The synthesis and spectroscopic characterisation of hydrotalcite formed from aluminate solutions

Raman spectroscopy has been used to characterise nine hydrotalcites prepared from aluminate and magnesium solutions (magnesium chloride and seawater). The aluminate hydrotalcites are proposed to have the following formula Mg(6)Al(2)(OH)(16)(CO(3)(2-))·xH(2)O, Mg(6)Al(2)(OH)(16)(CO(3)(2-),SO(4)(2-))·xH(2)O, and Mg(6)Al(2)(OH)(16)(SO(4)(2-))·xH(2)O. The synthesis of these hydrotalcites using seawater results in the intercalation of sulfate anions into the hydrotalcite interlayer. The spectra have been used to assess the molecular assembly of the cations and anions in the hydrotalcite structures. The spectra have been conveniently subdivided into spectral features based upon the carbonate anion, the hydroxyl units and water units. This investigation has shown the ideal conditions to form hydrotalcite from aluminate solutions is at pH 14 using a magnesium chloride solution at a volumetric ratio of 1:1. Changes in synthesis conditions resulted in the formation of impurity products aragonite, thenardite, and gypsum.     

镁铁水滑石的制备及其对小球藻油脂合成生物柴油的催化性能

用改良尿素法制备了镁铁水滑石(MgFe-LDH),对其在小球藻油脂合成生物柴油反应中的催化性能进行了研究。利用XRD、FT-IR、SEM及FT-IR拟合、去卷积分析等技术对所制备的MgFe-LDH进行了表征,考察了pH值、Mg/Fe摩尔比、反应温度和时间对其结构和性能的影响。结果表明,Mg/Fe摩尔比为3或4、pH值为9.5,在110 ℃条件下反应10 h,所制备的MgFe-LDH(Mg3Fe或Mg4Fe)结晶度最高,粒径均匀,结构规整。与Mg/Fe摩尔比为2的MgFe-LDH(Mg2Fe)相比,Mg3Fe或Mg4Fe在完全分解焙烧时,其层板结构保持稳定,具有较高的晶体结晶度、较多的催化活性位和较高的催化活性。以Mg3Fe金属氧化物为催化剂,在醇/油摩尔比为6时反应1.5 h,生物柴油产率可达87％;该催化剂循环使用3次,仍具一定催化活性。     

Preparation, Characterization of Hydrotalcites and the Catalytic Properties in Synthesis of o-Phenylphenol over Pt／CHT

Mg/Al mixed oxides with molar ratios of 2-6 of Mg to Al used as supports for platinum catalysts were obtained by the thermal decomposition method. The effect of the composition of the mixed oxides on the physicochemical properties was studied by TPD, nitrogen sorption, XRD and TG-DTA characterization methods. The synthesis of o-phenylphenol (OPP) from a dimer (obtained from cyclohexanone condensation) was investigated over Pt/CHT catalysts and compared with those over Pt/MgO and Pt/Al2O3 catalysts. These catalysts show a high activity and selectivity for OPP, with a conversion reaching 93.8% and a selectivity reaching 87.9% in some experiments. For Pt/CHTx catalysts, the calcined hydrotalcites exhibited strong base sites, which were necessary to catalyze the synthesis of OPP.     

硝酸镁在γ-Al2O3上的热分解及MgO/γ-Al2O3

研究了不同载量时Mg(NO     

Hydrogen production from simulated hot coke oven gas by catalytic reforming over Ni/Mg(A1)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 ceking, which may become promising catalysts in the catalytic reforming of HCOG.     

Aldol condensation of furfural and acetone on layered double hydroxides

The Aldol condensation of furfural (Fur) with acetone (Ac) to 4-(2-Furyl)-3-buten-2-one (FAc) is one of the most important processes in the aqueous-reforming of oxygen-containing biomass derivatives and has been carried out in the presence of solid-base catalysts, calcined-rehydrated Layered Double Hydroxides (LDH). The Mg-Al Layered Double Hydroxides has been prepared by the coprecipitation, calcination and regeneration from mixed oxides by rehydration. The catalyst prepared with different Mg/Al molar ratios showed different catalytic performance and the best catalyst was with the Mg/Al molar ratio of 2.5. Phenol adsorption showed that the best catalyst had the largest numbers of accessible basic sites. The appropriate rehydration temperature and time for mixed oxides obtained by calcination were also investigated. The Mg-Al LDH catalysts can be regenerated by calcination at 773 K and rehydration in decarbonate water, but the regeneration is complex and incomplete. In addition, the catalyst calcined at high temperature also had activity, which was attributed to the formation of the Mg-Al spinels.     

Fourier transform infrared study of low-temperature CO adsorption on CuMgAl-hydrotalcite

Single-phase CuMgAl ternary hydrotalcite with (Cu+Mg)/Al atomic ratio of 3.0 and Cu/Mg atomic ratio of 1.0 was synthesized by coprecipitation. Thermoanalytical studies of this sample showed transformations in three stages in the temperature range up to ca. 900 K yielding mainly CuO phase. In situ diffuse reflectance infrared Fourier transform (DRIFT) spectroscopic measurements showed the presence of carbonates even after calcination of the sample at 973 K. The genesis of Cu+ sites during thermal treatment in vacuo at different temperatures for this sample was followed by IR spectroscopy of CO adsorbed at low temperature. Essentially no Cu+ sites are present on a sample calcined at 723 K, consistent with X-ray photoelectron spectroscopic (XPS) data. However, sample subjected to activation (1 h of O2 treatment at 723 K followed by 1 h of evacuation at the same temperature) upon CO adsorption at 85 K unambiguously showed the presence of Cu+ sites. 12CO-13CO coadsorption studies confirmed the presence of dicarbonyls, which are converted to linear Cu+-CO species during evacuation at 85 K. Concentration of the accessible Cu+ sites increased with the increase in activation temperature up to 873 K and decreased with a further temperature rise. The copper sites on the sample are heterogeneously distributed and their distribution depends on the activation temperature. Two routes of reduction of Cu2+ to Cu+ are proposed: (i) autoreduction during evacuation and (ii) reduction by CO.     

Preparation of supported metal catalysts starting from hydrotalcites as the precursors and their improvements by adopting “memory effect”

Hydrotalcite-like compounds (HTlcs) can be used as the catalysts as it is since they contain various transition metal cations as the catalytically active species well dispersed on the basic support materials. Moreover, increasing numbers of the applications of HTlcs after the heat treatment have been found since the oxides with very small crystal size, stable to thermal treatments, are obtained after the calcination. The oxides possess interesting properties such as high surface area, basic properties and further form small and thermally stable metal crystallites by reduction. Moreover, the calcined oxides show a unique property, i.e., “memory effect,” which allows the reconstitution of the original hydrotalcite structure. We have developed the catalytic applications of hydrotalcites as it is and moreover the mixed oxides derived from hydrotalcites for various catalytic reactions, i.e., oxidation, dehydrogenation and reforming of hydrocarbons, and even for the reforming of methanol and the CO shift reaction. Aerobic oxidation of alcohols, Baeyer−Villiger oxidation of ketones and O₃ oxidation of oxalic acid have been successfully carried out with the Mg−Al hydrotalcites containing Ni, Fe and Cu, respectively, as the catalysts in liquid phase. In the O₃ oxidation of oxalic acid, the catalytic activity was enhanced by the “memory effect,” i.e., Mg(Cu)–Al hydrotaclite was reconstituted on the surface of Mg(Cu,Al)O periclase particles and oxalic acid was incorporated as anions in the hydrotalcite layer, resulting in an enhanced oxidation of oxalic acid. As the catalysts in the vapor phase reactions, Mg/Fe/Al mixed oxides prepared from Mg–Al(Fe) hydrotalcites and effectively catalyzed the dehydrogenation of ethylbenzene. Supported Ni metal catalysts have been prepared from Mg(Ni)–Al hydrotalcites and successfully used in the steam reforming and the oxidative reforming of methane and propane. Moreover, the Ni catalysts have been improved by combining a trace amount of noble metals by adopting the “memory effect” and used in the production of hydrogen for the PEFC under the daily startup and shutdown operation. Also starting from aurichalcite or hydrotalcite precursor as the precursor, Cu/Zn/Al catalysts with high Cu metal surface area have been prepared and successfully applied in the steam reforming of methanol and dimethyl ether, and moreover in the CO shift reaction.     

Cu(Al)O复合物表面酸碱性质的微量吸附量热研究

673K分解Cu/AI物质的量比分别为0．5、1和2的Cu-AI水滑石转化为Cu(AI)O复合物。XRD测定仅显示CuO物相,表明组成成分较均一。微量吸附量热法测定Cu(AI)O复合物表面酸碱中心的强度和数量,给出了吸附分子CO2／NH3的吸附曲线。量热结果展示,样品的酸中心强度顺序是：0．5CAO＞CAO＞2CAO,而碱中心强度顺序是：0．5CAO＜CAO＜2CAO。显然,样品的酸性（碱性）随着AI(Cu)含量的提高而逐渐增强。研究表明,样品的NH3和CO2起始吸附热与其Sanderson电负性线性相关。     

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.     

RhCo双金属催化剂的研究 Ⅱ. Rh+Co/Al2O3上CO吸附态的动态行为与CO歧化

利用CO与NO作为双探针分子和TP-IR动态方法研究了Rh+Co/Al2O3催化剂上的吸附中心类型, CO吸附态的动态行为以及CO歧化反应。结果表明在Rh+Co/Al2O3上存在大量的孪生CO吸附中心和少量的线式CO吸附中心以及Co上的NO吸附中心。在TPD(真空中)动态过程中, 孪生CO谱带强度逐渐减弱并在325℃完全脱除。明显低于Rh4/Al2O3上孪生CO谱带的脱附温度, 表明Co的加入减弱了孪生中心对CO的吸附强度。在TP(CO中)动态过程中, 吸附的CO谱带上250℃以上才发生强度减小直至消失的行为表明CO歧化在250℃以上才发生。并且孪生中心上的歧化速率高于线式中心。     

CaO/MgO和CaO/Ca9Al6O18同时捕集CO2/SO2的循环吸收特性

以葡萄糖酸钙与葡萄糖酸镁及L-乳酸铝为前驱物,湿法制得了四种CaO/MgO和CaO/Ca₉Al₆O₁₈吸收剂,并进行了同时捕集CO₂/SO₂的实验。考察了吸收剂种类、质量配比、SO₂浓度及煅烧温度等对吸收剂吸收性能的影响。结果表明,CaO/MgO(质量比为75%/25%)吸收剂和CaO/Ca₉Al₆O₁₈(质量比为75%/25%)吸收剂分别保持了最好的吸收CO₂能力和最好的循环稳定性。SO₂严重阻碍了吸收剂对CO₂的捕集。SO₂浓度越高,吸收剂吸收CO₂能力下降的越快,但同时吸收SO₂的转化率也越高。数次循环后,总的Ca利用率开始上升,且SO₂浓度越高,上升趋势越明显。煅烧温度对CaO/MgO吸收剂和CaO/Ca₉Al₆O₁₈吸收剂循环吸收特性的影响略有不同。     

纳米二氧化锆催化剂上一氧化碳加氢合成异丁烯

 考察了纳米ZrO2的制备方法及Al2O3和KOH助剂的添加对ZrO2催化\r\nCO加氢合成异丁烯反应的影响．纳米ZrO2的制备方法对ZrO2的物理性质\r\n和催化性能有较大的影响．用超临界流体干燥法干燥并在流动N2气氛中\r\n焙烧制得的ZrO2催化剂对异丁烯具有较高的选择性．Al2O3和KOH助剂表\r\n现出非常优良的助剂效应，在大幅度提高催化剂对i－C4烃选择性的同\r\n时保持了和ZrO2同样高的催化活性．催化剂的酸碱性表征结果表明，酸\r\n碱性对催化剂的催化性能影响很大，催化剂上适宜的酸碱数量和酸碱比\r\n例是影响其催化CO加氢合成异丁烯性能的非常重要的因素．     

层状前体镍铁水滑石及磁性材料的制备及表征

提出了利用镍铁水滑石作为磁性前体再经高温焙制备尖晶石型铁氧体思路，深 入研究了水滑石的制备工艺及结构性能并初步探讨了其焙烧后的磁学性能。由共沉 淀法合成了Ni/Fe摩尔比为2，3，4，6的镍铁水滑石，XRD结果表明镍铁比为3时晶 形较为理想，且随着晶化温度的升高及晶化时间的延长，水滑石的晶体结构规整性 增强。热重-差热结果显示镍铁水滑石的分解有两个过程，当镍铁比为3时，水滑石 的热稳定性相对最高。高温焙烧后的镍铁水滑石具有磁性。     

XPS and TDS study of CO interaction with Pd–AlOx systems

The metal–substrate and metal–metal interactions (MSI, MMI) represent important effects determining the properties of supported catalysts, gas sensors and gettering alloys. We investigated the MSI and MMI effects by the X-ray photoelectron spectroscopy (XPS) and temperature programmed desorption (TPD) in the case of Pd films deposited on Al₂O₃ and Al substrates. The study shows that the particle-size dependent metal–substrate interaction plays an important role in CO–Pd chemisorption, namely, in the case of “aluminium rich” Pd–aluminium oxide interface. CO chemisorption exhibits a low-temperature desorption feature at 360 K characteristic for Pd–Al and very small Pd particles. The MSI is explained by the formation of a Pd–Al intermetallic interface exhibiting a strong bimetallic Pd–Al interaction.     

Synthesis and phosphate uptake behavior of Zr4+ incorporated MgAl-layered double hydroxides

We synthesized Zr(4+) incorporated MgAl-layered double hydroxides, Mg(AlZr)-LDH(A) (where A denotes a counteranion in the interlayer space and is expressed as CO(3) for carbonate and Cl for chloride ions), with different molar ratios of Mg/(Al+Zr). Then we characterized their uptake behavior toward phosphate ions. CO(3)-type tertiary LDH materials synthesized at room temperature show low crystallinity, whereas the highly crystalline Cl-type tertiary LDH, [Mg(0.68)Al(0.17)Zr(0.14)(OH)(2)][Cl(0.26)(CO(3))(0.04)1.24H(2)O], was synthesized for the first time using a hydrothermal treatment at 120 degrees C. The distribution coefficients (K(d)) of oxo-anions were measured with a mixed solution containing trace amounts of the anions. The selectivity sequences were Cl(-), NO(-)(3)相似文献   

Catalytic reduction of NO_x by CO on hydro-talcites-derived mixed oxides Co AIM and MgAlM (M = Cr, Mn, Fe, Co, Ni, Cu)

Two series of mixed oxides, CoAlM and MgAlM (M= Cr, Mn, Fe, Co, Ni, Cu) , were prepared by calcining their corresponding hydrotalcite-like compounds (HTLc) . The ratio of Mg: Al: M (or Co: Al: M) was 3:1:1. The catalytic activity of all samples for the reaction of NO CO was investigated. The results showed that the activity of CoAlM was much higher than that of MgAlM. The structure and the property of redox were characterized by XRD and H2-TPR. The results indicated that only MgO phase was observed after calcining MgAlM hydrotalcites, and the transition metals became more stable. The spinel-like phase appeared in all of CoAlM samples after the calcination, and the transition metals were changed to be more active, and easily reduced . The activities of three series of mixed oxides CoAlCu obtained from different preparation methods, different ratio of Co:Al:Cu and at different calcination temperatures, were studied in detail for proposing the mechanism of reaction. The ability of adsorption of NO and CO     

温度对Mg-Al-O复合氧化物催化剂体相和表面酸碱性质的影响

用ＮＨ３和ＣＯ２作探针分子,采用红外光谱,真空原位测定Ｍｇ－Ａｌ－Ｏ复合氧化物表面酸碱中心的类型结果表明,主要存在Ｌ酸,碱中心是氧阴离子,而焙烧温度对样品表面碱中心的类型几乎没有影响,在６７３、８７３和１０７８Ｋ焙烧样品的固态ＭＡＳ＾２７Ａｌ核磁共振结果显示,样品呈现显著的物相转变,炽的过渡态对确定它们碱性质显得非常重要。ＸＰＳ测定样品中Ａｌ２ａ和Ｏ１ａ结合能与样品表面酸碱中心的强度相关。     

焙烧温度对Mg(Al)O复合物结构和表面酸碱性质影响的研究

分别在673、873和1073K分解Mg/Al摩尔比为3的水滑石生成Mg(Al)O复合物.XRD测定均显示MgO物相.873K以上焙烧的样品同时存在MgAl2O4尖晶石物相.微量吸附量热测定其表面酸碱中心的强度和密度,发现碱中心强度和密度顺序为:MAO-2＞MAO-3≈MAO-1,而酸中心强度和密度顺序是:MAO-1＞MAO-3≈MAO-2.红外光谱表明,Mg(Al)O复合物表面酸碱中心主要存在L酸,碱中心是氧阴离子.焙烧温度对表面碱中心类型几乎没有影响.固态MAS27Al核磁共振结果展示,这些样品呈现出显著的Al3+配位情况的变化.     

新型固体酸SO42-/Al2O3-Al 的制备与表征

采用铝阳极氧化法制备了A12O3-Al一体型载体．并通过浸渍硫酸的方法制备了新型固体酸SO4^2-／Al2O3-Al催化剂．采用BET、XRD、XPS和NH3-TPD对其结构和酸性进行了表征．结果表明，该催化剂具有合适的孔结构．Al2O3-Al载体为无定形结构．NH3-TPD结果表明．该催化剂同时具有弱酸及强酸位．用乙酸／乙醇酯化催化反应评估了该固体酸的催化性能．