混合导体透氧膜反应器中甲烷部分氧化反应的催化行为(英文)

应用组成为Ba0.5Sr0.5Co0.8Fe0.2O3-(的钙钛矿型混合导体陶瓷膜制成膜反应器。该膜在进行氧分离的同时具有活化甲烷氧化偶联的催化功能。随着温度升高和膜的富氧端氧分压的增大,透氧量有所增加。在空气、氦气的氧分压梯度下,850(C,膜厚度为1.5 mm时,JO2可达到1.2 mL/(cm3(min)。同时在800(C~900(C温度范围内,该膜对于甲烷转化为乙烷和乙烯一般只具有0.5%~3.5%的低转化率,而选择性可达40%~70%。在反应尾气中发现了大量的未反应的分子氧,说明过量的氧与甲烷未经催化反应的气相反应导致了C2的选择性相对较低。OCM膜反应模式情况下的透氧量与空气、氦气梯度情况下的透氧量相比只有微小增加,这与POM膜反应模式情况下透氧量大量增加显著不同。     

SrSn0.1Fe0.1Co0.8O3-δ和Ba0.1Sr0.1Fe0.1Co0.8O3-δ膜的氧渗透性能

致密陶瓷膜;电导;SrSn0.1Fe0.1Co0.8O3-δ和Ba0.1Sr0.1Fe0.1Co0.8O3-δ膜的氧渗透性能     

微波-固相复合加热技术合成LiNi0.5Co0.5O2及其性能研究

用高分子分散及微波-固相复合加热技术合成了层状锂离子电池正极材料LiNi0.5Co0.5O2. 采用循环伏安、充放电循环、扫描电子显微镜(SEM)以及X射线粉末衍射(XRD)等测试技术, 研究了煅烧条件对材料微观形貌、相结构以及电化学性能的影响规律. 研究结果表明: 在750 ℃煅烧4 h即可得到形状为类球形的纯相层状LiNi0.5Co0.5O2正极材料, 该材料的最大放电容量达到154 mA·h/g, 循环10周后放电容量仍保持在148 mA·h/g以上.     

CS/La0.7Ca0.3Fe0.25Co0.75O3复合纳米颗粒的制备及光催化性能研究

采用甘氨酸-硝酸盐燃烧法成功的制备了La0.7 Ca0.3 Fe0.25 Co0.75 O3钙钛矿型复合氧化物,将钙钛矿La0.7Ca0.3Fe0.25Co0.75O3与壳聚糖(CS)共混交联制备出一种新型的光催化剂,通过XRD、SEM、FT-IR对催化剂的结构进行了表征.以酸性橙为对象,高压汞灯紫外光为光源,研究了一...     

聚苯胺/Co_(0.5)Zn_(0.5)Fe_2O_4纳米复合材料的制备及电磁性能

采用高分子凝胶法制备尖晶石型Co0.5Zn0.5Fe2O4,原位聚合法制备纯聚苯胺和聚苯胺/Co0.5Zn0.5-Fe2O4纳米复合材料.使用傅立叶红外光谱(FTIR)、紫外可见吸收光谱(UV-Vis)、X射线衍射仪(XRD)和透射电子显微镜(TEM)对复合材料进行了表征.FTIR和XRD的结果表明样品为纯聚苯胺和聚苯胺/Co0.5Zn0.5-Fe2O4.UV-Vis光谱表明聚苯胺/Co0.5Zn0.5Fe2O4苯环上的π-π*和n-π*分别红移了23nm和5nm.TEM照片可知,聚苯胺和聚苯胺/Co0.5Zn0.5Fe2O4粒子的平均粒径分别约为50nm和70nm.在8.2～12.4GHz测试频率范围内,聚苯胺/Co0.5Zn0.5Fe2O4的ε″数值在9.2～12.3之间,u″数值在0.15～0.16之间;聚苯胺/Co0.5-Zn0.5Fe2O4介电损耗低于纯聚苯胺,而磁损耗高于纯聚苯胺.     

CuO/Ti0.5Zr0.5 O2催化剂上NO+CO反应活性的研究

以Ti0.5Zr0.5O2复合氧化物为载体，采用浸渍法制备了不同负载量的CuO／Ti0.5Zr0.5O2(TZ)催化剂，考察了催化剂对NO的反应活性，并用TPR、TG-DTA和NO-TPD等技术对催化剂进行了表征。结果表明，CuO的负载量和焙烧温度对催化剂的活性均有影响。30％CuO／Ti0.5Zr0.5O2(500℃，2h)在反应温度为400℃时NO转化率为100％。TPR结果表明，CuO负载量≤12％时，在TPR上出现了2个还原峰(即α和β峰)；而进一步提高CuO的负载量，出现了γ还原峰，推测α峰为高度分散Cu物种的还原，β峰为孤立的Cu物种的还原，γ峰则为晶相CuO的还原峰。TG-DTA图谱显示在725℃左右的放热峰是ZrTiO4晶化过程的完成。NO-TPD结果表明NO吸附在TZ上的热脱附过程中，出现2个脱附峰；而NO吸附在12％CuO／TZ上，500℃和750℃焙烧的催化剂上出现3个脱附峰；而在850℃和950℃焙烧的催化剂上只出现2个脱附峰，且NO在上述不同焙烧温度的催化剂上的脱附峰温均低于载体，这表明NO吸附在CuO／TZ催化剂上比吸附在Ti0.5Zr0.5O2上更容易脱出和分解。     

不同的制备方法对Co3O4-CeO2催化剂的影响

用水热法、共沉淀法、柠檬酸络合物法和多元醇法分别合成了铈钴摩尔比1:1的Co3O4-CeO2催化剂,并用XRD、TPR、TPD、FT-IR、BET等对催化剂的晶相结构、还原性能、吸附性能及比表面积等进行了表征。结果表明,制备方法对Co3O4-CeO2催化剂的催化性能具有较大的影响,其中多元醇法制备的催化剂能促进Co3O4和CeO2的相互作用,该催化剂还原温度较低、CO脱附面积较大,在140℃温度下,CO的转化率达到90%以上。     

制备方法对Co_3O_4-CeO_2催化剂催化性能的影响研究

用水热法、共沉淀法、柠檬酸络合物法和多元醇法分别合成了铈钴摩尔比1∶1的Co3O4-CeO2催化剂,并用XRD、TPR、TPD、FT-IR、BET等对催化剂的晶相结构、还原性能、吸附性能及比表面积等进行了表征.结果表明,制备方法对Co3O4-CeO2催化剂的催化性能具有较大的影响,其中多元醇法制备的催化剂能促进Co3O4和CeO2的相互作用,该催化剂还原温度较低、CO脱附面积较大,在140℃温度下,CO的转化率达到90%以上.     

Co/Fe/Al2O3/cordierite催化C3H6选择性还原NO的实验研究

采用溶胶凝胶法和浸渍法制备了负载于蜂窝陶瓷上的Co/Fe/Al₂O₃/cordierite催化剂,在陶瓷管流动反应器上对其催化C₃H₆选择性还原NO的性能进行了测试。结果表明,该催化剂表现出最优脱硝性能,在模拟烟气条件下,当反应温度为550 ℃时可实现97%的脱硝效率。Co的引入可显著增强Fe/Al₂O₃/cordierite催化剂抗SO₂和H₂O的能力。在模拟烟气中同时引入0.02% SO₂和3% H₂O后,1.5Co/Fe/Al₂O₃/cordierite的脱硝性能受影响甚微,当反应温度高于500 ℃时1.5Co/Fe/Al₂O₃/cordierite催化C₃H₆还原NO的效率均可达到90%以上;相比之下,未经Co修饰的催化剂Fe/Al₂O₃/cordierite脱硝性能受到了严重的抑制,在整个反应温度区间（200-700 ℃）内,其催化C₃H₆还原NO的效率最高不足50%。XRD和SEM表征结果表明,经过适量的Co修饰后的1.5Co/Fe/Al₂O₃/cordierite表面变得更疏松,且形成了以钴铁和钴铝双金属氧化物为主要成分的球状晶粒。H₂-TPR结果表明,相比于Fe/Al₂O₃/cordierite,1.5Co/Fe/Al₂O₃/cordierite有更好的低温还原性能。Py-FTIR结果表明,Co的引入可使催化剂表面的Lewis酸明显增加,且生成了Brønsted酸。N₂吸附-脱附表征结果表明,Co可增大催化剂的比表面积。     

Cu修饰的Fe2O3/Al2O3氧载体的循环反应稳定性研究

采用冷冻干燥法制备了经Cu修饰（10%）的Fe₂O₃/Al₂O₃氧载体。利用热重分析仪分别在850、900和950 ℃等温环境下,使氧载体交替接触还原气体和氧化气体,来模拟氧载体在化学链燃烧中的循环过程。结果表明,经Cu修饰的Fe₂O₃/Al₂O₃氧载体在850和900 ℃下的等温循环过程中反应性能都很稳定,在950 ℃时的循环反应前期有微量烧结,但在循环后期反应性能也很稳定。随着反应温度的升高,氧载体氧化速率增大,还原速率和载氧率先减小后增大。与未经修饰的Fe₂O₃/Al₂O₃氧载体相比较,在900 ℃下作等温循环实验,经Cu修饰的Fe₂O₃/Al₂O₃氧载体具有较高的载氧能力和还原速率,但氧化速率较低;两者都具有较好的循环稳定性。     

Detailed Description of Pulse Isotopic Exchange Method for Analyzing Oxygen Surface Exchange Behavior on Oxide Ion Conductors

A novel pulse ¹⁸O-¹⁶O isotopic exchange (PIE) technique for measurement of the rate of oxygen surface exchange of oxide ion conductors was presented. The technique employs a continuous flow packed-bed micro-reactor loaded with the oxide powder. The isothermal response to an ¹⁸O-enriched pulse passing through the reactor, thereby maintaining chemical equilibrium, is measured by on-line mass spectrometry. Evaluation of the apparent exchange rate follows from the uptake of ¹⁸O by the oxide at given reactor residence time and surface area available for exchange. The developed PIE technique is rapid, simple and highly suitable for screening and systematic studies. No rapid heating/quenching steps are required to facilitate ¹⁸O tracer anneal or analysis, as in other commonly used techniques based upon oxygen isotopic exchange. Moreover, the relative distribution of the oxygen isotopologues ¹⁸O₂, ¹⁶O¹⁸O, and ¹⁶O₂ in the effluent pulse provides insight into the mechanism of the oxygen exchange reaction. The PIE technique has been demonstrated by measuring the exchange rate of selected oxides with enhanced oxide ionic conductivity in the range of 350?900 oC. Analysis of the experimental data in terms of a model with two consecutive, lumped steps for the isotopic exchange reaction shows that for mixed conductors Ba_0.5Sr_0.5Co_0.8Fe_0.2O_3-δ(BSCF) and La₂NiO_4+δ the reaction is limited by the apparent rate of dissociative adsorption of O₂ molecules at the oxide surface. For yttria-stabilized zirconia (YSZ), a change-over takes place, from rate-limitations by oxygen incorporation below ∽800 oC to rate-limitations by O₂ dissociative adsorption above this temperature. Good agreement is obtained with exchange rates reported for these materials in literature.     

Low-temperature Catalytic Reduction of Nitrogen Monoxide with Carbon Monoxide on Copper Iron and Copper Cobalt Composite Oxides

Copper iron composite oxides (CuO/Fe2O3) and copper cobalt composite oxides (CuO/Co3O4) for the catalytic reduction of NO with CO at low temperature were prepared by co-precipitation. The catalytic activity and thermal stability of the catalysts were evaluated by a microreactor-GC system. The 100% conversion temperatures of NO are 80 oC for CuO/Fe2O3 and 90 oC for CuO/Co3O4. The catalysts possess high catalytic activity and favorable thermal stability for NO reduction with CO in a wide temperature range and long time range. A systematic study of the molar ratios of the reactants, the volume of NaOH, aging time, and calcination temperature/time was carried out to investigate the influence preparation conditions on the catalytic activity of the catalysts.     

Partial Oxidation of Methane Over the Perovskite Oxides

Introduction The conversion of methane to syngas is a very appealing route for the conversion of the large reserves of natural gas1, from which a wide variety of valuable hydrocarbons and oxygenates, such as methanol and formaldehyde, can be synthesized. A great research effort is presently being carried out on the catalytic partial oxidation of methane to syngas2. In the present work, two oxides with the perovskite structure, Ba0.5Sr0.5Co0.8Fe0.2O3- and Ba0.5Sr0.5Co0.8Ti0.2O3-?were sys…     

Sm0.5Sr0.5Co0.4M0.6O3 (M=Co,Mn, Fe)作为IT-SOFCs阴极的结构与性能

通过X射线衍射(XRD)、热重、热膨胀、电导率以及交流阻抗等测试方法, 研究了Sm0.5Sr0.5Co0.4M0.6O3(M=Co, Mn, Fe; 分别简写为SSCC, SSCM, SSCF)作为中低温固体氧化物燃料电池(IT-SOFCs)阴极的结构与性能. 研究表明, 固相法合成的Sm0.5Sr0.5Co0.4M0.6O3均为正交钙钛矿型结构, 材料的结构参数和性能都与M元素半径及M—O的键能有关. 晶胞参数随着Co、Mn、Fe的顺序增大.材料的氧空位浓度、热膨胀系数、电导率、电极催化活性随着Co、Fe、Mn的顺序降低. 同时由于SSCM较低的氧空位浓度, 使得电极反应受到氧在电极内的扩散过程控制, 具有较差的电极催化性能, 而SSCC和SSCF较高的氧空位浓度, 电极反应同时受到电极表面氧还原反应和氧离子在电极中的扩散过程混合控制. 由于SSCF具有较高的氧扩散系数, 使得700 ℃以上SSCF电极表面氧还原电阻(ASR)也低于SSCC的, 因而出现了SSCF的总电极催化活性高于SSCC的现象.     

无气相氧条件下La0.8Sr0.2Fe0.9Co0.1O3钙钛矿氧化物的氧物种直接氧化甲烷

以La0.8Sr0.2Fe0.9CO0.1O3钙钛矿氧化物作氧载体,采用连续流动反应和连续顺序Redox反应考察了氧物种氧化甲烷的反应性能.结果表明,连续流动反应中La0.8Sr0.2Fe0.9CO0.1O3氧化物的氧物种能选择氧化甲烷生成合成气.在适宜的再氧化条件下,通过连续顺序Redox反应实现了La0.8Sr0.2Fe0.9CO0.1O3氧化物的氧物种氧化甲烷连续生成合成气,消耗的氧物种可通过与气相氧反应而得到补充.但随着Redox反应的进行,氧化物的持续供氧性能下降,钙钛矿结构被破坏.     

中温固体氧化物燃料电池复合阴极Pr0.6-zSr0.4Co0.8Fe0.2O3-δ-SDC性能研究

采用改进的溶胶-凝胶法合成固体氧化物燃料电池阴极系粉体Pr0.6-zSr0.4Co0.8Fe0.2O3-δ(PSCF)(z=0,0.02,0.05,0.1)。使用X射线衍射(XRD)、扫描电子显微镜(SEM)对其相结构与形貌进行了分析,结果表明:900℃以上焙烧后的阴极粉体Pr0.6-zSr0.4Co0.8Fe0.2O3-δ(z=0,0.02,0.05,0.1)为单一的钙钛矿结构。1000℃烧结的样品内粒子分布比较均匀,且颗粒内部存在一定程度的空隙,并与电解质附着情况良好。用直流四电极法测试阴极体系样品在400～750℃的电导率,发现各试样混合离子电子电导率均高于786 S.cm-1,能够满足固体氧化物燃料电池对阴极电导率的要求。用交流阻抗法测定PSCF-Ce0.8Sm0.2O1.9体系样品的阻抗谱,得到1000℃烧结的阴极体系对称电池在测试温度为750℃z=0,z=0.02,z=0.05时的极化电阻分别为0.041,0.040,0.034Ω.cm-2。     

Comparison of reduction behavior of Fe2O3, ZnO and ZnFe2O4 by TPR technique

Advanced integrated gasification combined cycle (IGCC) power generation systems require the development of high-temperature,regenerable,desulfurization sorbents capable of removing hydrogen sulfide from coal gasifier gas to very low levels.As a sort of effective desufurizer,such as Fe2O3,ZnO and ZnFe2O4,it will endure strong reducing atmosphere in desulfurization process.The reduced degree of desufurizer can have an effect on its desulfurization reactivity.In this paper,Fe2O3,ZnO and ZnFe2O4 were synthesized by precipitation or co-precipitation at constant pH.After aging,washing and drying,the solids were calcined at 800℃.The reduction behaviors of sample were characterized by temperature-programmed reduction (TPR).It is found that there are two reduction peaks for Fe203 in TPR,and whereas no reduction peaks for ZnO are found.The reduction process of ZnFe2O4 prepared by co-precipitation is different from that of Fe2O3.ZnFe2O4 is easier to be reduced than Fe2O3.The activation energy of reduction process for Fe2O3 and ZnFe2O4 is obtained at different reduction periods.     

氧化铝基表层ZrO2的相结构、孔结构及性能研究

近年来，双组份氧化物的性质和作用越来越受到人们的重视，国内外学者对TIOZ／A1203，Ceo。／AI。oa＊，MgO／AI。osRI等作了大量的研究．Zro。既可以做工业催化剂的载体，又可作添加剂或活性组份，它具有酸、碱、氧化和还原四种化学性质，在一氧化碳加氢合成甲醇中更具有重要作用·本文通过改变在7－AI。O3表面上Zro：负载量，研究了Zro。－AI。Oa体系的相结构及孔结构，并以CO氧化为模型反应，结合TPD－MS等实验技术研究并考察了添加Zroz对Alzoa基催化氧化及表面氧性能的影响，探讨Zroz的助催化作用·1实验部分（1）实验样…