NO在Au／Al2O3催化剂上还原反应的TPD-MS研究

 考察了沉积－沉淀法制备的Au／Al2O3催化剂在O2存在下催化C3H6还原NO的反应，并用程序升温脱附－质谱（TPD－MS）手段研究了吸附于催化剂上的NO或NO－O2的脱附性能．结果表明：在O2存在的条件下，对于C3H6还原NO的反应，1％Au／Al2O3的催化活性最高，可于375℃左右使NO生成N2，转化率达60％．这与催化剂对所吸附NO的脱附性能密切相关，N2O可能是C3H6还原NO反应过程中产生的比较稳定的中间体．     

噻吩在γ-Mo_2N(100)表面上加氢脱硫反应的密度泛函理论研究

利用密度泛函理论研究了γ-Mo2N(100)表面上的噻吩加氢脱硫(HDS)过程.噻吩在γ-Mo2N(100)表面上不同作用形式的结构优化结果显示,η5-Mo2N吸附构型最稳定,具有最大的吸附能(-0.56 eV),此时噻吩通过S原子与Mo2原子相连平行表面吸附在四重空位(hcp位).H原子和噻吩在hcp位发生稳定共吸附,hcp位是噻吩HDS的活性位点.噻吩在γ-Mo2N(100)表面进行直接脱硫反应,HDS过程分为S原子脱除和C4产物加氢饱和两部分.过渡态搜索确定了HDS最可能的反应机理及中间产物,首个H原子的反应需要最大的活化能(1.69 eV),是噻吩加氢脱硫的控速步骤.伴随H原子的不断加入,噻吩在γ-Mo2N(100)表面上优先生成―SH和丁二烯,随后―SH加氢生成H2S,丁二烯加氢饱和生成2-丁烯和丁烷.由于较弱的吸附,H2S、2-丁烯和丁烷很容易在γ-Mo2N(100)表面脱附成为产物.     

用TPD研究SO2对NO催化氧化过程的影响

 针对活性氧化铝载体及过渡金属氧化物催化剂上SO2增强NO吸附并促进其氧化的实验事实，考察了反应温度对SO2发挥促进作用的影响．结果发现，在50～250℃间存在一适宜的温度范围，能使氧化铝上原本不氧化的NO在SO2气氛中发生氧化．对氧化铝预吸附不同组成的气体及在不同温度下吸附NO－O2－SO2后进行了TPD研究．结果表明，SO2的存在对NO氧化吸附生成NO2高温脱附物种有利．对Co3O4／Al2O3催化剂上吸附SO2－NO2的TPD研究结果显示，SO2先吸附或与NO2共吸附都能使NO2高温物种脱附增强，同时SO2的弱吸附物种转变成强吸附物种或表面硫酸盐物种，意味着弱吸附的SO2能与NO2形成稳定的物种；而后吸附的SO2竞争占据NO2的吸附位．推测表面上弱吸附的SO2与NO－O2或NO2之间形成了多分子的活性物种．     

介质阻挡放电等离子体与吸附在CuZSM-5上的NO或NO/O2的相互作用

采用吸附和程序升温脱附(TPD)技术研究了介质阻挡放电等离子体对CuZSM-5催化剂上吸附的氮氧化物作用. 实验表明, 介质阻挡放电等离子体使催化剂表面吸附的NO及Cu活性位上吸附的NOx物种脱附, 并引发表面化学反应生成新的氮氧化物. 对于NO/N2体系, 介质阻挡放电等离子体与吸附在CuZSM-5上NO作用, 主要生成N2O和O2. 在富氧体系NO/O2/N2, 则生成较大量的N2O、NO2和NO. 等离子体预处理活性下降的CuZSM-5, 可明显提高其催化分解NO活性. 对比有或无介质阻挡放电等离子体预处理NO或NO/O2饱和吸附的CuZSM-5上的NO-TPD结果表明, 等离子体提高催化剂活性的原因与其使催化剂Cu活性位上吸附的NOx物种脱附有关.     

介质阻挡放电等离子体与吸附在CuZSM-5上的NO或NO/O2的相互作用

采用吸附和程序升温脱附(TPD)技术研究了介质阻挡放电等离子体对CuZSM-5催化剂上吸附的氮氧化物作用.实验表明,介质阻挡放电等离子体使催化剂表面吸附的NO及Cu活性位上吸附的NOx物种脱附,并引发表面化学反应生成新的氮氧化物.对于NO/N2体系,介质阻挡放电等离子体与吸附在CuZSM-5上NO作用,主要生成N2O和O2.在富氧体系NO/O2/N2,则生成较大量的N2O、NO2和NO.等离子体预处理活性下降的CuZSM-5,可明显提高其催化分解NO活性.对比有或无介质阻挡放电等离子体预处理NO或NO/O2饱和吸附的CuZSM-5上的NO-TPD结果表明,等离子体提高催化剂活性的原因与其使催化剂Cu活性位上吸附的NOx物种脱附有关.     

程序升温脱附研究CoH-FBZ上NOx的吸附

富氧条件下具有FAU和BEA两种拓扑结构的CoH-FBZ选择催化CH4还原NO，显示出较CoH Y和CoH Beta机械混合催化剂更好的催化活性。应用吸附和程序升温脱附(TPD)方法研究了NO和NO+O2与催化剂表面间的相互作用。结果表明，载体的拓扑结构直接影响N、O物种在催化剂表面的稳定性。NO与O2在CoH-FBZ表面形成的吸附态 NOy及NO在CoH-FBZ表面形成的吸附态相对更稳定。CoH-FBZ的NO+O2-TPD脱附曲线在630K和660K形成两个NO2脱附峰，表明在CoH-FBZ表面形成了新的 NOy吸附中心，即可能有新的Co位产生，该新Co位与沸石催化剂CoH-FBZ中新强酸位协同作用，使CoH-FBZ表现出新的CH4-SCR催化特性。     

氮在含氧Mo(100)面上的吸附与反应

 用HREELS, AES, LEED和TDS考察了氮在含氧Mo(100)上的吸附和热脱附. 120 K下氮在含氧Mo(100)上吸附时存在着N—N伸缩振动频率2150和1600 cm-1, 分别对应于线式(γ态)和侧位(α态)两种分子吸附态. 升温引起γ态氮的脱附和α态氮的解离. 其中γ态氮的脱附峰温位于155 K, 遵循一级脱附动力学; 由α态解离生成的N原子占据Mo(100)的四重空位(即β态), 并在高于1?150 K的温度重新化合形成氮而脱附. 120 K时,氮的吸附是无序的; 吸附了氮的表面经1100 K退火后生成了有序的c(2×2)-N表面结构.     

ZrO_2酸碱性质的TPD表征Ⅰ.单组分吸附研究

以NH3、吡啶、Et3N、CO2和苯酚为探针，用TPD－MS方法对ZrO2催化剂的酸碱性质进行了表征．ZrO2上碱性探针（NH3、吡啶和Et3N）的脱附温度远低于在强酸性SiO2－Al2O3上；而酸性探针CO2的脱附温度远低于在强碱性MgO上的结果．为ZrO2的弱酸弱碱性质提供了证明．NH3吸附IR结果表明ZrO2表面配位不饱合Zr4＋为酸（Lewis酸）中心．NH3、吡啶和Et3N与这些酸中心作用的方式和能量分布相似．NH3和CO2的TPD谱图均存在三个脱附峰，且相应脱附峰的温度范围相近．表明ZrO2的酸中心和碱中心具有匹配相当的酸、碱强度，ZrO2为典型的酸－碱双功能催化剂，在苯酚的TPD过程中，ZrO2的特征表现为对苯酚的强吸附和对苯酚分解的高活性．文中结合IR结果，对与NH3和CO2的脱附相联系的表面吸附物种分别进行了讨论．     

Mo2N的表面性质和加氢脱氮活性

以XRD、H2－TPD、TPS方法研究了钝化和硫化处理对Mo2N体相结构和表面性质、以及对吡啶加氢脱氮（HDN）催化活性的影响。Mo2N经钝化或在673K硫化后，虽然其体相结构不发生变化，但其表面性质却发生了明显的异变，并伴随其加氢脱氮活性的显著降低．由Mo2N在不同钝化条件下生成的部分氧化产物以及H2－TPD结果，推测在缓慢钝化条件下，Mo2N表面钝化层为MoO2根据Mo2N硫化后的H2－TPD和相应HDN活性变化，以及Mo2N的TPS结果，认为Mo2N经673K硫化后其表面结构发生了硫化异变．     

铁助剂对Rh-Mn-Li/SiO2催化剂表面上的CO脱附和CO加氢行为的影响

 采用一氧化碳程序升温脱附（CO－TPD）和吸附的一氧化碳加氢程序升温表面反应（TPSR）考察了Fe助剂对Rh基催化剂上CO的脱附行为及吸附CO的加氢行为的影响．CO－TPD实验表明，在Rh／SiO2催化剂上CO有三个脱附峰．在Rh－Mn－Li／SiO2中加入0．05％Fe后，高温脱附CO比Rh／SiO2催化剂上相应的CO量大．增加Fe的负载量，CO的脱附量减少．TPSR实验中，CO加氢反应的主要产物是甲烷．不同组分的催化剂上甲烷的生成温度有如下顺序：Rh／SiO2（482K）＜Rh－Mn－Li／SiO2（489K）＜Rh－Fe／SiO2（494K）＜Rh－Mn－Li－Fe／SiO2（501K）．甲烷峰的产生伴随着CO（s）高温脱附峰的消失，说明甲烷是由强吸附的CO加氢生成的．     

微量热法研究γ-Mo2N催化剂表面氢的微分吸附热

Differential heats of H 2 adsorption on γ-Mo2N catalysts were studied by using microcalorimetry. Samples with high and medium surface areas (90 and 17 m2•g -1 ) present a homogeneous energetic distribution of surface sites, which corresponds with the preferential orientation of their (200) planes. Molybdenum nitride with low surface area (8 m2•g -1 ) displays a heterogeneous energetic distribution of H 2 adsorption sites. The higher initial differential heat of hydrogen adsorption observed for the low surface Mo nitride was attributed to species adsorbed on surface sites associated with the (111) plane.     

Valence state of Mo and surface coverage of alumina by molybdenum-oxygen species in MoOx/Al2O3

CO₂ chemisorption, BET surface area and the degree of reduction of Mo(VI) (e/Mo) have been determined in MoO_x/Al₂O₃ samples, reduced with hydrogen at temperatures between 673 and 1173 K. The free alumina surface figures calculated from the surface area and e/Mo values were identical with those obtained from direct CO₂ chemisorption measurements. This identity indicates that all of the oxygen ions of the surface molybdenum-oxygen species block the alumina surface.     

Temperature-programmed desorption and adsorption of hydrogen on Mo2N

Hydrogen adsorption-desorption over Mo₂N has been studied using a temperature-programmed technique. It is revealed that hydrogen on Mo₂N exhibits very high mobility leading to migration of the surface hydrogen into the sublayer and bulk of the sample or the reverse. The surface hydrogen species are preferentially formed when adsorption is carried out below 573 K. On increasing the adsorption temperature to above 573 K, the quantity of hydrogen species located in the sublayer or/and bulk of the Mo₂N sample increases significantly.     

Hydrogen desorption of reduced Pt/TiO2 catalyst

The temperature-programmed desorption of hydrogen from a Pt/TiO₂ catalyst reduced in a wide temperature range (RT-773 K) has been studied. It is found that the presence of labile surface oxygen species increases the amount of hydrogen species formed at room temperature, and greatly decreases the quantities of adsorbed hydrogen species at medium temperatures. After the catalyst was reduced at high temperature, it is observed that two strong hydrogen desorption peaks appear at 450–600 K and above 600 K, which are ascribed to surface titanium hydride and the hydrogen species stored in the sublayer and bulk of the support, respectively.     

IR-analysis of H-bonded H2O on the pure TiO2 surface

The surface state of optically pure polydisperse TiO₂ (anatase and rutile) was determined by infra-red (IR) spectroscopy analysis in the temperature range of 100–453 K. Anatase A300 spectrum, contrary to rutile R300 one, has a broad three-component absorption band with peaks at 1048, 1137 and 1222 cm⁻¹ in the spectral range of δ(Ti–O–H) deformation vibrations. For rutile R300 we observed a very weak band at 1047 cm⁻¹, and for the thermal treated rutile R900 these bands were not appeared at all. The analysis of temperature dependencies for the mentioned absorption bands revealed the spectral shift of 1222 cm⁻¹ band towards the high frequencies, when the temperature increased, but the spectral parameters of 1137 and 1048 cm⁻¹ bands remained the same. The temperature of 1222 cm⁻¹ band maximum shift was 373–393 K and correlated with DSC data. Obtained results allowed to assign 1222 cm⁻¹ band to the deformation vibrations of OH-groups, bounded to the surface adsorbed water molecules by weak hydrogen bonds (5 kcal/mol). During the temperature growth these molecules desorbed, which also resulted in the intensity decreasing of stretching OH-groups vibration IR-bands at 3420 cm⁻¹. The destruction and desorption of surface water complexes led to Ti–O–H bond strengthening. IR bands at 1137 and 1048 cm⁻¹ were attributed to the stronger bounded adsorbed water molecules, which are also characterized with stretching OH-groups vibration bands at 3200 cm⁻¹. These surface structure were additionally stabilized by hydrogen bonds with the neighbouring TiO₂ lattice anions and other OH-groups, and desorbed at higher temperatures.     

H2在K0-MWCNTs上储存和吸附/脱附特性研究

利用高压容积法辅以卸压升温脱附排水法, 测定金属K修饰多壁碳纳米管对H₂的吸附储存容量. 结果表明, 在室温(25 ℃), 7.25 MPa实验条件下, x%K⁰-MWCNTs (x%＝30%～35%, 质量百分数)对H₂的吸附储存容量可达3.80 wt%(质量百分数), 是相同条件下单纯MWCNTs氢吸附储量的2.5倍; 室温下卸至常压的脱附氢量为3.36 wt%(占总吸附氢量的～88%), 后续升温至673 K的脱附氢量为0.41 wt%(占总吸附氢量的～11%). 利用LRS和H₂-TPD-GC/MS等谱学方法对H₂/K⁰-MWCNTs吸附体系的表征研究表明, H₂在K⁰-MWCNTs上吸附存在非解离 (即分子态)和解离(即原子态)两种吸附态; 在≤723 K温度下, H₂/K⁰-MWCNTs体系的脱附产物几乎全为H₂气; 723 K以上高温脱附产物不仅含H₂, 也含有CH₄, C₂H₄和C₂H₂等C₁/C₂-烃.     

Conversion of NO in NO/N2, NO/O2/N2, NO/C2H4/N2 and NO/C2H4/O2/N2 Systems by Dielectric Barrier Discharge Plasmas

An experimental study on the conversion of NO in the NO/N₂, NO/O₂/N₂, NO/C₂H₄/N₂ and NO/C₂H₄/O₂/N₂ systems has been carried out using dielectric barrier discharge (DBD) plasmas at atmospheric pressure. In the NO/N₂ system, NO decomposition to N₂ and O₂ is the dominating reaction; NO conversion to NO₂ is less significant. O₂ produced from NO decomposition was detected by an on-line mass spectrometer. With the increase of NO initial concentration, the concentration of O₂ produced decreases at 298 K, but slightly increases at 523 K. In the NO/O₂/N₂ system, NO is mainly oxidized to NO₂, but NO conversion becomes very low at 523 K and over 1.6% of O₂. In the NO/C₂H₄/N₂ system, NO is reduced to N₂ with about the same NO conversion as that in the NO/N₂ system but without NO₂ formation. In the NO/C₂H₄/O₂/N₂ system, the oxidation of NO to NO₂ is dramatically promoted. At 523 K, with the increase of the energy density, NO conversion increases rapidly first, and then almost stabilizes at 93–91% of NO conversion with 61–55% of NO₂ selectivity in the energy density range of 317–550 J L⁻¹. It finally decreases gradually at high energy density. A negligible amount of N₂O is formed in the above four systems. Of the four systems studied, NO conversion and NO₂ selectivity of the NO/C₂H₄/O₂/N₂ system are the highest, and NO/O₂/C₂H₄/N₂ system has the lowest electrical energy consumption per NO molecule converted.     

NO在Mn_2O_3(110)表面吸附的密度泛函理论研究

基于第一性原理密度泛函计算方法研究了NO在Mn_2O_3(110)面的吸附行为,计算了Mn_2O_3(110)面吸附NO和O_2的吸附构型的结构参数、吸附能和电子结构.结果表明,在Mn_2O_3(110)表面上,NO倾向于吸附在Mn top位,吸附前后的结构总能变化在-0.61~-1.29 eV之间,NO吸附后Mn吸附位周围的配位结构发生变化,使得Mn的电子向NO转移.进一步研究了吸附O_2后的Mn_2O_3表面再进一步吸附NO的行为,发现了ONOO*结构的形成.NO和O_2在表面共吸附形成ONOO*结构时的吸附能(-1.23和-1.39 eV)高于单纯吸附NO时的吸附能,此时Mn的电子向ONOO*结构转移,NO和O_2投影态密度的电子峰广泛交叠,说明成键原子之间有强共价键作用.     

Co-K-Mo/γ-Al2O3催化剂的合成低碳醇性能及其结构研究

氧化态Ｋ－ＭｏＯ３／γ－Ａｌ２Ｏ３催化剂中添加Ｃｏ（ＮＯ３）２后在空气中四个不同温度下焙烧再硫化,制得Ｃｏ－Ｋ－ＭｏＯ３／γＡｌ２Ｏ３催化剂,对其ＣＯ加氢合成低碳醇的催化反应性能进行了评价,运用ＸＲＤ,ＬＲＳ及ＥＸＡＦＳ等手段对催化剂及其氧化态前躯体的结构进行了表征,活性测试结果表明加Ｃｏ后于５００－６５０℃焙烧制得的催化剂活性较高,且使Ｃ２＋醇比例增加,结构分析结果显示加Ｃｏ后３５０℃焙烧时,Ｃ     

Kinetic investigation of the textile bleaching process

Volumetric H₂-uptake measurements on an Mo₂N (79 m²g^–1) sample reduced at 673 K have been carried out and the uptake isotherms in the temperature range of 308–623 K have been determined. Both the total and reversible hydrogen uptake increased with the uptake temperature. The irreversible hydrogen uptake increased abruptly when the uptake temperature was raised up to 423 K. The maximum of irreversible hydrogen uptake was measured at 473 K. The H_IR/Mo ratio calculated from the uptakes obtained in the temperature range of 308–623 K varies in the range of 0.0010–0.0202. One possible mechanism for hydrogen adsorption is proposed to be heterolytic dissociation on Mo-N paris, in which the molybdenum atoms are in unsaturated coordination.