Sm2O3对Ni／sepiolite甲烷化催化剂的影响

采用浸渍法制备了Ni/sepiolite及Ni-Sm/sepiolite催化剂并测定了催化剂的CO甲烷化活性，采用抗热实验，XPS及CS2中毒等手段研究了钐对Ni/sepiolite催化剂的影响，结果表明，加入Sm2O3提高了Ni/sepiolite催化剂的甲烷化活性，催化剂热稳定性及抗毒能力，降低了镍原子的电子结合能。     

Sm2O3对Ni/海泡石催化剂的改性研究

采用浸渍法制备了一系列的Ni-Sm/海泡石催化剂，以二氧化碳甲烷化为探针反应，TPR，XPS及CS2中毒为手段，研究了Sm2O3对Ni/海泡石催化剂的改性机制。结果表明，Sm2O3的加入提高了Ni/海泡石催化剂的加氢活性和抗毒能力，增加了表面镍原子的分散度及催化剂的活性原子数；Sm2O3的影响既有电子效应，又有几何效应，但以电子效应为主。     

新型Ni基加氢催化剂的研究(英文)

以酸处理海泡石为载体,用浸渍法制备了一系列含不同助剂的Ｎｉ基海泡石催化剂。以二氧化碳甲烷化、苯加氢、抗毒及抗热实验对助剂的影响进行了考查。结果表明,助剂尤其是钐的加入能显著地提高Ｎｉ基催化剂的加氢活性、热稳定性及抗毒能力。     

硅酸盐修饰Ni/海泡石催化剂的制备

Under the hydrothermal condition, the surface of sepiolite was restored with silicate and Ni was precipitated on the restored sepiolite by precipitating-reducing method. The surface of the samples was characterized by SEM, BET and XRD. The catalytic ability was examined by hydrogenation of toluene in gas phase over the silicate restored Ni/sepiolite catalyst. The experimental results show that distribution of Ni over the surface of the sample was even with bare aggregation and can be controlled, the ability of anti-aging of this catalyst was about ten times higher than that prepared by impregnation method at the same reactive condition.     

MoO_3对Ni/Sepiolite加氢催化剂的改性研究(英文)

用浸渍法制备了一系列镍基催化剂并以苯加氢反应及二硫化碳中毒为手段考查了ＭｏＯ３对Ｎｉ基催化剂的改性机制。结果表明,钼的加入能增加Ｎｉ催化剂的催化活性和抗二硫化碳毒性,原因是钼的加入增加了催化剂的活性中心数量和镍的分散度,改变了催化剂与反应物所形成中间体的活化焓及熵。根据过渡态理论,钼对Ｎｉ基催化剂的影响即有电子效应又有几何效应,但以电子效应为主。     

有机改性对粘土负载镍催化剂的促进作用及其萘加氢性能

以有机改性后的十六烷基三甲基溴化铵柱撑蒙脱石（CTAB-MMT）为载体,采用浸渍法制备了Ni/MMT催化剂. 通过傅里叶红外光谱、X射线衍射、H₂程序升温脱附、N₂物理吸附以及紫外漫散射等物理化学手段对催化剂进行了表征;并结合微型高压反应釜萘加氢反应,评价了催化剂的加氢性能. 结果表明,有机改性显著改善了Ni/MMT催化剂的金属Ni分散度和织构性质,且所制催化剂表现出优异的萘加氢性能,Ni萘转化率达到88.2%,不仅远高于未处理催化剂（13.1%）和Al₂O₃柱撑处理催化剂（24.2%）,而且高于Ni/SBA-15催化剂（68.2%）. 鉴于CTAB有机柱撑体在催化剂还原过程因热解而消除,其对催化剂所起的作用主要发生于浸渍过程,提出了有机改性在浸渍过程对Ni/MMT催化剂的促进作用机制.     

Effect of the detonation nanodiamond surface on the catalytic activity of deposited nickel catalysts in the hydrogenation of acetylene

A comparative study is performed of the catalytic activity of nanosized nickel deposited on detonation synthesis nanodiamond (DND) and coal (C_SUG) produced by burning sugar and crystalline quartz in the hydrogenation of acetylene. Nanosized nickel is obtained through the thermal decomposition of nickel formate under a dynamic vacuum. The catalysts are studied by means of scanning electron and transmission electron microscopy, X-ray fluorescence, IR-spectroscopy, X-ray diffraction, and pulse microcatalytic method. It is shown that Ni/DND is an active catalyst of acetylene hydrogenation, considerably surpassing Ni/quartz and Ni/C_SUG. The apparent activation energy of the hydrogenation of acetylene is calculated, and the region of the reaction are determined for all catalysts. It is found that the influence of the structure and nature of a functional coating of nanodiamond on the catalytic activity of Ni/DND deposited catalyst in the hydrogenation of acetylene. The ability of Ni/DND to hold active hydrogen is detected.     

炭包覆氧化铝负载镍催化剂的制备和表征及其催化加氢性能

以炭包覆A12O3(CCA)为载体,采用等体积浸渍法制备了17%Ni/CCA催化剂,采用热重-差示量热扫描、扫描电镜、X射线光电子能谱、N2物理吸附、H2程序升温还原和X射线衍射等手段对样品进行了表征,并用于粗1,4-丁二醇加氢反应中.结果表明,炭的引入显著改变了Al2O3的表面性质、负载Ni的存在形态以及金属.载体间...     

TiO2柱撑海泡石负载Ni2P的噻吩加氢脱硫性能

以氢氧化镍为镍源, 亚磷酸为磷源, TiO₂柱撑海泡石(Ti-Sep)为载体, 采用浸渍法制备了含磷化镍前驱体的样品, 然后采用程序升温还原法制备了Ni质量分数(w)为5%-25%的Ni₂P/Ti-Sep催化剂, 并考察了其噻吩加氢脱硫性能. 采用X射线衍射(XRD)、N₂吸附-脱附、热重分析(TGA)、透射电子显微镜(TEM)和傅里叶变换红外(FTIR)光谱对催化剂样品进行了表征. 结果表明, 海泡石经TiO₂柱撑之后层间距增大, 比表面积和孔容都明显变大, 热稳定性增强, 活性组分Ni₂P能很好地分散在海泡石层间及表面, 并且没有破坏海泡石的层状结构. 上述原因导致Ni₂P/Ti-Sep催化剂的噻吩加氢脱硫活性明显优于Ni₂P/Na-Sep(NaCl改性海泡石)和Ni₂P/HCl-Sep(HCl改性海泡石)催化剂. 当Ni负载量为15% (w)时, Ni₂P/Ti-Sep催化剂具有最好的噻吩加氢脱硫性能; 在反应温度为400℃时, 噻吩转化率达100%.     

Effect of transition metals (Cr, Mn, Fe, Co, Ni and Cu) on selective hydrogenation of cinnamaldehyde over Pt/CNTs catalyst

Summary The effect of transition metals (Cr, Mn, Fe, Co, Ni and Cu) on the selective hydrogenation of cinnamaldehyde (CMA) to the corresponding semi-hydrogenated product over Pt/CNTs catalyst has been studied in ethanol at 343 K under 2.0 MPa H₂ pressure. PtNi/CNTs catalyst shows good catalytic activity and selectivity of C=C bond hydrogenation, 68.4% for conversion of CMA and 97.0% for selectivity of hydrocinnamaldehyde (HCMA). PtCo/CNTs catalyst shows good catalytic activity and selectivity of C=O bond hydrogenation, 91.3% for conversion of CMA and 88.2% for selectivity of cinnamylalcohol (CMO).     

Catalytic pyrolysis of Pubescens to phenols over Ni/C catalyst

The pyrolysis of Pubescens over Ni/C catalyst was studied at 350 °C in H₂ flow. The presence of Ni/C catalyst efficiently improved the degradation of raw materials, and produced bio-oil with high content of phenols but low contents of acetic acid, furfural and water. In the reaction, Ni/C catalyst plays the role of catalytic decomposition and catalytic hydrogenation. The existence of the carbon carrier favors the formation of active Ni in small sizes with more defects, which results in high catalytic activity of Ni in biomass decomposition and selective production of phenols.     

金属有机骨架材料负载镍纳米颗粒催化硝基苯加氢

以MIL-53(Al)、MIL-96(Al)和MIL-120(Al) (MIL: Material Institute of Lavorisier)三种金属有机骨架材料为载体, 采用浸渍法制备了负载廉价金属镍纳米颗粒的催化剂. 将其用于催化硝基苯加氢合成苯胺反应, 发现以MIL-53(Al)为载体制得的催化剂表现出优异的催化性能. 采用不同的镍前驱体, 如硝酸镍、醋酸镍、乙二胺合镍, 制备了一系列Ni/MIL-53(Al)催化剂. 通过X射线衍射、傅里叶变换红外光谱、电感耦合等离子体、N₂物理吸附、H₂程序升温还原、透射电镜等技术对其进行了表征, 研究了镍前驱体对金属-载体相互作用、镍颗粒尺寸以及分散程度的影响.结果表明:以乙二胺合镍为镍前驱体制得的催化剂具有金属-载体相互作用适中、镍纳米颗粒更小(4-5 nm)和分布更均匀的特点, 在硝基苯加氢反应中表现出优异的催化性能, 硝基苯转化率达到100%.回收重复使用5次后, 此催化剂仍保持催化活性,硝基苯转化率达92%.     

Highly selective hydrogenation of acetophenone over supported amorphous alloy catalyst

Alpha-phenylethanol (PE) is an essential chemical in the field of medicine and synthetic perfumery. Therefore, in this work, we used a supported Ni–B–P amorphous alloy catalyst (Ni–B–P/SiO₂) in the hydrogenation of acetophenone (AP) to α-PE, which demonstrated excellent catalytic activity and selectivity, compared with Ni–B/SiO₂ (KBH₄ reduction of nickel salt). Ni–B–P/SiO₂ exhibited a high AP hydrogenation conversion of approximately 99%, whereas the PE selectivity reached up to 94%, which is approximately 1.4-fold higher than that of Ni–B/SiO₂ (about 69%), thereby directly proving the unique inhibition of AP hydrogenation over hydrogenation of P in the Ni–B catalytic system. The doped P in Ni–B–P/SiO₂ enhances the oxidation resistance and maintains the valence stability of Ni and B. Furthermore, sufficient experimental data were collected to determine the kinetic parameters. Based on the Langmuir–Hinshelwood model, we assumed that (i) AP and H₂ compete for adsorption on Ni–B–P/SiO₂; (ii) AP has strong adsorptive capacity on Ni–B–P/SiO₂; and (iii) PE coverage on the catalyst was negligible. Then, the dynamic equation was derived, which indicated that experimental data agree well with the dynamic model. Finally, the activation energy was confirmed to be 50.73 KJ/mol. This report will open up an avenue for the industrialization of amorphous alloy catalysts.     

Carbonate Hydrogenated to Formate in the Aqueous Phase over Nickel/TiO2 Catalysts

Carbonate hydrogenation to formate is a promising route to convert captured carbon dioxide into valuable chemicals, thus reducing carbon emissions and creating a revenue return. Developing inexpensive catalysts with high activity, selectivity, and stability remains challenging. We report a supported non-noble metal catalyst, Ni/TiO₂, with great selectivity over 96 % and excellent stability in catalyzing the conversion of carbonate into formate in aqueous solution. Ni⁰ and Ni²⁺ species are both observed in Ni/TiO₂ catalysts, and the synergistic effect of these two Ni components leads to high activity and high selectivity of carbonate hydrogenation to formate.     

Mild hydrotreating over NiMo/sepiolite catalyst

Summary In order to introduce an alternative catalyst for hydrotreating (HDT) reaction a study of NiMo supported on natural sepiolite catalysts is presented. The sepiolite catalyst has been prepared in this laboratory and a NiMo/Al₂O₃ commercial catalyst is used as a reference. The textural properties of the materials and their catalytic activity in hydrotreating (HDT) and hydrodesulfuration (HDS) using a FCC feed at 400-475°C and 50 MPa total pressure, have been evaluated. The support of the commercial catalyst is alumina containing mesopores. The sepiolite support is a hydrated magnesium phylosilicate containing micropores but with an open structure that confers the possibility to use it as a catalyst. The hydrotreating conversion (wt.% HDT) is defined here as the net hydrotreating conversion into products boiling below 380°C. For the commercial catalyst the wt.% HDT was only 5% higher than for the catalyst supported on sepiolite and the product selectivity was very similar. HDS conversion was 20% lower for the sepiolite supported catalyst. Taking into account these results the sepiolite is a suitable support of HDS catalysts.     

CO2 methanation over nickel-based catalysts prepared by citric acid complexation method

Catalytic hydrogenation of carbon dioxide to methane can not only achieve the recycling of carbon resources, but also effectively meet the increasing demand for natural gas. In this paper, Ni-based catalysts on different supports including ZrO₂, CeO₂ and Al₂O₃ were synthesized using citric acid complexation method and their CO₂ methanation performances were tested. Among these catalysts, the Ni/ZrO₂ catalyst achieved the best CO₂ methanation activity. The catalysts were characterized by N₂-physisorption, XRD, H₂-TPR and H₂-TPD. The results indicate that the superiority of the Ni/ZrO₂ catalyst can be mainly ascribed to its not only high Ni dispersion but also high reduction degree. Since the reduction degree of Ni/Al₂O₃ is low, it exhibits poor activity. The preparation condition for the Ni/ZrO₂ catalyst was further optimized. The result shows that at molar ratio of citric acid to Ni ions of 3, the catalyst exhibits the best activity owing to the highest Ni dispersion, the largest Ni surface area, an appropriate metal-support interaction and the most moderate basic sites.     

Multi-wall carbon nanotubes supported ruthenium for glucose hydrogenation to sorbitol

Multi-wall carbon nanotubes (MWNTs) supported ruthenium prepared with an impregnation method was used as catalyst in glucose hydrogenation to sorbitol. The effects of ruthenium loading, reaction time, temperature and initial hydrogen pressure on glucose hydrogenation were investigated. Compared with Raney Ni and ruthenium supported on Al₂O₃, SiO₂, Ru/MWNTs showed higher catalytic activity.     

助剂对Ni/海泡石催化剂加氢性能的影响

以海泡石为载体,Ｎｉ为活性组,用浸渍法制备了一系列含不同助剂的Ｎｉ基海泡石催化剂,以ＣＯ２甲烷化及苯加氢为探针反应,研究了催化剂的活性及抗硫性能,用Ｈ２－ＴＰＤ、ＸＰＳ、活性表面积及活化能的测定等于段,对催化剂进行表征,并从热力学上探讨ＣＯ２甲烷化的适宜温度。实验结果表明,海泡石或助剂的加入,能使镍晶粒变小,增加活性镍的表面积以及使镍原子的电子云密度升高,从而提高了催化剂的活性和使用寿命。能使镍晶     

超细负载型Ni/SiO2 催化剂用于虫白蜡加氢反应

用醇盐法制备了超细负载型催化剂Ni／SiO2,并应用于虫白蜡的高压催化加氢反应。通过TEM,XRD考察了催化剂的物相及结构特征。结果表明该催化剂载体物相为非晶态,催化剂活性中心高度分散于载体上,粒径小于10nm。催化剂的加氢活性随Ni负载量的增加而提高,负载量为20％时氢化效果最佳。     

Vapour Phase Hydrogenation of Cinnamaldehyde over Nano Ni and Ni/SiMCM‐41 Catalysts

Ni nanoparticles (Ni(1) and Ni(2)) and Ni loaded SiMCM‐41 (15Ni/SiMCM‐41) were prepared and characterized with XRD, TEM, N₂ adsorption, CO chemisorption, and H₂‐TPR. The Ni specific surface area followed the order of 15Ni/SiMCM‐41 > Ni(1) >> Ni(2), whereas the Ni particle size exhibited the opposite trend. These catalysts were utilized for vapour phase hydrogenation of cinnamaldehyde at 1 atm and 200 °C in a fixed‐bed, down flow reactor. The main products include hydrocinnamaldehyde, styrene, ethylbenzene, and 2‐phenyl‐1‐propanol. The catalytic activity decreased in the same order as that of Ni specific surface areas. The SiMCM‐41 support possessed very large surface area, leading to enhanced dispersion and specific surface area of Ni nanoparticles. As a result, the 15Ni/SiMCM‐41 catalyst exhibited the highest activity. Based on the investigation of reaction pathways, it is important to emphasize that both hydrogenation and hydroelimination of formaldehyde (hydrodeformylation) occur in the vapour phase reaction.