以水滑石及类水滑石为前体制备的Ni、Mg、Al混合氧化物的合成和表征

采用了BET、XRD、TG-DSC、TPR、FTIR、微量量热吸附和异丙醇催化反应等测试方法，对以共沉淀法合成的水滑石(HT)和类水滑石(HTLcs)为前体制备的4Mg/Al、3Ni/Mg/Al、3.5Ni/0.5Mg/Al和4Ni/Al混合氧化物和前体进行了研究。测定表明：制备的混合氧化物的比表面积较大、随着镍含量的增大而降低。由于Ni²⁺离子的氧化还原属性，Ni²⁺离子进入后，削弱了HT层对阴离子的键合能力，从而使得样品的热分解温度及热稳定性降低，导致焙烧后     

镍镁铝类水滑石的超分子结构、电子性质及稳定性

以Ni²⁺同晶取代Mg²⁺的方式构建镍镁铝类水滑石(HT)的周期性计算模型, 通过进行密度泛函理论计算,研究了含镍水滑石的的超分子结构、电子性质及稳定性. 结果表明, 随着镍离子逐渐取代镁离子, 金属离子之间的平均距离逐渐减小, 层间距逐渐增大, 与实验结果一致. 与此同时, 电子逐渐从主体层板向客体阴离子传递,导致主客体之间的静电作用力及整体超分子作用力逐渐增强, 结合能的绝对值逐渐增大, 体系的稳定性增加.在微观结构上, 电子传递行为使层板中平均金属―氧键键长逐渐减小, 且金属配位角的畸变情况得到一定程度的缓解, 这些变化都有利于形成更稳定的体系, 说明镍铝类水滑石在理论上比镁铝水滑石更稳定.     

水滑石焙烧产物-镁铝复合氧化物表面性质的反相气相色谱研究

用共沉淀法制备的镁铝水滑石(Mg/Al物质的量比为3),经一定温度焙烧后,得到“笼”状结构的复合氧化物,并采用反相气相色谱法(IGC)对复合氧化物和混合氧化物(氧化镁和氧化铝)的表面性质进行了研究。实验测得一系列探针分子在复合氧化物和混合氧化物上的保留时间,可计算出其吸附热力学函数(吸附自由能(ΔG^?),吸附焓(ΔH^?),吸附熵(ΔS^?)),表面能色散组分(γ_S^d)及复合氧化物的表面酸碱参数(K_A,K_D),并探讨了探针分子在复合氧化物上的吸附机理。结果表明,探针分子进入复合氧化物的“笼”状结构后,可以减小温度对探针分子吸附过程的影响。此外,计算出复合氧化物的表面酸碱参数K_A=3.21及K_D=21.02,定量地表明镁铝复合氧化物是一种两性偏碱的材料。     

Co2+含量对CoAl-LDHs焙烧产物结构、组成及其生长碳纳米管的影响

采用成核晶化隔离法将Co²⁺引入层状双金属氢氧化物(LDHs),得到了含不同Co²⁺/Al³⁺物质的量的比为1∶1,2∶1,3∶1的二元钴铝碳酸根型LDHs(CoAl-LDHs)。通过X射线衍射(XRD)、透射电镜(TEM)、扫描电镜-能量散射谱(SEM-EDS)、拉曼光谱(Raman)、程序升温还原(TPR)及X射线光电子能谱(XPS)等方法对CoAl-LDHs焙烧产物的结构、组成及其化学气相沉积(CCVD)催化生长多壁碳纳米管(CNTs)进行了研究。结果表明：CoAl-LDHs前体中钴的含量可以明显改变焙烧产物的组成分布和还原性能,并最终影响CNTs的生长,其中以n_Co²⁺/n_Al³⁺比为2/1的LDHs作为催化剂前体可以得到管径均匀和石墨化程度高的CNTs,这与还原得到的纳米活性Co颗粒均匀分散有关。     

镍铁水滑石及其衍生混合氧化物的制备和表征

采用共沉淀法合成了Ni/Fe摩尔比为1、2、3、6和10的NiFe水滑石。热重-差热结果显示NiFe水滑石的分解有二个过程，分别对应于200℃和300℃的吸热峰。经400℃焙烧后，NiFe水滑石转变为具有较高表面积的NiFeO混合氧化物(约100 m²/g)，其XRD结果仅显示NiO的衍射峰；经800℃焙烧后，NiFeO仍有15 m²/g左右的表面积。穆斯堡尔谱测定表明NiFeO混合氧化物较Fe₂O₃易还原。     

层状钴氧化物Bi2-xAgxSr2Co2O8-δ的高温热电性能及XPS研究

采用固相反应法制备了组成为Bi_2-xAg_xSr₂Co₂O_8-δ(x=0.0, 0.4, 0.8,略写为BAC-222)的层状钴氧化物陶瓷。利用X-射线光电子能谱考察该类化合物的电子结构,结果表明钴离子以Co³⁺和Co⁴⁺混合价态形式存在,n_Co⁴⁺/n_Co³⁺的比例随着Ag掺杂的量增加而增加。O1s光电子谱显示在所有样品中均存在点阵氧和吸附氧。热电性能测试结果显示,随着Ag掺杂量的增加,电导率显著增加而Seebeck系数几乎保持不变,Ag的引入极大的影响了BAC-222的电子输运性质,其功率因子在1 123 K时达到了1.23×10^-4 W·m^-1·K^-2,是一种具有很好应用前景的热电材料。     

以镁铝水滑石为前驱体制备复合氧化物催化丙酮气相缩合反应

采用共沉淀-恒温晶化法制备了系列镁铝水滑石(Mg-Al-LDH)样品,对镁铝水滑石在500 ℃焙烧得到镁铝复合氧化物(Mg-Al-LDO),采用IR、XRD、CO₂-TPD、SEM及N₂吸附-脱附等方法对Mg-Al-LDH和Mg-Al-LDO进行了表征。在温度250 ℃、液时空速1 h^-1条件下,采用固定床对镁铝复合氧化物催化剂对丙酮缩合反应的性能进行微反活性评价。研究结果表明,晶化时间与镁铝复合氧化物的弱碱性位和强碱性位的密度相关。丙酮缩聚反应的主要产物为异佛尔酮(IP)和异丙叉丙酮(MO),以及少量的异丙烯基丙酮、双丙酮醇,均三甲苯等。丙酮缩聚制备异佛尔酮的反应需要催化剂表面弱碱性位(S_w)与强碱性位(S_s)的协同作用,S_w与S_s需要匹配。晶化12 h得到的镁铝复合氧化物催化剂(LDO-12)的S_w/S_s=1.3,异佛尔酮(IP)选择性为65.3%,单程有效收率(IP+MO)为14.8%。     

Co金属有机骨架模板制备NiCo水滑石/泡沫镍复合材料及电容性能

通过两步法先在泡沫镍(nickel foam,NF)上原位生长Co金属有机骨架(Co metal-organic framework,Co-MOF)纳米片阵列,再浸入不同浓度Ni²⁺离子溶液刻蚀Co-MOF纳米片,在NF表面得到NiCo水滑石(NiCo layered double hydroxide,NiCo-LDH)。NiCo-LDH/NF继承了Co-MOF纳米片结构形成一级纳米片阵列,并在一级纳米片表面形成次级纳米片褶皱。在2 mmol Ni(NO₃)₂·6H₂O溶液中刻蚀得到的NiCo-LDH/NF表现出高容量、高倍率性能,在电流密度为5 mA·cm^-2时比电容为7 764.5 mF·cm^-2,电流密度为20 mA·cm^-2时比电容为6 098.2 mF·cm^-2,容量保持率为78.5%,在20 A·g^-1电流密度下经过5 000次长循环后,容量保持率为85.9%。与活性炭组装的混合电容器达到38.9 Wh·kg^-1的最大能量密度和8 000.0 W·kg^-1的最大功率密度。     

NiAl类水滑石/皂石层状复合材料的制备及结构表征

以NiAl类水滑石和八面体片阳离子为Zn²⁺的皂石为前体，利用两前体层板带电荷的相反性和层间域离子的可交换性，在室温、常压的温和实验条件下，将带正电荷的类水滑石层板引入到带负电荷的皂石层间，首次合成出了一种新型层状复合材料——NiAl类水滑石/皂石层状复合材料。XRD、DTA、IR和²⁷Al MAS NMR的测试结果表明，类水滑石八面体层板已顺利插层到皂石片层之间，复合材料在c轴方向是单个皂石层板与单个类水滑石层板的交叉堆叠。DTA分析结果还表明，该层状复合材料具有高热稳定性，结构破坏温度高达837 ℃。     

富氧条件下Co/ZSM-5催化剂对C3H8选择还原NOx的性能

采用多种物理化学手段研究了在模拟的轻型柴油车尾气中不同Co担载量及Cu掺杂的Co/ZSM-5催化剂的Co组分分散状态、可还原性、NO吸附脱附性质对C₃H₈选择性催化还原NO_x性能的影响。结果表明,浸渍法制备的Co/ZSM-5催化剂上既有外表面上的Co³⁺和Co²⁺物种,也有孔内的Co²⁺离子。富氧条件下Co/ZSM-5催化剂上C₃H₈选择性催化还原NO_x的活性主要与ZSM-5载体孔外表面分散的CoO_x物种中的钴离子可还原能力和NO吸附脱附性能密切相关。Co/ZSM-5催化剂上适宜的Co担载量约为4.0wt%,低担载量时随Co担载量增加,表面CoO_x物种中钴离子可还原能力增强,C₃H₈选择性催化还原NO_x的低温转化活性增加;高担载量时,随Co担载量增加,单位Co离子的NO吸附量的减少以及催化剂表面活性中心数的减少,导致了Co/ZSM-5催化剂NO_x的转化率和催化剂比速率（k）的下降。孔外表面Co₃O₄晶体的存在使催化剂表面产生较强的NO吸附,并在高温时有利于C₃H₈的氧化燃烧,使C₃H₈选择性催化还原NO_x的活性降低。     

Co-Mg/Al类水滑石衍生复合氧化物上N2O催化分解的研究

恒定二价与三价阳离子比为3((nCo+nMg)/nAl=3), 采用共沉淀法制备不同Co含量的系列类水滑石前驱物CoxMg3-xAl-HT(x=0, 0.5, 1, 1.5, 2, 2.5, 3), 经焙烧得到其衍生复合氧化物催化剂CoxMg3-xAlO. 采用XRD、BET、TG-DSC和TPR等表征手段考察了Co含量对材料前驱物及其衍生复合氧化物组成和结构等方面的影响, 研究了系列CoxMg3-xAlO催化剂的催化N2O分解性能; 同时探讨了反应条件, 如N2O浓度、空速、O2和H2O等因素对催化剂活性的影响. 结果表明, 所有前驱物材料均能形成完整的层状水滑石结构；经高温焙烧后形成了以Co-Al尖晶石为主相的复合氧化物, 且Co掺杂有助于尖晶石相的生成； Co含量对材料的热稳定性、比表面、可还原性和催化分解活性有显著的影响；含Co复合氧化物催化材料存在两个还原峰, 还原过程为Co3+→Co2+→Co；Mg有助于提高催化剂的热稳定性；随着Co含量增加, 催化剂比表面下降, 但比表面不是影响催化剂活性的主要因素； 500 ℃焙烧后的Co2.5Mg0.5AlO催化剂具有较好的N2O催化分解活性；提高前驱物的焙烧温度导致催化剂的活性下降；N2O浓度、空速及O2对催化剂活性的影响较小, 而H2O则对催化剂的活性有较大的影响.     

Synthesis of Ni／Mg／Al Layered Double Hydroxides and Their Use as Catalyst Precursors in the Preparation of Carbon Nanotubes

Ni/Mg/Al layered double hydroxides(LDHs) with different n(Ni) : n(Mg) : n(Al) ratio values were prepared via a coprecipitation reaction. Then Ni/Mg/Al mixed oxides were obtained by calcination of these LDHs precursors. Carbon nanotubes were produced in the catalytic decomposition of propane over the Ni/Mg/Al mixed oxide catalysts. The quality of as-made nanotubes was investigated by SEM and TEM. The nanotubes were multiwall with a high length-diameter ratio and appeared to be flexible. The catalytic activities of these mixed oxides increased with increasing the Ni content. The Ni/Mg/Al mixed oxide with the highest Ni content [ n( Ni)/n( Mg)/n(Al) = 1/1/1 ] showed the highest activity and the carbon nanotubes grown on its surface had the best quality.     

Hydrotalcite-derived Co-containing mixed metal oxide catalysts for methanol incineration

The Co–Mg–Al mixed metal oxides were prepared by calcination of co-precipitated hydrotalcite-like precursors at various temperatures (600–800 °C), characterised with respect to chemical (AAS) and phase (XRD) composition, textural parameters (BET), form and aggregation of cobalt species (UV–vis-DRS) and their redox properties (H₂-TPR, cyclic voltammetry). Moreover, the process of thermal decomposition of hydrotalcite-like materials to mixed metal oxide systems was studied by thermogravimetric method combined with the analysis of gaseous decomposition products by mass spectrometry. Calcined hydrotalcite-like materials were tested as catalysts for methanol incineration. Catalytic performance of the oxides depended on cobalt content, Mg/Al ratio and calcination temperature. The catalysts with lower cobalt content, higher Mg/Al ratio and calcined at lower temperatures (600 or 700 °C) were less effective in the process of methanol incineration. In a series of the studied catalysts, the best results, with respect to high catalytic activity and selectivity to CO₂, were obtained for the mixed oxide with Co:Mg:Al molar ratio of 10:57:33 calcined at 800 °C. High activity of this catalyst was likely connected with the presence of a Co–Mg–Al spinel-type phases, containing easy reducible Co³⁺ cations, formed during high-temperature treatment of the hydrotalcite-like precursor.     

XPS characterization of the reduction and synthesis behaviour of Co/Mn oxide catalysts for Fischer-Tropsch synthesis

Summary The surface composition of Co/Mn oxide catalysts after calcination, reduction and during CO hydrogenation experiments were investigated by XPS. The bulk changes during reduction were studied by Temperature Programmed Reduction (TPR). The calcined catalysts showed Co/Mn oxides of different compositions in their surfaces. The Co surface concentration, of the catalysts with high Co content, decreased after calcination compared to the bulk composition, but after reduction the bulk concentration was almost reached again. The catalysts with low Co content showed no decrease in the surface concentrations after calcination. Significant differences in surface concentrations for the catalysts Co20 and Co5 were observed by analysing the Co 2p and 3p levels, respectively; these can be explained by an internal reduction model. After reduction the sample Co100 was completely reduced to metallic cobalt. In the manganese-containing catalysts, after in-situ reduction, Co³⁺ and Co²⁺ were found; all manganese was reduced to Mn²⁺. A comparison of the results of the in-situ reduction and the TPR profiles led to the development of a so called internal reduction model. This model assumes migration of the Co²⁺ ions to the reduction front in inner layers of the catalysts, where they will be reduced to metallic cobalt; this is enriched in the bulk and cannot be found at the surface. The manganese matrix stabilizes the surface oxide layer so that all catalysts exhibited Co/Mn spinels in the surface. Synthesis experiments in the reaction chamber of the XPS apparatus did not lead to changes of the catalyst surfaces as a function of the reaction pressure, synthesis time or synthesis gas composition. The differences in the synthesis behaviour observed for the catalysts must be due to other effects, (i.e. a change in adsorption of hydrogen connected with a change in hydrogenation activity or the different cobalt concentrations).     

含钯类水滑石衍生复合氧化物Pd/M3AlO(M=Mg,Co, Ni,Cu, Zn)催化剂上氯苯的催化氧化

采用共沉淀法制备了系列含Pd类水滑石材料, 类水滑石基体为M3Al-HT (M=Mg, Co, Ni, Cu, Zn), 经焙烧制备出含Pd类水滑石衍生复合氧化物催化剂. 通过X射线衍射(XRD), 热重-差热分析(TG-DTG), H2程序升温还原(H2-TPR), O2程序升温脱附(O2-TPD)和N2吸脱附等表征技术手段研究了不同二价金属元素对含Pd类水滑石衍生复合氧化物催化剂物理化学性质及其对挥发性有机污染物氯苯催化氧化性能的影响. XRD和TG-DTG结果表明, 不同二价金属元素, 除Cu外, 都能形成类水滑石层状结构, Pd在不同类水滑石前驱物中均能良好分散. 不同的二价金属元素对催化剂性能的影响不同, 其中Pd/Co3AlO催化剂表现出最高的氯苯催化氧化活性, 其起燃温度和全转化温度分别为182和283 ℃. H2-TPR和O2-TPD测试表明, Pd和类水滑石衍生复合氧化物存在着协同作用, Pd的引入促进了复合氧化物的还原, 从而影响氧化物的氧化还原性能. Pd/M3AlO系列催化剂的活性主要受催化剂的氧化还原性能及其表面活性氧物种的影响.     

＂Intelligent＂ reforming catalysts： Trace noble metal-doped Ni/Mg（A1）O derived from hydrotalcites

Trace amounts of noble metal-doped Ni/Mg(Al)O catalysts were prepared starting from Mg-Al hydrotalcites (HTs) and tested in daily start-up and shut-down (DSS) operation of steam reforming (SR) of methane or partial oxidation (PO) of propane. Although Ni/Mg(Al)O catalysts prepared from Mg(Ni)-Al HT exhibited high and stable activity in stationary SR, PO and dry reforming of methane and propane, the Ni/Mg(Al)O catalysts were drastically deactivated due to Ni oxidation by steam as purge gas when they were applied in DSS SR ofmethane. Such deactivation was effectively suppressed by doping trace amounts of noble metal on the catalysts by using a “memory effect” of HTs. Moreover, the noble metal-doped Ni/Mg(Al)O catalysts exhibited “intelligent” catalytic behaviors, i.e., self-activation and self-regenerative activity, leading to high and sustainable activity during DSS operation. Pt was the most effective among noble metals tested. The self-activation occurred by the reduction of Ni2+ in Mg(Ni,Al)O periclase to Ni0 assisted by hydrogen spillover from Pt (or Pt-Ni alloy). The self-regenerative activity was accomplished by self-redispersion of active Ni0 particles due to a reversible reductionoxidation movement of Ni between the outside and the inside of the Mg(Al)O periclase crystal; surface Ni0 was oxidized to Ni2+ by steam and incorporated into Mg(Ni2+,Al)O periclase, whereas the Ni2+ in the periclase was reduced to Ni0 by the hydrogen spillover and appeared as the fine Ni0 particles on the catalyst surface. Further a “green” preparation of the Pt/Ni/[Mg3.5Al]O catalysts was accomplished starting from commercial Mg3.5-Al HT by calcination, followed by sequential impregnation of Ni and Pt.     

Hydrogen production from simulated hot coke oven gas by catalytic reforming over Ni/Mg（Al）O catalysts

Hydrogen production by catalytic reforming of simulated hot coke oven gas (HCOG) with toluene as a model tar compound was investigated in a fixed bed reactor over Ni/Mg(Al)O catalysts. The catalysts were prepared by a homogeneous precipitation method using urea hydrolysis and characterized by ICP, BET, XRD, TPR, TEM and TG. XRD showed that the hydrotalcite type precursor after calcination formed (Ni, Mg)Al₂O₄ spinel and Ni-Mg-O solid solution structure. TPR results suggested that the increase in Ni/Mg molar ratio gave rise to the decrease in the reduction temperature of Ni²⁺ to Ni⁰ on Ni/Mg(Al)O catalysts. The reaction results indicated that toluene and CH₄ could completely be converted to H₂ and CO in the catalytic reforming of the simulated HCOG under atmospheric pressure and the amount of H₂ in the reaction effluent gas was about 4 times more than that in original HCOG. The catalysts with lower Ni/Mg molar ratio showed better catalytic activity and resistance to coking, which may become promising catalysts in the catalytic reforming of HCOG.     

Catalytic Combustion of Methane over CO1-xMgxO/Al2O3/FeCrAl Monolithic Catalysts

A series of CoxMgxO/Al2O3/FeCrAl catalysts （x=0-1） were prepared. The structures of the catalysts were characterized using XRD, SEM, and TPR analyses. The catalytic activity of the catalysts for methane combustion was evaluated in a continuous flow microreactor. The results indicated that the active washcoats adhered well on the FeCrAl foils. The phases in the catalysts were Co--xMgxO solid solutions, α-Al2O3, and γ-Al2O3. The surface particle size of the catalysts varied with variations in the molar ratios of Co to Mg. The Co component of the Co1_xMgxO/Al2O3/FeCrAl catalysts played an important role in the catalytic activity for methane combustion. In the Co1-xMgxO/AluO3/FeCrAl series catalyst （x=0.2-0.8）, the catalytic activity in terms of x was in the order of 0.5〉0.2〉0.8 under the experimental conditions. The presence of Mg in these catalysts could promote the thermal stability to a large extent. There were strong interactions between the Co1-xMgxO oxides and the AluO3/FeCrAl supports.     

Cu-Mg/Al复合氧化物催化碳颗粒物燃烧性能的研究

恒定二价与三价阳离子比为3(nM2+/nM3+=3),采用共沉淀法制备不同Cu含量的系列水滑石前驱物, 800 ℃焙烧4 h形成复合氧化物(CuO质量百分数分别为0％、5％、10％、15％、20％、30％、40％)用作柴油车排放碳颗粒物燃烧的催化剂,并采用XRD、BET、TG-DSC、FT-IR、TPR等表征手段研究了Cu、Mg含量对材料前驱物物化性能的影响及对其衍生复合氧化物催化碳颗粒物燃烧性能的影响．结果表明,Cu、Mg含量对材料的热稳定性、比表面和催化氧化活性有显著的影响. Mg有助于提高催化剂的热稳定性; Cu含量增加,催化剂比表面下降,但比表面不是影响催化剂活性的主要因素. CuO含量为15％时,催化剂具有最好的催化活性和稳定性,碳颗粒物的起燃温度(T10)和半转化温度(T50)分别为336 ℃和409 ℃.在CuO含量≤30％时可以形成结构完整的水滑石前驱物, CuO含量为40％时出现Cu(OH)2杂相; CuO含量< 20％时,经高温焙烧可得到均匀的复合氧化物, CuO含量≥20％时出现CuO偏析． TPR结果表明焙烧温度和复合氧化物的组成决定了材料的可还原性能．