO2和Mn2O3的还原峰融合成一个还原峰。Mn  相似文献   

8.
La—Cu—Mn系钙钛矿型(ABO3)催化剂性能   总被引:11,自引:0,他引:11  
采用共沉淀法制得了Cu2+部分取代La3+的La1-xCuxMnO3钙钛矿型催化剂,通过XRD、TPR、电镜分析及活性评价,研究了Cu2+的部分取代对La1-xCuxMnO3系催化剂性能的影响.结果表明,Cu2+部分取代La3+后,使催化剂易被还原,活化能降低,对CH4、CO氧化反应,均有最佳取代量使催化剂的活性最佳,其值分别为0.2和0.4,这是由于随x值的增大,催化剂晶格缺陷增多,晶格氧的化学势增大的缘故  相似文献   

9.
本文用硝酸盐水溶液等浸渍法制备了一系列Cr-Ag/γ-Al2O3双金属及单金属的 物催化剂,测定了CO氧化转化率。用BET,XRD,TPR,TPD-MS技术研究了助剂Ag对Cr/γ-Al2O3催化剂CO氧化反应的作用。  相似文献   

10.
姚心侃  谢庆兰 《结构化学》1996,15(3):193-198
三环己基锡O,O’-二(4-氯苯基)二硫代磷酸酯(I),C30H41Cl2(O2PS2Sn,Mr=718.36,单斜晶系,P21/n,a=16.151(2),b=9.4159(1),c=22.987(3),A,β=105.69(1)°,Z=4,Dc=1.418g.cm^-3,R=0.063;二丁基锡双(O,O’-二(4-甲基苯基)二硫代磷酯酯(Ⅱ),C36H46O4P2S4Sn,Mr=851.66  相似文献   

11.
Ag-modified La0.6Sr0.4MnO3 catalysts were prepared and their catalytic performance for deep oxidation of CH4 and CH3OH at low concentrations were investigated. The results showed that the La0.6Sr0.4MnO3 host catalyst with the perovskite-type nano-crystallite structure displayed considerably high catalytic activity for deep oxidation of CH4 and CH3OH at low concentrations. Ag modification to the La0.6Sr0.4MnO3 host catalyst resulted in significant enhancement of the catalyst activity, making the T95 (the reaction temperature needed for conversion of 95%of CH4 or CH3OH) lowered down to 735K (for CH4) and 421K (for CH3OH) from 813 and 465 K over the Ag-free system under the reaction conditions:0.1MPa,CH4/O2/N2=2/12/86(molar ratio),GHSV=45000 h-1 and CH3OH/O2/N2= 0.2/1.0/98.8 (molar ratio),GHSV=58000 h-1,respectively.The carbon containing product was almost CO2 and the contents of HCHO and CO in the reaction exit gas were both under GC detectable limit in both cases.
The results of spectroscopic characterization indicated that modification by proper amount of Ag-dopant did not change the perovskite structure of the La0.6Sr0.4MnO3 host catalyst as a whole. Interaction of Ag-dopant with the surface of the host catalyst,La0.6Sr0.4MnO3,was in favor of high dispersion of the Ag component at the catalyst surface and led to the oxidation of part of the Mn3+species to Mn4+,resulting in an increase of amounts of the reducible Mnn+ species and a decrease of their reduction temperature. On the other hand, this interaction led also to enhancement of adsorption ability of the catalyst toward O2 at relatively low temperature. High activity of the Ag modified La0.6Sr0.4MnO3 catalyst for CH4 and CH3OH complete oxidation was closely related to high redox-activity of the catalyst and its prominent adsorption-activation ability to O2 at relatively low temperatures.  相似文献   

12.
采用非晶态多核配合的方法合成了La1-xCuxMnO3(x=0、0.05、0.1、0.2、0.3、0.4、0.5)系列催化剂, 并用X射线衍射(XRD)、透射电镜(TEM)、比表面测定仪(BET)等手段对催化剂的微观结构进行了表征. 研究了Cu掺杂对钙钛矿结构及其对CO催化氧化发光性能及催化氧化CO、CH4性能的影响规律. 结果表明, 当x≤0.1 时, Cu掺杂仍可形成单相的钙钛矿结构; 当x>0.1时, 过量掺杂的Cu以CuO杂相存在. Cu掺杂可改善La1-xCuxMnO3催化剂对CO和CH4的催化氧化活性. 经700 ℃焙烧3 h制备的La0.9Cu0.1MnO3催化剂具有最高CO催化氧化活性(T100%=170 ℃), 该结果与CO催化氧化发光结果一致.而La0.95Cu0.05MnO3催化剂对CH4的催化氧化活性最高(T95%=705 ℃).  相似文献   

13.
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   

14.
采用微波加热分解法制备了一系列CuO含量(0-25%, w)不同的CuO-Ce0.6Zr0.4O2催化剂, 并用X射线衍射(XRD)、透射电镜(TEM)、N2吸附-脱附(BET)和H2程序升温还原(H2-TPR)技术对催化剂进行了表征, 利用色谱流动法考察了其催化CO低温氧化性能. 结果表明: 当CuO含量为15%时, 所制备催化剂的催化活性最佳. 在催化剂中存在三种不同类型的铜物种, 即高分散、小颗粒和大颗粒的CuO. 催化剂表面高分散和小颗粒的CuO有利于催化活性的提高, 而大颗粒的CuO对催化活性具有抑制作用.  相似文献   

15.
采用并流淤浆混合法制备了一系列具有不同铜锌铝比的铜基甲醇合成催化剂CuO/ZnO/Al2O3,测试了其催化性能(甲醇收率和CO转化率)及物相结构,并对该制备方法进行评价。Cu∶Zn∶Al摩尔比为4∶5∶1 的铜基催化剂显示了最好的催化活性。通过对催化剂前驱物煅烧过程进行DTA分析及对前驱物进行XRD分析表明, 催化剂前驱物的物相与Al2O3的量有关。当Al2O3的量较低时,前驱物的物相以(Cu0.3 Zn0.7)5(CO3)2(OH)6为主;当Al2O3的量较高时,前驱物中物相(Cu0.3Zn0.7)5(CO3)2(OH)6的量下降,而物相Cu2CO3(OH)2的量增加。物相(Cu0.3 Zn0.7)5(CO3)2(OH)6对终态催化剂的活性是十分有利的 。  相似文献   

16.
A series of hybrid catalysts were made by physically mixing Cu-ZrO 2 and γ-Al 2 O 3,for former it was modified with different loadings of La 2 O 3 prepared by co-precipitation method.The catalysts were characterized by BET,XRD,N 2 O-adsorption,EXAFS,H 2-TPR,NH 3-TPD techniques and evaluated in the synthesis of dimethyl ether from syngas.The results show that La 2 O 3 promoted catalysts displayed a significantly better catalytic performance compared with Cu-ZrO 2 /γ-Al 2 O 3 catalyst in CO conversion and DME selectivity,and the optimum catalytic activity was obtained when the content of La 2 O 3 was 12 wt%.The characterizations reveal that high copper dispersion,facile reducibility of copper particles and appropriate amount of acidic sites are responsible for the superior catalytic performance.  相似文献   

17.
Catalytic oxidation of NO by O2 over La0.8Sr0.2MnO3 was tested in a tubular reactor.The reaction temperature ranged from 373 to 473 K,space time from 0.090 to 0.720 s,inlet NO concentration from 300 to 2000μL/L, and O2 volume fraction from 3%to 9%.The steady-state conversion of NO was increased significantly with increasing reaction temperature and the space time,slightly with increasing the O2 concentration but decreased with increasing the inlet NO concentration at a lower temperature.Under the conditions of 0.720 s space time,500μL/L NO concentration, 5%O2 volume fraction and 473 K,NO conversion reached 90%.A kinetic model including a network of 12 elementary reactions with the desorption of NO2 as the rate-limiting step is established and fits the experimental data well.The activation energy of NO2 desorption from the catalyst surface is determined to be 101 kJ/mol.  相似文献   

18.
用浸渍法制备γ-Al2O3负载的Ni-Mn双金属催化剂.在500-700。C按照17:17:2的C02/CHa/N2比例,以36mL/min的载气流速进行甲烷二氧化碳重整反应,利用甲烷二氧化碳的转化率、生成的合成气H2/CO比例以及长期稳定性等指标评价了催化剂的催化性能.实验表明,添加Mn提高催化性能并使双金属催化剂的稳定性更高,比单金属催化剂更好地抑制焦炭生成,Mn最合适的添加量为0.5wt%.通过BET、C02-TPD、TGA、XRD、SEM、EDX和FTIR各种技术对催化剂进行了表征.  相似文献   

19.
在1mmol·L-1H2PtCl6+1mmol·L-1RuCl3+0.1mol·L-1H2SO4镀液中采用电沉积法在化学镀金膜的红外窗口Si反射面上制备Pt50Ru50合金电极.利用原子力显微镜(AFM)可以观察到制备的Pt50Ru50合金电极形貌呈现出100-200nm大小的颗粒.常规电化学分析方法得出该电极具有典型的合金特征,对CO和CH3OH具有很好的催化氧化作用.应用电化学现场衰减全反射表面增强红外光谱法(ATR-SEIRAS)可以观察到该电极上Pt位和Ru位上CO的振动谱峰,且表现出Pt-Ru二元金属良好的协同催化性能.  相似文献   

设为首页 | 免责声明 | 关于勤云 | 加入收藏

Copyright©北京勤云科技发展有限公司  京ICP备09084417号