Ni/SiO_2催化剂的合成及其甘油氢解制1,2-丙二醇性能

以硝酸镍和偏硅酸钠为原料,采用并流共沉淀和氢气还原-钝化的方法制备了Ni/Si O2催化剂,通过BET、XRD、H2-TPD、NH3-TPD、HRTEM、XPS等手段对催化剂的理化性质进行了表征,发现合成得到的Ni/Si O2催化剂具有良好的织构性质、极高的金属分散度和活性比表面积,并且对甘油氢解生成1,2-丙二醇的反应表现出良好的活性和选择性.研究还考察了催化剂的镍硅比、反应停留时间、反应压力、甘油浓度对甘油氢解性能的影响,发现在镍硅比为0.5,反应停留时间为2 h,反应压力为5.5 MPa,甘油浓度为10%的条件下,甘油的单程转化率达78.8%,1,2-丙二醇的选择性高达92.9%.     

Ni-Co@C-N催化剂的制备及其催化硝基芳烃还原偶联反应

以ZIF-67为前驱体,通过高温热解和乙二醇还原的方法制备了低成本的负载镍纳米粒子催化剂Ni-Co@C-N。研究了催化剂对硝基芳烃化合物合成相应氧化偶氮苯类化合物的催化性能,并讨论了碱及分散剂种类对催化剂结构与性能的影响。结果表明,碱性增强可以加快纳米粒子的成核速率,分散剂分子量增加则会限制纳米粒子的粒径增长。其中,由弱碱与低分子量分散剂制备的Ni-Co@C-N-4对硝基芳烃还原具有良好的催化活性,原料的转化率和产率在反应30 min后分别达到92.8%和89.3%,且循环实验表明Ni-Co@C-N-4具有良好的稳定性。     

Nanoparticles positioning effect on properties of (PS-PANI/NiNPs) nanocomposite films

This work presents the effect of driven nickel nanoparticles (NiNPs) towards the surface of (PS-PANI)/NiNPs nanocomposite upon the application of a uniform magnetic field. The purpose is to obtain distinguishable optoelectronic and electrical properties. This process increases the surface roughness and its reactivity, and enables the tuning of the optical and electrical properties. Based on the results from X-ray photoelectron and Fourier-transform infrared spectroscopies, the magnetically-driven NiNPs to the surface are oxidized, forming NiONPs and NiOHNPs. This oxidation effect transforms the surface from a hydrophilic to a hydrophobic state. In addition, the optical bandgap energy decreases from 4.04 to 3.77 eV, and the electrical conductivity increases from 12.77 μS/cm to 57.80 μS/cm and 77.52 μS/cm, for 50 and 100 mT magnetic fields, respectively, which is attributed to the well-dispersed magnetic nanoparticles in the PS-PANI polymer matrix, resulting in a high homogeneous nanocomposite film.     

Ni-Co@C-N催化剂的制备及其催化硝基芳烃还原偶联反应

以ZIF-67为前驱体,通过高温热解和乙二醇还原的方法制备了低成本的负载镍纳米粒子催化剂Ni-Co@C-N。研究了催化剂对硝基芳烃化合物合成相应氧化偶氮苯类化合物的催化性能,并讨论了碱及分散剂种类对催化剂结构与性能的影响。结果表明,碱性增强可以加快纳米粒子的成核速率,分散剂分子量增加则会限制纳米粒子的粒径增长。其中,由弱碱与低分子量分散剂制备的Ni-Co@C-N-4 对硝基芳烃还原具有良好的催化活性,原料的转化率和产率在反应30 min 后分别达到92.8%和89.3%,且循环实验表明Ni-Co@C-N-4具有良好的稳定性。     

固相浸渍法制备NiO/CeO2催化剂及其在CO氧化反应中的应用

采用固相浸渍法制备了一系列NiO/CeO2催化剂,并通过与常规湿浸渍法比较,考察了制备方法对催化剂和CO氧化反应性能的影响.同时结合X射线衍射(XRD),N2吸附-脱附(BET),透射电镜(TEM),氢气-程序升温还原(H2-TPR),拉曼(Raman)光谱,X射线光电子能谱(XPS)等手段对催化剂的结构和表面物种分散状态进行了表征.CO氧化活性测试结果表明,当镍负载量相同时,固相浸渍法制备的催化剂相比于湿浸渍法表现出更好的催化性能.TEM、XPS、H2-TPR结果表明,固相浸渍法更有利于加强镍铈间的相互作用和得到高分散的镍物种,从而促进镍物种的还原.Raman结果表明固相浸渍法相比于湿浸渍法能产生更多氧空位,这有利于氧气在催化剂表面的活化,使得CO氧化反应更容易进行.     

Y-Mg-Al-F催化剂用于1,1,1,2-四氟乙烷裂解制备三氟乙烯

采用沉积沉淀法制备了Y-Mg-Al-F催化剂,应用XRD、NH3-TPD和Raman光谱等技术手段对催化剂进行表征,并与AlF3催化剂作比较,且将催化剂应用于四氟乙烷(HFC-134a)裂解制备三氟乙烯反应中。 结果表明,1100 ℃焙烧的Y-Mg-Al-F催化剂具有较高的活性和反应稳定性。 反应温度400 ℃时,四氟乙烷转化率大于25%。 催化剂表面酸性和积碳是影响催化剂活性和稳定性的主要因素。     

基于Fe负载的HZSM-5催化热解制备生物油实验研究

通过离子交换法制备含2%Fe(质量分数)的HZSM-5催化剂,采用X射线衍射仪(XRD)、激光粒度分析仪以及比表面积及孔径分析仪对催化剂进行表征,并在550℃下进行木屑的催化热解实验。对无催化剂和不同比例催化剂条件下得到的生物油进行GC-MS分析,结果表明,在Fe负载的HZSM-5作用下,生物油产率明显升高(最大增幅7%),轻质组分产率明显升高,重质组分产率略微升高。同时,轻质组分中的酮类、呋喃等含氧化合物含量降低,酚类、酸含量升高;重质组分中的酮类、呋喃类等含氧化合物含量明显降低,酚类、萘类含量明显增多。Fe负载的HZSM-5催化剂对木屑的热解反应有较好的催化效果,加强了对热解初始蒸汽的择形修饰,从而抑制了生物质三组分木质素初始热解产物中的醌类等容易一次或二次结焦物质的生成,孔道结构对蒸汽的二次反应被抑制,产物向较小分子的轻质产物上富集。     

Nickel ferrite spinel as catalyst precursor in the dry reforming of methane:Synthesis,characterization and catalytic properties

Dry reforming of methane by CO2 using nickel ferrite as precursor of catalysts was investigated.Nickel ferrite crystalline particles were prepared by coprecipitation of nitrates with NaOH or ammonia followed by calcination,or by hydrothermal synthesis without calcination step.The textural and structural properties were determined by a number of analysis methods,including X-ray diffraction (XRD),Raman spectroscopy and X-ray photoelectron spectroscopy (XPS),among which X-ray diffraction (XRD) was at room and variable temperatures.All synthesized oxides showed the presence of micro or nanoparticles of NiFe2O4 inverse spinel,but Fe2O3 (hematite) was also present when ammonia was used for coprecipitation.The reducibility by hydrogen was studied by temperature-programmed reduction (TPR) and in situ XRD,which showed the influence of the preparation method.The surface area (BET),particle size (Rietveld refinement),as well as surface Ni/Fe atomic ratio (XPS) and the behavior upon reduction varied according to the synthesis method.The catalytic reactivity was investigated using isopropanol decomposition to determine the acid/base properties.The catalytic performance of methane reforming with CO2 was measured with and without the pre-treatment of catalysts under H2 in 650-800 C range.The catalytic conversions of methane and CO2 were quite low but they increased when the catalysts were pre-reduced.A significant contribution of reverse water gas shift reaction accounted for the low values of H2 /CO ratio.No coking was observed as shown by the reoxidation step performed after the catalytic reactions.The possible formation of nickel-iron alloy observed during the study of reducibility by hydrogen was invoked to account for the catalytic behavior.     

不同活性炭负载的镍基催化剂上废塑料裂解制碳纳米管性能

以椰壳炭、竹炭和木炭三种活性炭为载体,采用浸渍法制备炭负载金属镍的催化剂,考察其在废塑料裂解制备碳纳米管过程中的催化反应性能;采用X射线衍射、扫描电镜、透射电镜、拉曼光谱仪、同步热分析仪、比表面积分析仪等手段分析了催化剂和产物碳纳米管的形貌和结构。结果表明,椰壳活性炭为载体制备的镍基催化剂上碳纳米管产量最高、石墨化程度最好。以椰壳活性炭为载体制备的镍基催化剂为例,研究了反应温度和镍负载量对其催化性能的影响。     

甲烷催化部分氧化制合成气的反应机理

借助脉冲反应、质谱-程序升温表面反应（MS-TPSR）等技术研究了Ni／α-Al2O3催化剂上甲烷催化部分氧化制合成气（POM）的反应机理．结果表明,NiO上CH4不能解离产生H2只有当NiO被CH4还原为Ni0后,CH4才能解高产生H2,Ni0是CH4活化和POM反应的活性相;POM反应机理遵循直接氧化机理,CH4和O2均在Ni0上活化,活化过程形成的Ni…C和Niδ…Oδ物种是反应历程中的关键物种,Niδ …Oδ物种高选择性地与CH4解离产生的碳物种Ni…C反应生成CO．     

前驱体中N含量对FeN/C催化剂氧还原活性的影响研究

采用热解法制备FeN/C催化剂,考察催化剂前驱体中氮含量对其氧还原活性的影响. 使用X射线衍射、比表面积和孔径分布测试、透射电子显微镜以及热重分析等方法对催化剂的结构、形貌及催化剂前驱体的热性质等进行表征,使用线性扫描伏安法对催化剂的氧还原活性进行测试. 结果表明,以1,10-菲啰啉为氮源,FeCl₃为铁源,Black Pearl 2000为载体,催化剂前驱体中1,10-菲啰啉含量为20wt%,Fe含量为1wt %时,热处理制备所得催化剂粒子分布均匀,比表面积为824.48 m ²·g ^-1,平均孔隙为10.58 nm,表面的氮元素含量为0.31wt%;并具有最好的氧还原催化活性.催化剂前驱体中氮源含量在热解过程中导致催化剂的比表面积、孔径结构及表面氮元素含量的变化是影响催化剂活性的关键因素.     

Ni catalysts supported on nano-crystalline aluminum oxide prepared by a microemulsion method for dry reforming reaction

Mesoporous nano-crystalline γ-Al₂O₃ with high surface area prepared by a microemulsion (ME) method was employed as carrier for nickel catalysts in dry reforming of methane for syngas production. The structural properties of the catalysts were characterized by X-ray diffraction, Brunauer–Emmett–Teller surface area analysis, temperature programmed reduction and oxidation and scanning electron microscopy techniques. Microemulsion showed it to be a promising way for the production of nano-crystalline aluminum oxide, and the nickel catalysts prepared with this support have significant features and properties to use in the dry reforming reaction. The results revealed that the prepared γ-Al₂O₃ exhibited a nano-crystalline structure (crystal size: c.4.8 nm) with a high specific surface area (308 m² g^?1). In addition, the catalysts with different nickel contents exhibited high catalytic activity in the dry reforming reaction. The results also showed that an increase in Ni loading from 5 to 15 wt% caused a decrease in the specific surface area and nickel dispersion.     

NiO/LaMnO3催化剂用于乙醇水蒸气重整反应

采用柠檬酸络合-浸渍法制备了NiO/LaMnO3钙钛矿型复合氧化物催化剂并将其应用于乙醇水蒸汽重整制氢反应, 考察了NiO含量、焙烧温度对催化剂性能的影响, 采用XRD、TPR和热分析等手段对催化剂进行了表征. 结果表明, 该催化剂具有高活性、高选择性和良好的稳定性. 催化剂中的NiO含量和焙烧温度对催化性能有显著影响. 在原料气体积组成为20%(体积分数, φ) C2H5OH 和水以及80%(φ)N2, 其中水醇摩尔比为3:1, 空速为80000 mL·h-1·g-1 cat, 反应温度为400 ℃时, 15%(质量分数, w)的NiO/LaMnO3上, 乙醇转化率接近100%. 关联催化剂活性和TPR及XRD实验结果, 发现催化剂的高活性源于由催化剂前驱体中进入钙钛矿型复合氧化物晶格中的镍离子被还原所得的金属镍.     

Ni2P/SBA-15催化剂的结构及加氢脱硫性能

以硝酸镍为镍源, 磷酸氢二铵为磷源, 介孔分子筛SBA-15为载体, 用共浸渍法制备了含磷化镍前驱体的样品, 然后在氢气流中采用程序升温还原法, 制备了Ni2P质量分数为5%-40%的Ni2P/SBA-15催化剂. 用X射线衍射(XRD)、N2吸附脱附、透射电子显微镜(TEM)、傅立叶变换红外光谱(FTIR)等分析测试技术对催化剂的结构进行了表征, 以噻吩和二苯并噻吩(DBT)为模型化合物, 在微型固定床反应器上对催化剂的加氢脱硫(HDS)性能进行了评价. 结果表明, Ni2P/SBA-15催化剂中SBA-15 的介孔结构依然存在, 活性组分Ni2P具有良好的分散性, 但随Ni2P含量的增加, 催化剂的比表面积、孔容和孔径均有明显减小. 当反应温度为320 ℃时, Ni2P含量为15%-25%(w)的催化剂就具有很好的加氢脱硫催化性能; 反应温度在360 ℃以上时, 所有催化剂都具有优异的深度脱硫催化性能. Ni2P/SBA-15催化剂对二苯并噻吩的加氢脱硫(HDS)主要以直接脱硫机理(DDS)进行.     

Deep Oxidation of Methane over Nano-Sized Ferrites with Spinel Structures

Ferrites with spinel structures as catalysts for the deep oxidation of methane have been studied by X-ray phase analysis and temperature programmed reduction. The most active catalysts are the nano-sized ferrites of cobalt and nickel, prepared by the decomposition of polynuclear complexes, with Al₂O₃ as carrier and with addition of a surface active agent to increase the thermal stability of the catalysts. At low temperatures (up to 450 °C), the effect of the size factor appears with the increase in specific catalytic activity of cobalt and nickel ferrites with decreasing of their particles. A correlation of the catalytic activity with the quantity and mobility (reactivity) of oxygen in the ferrites has been established.     

基于TG-FTIR的生物质催化热解试验研究

运用热重－傅里叶红外光谱联用技术(TG-FTIR)，以麦秸为研究对象，探讨催化与非催化条件下生物质的热解挥发分析出特性，分析研究热解温度、催化剂种类对生物质热解主要析出产物的影响。通过热重TG和DTG曲线，获得了相关热解特性参数及动力学参数。结果表明，添加NiO和CaO存在两个失重峰，并促进麦秸热解反应进行，降低表观活化能，其中NiO对提高热解析出产率作用更显著。通过红外光谱对热解产物实时测量的分析表明，CO与CO2的析出与失重峰基本一致，而CH4的析出滞后于前两者。添加NiO和CaO有利于减少热解产物中的CO2的浓度，促进挥发分产物CO、CH4的生成。其中CaO更有利于生物质在温度800℃以下的热解性能改善，而NiO在800℃以上具有更好的催化作用。     

担载Ni2（C5H5）2（CO）2催化剂的EXAFS表征

以Ni_2Cp_2(CO)_2(Cp=C_5H_5)为催化剂母体化合物,γ-Al_2O_3,SiO_2为担体制备了担载型镍催化剂,对母体化合物及热分解处理前后的催化剂样品在同步辐射装置上进行了外延X-光精细结构(Extended X-ray Absorpdon Fine Structure)测定,以先进的球面波理论对实验结果进行拟合,标样拟合结果与文献XRD完全一致。催化剂的EXAFS表征结果表明,母体化合物与氧化物担体表面发生了较强的化学作用,镍组分具有较高的分散度,镍在氧化硅表面存在Ni[(O)_8]_n,Ni—Ni两种配位,而在氧化铝表面几乎只存在Ni[(O)s)_n配位,催化剂上Ni—Ni键长比母体化合物Ni—Ni键长增加0.01nm左右,Ni—Ni键的伸长及其配位状态可能对其催化行为有重要影响。     

Corundum impregnation conditions for preparing supported Ni catalysts for the synthesis of a uniform layer of carbon nanofibers

Impregnation techniques for corundum (S _BET = 0.5 m²/g) as a support for Ni catalysts for C₃–C₄ alkane pyrolysis into catalytic filamentous carbon (CFC) are compared. The effects of the following factors on the uniformity of the active component (Ni) deposition on the inert support and on the CFC yield (g CFC)/(g Ni) are reported: (1) pH of the nickel nitrate solution, (2) presence of aluminum(III) nitrate in the solution, (3) addition of viscosifying agents (glycerol, glucose, sucrose) to the solution, (4) catalyst calcination conditions before pyrolysis, and (5) catalyst drying technique. The surface morphology of the Ni catalysts and of the carbon deposits resulting from the catalytic pyrolysis of C₃–C₄ alkanes in the presence of hydrogen has been investigated by scanning electron microscopy. The optimum way of preparing the supported Ni catalysts is by carrying out the incipient wetness impregnation of corundum with a nickel nitrate solution (0.05–0.1 mol/l) containing glycerol (20–25 vol %), drying the product in a microwave oven, and burning away the glycerol before alkane pyrolysis.     

整体式Mn-Fe/ZrO2-TiO2催化剂的制备及在低温NH3-SCR反应中的性能

以锆钛复合氧化物为载体, 制备整体式Mn基催化剂并研究其在低温氨选择性催化还原(NH3-SCR)氮氧化物反应中的性能; 用BET、XRD、储氧量(OSC)、程序升温还原(TPR)和XPS对催化剂进行表征. 实验结果表明, 与以TiO2为载体的催化剂相比, 以ZrO2-TiO2为载体的催化剂具有较大的比表面积、更稳定的晶相结构和较多的储氧量, 并具有较强的低温氧化性能和较高的表面Mn含量, 表现出良好的低温活性和高温稳定性. 在700 ℃焙烧后, Mn-Fe/ZrO2-TiO2在高空速55000 h-1条件下, 仍具有较好的起燃温度(182 ℃)和NO的转化率(78%), 并具有较强的抗水性能, 表现出很好的应用前景.     

Mesoporous Nickel–Alumina Catalysts for Hydrogen Production by Steam Reforming of Liquefied Natural Gas (LNG)

Recent progress on the mesoporous nickel–alumina catalysts for hydrogen production by steam reforming of liquefied natural gas (LNG) was reported in this review. A number of mesoporous nickel–alumina composite catalysts were prepared by a single-step surfactant-templating method using cationic, anionic, and non-ionic surfactant as structure-directing agents for use in hydrogen production by steam reforming of LNG. For comparison, nickel catalysts supported on mesoporous aluminas were also prepared by an impregnation method. The effect of preparation method and surfactant identity on physicochemical properties and catalytic activities of mesoporous nickel–alumina catalysts in the steam reforming of LNG was investigated. Regardless of preparation method and surfactant identity, nickel oxide species were finely dispersed on the surface of mesoporous nickel–alumina catalysts through the formation of surface nickel aluminate phase. However, nickel dispersion and nickel surface area of mesoporous nickel–alumina catalysts were strongly affected by the preparation method and surfactant identity. It was found that nickel surface area of mesoporous nickel–alumina catalyst served as one of the important factors determining the catalytic performance in hydrogen production by steam reforming of LNG. Among the catalysts tested, a mesoporous nickel–alumina composite catalyst prepared by a single-step non-ionic surfactant-templating method exhibited the best catalytic performance due to its highest nickel surface area.