天然气和二氧化碳转化制合成气的研究 Ⅴ．甲烷脱氢积炭反应特征

采用ＴＧ、ＸＲＤ、ＳＥＭ、ＥＤＡＸ和脉冲色谱技术，研究了Ｎｉ／Ａｌ２Ｏ３和Ｎｉ／ＡＲＭ催化剂的甲烷脱氢积炭反应特征。结果指出，甲烷脱氢反应的积炭行为与催化剂上镍的分散状态有关。Ｎｉ－２催化剂上Ｎｉ的分散度小，晶粒大，甲烷脱氢形成的炭丝较长，主要以石墨型炭游离存在：而Ｎｉ／ＡＲＭ催化剂上Ｎｉ的分散度大，镍晶粒小，甲烷脱氢形成的炭丝较短，主要覆盖在催化剂活性中心表面。甲烷脱氢主要产生无定型炭和石墨型炭，其中无定型炭可以被ＣＯ２部分消除。在催化剂制备时，通过提高镍在催化剂表面的分散度，减小镍的晶粒大小，不仅可以提高催化剂的活性，而且可以提高ＣＯ２对积炭的消炭性能。     

Furfural Hydrogenation on Nickel‐promoted Cu‐containing Catalysts Prepared from Hydrotalcite‐Like Precursors

The nickel‐promoted Cu‐containing catalysts (Cu_xNi_y‐MgAlO) for furfural (FFR) hydrogenation were prepared from the hydrotalcite‐like precursors, and characterized by X‐ray powder diffraction, inductively‐coupled plasma atomic emission spectroscopy, N₂ adsorption‐desorption, UV‐Vis diffuse reflectance spectra and temperature‐programmed reduction with H₂ in the present work. The obtained catalysts were observed to exhibit a better catalytic property than the corresponding Cu‐MgAlO or Ni‐MgAlO samples in FFR hydrogenation, and the CuNi‐MgAlO catalyst with the actual Cu and Ni loadings of 12.5 wt% and 4.5 wt%, respectively, could give the highest FFR conversion (93.2%) and furfuryl alcohol selectivity (89.2%). At the same time, Cu⁰ species from the reduction of Cu²⁺ ions in spinel phases were deduced to be more active for FFR hydrogenation.     

溶剂化金属原子浸渍法制备高分散负载型催化剂(Ⅶ)——Ni-Cu/SiO2双金属催化剂的结构与性能

利用金属蒸气法制备了不同组成的Nj-CujSiO₂双金属催化剂,XRD、TEM和磁性测定表明有Ni-Cu合金形成,合金颗粒的组成不均匀,而且有部分自由的Ni和Cu存在;Ni/Cu摩尔比为1:1催化剂的催化活性大于2:1和3:1的双金属催化剂以及Ni和Cu的单金属催化剂。     

PROPERTIES OF Ni-Cu/SiO_2 BIMETALLIC CATALYSTSPREPARED BY SOLVATED METAL ATOM DISPERSION(SMAD) TECHNIQUE

IntroductionAsoneofthemethodsofpreparationofsupportedmetalcatalysts,solvatedmatalatomdispersion(SMAD)onoxidesupportsattractsmuchattentionnowadays.TIstechniquehasbeendevelopedbyKlabunde'SandOzin'sresearchgroups.Itprovidesanumberofadvantages,ascomparedwitht…     

PROPERTIES OF POLYMER SUPPORTED Ni-Cu BIMETALLIC CATALYSTS PREPARED BY SOLVATED METAL ATOM IMPREGNATION

D-72 resin supported nickel-copper catalysts prepared by solvated metal atom impreg-nation (SMAI) were studied by magnetic measurements and X-ray photoelectron spectro-scopy (XPS). The Ni particles on the catalysts are very highly dispersed and displaysuperparamagnetic behaviour. Ni-Cu alloy clusters were found to be formed. The sur-face compositions are different from the bulk concentrations. In contrast with the surfaceenrichment in copper generally observed on conventional Ni-Cu catalysts, the surfaces ofthese catalysts are enriched in nickel. The nickel is in both zero and valent states, whilecopper is mainly in metallic state. Catalytic data show that the formation of Ni-Cu alloyclusters has a profound effect on the catalytic activities of the catalysts in the hydrogena-tion of furfural. The activity of the Ni:Cu ratio of one bimetallic catalysts is much higherthan that of the Ni or Cu monometallic catalyst.     

铜钼组分对γ-Al2O3负载镍催化剂脂肪酸甲酯加氢脱氧性能的影响

制备一系列包含或不包含铜、钼组分的Ni/γ-Al₂O₃催化剂,并对其进行表征和性能测试。考察了铜、钼负载量,浸渍顺序（包括连续浸渍和共浸渍）,反应条件对脂肪酸甲酯加氢脱氧反应性能的影响。根据TG数据,使用过的20Ni-6Cu/γ-Al₂O₃催化剂其热失重小于20Ni/γ-Al₂O₃催化剂,这表明,铜的引入能够有效抑制反应过程中催化剂表面的积炭行为。对于20Ni-6Cu/γ-Al₂O₃和20Ni-6Cu-nMo/γ-Al₂O₃（n=2、5、8和12）催化剂,NH₃-TPD分析结果显示,钼物相的引入对载体γ-Al₂O₃的酸性位有着显著影响,当钼负载量达到5%时,可以观察到一个新的酸位对应于中强酸位。铜和钼修饰过的催化剂其催化性能要高于Ni/γ-Al₂O₃催化剂。从XPS的分析可以看出,催化剂中的铜主要以正二价形式存在,钼主要以正四价和正六价形式存在,而且不同的浸渍顺序会影响催化剂表面活性组分的实际含量。此外,脂肪酸甲酯的转化率和烷烃产品的收率也和所制备出来的催化剂的浸渍顺序有关。在所有的催化剂中,使用连续浸渍（先浸渍镍铜组分、浸渍钼组分）所制备的三金属20Ni-6Cu-5Mo/γ-Al₂O₃催化剂展现了优异的催化性能。在适宜的反应条件下（350 ℃,2.5 MPa,WSHV=2.0 h^-1,H₂/oil ratio=1250 mL/mL）,脂肪酸甲酯的转化率和烷烃产品的收率分别达到98.4%和94.2%。     

Effect of promoter on selective hydrogenation of furfural over Cu-Cr/TiO2 catalyst

The selective hydrogenation of furfural has been investigated over the titania-supported monometallic (Cu) and bimetallic (Cu–Cr) catalysts. The catalytic performances were assessed over 4 h of run length under atmospheric pressure at the hydrogen-to-hydrocarbon ratio of 10.6 and 453 K. The results represented that the level of furfural conversion over the non-promoted catalyst was very low (below 10%) while the promoted one showed considerable furfural conversion during this period (higher than 70%). However, both catalysts exhibited high durability and selectivity towards furfuryl alcohol.

     

Highly Stable Carbon-Shell Encapsulated Ni−Cu Bimetallic Catalysts for Efficient Conversion of Levulinic Acid to γ-Valerolactone

Non-noble Ni−Cu alloys serve as an alternative catalytic material for noble metal-based catalysts that could be applied in the efficient conversion of levulinic acid (LA) into the high value γ-valerolactone (GVL). However, maintaining the catalytic stability for Ni−Cu nanoparticles in the LA hydrogenation process remains a substantial challenge, Herein, this problem is solved by constructing carbon-protected catalytic sites within carbon layer-coated Ni−Cu nanoalloy composite via pyrolysis of NiCu_x(OH)/glucose precursor. The optimized NiCu_0.68@C catalyst exhibits excellent stability and selectivity to GVL (>99 %) in the hydrogenation of LA reaction. Various characterization indicates that the enhancement in stability originates from the protective effect of the carbon layer, which prevents the metal leaching, oxidation and aggregation of Ni−Cu nanoparticles during the reaction process. This work greatly advances non-noble metal-catalyzed conversion of LA to GVL and helps the rational design of bimetallic catalysts.     

不同硅源的Cu/SiO2催化糠醛加氢制2-甲基呋喃

以硅溶胶和气相二氧化硅为载体,采用氨蒸法制备了Cu/SiO₂-sol和Cu/SiO₂-aer两种催化剂,采用N₂吸附脱附、X射线衍射（XRD）、傅里叶红外光谱（FT-IR）、透射电子显微镜（TEM）、N₂O-H₂滴定、氢气程序升温还原（H₂-TPR）、氨程序升温脱附（NH₃-TPD）及X射线光电子能谱（XPS）对样品进行表征,在固定床反应器中考察两种催化剂对糠醛气相加氢制2-甲基呋喃的催化性能。结果表明,Cu/SiO₂-sol催化剂具有更好的催化活性,在150 h反应时间内,糠醛转化率为100%,2-MF选择性在91%以上。这主要归因于以硅溶胶为硅源可以生成更多页硅酸铜,还原后催化剂表面Cu的分散性更高、弱酸位更多,有利于提高糠醛的转化率与2-甲基呋喃的选择性。同时Cu/SiO₂-sol具有较大的孔容孔径,有利于降低反应过程中积炭,延长催化剂寿命。     

沸石和活性炭为载体的Fe3+和Cu2+型催化剂催化氧化苯酚的比较

以沸石和活性炭为载体，制备了Fe3 和Cu2 型沸石和活性炭催化荆，研究了非均相Fe和Cu催化剂催化氧化高浓度含酚废水．在Fenton反应机理的基础上，探讨了Cu2 的均相和非均相催化氧化机理，以人造沸石和活性炭为栽体制备了相应的4种非均相催化剂，进行了均相、非均相Fe和Cu催化剂催化氧化高浓度含酚废水的对比试验，分析了这两种载体的比表面积、孔径分布和中孔孔容，比较了4种非均相催化剂对苯酚降解率的影响．结果发现Cu2 不仅能大大提高反应速率，而且其均相、非均相反应体系的苯酚降解率均可达到约97％．     

Cr-free Co-Cu/SBA-15 catalysts for hydrogenation of biomass-derivedα-,β-unsaturated aldehyde to alcohol

Cr-free bi-metallic SBA-15-supported Co–Cu catalysts were examined in the conversion of bio-mass-derived α-, β-unsaturated aldehyde (furfural) to value-added chemical furfuryl alcohol (FOL). Co–Cu/SBA-15 catalysts with a fixed Cu loading of 10 wt% and varying Co loadings (2.5, 5, and 10 wt%) were prepared by the impregnation method. The catalysts were characterized by X-ray dif-fraction, N2 sorption, H2 temperature-programmed reduction, scanning electron microscopy, ener-gy-dispersive X-ray spectroscopy, high-resolution transmission electron microscopy, CO chemi-sorption, and inductively coupled plasma mass spectrometry. The influence of different reaction parameters such as temperature, pressure, catalyst dosage, and furfural concentration on the cata-lyst performance was evaluated. Relative to catalysts supported on amorphous silica, the current SBA-15-supported Co–Cu catalysts displayed higher performance, attaining a furfural conversion of 99% and furfuryl alcohol selectivity of 80%. The catalytic reactions were conducted in a 100-mL autoclave at 170 °C and 2 MPa H2 pressure for 4 h.     

镁铝混合氧化物负载镍催化剂上液化石油气的预重整

采用共沉淀-浸渍法并在较低温度(400～700℃)下焙烧制备了镁铝混合氧化物(MgmAl)负载的Ni催化剂.X射线衍射和程序升温还原结果表明,Ni物种高度分散于催化剂表面,没有形成尖晶石NiAl2O4.在650℃可被还原成金属Ni纳米晶粒,在400℃和较低水/碳摩尔比(S/C=2)条件下表现出较好的催化液化石油气(LP...     

Properties of anodic RuNiO<Subscript><Emphasis Type="Italic">x</Emphasis></Subscript>(OH)<Subscript><Emphasis Type="Italic">y</Emphasis></Subscript> catalysts synthesized on carbon supports with various dispersion degree

A number of catalysts of the (Ru-Ni)/C system is synthesized and studied for application in anodes of alkaline ethanol-air fuel cells. The carbon supports used are carbon blacks with different specific surface area and graphite powders. The X-ray photoelectron spectroscopy technique allowed detecting on the catalyst surface metallic ruthenium and nickel in the form of Ni(OH)2 hydroxide and possibly oxyhydroxide NiOOH. It is shown that the catalyst activity in the reaction of ethanol electrochemical oxidation grows at an increase in the specific surface area of the carbon support. The method of carbon monoxide oxidative desorption was used to determine the values of the specific surface area of the catalyst metallic phase. It is shown that at an increase in the relative ruthenium content from (1Ru3Ni)/C to Ru/C, the specific catalytic activity in the catalysts of the (Ru-Ni)/C system reaches the maximum value near the composition of (2Ru1Ni)/C. It is shown that the found optimum catalyst composition is independent of the carbon support dispersion degree. Activity in ethanol electrooxidation of the (2Ru1Ni)/C catalyst supported on the Ketjenblack EC-600 carbon black is 18 ± 3 A/g of the catalyst (>120 A/g of Ru) at 40°C and potential E = 0.5 V in the 2MKOH + 1 M C₂H₅OH electrolyte.     

Cu-Ni-Zn三元脂肪醇胺化催化剂的研究

 长链烷基二甲基叔胺是一类重要的有机中间体,目前其主要的制备工艺是由脂肪醇和二甲胺在脱氢－加氢类催化剂的作用下进行胺化反应．改进脂肪醇胺化催化剂的主要目标是提高其选择性．对以Cu和Ni为活性组分,以碳酸钙为载体的催化剂体系中加入Zn助催化剂组分对催化剂选择性的影响进行了研究．结果发现,在相同Cu／Ni比的条件下,Zn在Cu－Ni催化剂体系中的一个主要作用是能够阻碍氧化态镍的还原,而催化剂的选择性与催化剂中镍的还原程度密切相关．     

Enhanced methane decomposition over transition metal-based tri-metallic catalysts for the production of COx free hydrogen

In this study, COx-free hydrogen production via methane decomposition was studied over Cu–Zn-promoted tri-metallic Ni–Co–Al catalysts. The catalysts have been prepared by the constant pH co-precipitation method, and the nominal Ni metal loading was fixed at 50 wt % along with other metals at 10 wt% each. The catalyst activity for methane decomposition reaction was examined in a reactor between 400 °C and 700 °C and at atmospheric pressure. Different techniques such as N₂-physisorption, X-ray diffraction, H₂-TPR SEM, TEM, ICP-MS, TGA, and Raman spectroscopy were applied to characterize the catalysts. The relation between the catalyst composition and their catalytic activity has been investigated. The controlled synthesis has resulted in a series of catalysts with a high surface area. Ni–Co–Cu–Zn–Al was the most active and productive catalyst. Various characterizations indicate that the promotional effects of Cu–Zn interaction were the critical factor in catalysts' activity and stability. Ni–Co–Cu–Zn catalyst gave the highest methane conversion of 85% at 700 °C. Zn addition improves the stability of the catalyst by retaining the active metal size during the decomposition reaction. The catalyst was active for 80 h of stability study. The rapid deactivation of the Ni–Co catalyst was due to the sintering of the catalyst at 650 °C. Moreover, carbon species accumulated during the methane decomposition reaction depend on the catalysts' composition. Zn promotes the growth of reasonably long and thin carbon nanotubes, whereas the diameter of carbon nanotubes on unpromoted catalysts was large.     

流化床反应器中不同Ni/Al2O3催化剂上CH4-CO2重整反应性能的比较研究

采用浸渍法、溶胶 凝胶过程与普通干燥、超临界干燥过程相结合的方法制备了三种20%的NiO-Al2O3体系催化剂，利用BET、XRD、H2 TPR、H2-TPD等方法对各催化剂样品物化性质进行了表征，并考察了催化剂在流化床反应器中CH4-CO2重整反应的催化性能。研究结果表明，经923K焙烧后气凝胶催化剂中镍与载体间作用力最强，主要为固定NiO和尖晶石NiAl2O4结构，而浸渍型催化剂和干凝胶催化剂中镍与载体间作用力较弱。三种催化剂中，气凝胶催化剂具有比表面积较大、堆密度较低、Ni还原度及分散度较高的特点。它在流化床反应器中所形成的聚团流态化状态具有较高的床层膨胀率，大量多孔疏松状的纳米颗粒聚团在床内的循环运动有效地提高了传质效率，能使得生成的沉积炭快速得到气化，从而抑制了催化剂失活；对于浸渍型催化剂和干凝胶催化剂，流化床反应器中床层膨胀率较低、颗粒循环量较少、传质效率较低，易于造成催化剂表面积炭失活。经用TG和XRD等方法对反应后催化剂分析表征，证明催化剂表面石墨碳的沉积是导致浸渍型催化剂和干凝胶催化剂失活的主要原因。     

石墨烯负载镍催化CO_2加氢甲烷化

采用改进的Hummers法制备了氧化石墨烯(GO),经水合肼还原得到石墨烯(RGO),通过浸渍法制备了石墨烯负载的镍基催化剂(Ni/RGO);对其催化二氧化碳甲烷化反应的性能进行了研究,并与以碳纳米管(CNTs)和活性炭(AC)为载体负载的Ni基催化剂进行了比较.由于催化剂的载体分别为RGO,CNTs和AC,所以Ni将会表现出不同的形态.利用红外光谱(FTIR)、比表面积(BET)测试、程序升温还原(H2-TPR)、X射线衍射(XRD)分析和透射电子显微镜(TEM)等表征手段对其结构及物理性质进行了表征.结果表明,Ni/RGO具有相对较大的比表面积(316 m~2/g),Ni在Ni/RGO上的颗粒尺寸(5.3 nm)小于其在Ni/CNTs(8.9 nm)和Ni/AC(11.6 nm)上的颗粒尺寸;该催化剂在二氧化碳甲烷化反应中具有更高的催化活性和选择性,而且具有良好的使用寿命.     

Aqueous-phase catalytic hydrogenation of furfural to cyclopentanol over Cu-Mg-Al hydrotalcites derived catalysts: Model reaction for upgrading of bio-oil

A series of Cu-Mg-Al hydrotalcites derived oxides with a (Cu+Mg)/Al mole ratio of 3 and varied Cu/Mg mole ratio (from 0.07 to 0.30) were prepared by co-precipitation and calcination methods, then they were introduced to the hydrogenation of furfural in aqueous-phase. Effects of Cu/Mg mole ratio, reaction temperature, initial hydrogen pressure, reaction time and catalyst amount on the conversion rate of furfural as well as the selectivity toward desired product cyclopentanol were systematically investigated. The conversion of furfural over calcined hydrotalcite catalyst with a Cu/Mg mole ratio of 0.2 was up to 98.5% when the reaction was carried out under 140 °C and the initial hydrogen pressure of 4 MPa for 10 h, while the selectivity toward cyclopentanol was up to 94.8%. The catalysts were characterized by XRD and SEM. XRD diffraction of all the samples showed characteristic pattern of hydrotalcite with varied peak intensity as a result of different Cu content. The catalytic activity was improved gradually with the increase of Cu component in the hydrotalcite.     

同晶取代法制备Cu-Ni双金属催化剂及其催化CO加氢合成乙醇性能

采用定向同晶取代法制备了一系列镍孔雀石前驱体的Cu-Ni双金属催化剂。考察了前驱体结构以及催化剂表面组成对催化剂催化性能的影响,并采用浆态床反应器对催化剂的CO加氢制乙醇性能进行评价。实验结果表明,采用定向同晶取代法可以制备出（Cu,Ni）₂CO₃（OH）₂纯物相,取代后的Ni²⁺主要富集在前驱体（Cu,Ni）₂CO₃（OH）₂表面。焙烧后形成的（Cu_x,Ni_1-x）O固溶体均匀地分散在CuO晶体结构中。还原后的催化剂中Cu、Ni相互均匀分散形成活性界面,促进了低碳醇的合成。其中,不连续分布的Ni活性位点阻止了碳链的进一步增长,从而提高了乙醇选择性。当Ni/Cu原料比为45：100时,（Cu_x,Ni_1-x）O固溶体与CuO之间有较强的相互作用,表现出最好的反应活性和乙醇选择性。     

Effect of surface structure on the catalytic behavior of Ni：Cu/Al and Ni：Cu：K/Al catalysts for methane decomposition

Methane decomposition using nickel, copper, and aluminum （Ni：Cu/Al） and nickel, copper, potassium, and aluminum （Ni：Cu：K/Al） modified nano catalysts has been investigated for carbon fibers, hydrogen and hydrocarbon production. X-ray photoelectron spectroscopy （XPS）, static secondary ion mass spectrometry （SSIMS）, thermal gravimetric analysis （TGA）, Fourier transform infrared （FT-IR）, secondary electron microscopy/X-ray energy dispersive （SEM-EDX）, and temperature programmed desorption （TPD） were used to depict the chemistry of the catalytic results. These techniques revealed the changes in surface morphology and structure of Ni, Cu, Al, and K, and formation of bimetallic and trimetallic surface cationic sites with different cationic species, which resulted in the production of graphitic form of pure carbon on Ni：Cu/Al catalyst. The addition of K has a marked effect on the product selectivity and reactivity of the catalyst system. K addition restricts the formation of carbon on the surface and increases the production of hydrogen and C2, C3 hydrocarbons during the catalytic reaction whereas no hydrocarbons are produced on the sample without K. This study completely maps the modified surface structure and its relationship with the catalytic behavior of both systems. The process provides a flexible route for the production of carbon fibers and hydrogen on Ni：Cu/Al catalyst and hydrogen along with hydrocarbons on Ni：Cu：K/Al catalyst. The produced carbon fibers are imaged using a transmission electron microscope （TEM） for diameter size and wall structure determination. Hydrogen produced is COx free, which can be used directly in the fuel cell system. The effect of the addition of Cu and its transformation and interaction with Ni and K is responsible for the production of CO/CO2 free hydrogen, thus producing an environmental friendly clean energy.