掺杂碱金属与碱土金属的CuO-CeO_2催化剂的漫反射红外光谱分析

CuO-CeO2系列催化剂是高效的CO选择性氧化反应的催化剂,通过原位漫反射红外光谱对掺杂碱金属和碱土金属氧化物的CuO-CeO2催化剂表面的吸附物种进行了研究。结果表明CuO-CeO2系列催化剂上,2 106 cm-1处出现CO的红外吸附峰。在反应气氛中,此峰的强度随着温度先升高后降低,说明Cu+是CO主要的活性吸附中心。低温下催化剂表面吸附的CO主要以可逆形式脱附出来,而高温下CO则以不可逆的形式脱附出来。催化剂表面在3 660 cm-1处出现尖锐的红外峰,归属于CeO2经还原产生的Ce-(OH)2偕式基团。在1 568,2 838和2 948 cm-1附近处出现甲酸根的红外谱峰,以及1 257和1 633 cm-1处出现碳酸根物种的红外峰。甲酸根物种是气相的CO与表面的羟基反应生成的产物,该物种的C—H键断裂生成碳酸根物种,这两物种均会降低催化剂的高温活性。Cu1Li1Ce9Oδ催化剂出现较强的CO2和甲酸根的红外峰,温度高于180℃时,该催化剂上还能看到微弱的CO红外峰,说明锂离子的给电子性质有利于提高Cu1Li1Ce9Oδ催化剂上CO的不可逆脱附,抑制氢的活化吸附,同时促进了甲酸根物种的生成。低温下Cu1Mg1Ce9Oδ和Cu1Ba1Ce9Oδ催化剂上CO的吸附量较多,但主要以可逆脱附形式脱附出来,对CO选择性氧化没有贡献。     

CuO-CeO2-MnOx/γ-Al2O3催化剂选择性催化脱除NO机理研究

利用溶胶凝胶法制备CuO-CeO2-MnOx/γ-Al2O3催化剂颗粒,在固定床上测试其催化脱硝活性.CuO-CeO2-MnOx/γ-Al2O3催化剂在200～450℃范围内脱硝效率保持在70%以上.利用程序升温方法研究了催化剂对NH3的氧化性能,活性组分负载量增多,加强了催化剂对NH3氧化性能.红外表征显示NH3被吸附在催化剂的L酸位和B酸位.NO以多种硝酸盐物种在催化剂表面吸附.吸附态NH3参与SCR反应,但吸附态NO物种仅部分参加SCR反应.     

Ni_2P/介孔分子筛催化剂的原位漫反射红外光谱研究

以介孔分子筛MCM-41,MCM-48,SBA-15,SBA-16为载体,硝酸镍为镍源,磷酸氢二铵为磷源,通过浸渍法制备了含有磷化镍前体的介孔分子筛样品,然后在氢气气氛中进行程序升温还原,得到了磷化镍/介孔分子筛催化剂.采用原位漫反射红外光谱法,用CO作为探针分子,对样品的吸附特征进行了研究.结果表明,在介孔分子筛表面CO存在着较弱的物理吸附.在Ni2P/MCM-41催化剂样品表面有四种CO的吸附态:(1)在2055cm-1处形成的Ni(CO)4物种的吸附,(2)在2 091cm-1处的配位不饱和Niδ(0<δ<1)物种上的吸附,(3)在2 127 cm-1处的Ni+物种上的吸附,(4)在2 198～2 202 cm-1范围内的P物种上的吸附.在Ni2P/MCM-48,Ni2P/SBA-15,Ni2P/SBAZ-16催化剂样品表面有二种CO的吸附态:在2 051～2 055cm-1处的Ni(CO)4吸附和在2 093～2 096 cm-1处的配位不饱和Niδ+(0<δ<1)物种上的吸附.     

CO选择性氧化用Cu_1Zr_1Ce_9O_δ催化剂的红外光谱研究

采用共沉淀法制备了Cu1Zr1Ce9Oδ催化剂,用于富氢气体中CO的选择性氧化反应,利用原位漫反射红外光谱技术考察了Cu1Zr1Ce9Oδ催化剂表面上的吸附物种和反应中间产物。研究发现,H2,O2和CO物种竞争吸附于Cu1Zr1Ce9Oδ表面相同的吸附位上。氢气预处理会引起Cu1Zr1Ce9Oδ催化剂上Cu+物种的深度还原,降低了CO的吸附量。氧气预处理为催化剂提供了较多的活性氧物种,同时抑制了Cu+物种的深度还原。氦气预处理仅起到净化催化剂表面的作用。180℃时Cu1Zr1Ce9Oδ催化剂在2938.7和2843.8cm-1处出现桥式和双齿型甲酸根物种的红外吸收峰。Cu1Zr1Ce9Oδ催化剂上活性较高的氧阴离子在常温下即可将催化剂表面上吸附的CO氧化成表面碳酸根。甲酸根和碳酸根物种占据Cu1Zr1Ce9Oδ催化剂的吸附中心,导致催化剂活性降低。300℃下用氦气吹扫Cu1Zr1Ce9Oδ催化剂表面,双齿型的甲酸根物种分解生成碳酸根物种,碳酸根物种再继续分解生成CO2,释放出催化剂表面的吸附位,恢复了Cu1Zr1Ce9Oδ催化剂的活性。     

Ni2(OCH3)2/SiO2催化剂上CO2和CH3OH的吸附和反应性能

采用表面改性和离子交换相结合的方法制备了Ni2 (OCH3 ) 2 /SiO2 负载型双核金属甲氧基配合物催化剂 ,利用红外光谱 (IR)、程序升温脱附 (TPD)、程序升温表面反应 (TPSR)和微反技术考察了催化剂的表面结构以及CO2 和CH3 OH的化学吸附和反应性能 .结果表明 :Ni2 (OCH3 ) 2 /SiO2 中Ni2 + 与载体SiO2 表面O2 -以双齿配位形式键合 ,甲氧基以桥基形式联结双金属离子形成双核物种Ni2 (OCH3 ) 2 ;CO2 在催化剂表面存在甲氧碳酸酯基物种和桥式两种吸附态 ,CH3 OH则只有一种分子吸附态 ;在 10 0～ 2 0 0℃条件下 ,CO2 和CH3 OH在催化剂上的反应产物主要是DMC和H2 O ;根据反应结果 ,讨论了催化反应机理 .     

微细腔内变组分CH_4/O_2/H_2O自热重整积碳特性

针对微动力装置中重整腔内催化剂表面容易积碳,重整反应需要大量能量等问题,在重整腔入口引入氧气,使甲烷发生部分氧化反应为催化重整提供热量。本文采用数值方法研究了微细腔中CH_4/O_2/H_2O镍基催化剂上的自热重整反应,重点分析CH_4/O_2/H_2O混合物组分对甲烷自热重整反应及积碳的影响。结果表明:在混合物组分CH_4/O_2/H_2O摩尔比为1:0.2:2时,甲烷自热反应放热量刚好能满足甲烷重整反应的需求,氢气质量分数较高为3.32%,积碳浓度较低为1.19×10~(-6) kmol/m~2。     

LaFe_(1-x)Ni_xO_3钙钛矿型氧化物用于甲烷化学链水蒸气重整

采用燃烧法制备了钙钛矿型氧化物LaFe_(1-x)Ni_xO_3(x=0.1、0.15、0.2、0.3)用于甲烷化学链水蒸气重整过程,通过两步分别获得合成气(H_2+CO)和H_2。在固定床反应装置上考察甲烷与载氧体的部分氧化过程以及还原态的载氧体与水蒸气的氧化反应过程。结果表明,CH4与LaFe_(1-x)Ni_xO_3载氧体恒温反应的最佳温度为800~850℃,反应的前10min甲烷与载氧体以部分氧化为主,主要生成合成气H_2和CO。10 min之后反应以CH4裂解为主。水蒸气氧化阶段,Ni的掺杂量为x=0.1和x=0.3时的H_2浓度最高,分别为7.2%和8.3%。     

氧碳比对微细腔内自热重整积碳的影响

针对微动力装置中重整腔内强吸热重整反应和催化剂积碳等问题,耦合甲烷部分氧化反应,实现系统自供热并抑制积碳.为了优化微细腔内甲烷湿空气自热重整反应条件,采用数值方法研究预热温度为800 K,不同水碳比下,氧碳比对绝热的微细腔内甲烷湿空气自热重整反应的影响.结果表明:反应气中水碳比为1～2.5,微细腔内甲烷湿空气自热重整的...     

Ni2（OCH3）2／SiO2催化剂上C02和CH30H的吸附和反应性能

采用表面改性和离子交换相结合的方法制备了Ni2(OCH3)2／Si02负载型双核金属甲氧基配合物催化剂，利用红外光谱(IR)、程序升温脱附(TPD)、程序升温表面反应(TPSR)和微反技术考察了催化剂的表面结构以及C02和CH30H的化学吸附和反应性能．结果表明：Ni2(OCH3)2／SiO2中Ni^2+与载体SiO2表面O^2-以双齿配位形式键合，甲氧基以桥基形式联结双金属离子形成双核物种Ni2(OCH3)2；CO2在催化剂表面存在甲氧碳酸酚基物种和桥式两种吸附态，CH30H则只有一种分子吸附态；在100—200℃条件下，C02和CH30H在催化剂上的反应产物主要是DMC和H20；根据反应结果，讨论了催化反应机理．     

CO吸附和加氢反应过程的原位高压MAS NMR研究

应用原位变温高压MAS核磁共振技术,对比研究了CO在不同Rh基催化剂上的吸附和加氢反应过程. ²⁹Si MAS NMR研究结果表明：Rh基催化剂中加入金属助剂后,载体Silicate-1上的表面硅羟基减少,助剂金属与硅羟基作用锚锭在载体表面.¹³C MAS NMR研究结果表明：当引入CO/H2混合气后,在Rh/Silicate-1催化剂上只能观测到气相CO、线式吸附CO和孪式吸附CO的快速交换信号;而在Rh-Mn/Silicate-1和Rh-Mn-Li/Silicate-1催化剂上,还观测到了倾斜式吸附的CO共振信号,表明助剂Mn或Mn-Li的加入促进了CO的吸附. 随着反应温度升高,CO/H₂在Rh/Silicate-1催化剂上转化生成CO_²,进一步升高温度会有CH₄生成;而CO/H₂在RhMnLi/Silicate-1催化剂上反应活性更高,在较低的温度下就会转化生成CO₂,但未观测到甲烷的生成. ¹H MAS NMR 谱显示,反应后载体Silicate-1上硅羟基的量会减少,表明CO与载体部分表面硅羟基反应生成了CO₂.     

DRIFTS study of Cu1Zr1Ce9Odelta catalysts for selective CO oxidation

The Cu1Zr1Ce9Odelta catalysts synthesized with coprecipitation method were used into the selective CO oxidation in hydrogen-rich gas. The adsorbed species and the intermediates on Cu1Zr1Ce9Odelta catalysts were examined by in-situ diffuse reflectance FTIR spectroscopy (in-situ DRIFTS) technique. It was found that hydrogen, oxygen and CO in the feed stream were adsorbed competitively at the same adsorption sites on the surface of Cu1Zr1Ce9Odelta catalysts. The pretreatment with hydrogen caused the deep reduction of Cu+ species to Cu0 species and decreased the capacity of CO adsorption on the catalyst surface. The Cu1Zr1Ce9Odelta catalyst pretreated with oxygen offered more active oxygen species and inhibited the deep reduction of Cu+ species. The helium pretreatment only purified the surface of Cu1Zr1Ce9Odelta catalyst. Two IR bands at 2938.7 and 2843.8 cm(-1) due to bridged formate and bidentate formate species appeared at 180 degrees C. The active oxygen anion of Cu1Zr1Ce9Odelta catalyst could react with CO and produce carbonate species at room temperatures. The carbonate and formate species occupied the adsorption sites and deteriorated the catalytic performance of Cu1Zr1Ce9Odelta. Flushing the Cu1ZnrCe9Odelta catalyst with helium at 300 degrees C, the bidentate formate species on the catalyst surface decomposed to monodentate carbonate species and then further decomposed to CO2, which could release the adsorption sites and restore well the catalytic activity.     

常压等离子体作用下CO2氧化CH4转化反应的光谱分析

采用光谱原位诊断技术在200～900nm范围内采集并标识了不同CO2添加量时CH4等离子体光谱。确定了常压下不同CO2添加量时CH4等离子体的活性物种。CO2添加量不同活性物种谱峰相对强度变化趋势不同,O活性物种谱峰相对强度随CO2添加量增加迅速增加。C2活性物种谱峰相对强度随CO2添加量增加逐渐降低。反应体系产生的活性O对CH4转化反应产物具有明显影响,CO2添加量不同,CH4转化反应机理不同。当CO2添加量小于30%时,CH4转化以偶联反应为主。CO2添加量大于30%时,CH4转化以重整反应为主。     

The AC monitoring of a mixed conducting Li-Ni-Co-O catalyst during temperature programmed reactions

The temporal analysis of effluent species with temperature linearly increasing with time for two reactions, carbon dioxide hydrogenation (250° to 600°C) and the oxidative coupling of methane (400° to 800°C) have been studied. A non-stoichiometric, mixed-oxide catalyst, Li_0.9Ni_0.5Co_0.5O_2-δ, containing both mobile ions and electrons at elevated temperatures was investigated. The exit gas stream was monitored by using the multiple-ion monitoring facility of a quadrupole mass spectrometer. The AC electrical characteristics of the catalyst pellet between 100 Hz and 1 MHz were simultaneously monitored in-situ. A clear correlation between catalytic behaviour and electrical properties was obtained. Frequency-dependent AC losses due to surface dipole effects were dominant during phases of strong chemisorption and reaction, whilst reversion to thermally activated behaviour occurred during times of reduced chemical activity. In the case of carbon dioxide hydrogenation, the catalyst becomes partially reduced as a result of the chemical reaction, as shown by the changes in conductance-temperature-frequency characteristics. The original oxidised state could be recovered by re-oxidation at 700°C for 1 hour in air. For the partial oxidation of methane, mobile lattice oxygen participates in the reaction. The temporary changes in the state of oxidation of the catalyst during this reaction are correlated with changes in the electrical characteristics of the material. Paper presented at the 3rd Euroconference on Solid State Ionics, Teulada, Sardinia, Italy     

Studies of catalytic process of complete oxidation of methane by SSITKA method

This paper presents the results obtained by means of the steady state isotopic transient kinetic analysis for complete methane oxidation over the Pd(PdO)Al₂O₃ catalyst. The average surface life-time and surface concentration of methane and carbon dioxide were determined. It was found out that on the palladium catalyst there are adsorbed small amounts of methane (which does not take part in the process of oxidation) only at the temperature corresponding to the starting point of methane oxidation. Additionally, in the steady state of methane oxidation on the palladium catalyst there are present two different kinds of carbon dioxide: short- and long-resided on the catalyst surface. The average surface life-time of both kinds of carbon dioxide decreases with temperature. The surface concentration of long-resided carbon dioxide increases with temperature whereas the small maximum at about 380 °C is noticed for the surface concentration of short-resided carbon dioxide.     

Cooperative activation effect on H2O adsorption in MnO–Co catalyzed steam methane reforming

Steam methane reforming is a very important chemical process in hydrogen production and solid oxide fuel cells (SOFCs). Cobalt (Co) is an important catalyst for dry and steam methane reforming. However, previous studies have confirmed that metal Co surfaces only have weak adsorption activity for H₂O, which is evidently unfavorable for steam reforming. In this work we used first-principles simulations to study the activity of MnO–Co catalysts for the adsorption of H₂O. Compared with the Co (111) surface and pristine Co clusters, the MnO–Co catalytic layer has a stronger adsorption capability for H₂O because of the introduction of the MnO substrate, which is crucial for improving the steam reforming reaction and inhibiting carbon disposition in SOFCs. The cooperation mechanism between MnO and Co is discussed based on the analysis of electronic structures. The conclusions from this work are universal for other metal-oxide composite catalyst layers.     

Interaction of carbon monoxide and oxygen at the surface of inverse titania/Au model catalyst

Interaction of carbon monoxide and oxygen on the surface of titania/Au(1 1 1) inverse model catalyst held at 200 K has been studied by reflection absorption infrared spectroscopy. It was found that CO adsorbs on the oxide/Au perimeter interface, whereas no or very weak adsorption was observed on Au(1 1 1) or titania surface, respectively. Exposing of such species to oxygen results in their decay possibly due to carbon dioxide formation. Efficiency of this effect is higher at lower CO initial concentration which points at the importance of free surface sites for the reaction process.     

Partial catalytic oxidation of methane to synthesis gas over rhodium: in situ Raman experiments and detailed simulations

The partial catalytic oxidation of methane to synthesis gas over Rh/ZrO₂ was investigated experimentally and numerically at fuel-to-air equivalence ratios of 2.5 and 4.0 and pressures of 4 and 6 bar. Experiments were performed in an optically accessible, laboratory-scale, channel-flow catalytic reactor and involved in situ one-dimensional Raman measurements of major species (CH₄, O₂, H₂O, CO₂, H₂, CO, and N₂) concentrations across the reactor boundary layer. The numerical model included a two-dimensional elliptic code with elementary homogeneous (gaseous) and heterogeneous (catalytic) chemical reaction schemes. Homogeneous ignition experiments and numerical predictions have validated the employed gas-phase reaction mechanism and have further delineated the reactor extent over which the contribution of the homogeneous reaction pathway was negligible. Over the reactor extent where oxygen was still available, the employed heterogeneous reaction scheme provided good agreement with the measured species concentrations, overpredicting only to a small degree the partial over the total oxidation route. In the oxygen-depleted zones of the reactor, however, the heterogeneous scheme overpredicted to a greater degree the impact of steam reforming and water gas shift reactions, resulting in higher computed hydrogen yields at the reactor exit. Additional experiments and predictions were carried out in a sub-scale gas-turbine honeycomb reactor, at operating conditions leading to oxygen breakthrough. The predictions again favored the partial over the total oxidation route. A modified heterogeneous scheme was proposed that provided very good agreement with measurements in the honeycomb reactor and in the oxygen-rich zones of the laboratory-scale reactor. The hydrogen produced during partial oxidation was partly re-adsorbed on the catalyst leading to superadiabatic surface temperatures, thus exemplifying the importance of proper thermal management in commercial reactors.     

大气压非平衡等离子体甲烷干法重整零维数值模拟

大气压非平衡等离子体由于其独特的非平衡特性,可为甲烷和二氧化碳稳定温室气体分子活化和重整提供非热平衡和活化环境.本文采用了零维等离子体化学反应动力学模型,考虑了详细的CH₄/CO₂等离子体化学反应集,重点研究了反应气体CH₄/CO₂摩尔分数(5%—95%)对大气压非平衡等离子体甲烷干法重整制合成气和重要含氧化合物的影响.首先,给出了进料气体不同体积比时电子密度和温度随时间的演化规律,结果表明初始甲烷摩尔分数的提高有利于获得较高的电子密度和电子温度.随后,讨论了主要自由基和离子数密度在不同的甲烷摩尔分数下随着时间的变化规律,并给出了反应气体的转化率、合成气体和重要含氧化合物的选择性.此外,还明确了合成气和含氧化合物主要生成和损耗的化学反应路径,发现甲基和羟基是合成含氧化合物的关键中间体.最后,归纳总结给出了主要等离子体粒子之间的总体等离子体化学反应流程图.     

In situ DRIFTS研究NO在Cu-ZSM-5上的表面吸附及选择性催化还原

Cu-ZSM-5分子筛催化剂选择性催化还原NO具有较好的低温活性,在613 K时NO还原成N2的转化率达70.6%。原位漫反射红外光谱(In situ DRIFTS)是研究催化剂表面吸附物种及催化机理的重要方法,应用该方法在298～773 K范围原位考察了以C₃H₆为还原剂及富O₂ 条件下,NO在Cu-ZSM-5催化剂上的表面吸附及选择性催化还原。认为NO在Cu-ZSM-5催化剂上还原为N₂的过程中,NO以一系列NO_x吸附态形式与丙稀的活化物种(C_xH_y或C_xH_iyO_z)反应,生成有机中间体,再进一步反应,最终生成N₂。有机中间体存在一个明显的从有机胺物种到腈(或—CN)再到有机氮氧物种(R—NO₂或R—ONO)的过程,催化剂表面形成有机中间物种是关键步骤,Cu的作用是促进NO_x形成,O₂ 的作用是促进C₃H₆活化,并且是有效产生有机-氮氧化物不可缺少的条件。     

Theoretical and experimental study of methane steam reforming reactions over nickel catalyst

In this work we perform DFT theoretical calculations of methane and steam interactions on Ni(1 1 1) surface. The calculations allow us to improve our understanding of the competition between these reactants by catalytic sites in methane steam reforming (MSR) process. For this purpose we compare theoretical results with kinetic measurements of MSR on a Ni(II)-Al(III) catalyst prepared from lamellar double hydroxides as precursor. This comparison shows that, for low H₂O/CH₄ ratios methane and water intermediate species adsorb on different catalytic sites. While CHO species adsorbs on top of Ni atom, OH one occupies preferentially a tri-coordinate surface site. On the other hand, for high H₂O/CH₄ ratios a competency between these species by Ni sites would establish, diminishing methane conversion. In addition competition between methane and steam for Ni sites would lead to a decrease in CO production. Nevertheless, intermediate species adsorbed on different active sites would produce CO₂, whatever the steam/methane ratio. Thus, it would be optimum steam concentration in hydrocarbon feed and active sites distribution on catalyst surface, which could maximize H₂ production and minimize CO selectivity. The theoretical findings agree with kinetic measurements, which show that maximum methane conversion depends on steam partial pressure in the feed; whereas always, selectivity to CO₂ increases and to CO diminishes.