Ni-Cu双金属催化剂上乙醇水蒸气重整制氢研究—制备方法对催化性能的影响

我们采用分步浸渍法和共浸渍法制备了一系列的Ni-Cu/mSiO₂催化剂.运用XRD、N₂吸附-脱附、H₂-TPR、SEM、TG-DTG等表征手段对催化剂反应前后的物理化学性质进行分析,催化剂对乙醇水蒸气重整（ESR）反应的催化性能通过常压固定床反应器进行评价.结果表明：催化剂的催化性能与载体上的活性组分分散有关,而活性金属的分散性与制备方法有关.共浸渍法制备的催化剂Ni₁₄-Cu/mSiO₂活性组分分散度较高,抗积碳能力与稳定性更好.在质量空速为2.7 h^-1,水醇摩尔比为9,反应温度为550℃的条件下进行稳定性测试,催化剂Ni₁₄-Cu/mSiO₂测试25 h没有出现失活现象,乙醇转化率保持在100%,H₂的选择性保持在70%以上,反应后的积碳含量仅为5.52%.     

SBA-15负载高分散纳米NiO的丙烷氧化脱氢制丙烯催化性能

采用浸渍法通过改变焙烧气氛制备了系列NiO/SBA-15 (w_NiO=20%)催化剂, 并考察了催化剂的丙烷氧化脱氢(ODHP)反应性能. 实验结果表明, 与在静止和流动空气中焙烧的催化剂相比, 在1%NO/He (V_NO/V_He=1:99)气氛中焙烧的NiO/SBA-15-NO具有优异的低温丙烷氧化脱氢制丙烯性能, 在350 ℃时, 丙烷的转化率和丙烯收率分别约达29%和13%. 反应温度升至450 ℃时, 丙烯的选择性仍保持在45%左右. X射线粉末衍射(XRD)和透射电镜(TEM)测试结果表明, 1%NO/He气氛可有效抑制焙烧过程中NiO纳米颗粒的团聚, 使NiO物种高分散于SBA-15 的孔道中. H₂-程序升温还原(H₂-TPR)和O₂-程序升温脱附(O₂-TPD)测试结果表明, 随着NiO在SBA-15上分散度的提高, 催化剂的抗还原性增强, ODHP活性氧物种O-的含量增加, 进而使1%NO/He气氛中焙烧的NiO/SBA-15-NO在较宽的温度范围内(350-450 ℃)均具有良好的丙烯选择性, 并显著提高了催化剂的低温活性.     

Ce0.5Zr0.5O2修饰的Ni/SiC、Fe/SiC和Co/SiC催化燃烧甲烷性能

以铈锆固溶体（Ce_0.5Zr_0.5O₂）修饰的高比表面积SiC为载体,采用两步浸渍法制备了Ni、Fe和Co基催化剂,研究了其在煤层气催化燃烧脱氧中的催化活性和稳定性. 利用X射线衍射（XRD）、X射线光电子能谱（XPS）、电感耦合等离子体质谱（ICP-MS）、高分辨透射电子显微镜（HRTEM）、比表面积（BET）、热重分析（TGA）和H₂程序升温还原（H₂-TPR）对催化剂进行了表征. 分析结果表明,Ni、Fe和Co部分进入Ce_0.5Zr_0.5O₂固溶体晶格内部,导致催化剂体相形成更多的缺陷;同时Ce_0.5Zr_0.5O₂固溶体有助于加速金属氧化物和金属之间氧化还原过程的进行,促进了氧吸附、传输和对甲烷的活化. 另外,SiC和Ce_0.5Zr_0.5O₂固熔体良好的抗积碳性能,有效避免了催化剂在富甲烷反应气氛中因积碳而失活,从而使三种催化剂均具有优良的催化燃烧脱氧活性和稳定性. 其中,Co/Ce_0.5Zr_0.5O₂/SiC活性最高,可在320 ℃活化催化甲烷,并在410 ℃实现完全脱氧.     

Ni-M/SiO2催化1,4-丁炔二醇加氢的金属助剂效应

以SiO₂气凝胶为载体,采用等体积浸渍法制备了Ni/SiO₂及不同金属助剂改性的Ni-M/SiO₂（M=Fe、Co、Cu）催化剂,利用ICP、BET、XRD、H₂-TPR、H₂-TPD等手段对催化剂进行了表征,考察了不同第二金属对催化剂结构与1,4-丁炔二醇加氢性能的影响.结果表明,第二金属与Ni物种具有不同程度的双金属协同效应,其中Cu的加入不仅能够提高Ni活性物种的分散度,而且Ni-Cu双金属间的相互作用改善了NiO物种的还原性能及氢活化能力,有利于氢和1,4-丁炔二醇在活性位点的快速转化.在反应温度50℃,氢压1 MPa,反应时间3 h的加氢评价条件下,15Ni5Cu/SiO₂催化剂不仅可以实现1,4-丁炔二醇的完全转化,而且能够有效降低难分离副产物2-羟基四氢呋喃的含量,具有最优的加氢活性和对1,4-丁烯二醇的选择性.     

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.     

Nd,Ce和La改性对Ni/SBA-15催化剂在CH4/CO2重整反应中性能的影响

以稀土金属Nd,Ce或La的氧化物为助剂,采用β-环糊精浸渍法对Ni/SBA-15催化剂进行了改性,并运用X射线衍射、N₂吸附-脱附、程序升温还原和热重等手段考察了改性的催化剂在CO₂重整CH₄制合成气反应中的催化性能. 结果表明,Nd等稀土金属氧化物的添加对催化剂孔结构和晶相结构等性质影响不大,但可影响NiO的还原; Nd的添加使NiO与载体之间以Ni-Nd-O形式相互作用,促进了活性组分NiO的还原. 其中,Nd的添加量为5-10 wt%时所制备的催化剂在重整反应中的催化活性最高,且具有很强的抗积碳性能. La和Ce氧化物促进的Ni催化剂也表现出类似的性质和催化性能.     

高性能麦芽糖加氢Ru-B/SBA-15非晶态合金催化剂的制备

以介孔氧化硅(SBA-15)为载体, 采用超声辅助(NH₄)₂RuCl₆浸渍和BH₄^-还原法制备了负载型Ru-B催化剂, 并通过X射线衍射、X光电子能谱、差示扫描量热法和透射电子显微等技术表征了该催化剂.结果表明, 所制得的Ru-B-X/SBA-15催化剂具有非晶态合金结构, 且Ru-B颗粒高分散在SBA-15的孔道中.在液相麦芽糖加氢反应中, 与采用RuCl₃为金属源制得的Ru-B-C/SBA-15相比, Ru-B-X/SBA-15催化剂具有更高的活性, 是非负载型Ru-B-C催化剂的7倍以上, 且能重复套用11次而未发生显著的失活.     

助剂对Ni/γ-Al2O3催化剂上多环烃JP-10重整制氢反应性能的影响

采用等体积浸渍法制备了碱金属Na、碱土金属Mg以及稀土金属Ce改性的15% Ni-5% M/γ-Al₂O₃镍基负载型催化剂(标记为NMA,M=Na、Mg、Ce)。通过XRD (X射线衍射)、N2吸附-脱附、H₂-TPR (H₂-程序升温还原)、TEM (透射电镜)、NH₃-TPD (NH₃-程序升温脱附)、TG (热重)和拉曼光谱技术对催化剂的物相、织构、表面性质等进行了表征分析,并在微通道反应器内研究了多环烃挂式四氢双环戊二烯(JP-10)催化重整制氢性能。结果表明,不同助剂的加入均在一定程度上提高了Ni/γ-Al₂O₃(NA)催化剂的活性和抗积碳性能。其中,NNaA催化剂的表面活性镍物种的浓度最高,颗粒尺寸最小,且其表面总酸量较低,在高温重整反应中对活性组分镍的抑制聚集作用最为明显,从而使其获得最佳的改性效果。在常压、750℃、水碳比(S/C)为2.4、重时空速(WHSV)为472 h^-1条件下,NNaA催化剂上JP-10的转化率和H₂选择性分别可达82.9%和73.3%,而积碳量仅为0.53 mg·g_feed^-1。反应后该催化剂的积碳多为丝状碳,而其他催化剂的积碳多为无定形碳。     

溶液中肼还原钴离子制备纳米金属钴的反应动力学

通过加入NaBH₄作为诱导剂, 可在室温下引发肼与Co^2＋在水-乙醇体系中的还原反应, 制得高纯度纳米金属钴粉. 机理研究表明, 该反应分二段进行: 第一段主要发生Co^2＋被N₂H₄还原的反应(2Co^2＋＋N₂H₄＋4OH^－＝2Co¯＋N₂­＋4H₂O), 第二段主要为金属Co催化的肼分解反应(N₂H₄＝N₂­＋2H₂­)和歧化反应(3N₂H₄＝N₂­＋4NH₃­). Co^2＋被N₂H₄还原是典型的自催化过程, 因此, 加入少量NaBH₄即可在288 K下启动反应. 通过测量气体产物的生成速率, 获得了Co^2＋还原的反应动力学方程, 发现Co^2＋, N₂H₄和产物Co的反应级数分别为1, 0和1, 反应活化能约为89 kJ/mol. 调节Co^2＋的浓度, 纳米金属钴的表面积可从11增加到25 m²/g.     

B助剂对Ni2P/SBA-15催化剂结构及其加氢脱硫性能的影响

以介孔分子筛SBA-15为载体, 磷酸氢二铵为磷源, 硝酸镍为镍源, 硼酸为硼源, 采用共浸渍法制备了B-Ni₂P/SBA-15催化剂前驱体, 然后采用程序升温氢气还原法, 制备了n_P/n_Ni=0.8, B含量为0.35%-2.10%(w)的一系列B-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)和氨气程序升温脱附(NH₃-TPD)等表征技术对催化剂的结构进行了研究, 以1%(w)二苯并噻吩(DBT)/十氢萘溶液为模型化合物, 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, B-Ni₂P/SBA-15催化剂仍具有介孔结构, Ni₂P为主要的活性物相. 适量B助剂的加入可促使Ni₂P晶粒减小, 催化剂比表面积增加. 此外, 随着B含量的增加, B-Ni₂P/SBA-15催化剂的总酸量也增加. 当反应压力为3.0 MPa, 反应温度由300 ℃升高至360 ℃时, B含量对Ni₂P/SBA-15催化剂活性有明显的影响, B含量为1.40%(w)的B-Ni₂P/SBA-15催化剂加氢脱硫活性最高. B-Ni₂P/SBA-15催化剂上二苯并噻吩的加氢脱硫的反应机理以直接脱硫为主.     

Effect of the order of Ni and Ce addition in SBA-15 on the activity in dry reforming of methane

Dry reforming of methane has been carried out on SBA-15 catalysts containing 5 wt% Ni and 6 wt% Ce. The effect of the order of Ni and Ce impregnation on the catalytic activity has been studied. Both metals were added using the “two-solvent” method that favors metal dispersion inside the pores. Characterizations by XRD (low and high angles), N₂ sorption, SEM and TEM of the materials after metal addition and calcination indicate good preservation of the porosities and high NiO and CeO₂ dispersion inside the porous channels. Reduction was carried out before the catalytic tests and followed by TPR measurements. The most active reduced catalyst was the Ni–Ce/SBA-15 sample prepared by impregnating cerium first, then nickel. All catalysts were highly active and selective towards H₂ and CO at atmospheric pressure. Full CH₄ conversion was obtained below 650 °C. The higher performances compared to those reported in the literature for mesoporous silica with supported Ni and Ce catalysts are discussed.     

Hydrogen production through glycerol steam reforming using Co catalysts supported on SBA-15 doped with Zr,Ce and La

The steam reforming of glycerol has been studied at 500 and 600 oC using Co/SBA-15 and Co/M/SBA-15(M: Zr, Ce, or La) promoted catalysts. The prepared materials were characterized by inductively coupled plasma atomic emission spectroscopy(ICP-AES), X-ray powder diffraction(XRD), hydrogen temperatureprogramed reduction(H_2-TPR), ammonia temperature-programed desorption(NH_3-TPD), nitrogen physisorption analysis(N_2-BET), transmission electron microscopy(TEM) and thermogravimetric analysis(TGA). The incorporation of promoters like Zr, Ce and La on SBA-15 support and successive Co impregnation leaded to smaller cobalt crystallites improving metaldispersion. Besides, stronger metal-support interactions between Co species and M/SBA-15 supports were observed. Thanks to the incorporation of Zr, La and mainly Ce, promoted catalysts present higher glycerol conversion than Co/SBA-15 along 5 h of time on stream. Besides, at 600 oC, Co/M/SBA-15(M: Zr, Ce, or La) catalysts produce higher hydrogen amounts than Co/SBA-15.     

VO<Subscript>x</Subscript>/Zr–SBA-15 catalysts for selective oxidation of ethanol to acetaldehyde

Effect of zirconium presence in the silica framework and content and speciation of vanadium surface oxo-complexes on the catalytic behavior of VO_x/Zr–SBA-15 catalysts in oxidative dehydrogenation of ethanol was investigated. Experimental results bring evidence of successful incorporation of zirconium into ordered mesoporous silica framework with the preservation of ordered mesoporosity by hydrothermal template base synthesis method. The presence of zirconium in the SBA-15 framework increases reducibility of vanadium species and acidity of the catalysts. It is reflected in higher activity of vanadium species expressed as turn-over frequency (e.g., TOF of 20 h^?1 for 5%VO_x/Zr–SBA-15 sample in comparison with TOF of 12 h^?1 for 5%VO_x/SBA-15 sample) and also in significant decrease of selectivity to acetaldehyde (65% in comparison with 90% for mentioned samples) followed by increase in selectivity to ethylene (25% in comparison with 5%). This change in distribution of reaction products is related to stronger acidity character of surface OH groups and inhibition effect of formed water vapours on the oxidative dehydrogenation products (acetaldehyde). Catalytic data also reveal that oligomeric/polymeric tetrahedrally coordinated vanadium species exhibit higher activity in ethanol oxidative dehydrogenation than monomeric complexes. In addition, comparison of the catalytic performance of VO_x/Zr–SBA-15 catalysts with VO_x/SBA-15 catalysts showed that catalytic properties of VO_x/Zr–SBA-15 catalysts can be tuned by incorporation of controlled amount of zirconium into silica framework.     

Silylated Co/SBA-15 catalysts for Fischer-Tropsch synthesis

A series of silylated Co/SBA-15 catalysts were prepared via the reaction of surface Si-OH of SBA-15 with hexamethyldisilazane (HMDS) under anhydrous, vapor-phase conditions, and then characterized by FT-IR, N₂ physisorption, TG, XRD, and TPR-MS. The results showed that organic modification led to a silylated SBA-15 surface composed of stable hydrophobic Si-(CH₃)₃ species even after calcinations and H₂ reduction at 673 K. Furthermore, the hydrophobic surface strongly influenced both metal dispersion and reducibility. Compared with non-silylated Co/SBA, Co/S-SBA (impregnation after silylation) showed a high activity, due to the better cobalt reducibility on the hydrophobic support. However, S-Co/SBA (silylation after impregnation) had the lowest FT activity among all the catalysts, due to the lower cobalt reducibility along with the steric hindrance of grafted -Si(CH₃)₃ for the re-adsorption of α-olefins.     

New ZnCe catalyst encapsulated in SBA-15 in the production of 1,3-butadiene from ethanol

ZnO-CeO2/SBA-15 catalysts were prepared by two kinds of solid-state grinding method and used for the production of 1,3-butadiene(1,3-BD) from ethanol.A mixture of SBA-15(with or without organic template) and metal precursors were ground in solid-state.The obtained catalysts were characterized by TG,N2 adsorption-desorption,TEM,XRD,Py-FTIR and NH_3-TPD techniques.Superior dispersion of metal oxides and more exposed acid sites were achieved on the catalyst lOZn_1Ce_5-AS with the presence of organic template in SBA-15 during the solid-state grinding process.The catalytic performance was evaluated in a fixed-bed reactor and a 1,3-butadiene selectivity of as high as 45% is achieved.This is attributed to the coupling effect of Zn and Ce species in the mesopores of SBA-15,in which Zn promotes ethanol dehydrogenation and Ce enhances aldol-condensation,respectively.Additionally,solvent-free method inspires new catalyst synthesis strategy for the production of 1,3-butadiene from ethanol.     

Effects of titanium silicalite and TiO2 nanocomposites on supported Co‐based catalysts for Fischer–Tropsch synthesis

Titanium silicalite (TS) and TiO₂ nanocomposites were prepared by mixing TS and TiO₂ with different ratios in ethanol. They were impregnated with 15 wt% Co loading to afford Co‐based catalysts. Fischer–Tropsch synthesis (FTS) performance of these TS–TiO₂ nanocomposite‐supported Co‐based catalysts was studied in a fixed‐bed tubular reactor. The results reveal that the Co/TS–TiO₂ catalysts have better catalytic performance than Co/TS or Co/TiO₂ each with a single support, showing the synergistic effect of the binary TS–TiO₂ support. Among the TS–TiO₂ nanocomposite‐supported Co‐based catalysts, Co/TS–TiO₂‐1 presents the highest activity. These catalysts were characterized using N₂ adsorption–desorption measurements, X‐ray diffraction, X‐ray photoelectron spectroscopy, H₂ temperature‐programmed reduction, H₂ temperature‐programmed desorption and transmission electron microscopy. It was found that the position of the active component has a significant effect on the catalytic activity. In the TS–TiO₂ nanocomposites, cobalt oxides located at the new pores developed between TS and TiO₂ can exhibit better catalytic activity. Also, a positive relationship is observed between Co dispersion and FTS catalytic performance for all catalysts. The catalytic activity is improved on increasing the dispersion of Co.     

Influence of the pore structure of MCM-41 and SBA-15 silica fibers on atomic layer chemical vapor deposition of cobalt carbonyl

Mesoporous high surface area MCM-41 and SBA-15 type silica materials with fibrous morphology were synthesized and used as support materials for the ALCVD (atomic layer chemical vapor deposition) preparation of Co/MCM-41 and Co/SBA-15 catalysts. Co/MCM-41 and Co/SBA-15 catalysts were prepared by deposition of Co2(CO)8 from the gas phase onto the surfaces of preheated support materials in a fluidized bed reactor. For both silica materials, two different kinds of preparation methods, direct deposition and a pulse deposition method, were used. Pure silica supports as well as supported cobalt catalysts were characterized by various spectroscopic (IR) and analytical (X-ray diffraction, Brunauer-Emmett-Teller, elemental analysis) methods. MCM-41 and SBA-15 fibers showed considerable ability to adsorb Co2(CO)8 from the gas phase. For MCM-41 and SBA-15 silicas, cobalt loadings of 13.7 and 12.1 wt % were obtained using the direct deposition method. The cobalt loadings increased to 23.0 and 20.7 wt % for MCM-41 and SBA-15 silicas, respectively, when the pulse deposition method was used. The reduction behavior of silica-supported cobalt catalysts was found to depend on the catalyst preparation method and on the mesoporous structure of the support material. Almost identical reduction properties of SBA-15-supported catalysts prepared by different deposition methods are explained by the structural properties of the mesoporous support and, in particular, by the chemical structure of the inner surfaces and walls of the mesopores. Pulse O2/H2 chemisorption experiments showed catalytically promising redox properties and surface stability of the prepared MCM-41- and SBA-15-supported cobalt catalysts.     

Effect of the pore size of Co/SBA-15 isomorphically substituted with zirconium on its catalytic performance in Fischer-Tropsch synthesis

Cobalt catalysts supported on a series of mesoporous SBA-15 materials isomorphically substituted with zirconium (Zr/Si atomic ratio = 1/20) with different pore sizes (5.7 nm, 7.8 nm, 11.6 nm, 17.6 nm) have been synthesized. The catalysts were characterized by transmission electron microscopy, ²⁹Si solid state magic angle spinning (MAS) NMR, N₂ adsorption-desorption measurements, X-ray powder diffraction, X-ray photoelectron spectroscopy, H₂-temperature programmed reduction, H₂-temperature programmed desorption and O₂ titrations. The results indicated that larger pore size led to weaker interactions between cobalt and the supports which lowered the temperature of both reduction steps (Co₃O₄→CoO and CoO→Co⁰). The catalytic performances of the catalysts in Fischer-Tropsch synthesis (FTS) were tested in a fixed bed reactor. It was found that the FTS catalytic activity and product selectivity depended strongly on the pore size of the catalysts. The catalyst with a pore size of 7.8 nm showed the best FTS activity, and the catalyst with a pore size of 17.6 nm showed the highest selectivity to C₁₂–C₂₀ and C₂₀₊ hydrocarbons.     

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...     

Liquid Phase Hydrogenolysis of Biomass‐derived Lactate to 1,2‐Propanediol over Silica Supported Cobalt Nanocatalyst

Liquid phase hydrogenolysis of ethyl lactate to 1,2‐propanediol was performed over silica supporting cobalt catalysts prepared by two different methods: precipitation‐gel (PG) technique and deposition‐precipitation (DP) procedure. The cobalt species (Co₃O₄/cobalt phyllosilicate) present in the corresponding calcined PG and DP catalysts were different as a consequence of the preparation methods, and Co OH Co olation and Si O Co oxolation molecular mechanisms were employed to elucidate the chemical phenomena during the different preparation procedures. In addition, the texture (BET), reduction behavior (TPR and in‐situ XRD), surface dispersion and state of cobalt species (XPS), and catalytic performance differ greatly between the samples. Because of small particle size, high dispersion of cobalt species and facile reducibility, the Co/SiO₂ catalyst prepared by precipitation‐gel method presented a much higher activity than the catalyst prepared by deposition‐precipitation method. Metallic cobalt is assumed to be the catalytically active site for the hydrogenolysis reaction according to the catalytic results of both cobalt samples reduced at different temperatures and the structure changes after reaction.