Al2O3孔结构对纳米HZSM-5基催化剂改质FCC汽油性能的影响

采用NH₃-TPD、FT-IR、N₂吸附-脱附等手段对两种不同来源的氧化铝样品进行了表征。结果表明,两种Al₂O₃的总酸量及酸强度没有明显差别,酸类型均以Lewis酸为主,其中,Al₂O₃ (b)的平均孔径及孔体积较大。在固定床微型反应装置上考察了以两种Al₂O₃为载体制备的纳米HZSM-5基催化剂改质全馏分FCC汽油的性能。实验结果表明,以大孔Al₂O₃为载体的HZSM-5基催化剂具有较好的降烯烃、芳构化、异构化活性及稳定性。改性纳米HZSM-5负载的LaNiMo催化剂对FCC汽油的300 h评价结果表明,烯烃饱和率为83%,脱硫率为87%,同时维持了油品的辛烷值。     

载体对烯烃歧化制丙烯的影响

以SiO₂（SBA-15、MCM-48和SiO₂）和TiO₂-SiO₂（MTS-9）介孔分子筛为载体负载8%WO₃合成钨基催化剂,研究载体对丁烯歧化制丙烯性能的影响以及载体对丁烯转化率和丙烯选择性的影响。以SBA-15、MCM-48和SiO₂为载体时,催化剂的丁烯转化率在30%~37%;以MTS-9为催化剂载体时,丁烯的转化率高达到37%~42%。对所有使用的催化剂进行多种技术表征。结果表明,活性组分在各种载体上的分散度不同,载体MTS-9具有更好的分散能力,表面活性物种数量最多,催化剂WO₃/MTS-9的歧化性能最佳。     

ZrO2修饰Al2O3纳米片负载钴催化剂的制备及其费托反应性能研究

通过水热法合成了Al₂O₃纳米片（Al₂O₃-CN）,采用浸渍法制备20%（质量分数）钴基催化剂,并应用于费托合成反应。制备的Al₂O₃-CN（226 m²/g）与商业氧化铝（Al₂O₃-C,249 m²/g）具有相近的比表面积,但Al₂O₃-CN孔尺寸分布更加集中。浸渍钴后,与Co/Al₂O₃-C催化剂相比,Co/Al₂O₃-CN催化剂表现出较高的还原度及更均匀的钴颗粒粒径分布。因此,Co/Al₂O₃-CN催化剂表现出更高的CO转化率和低的甲烷选择性。为了进一步提高Co/Al₂O₃-CN的催化性能,采用不同含量ZrO₂对Al₂O₃-CN进行修饰。表征结果表明,随着ZrO₂修饰量的增加,Al₂O₃-CN载体比表面积变化不明显,孔体积和孔径增大;相对应催化剂的钴颗粒粒径减小,活性位点数目增加。在相同反应条件下,经ZrO₂修饰催化剂CO转化率进一步提高,甲烷选择性降低。     

新型大孔结构重油加氢催化剂的制备、表征与评价

将聚苯乙烯（PS）颗粒模板加入到铝溶胶中,经干燥、煅烧除去PS模板制备了大孔氧化铝载体;采用低温N₂吸附 脱附和SEM对合成Al₂O₃的孔结构进行了表征;将Co-Mo活性组分担载在大孔氧化铝载体上制得重油加氢催化剂,并以大港焦化蜡油为原料在固定床高压微反装置上对合成的催化剂进行活性评价。实验表明,加入PS模板后,Al2O3的比表面积增加了41.5m²/g,孔体积增加了0.35cm³/g;加氢脱硫活性提高了12%,脱氮活性提高了22%。     

双矿化剂对合成ZSM-5分子筛酸性和织构特征及其甲醇转化制丙烯催化性能的影响

采用静态水热法在F^--OH^-体系中,以四丙基氢氧化铵为模板剂、偏铝酸钠为铝源、正硅酸乙酯为硅源,合成了纳米SiO₂-ZSM-5分子筛,考察了F^-/Al₂O₃物质的量比对所合成的ZSM-5分子筛织构性质和甲醇转化制丙烯催化性能的影响。结果发现,随着初始溶胶F^-/Al₂O₃物质的量比的增大,产物中SiO₂的含量增大,ZSM-5分子筛的相对结晶度有所降低;同时,分子筛的比表面积和孔容减小、酸强度降低、酸量减少。对于甲醇转化制丙烯,最佳F^-/Al₂O₃物质的量比为12;此时,丙烯选择性高于45%,丙烯/乙烯（P/E）比值大于10。反应机理分析表明,过渡态择形选择性是控制烯烃选择性的重要因素。     

Al2O3助剂对Co/SiC催化剂F-T反应性能的影响

分别采用沉淀法、尿素水解法制备Al₂O₃/SiC复合载体,采用等体积浸渍法制备Co/Al₂O₃-SiC催化剂。结合N₂吸附、XRD、H₂-TPR、XPS等表征手段,研究Al₂O₃助剂对钴基催化剂物相结构、还原行为以及F-T合成性能等的影响。结果表明,氧化铝加入后增强了载体与钴物种之间的相互作用,提高了钴物种的分散度,降低了钴物种的还原度。尿素水解法引入Al₂O₃后,载体与钴物种具有适中的相互作用,表现出较高的反应活性。沉淀法制备的载体负载钴物种后由于较强的金属-载体相互作用,表现出较优的稳定性。     

不同载体负载的铂催化剂在丙酮酸乙酯不对称氢化反应中的活性及其铂流失率比较

以介孔树脂材料FDU-14和介孔碳材料CMK-3为载体制备了两种负载型铂催化剂, 用N₂气吸附、X射线衍射及CO化学吸附等手段对这两种催化剂进行了表征, 并将这两种不同的负载型铂催化剂在丙酮酸乙酯不对称氢化反应中的催化性能及其铂流失率与商品化Pt/Al₂O₃催化剂进行了比较. 研究结果表明, 尽管Pt/Al₂O₃催化剂的初始活性和光学选择性均较高, 然而相同反应条件下乙酸溶剂中Pt/FDU-14和Pt/CMK-3催化剂的铂流失率比Pt/Al₂O₃催化剂的低. 通过对催化剂进行CO吸附原位傅里叶变换红外漫反射光谱(DRIFTS)表征, 从载体的不同表面电子性质角度解释了不同载体负载的铂催化剂在丙酮酸乙酯不对称氢化反应中的活性和铂流失率的差异.     

负载Ni金属有序介孔氧化铝催化剂的制备及表征

采用原位合成法和传统浸渍法以价格低廉的硝酸铝作为铝源, 聚乙二醇1540为模板剂, 硝酸镍为镍源, 制备出负载Ni金属有序介孔氧化铝催化剂, 并采用BET、TEM、XRD、TG多种测试技术对合成催化剂的物理化学性质和结构特征进行了表征. 实验结果表明, 两种方法均能制备出比表面积大(＞210 m2·g-1)、孔径分布窄(4 nm左右)的负载Ni金属介孔氧化铝催化剂. 与浸渍法相比, 原位合成法所制备的负载Ni金属有序介孔氧化铝镍离子与载体具有更强的相互作用力, 且孔结构具有一定的有序性.     

硝酸盐制备三维有序大孔金属氧化物材料研究

用硝酸盐、柠檬酸和乙醇/水按一定摩尔比配置成前驱物溶液, 采用胶晶模板法, 制备了三维有序大孔金属氧化物材料: Al₂O₃, CeO₂, Cr₂O₃, NiO, MgO, In₂O₃, CeO₂/Al₂O₃, Cr₂O₃/Al₂O₃和NiO/Al₂O₃. SEM观察表明, 材料中大孔有序排列, 大孔间由小孔相连, 形成三维规则的笼状网络结构. XRD和TEM测试表明, 大孔孔壁由具有纳米尺寸的金属氧化物粒子组成. 实验表明, 加入乙醇、柠檬酸, 提高溶液对胶球润湿性, 改善溶液渗透能力, 避免粒子团聚, 有利于有序大孔结构的形成. 这一研究表明, 根据硝酸盐的物理化学性质, 调整溶液组成, 选择合适的热处理温度, 能得到大孔排列有序、三维规整性好的大孔结构材料. 此法具有原料易得, 操作简单的特点, 是3DOM材料的一种新型高效制备路线.     

钨含量对W/SiO2/Al2O3催化剂上1-丁烯自歧化反应的影响

采用浸渍法制备了一系列钨负载量不同的W/SiO₂/Al₂O₃ 催化剂. 采用X 射线衍射(XRD)、激光拉曼(Raman)光谱、紫外-可见(UV-Vis)光谱、氢气程序升温还原(H₂-TPR)和氨程序升温脱附(NH₃-TPD)等技术对催化剂进行了表征. 实验结果表明: 钨的负载量对催化剂上氧化钨物种的分散程度、还原性以及催化剂的酸性有非常重要的影响. 对该类催化剂上1-丁烯自歧化反应进行了详细考察, 结果表明: 当钨的质量分数为6.0%时,W/SiO₂/Al₂O₃催化剂表现出最佳的歧化活性和稳定性. 原因在于6.0%的钨负载量可以使催化剂上氧化钨物种具有中等程度的分散性、合适的还原性, 并且使催化剂具有一定程度的酸性, 这些因素有利于在催化剂上形成烯烃歧化活性位.     

Facile synthesis for ordered mesoporous gamma-aluminas with high thermal stability

The facile synthesis of highly ordered mesoporous aluminas with high thermal stability and tunable pore sizes is systematically investigated. The general synthesis strategy is based on a sol-gel process associated with nonionic block copolymer as templates in ethanol solvent. Small-angle XRD, TEM, and nitrogen adsorption and desorption results show that these mesoporous aluminas possess a highly ordered 2D hexagonal mesostructure, which is resistant to high temperature up to 1000 degrees C. Ordered mesoporous structures with tunable pore sizes are obtained with various precursors, different acids as pH adjustors, and different block copolymers as templates. These mesoporous aluminas have large surface areas (ca. 400 m2/g), pore volumes (ca. 0.70 cm3/g), and narrow pore-size distributions. The influence of the complexation ability of anions and hydro-carboxylic acid, acid volatility, and other important synthesis conditions are discussed in detail. Utilizing this simple strategy, we also obtained partly ordered mesoporous alumina with hydrous aluminum nitrate as the precursor. FTIR pyridine adsorption measurements indicate that a large amount of Lewis acid sites exist in these mesoporous aluminas. These materials are expected to be good candidates in catalysis due to the uniform pore structures, large surface areas, tunable pore sizes, and large amounts of surface Lewis acid sites. Loaded with ruthenium, the representative mesoporous alumina exhibits reactant size selectivity in hydrogenation of acetone, D-glucose, and D-(+)-cellobiose as a test reaction, indicating the potential applications in shape-selective catalysis.     

Metathesis of 1‐Butene to Propene over Mo/Al2O3@SBA‐15: Influence of Alumina Introduction Methods on Catalytic Performance

A series of Mo‐based catalysts for 1‐butene metathesis to propene were prepared by supporting Mo species on SBA‐15 premodified with alumina. The effects of the method of introduction of the alumina guest to the host SBA‐15 on the location of the Mo species and the corresponding metathesis activity were studied. As revealed by N₂ adsorption isotherms and TEM results, well‐dispersed alumina was formed on the pore walls of SBA‐15 if the ammonia/water vapor induced hydrolysis (NIH) method was employed. The Mo species preferentially interacted with alumina instead of SBA‐15, as evidenced by X‐ray photoelectron spectroscopy, time‐of‐flight secondary‐ion mass spectrometry, and IR spectroscopy of adsorbed pyridine. Furthermore, new Brønsted acid sites favorable for the dispersion of the Mo species and low‐temperature metathesis activity were generated as a result of the effective synergy between the alumina and SBA‐15. The Mo/Al₂O₃@SBA‐15 catalyst prepared by the NIH method showed higher metathesis activity and stability under the conditions of 120 °C, 0.1 MPa, and 1.5 h^?1 than catalysts prepared by other methods.     

Preparation of mesoporous alumina with large pore size and their supported rhenium oxide catalysts in metathesis of 1-butene and 2-butene to propene

Mesoporous γ-aluminas with large pore size(up to 19 nm,denoted as MA19) are prepared from dispersed pseudo-boehmite using pluronic P123 as template.It is found that these mesoporous alumina supported rhenium oxide catalysts were more active and have far longer working life-span in gas-phase metathesis of 1-butene and 2-butene to propene than rhenium oxide on conventional alumina with small pore size(5 nm).At 60°C and atmospheric pressure with WHSV = 1 h-1,the similar stable conversions of butene(ca.55%) for all the 13 wt% Re 2 O 7 /alumina catalysts were obtained near the chemical equilibrium,and the stable working life-spans of Re 2 O 7 /MA19 were far longer than that of Re 2 O 7 /Al 2 O 3,being about 70 h and 20 h,respectively.     

介孔氧化铝负载钒催化剂上丙烷氧化脱氢制丙烯

 采用浸渍法制备了介孔氧化铝 (m-Al2O3) 负载钒催化剂 (V/m-Al2O3), 并考察了其催化丙烷氧化脱氢制丙烯反应活性. 通过 N2 吸附-脱附、透射电镜、X 射线粉末衍射、紫外-可见漫反射光谱、氢-程序升温还原和氨-程序升温脱附对催化剂进行了表征. 结果表明, 介孔氧化铝具有大比表面积、窄孔径分布和两维六方相结构, 在其上负载适量的 V 可实现 V 活性物种的高分散及催化剂的弱酸性, 从而有利于提高丙烷转化率和丙烯选择性. 与共合成法制备的含 V 介孔氧化铝 V/m-Al2O3(C) 和浸渍法制备的 V/?-Al2O3 相比, V/m-Al2O3 表现出更高的催化活性. 这与载体较弱的酸性和较大的比表面积以及 V 物种的高分散有关.     

Effect of calcination temperature during preparation of Ru?Sn-alumina catalysts on the hydrogenation of carboxylic acid

The conversion of a carboxylic acid was increased to 90% with 100% selectivity to the corresponding alcohol by calcination of the catalyst precursor, Sn/alumina, of Ru–Sn/alumina in the hydrogenation of the carboxylic acid.     

SBA-15的孔壁碳膜修饰对钴基催化剂结构与催化性能的影响

在惰性气体中焙烧SBA-15制得孔壁被碳修饰的SBA- 15C样品,以它和SBA-15为载体,采用等量浸渍法制备了负载型Co基催化剂,并运用X射线衍射、N2物理吸附、程序升温还原、NH3吸附量热等手段对样品进行了表征.结果表明,SBA- 15C仍保持原有的六方有序的中孔结构,但其孔壁经碳修饰后发生增厚,比表面积略有下降...     

Unexpected Pd-catalyzed hydrogenation of phenol to 2-cyclohexene-1-one: enhanced activity and selectivity assisted by molecular oxygen

Addition of O(2) enables the liquid-phase hydrogenation of phenol using H(2) at low temperatures under atmospheric pressure with an unexpected selectivity towards 2-cyclohexene-1-one rather than cyclohexanone. As a catalyst, as-synthesized Pd/MCM-41 including the residual templates within the mesoporous channels exhibits a prominent positive effect on the catalytic performance.     

High surface area, mesoporous, glassy alumina with a controllable pore size by nanocasting from carbon aerogels

A strategy to synthesize amorphous, mesoporous alumina by nanocasting has been developed, involving carbon aerogel as a hard template and aluminum nitrate solution as an alumina precursor. The alumina generated exhibits small, transparent granules with a 3-6 mm diameter and has inherited the three-dimensional network structure of the carbon template. The mesopore surface area of the alumina can be as high as 365 m2 g(-1), and the pore volume reaches 1.55 cm3 g(-1) after calcination at 600 degrees C in air for 8 h. The pore parameters can be varied within a certain range by variation of the carbon aerogel template and the loading amount of the alumina precursor. At high loadings, the obtained glassy alumina clearly has a bimodal pore size distribution in the mesopore range.     

Template-free sol–gel synthesis of high surface area mesoporous silica based catalysts for esterification of di-carboxylic acids

High surface area mesoporous silica based catalysts have been prepared by a simple hydrolysis/sol–gel process without using any organic template and hydrothermal treatment. A controlled hydrolysis of ethyl silicate-40, an industrial bulk chemical, as a silica precursor, resulted in the formation of very high surface area (719 m²/g) mesoporous (pore size 67 Å and pore volume 1.19 cc/g) silica. The formation of mesoporous silica has been correlated with the polymeric nature of the ethyl silicate-40 silica precursor which on hydrolysis and further condensation forms long chain silica species which hinders the formation of a close condensed structure thus creating larger pores resulting in the formation of high surface mesoporous silica. Ethyl silicate-40 was used further for preparing a solid acid catalyst by supporting molybdenum oxide nanoparticles on mesoporous silica by a simple hydrolysis sol–gel synthesis procedure. The catalysts showed very high acidity as determined by NH₃-TPD with the presence of Lewis as well as Brønsted acidity. These catalysts showed very high catalytic activity for esterification; a typical acid catalyzed organic transformation of various mono- and di-carboxylic acids with a range of alcohols. The in situ formed silicomolybdic acid heteropoly-anion species during the catalytic reactions were found to be catalytically active species for these reactions. Ethyl silicate-40, an industrial bulk silica precursor, has shown a good potential for its use as a silica precursor for the preparation of mesoporous silica based heterogeneous catalysts on a larger scale at a lower cost.     

Lewis acid-modified mesoporous alumina: A new catalyst carrier for methyltrioxorhenium in metathesis of olefins bearing functional groups

Lewis acid-modified mesoporous alumina was found to be an efficient carrier as well as an activator for methyltrioxorhenium (MeReO₃) in olefin metathesis reactions. Especially, MeReO₃ doped on zinc chloride-modified mesoporous alumina catalyzed the metathesis of olefins with functional groups such as acetoxy, alkoxycarbonyl, acyl, chlorine, and bromine groups under mild conditions. The novel heterogeneous catalytic system promoted the metathesis of not only such functionalized olefins but also simple olefins without double bond migration that was often encountered on strong solid acids. We here present a new methodology for activation of a metal complex with Lewis acidic mesoporous materials in the metathesis reactions. This novel heterogeneous catalyst would be advantageous over conventional one from the viewpoint of environmental and economical organic synthesis.