Mild and efficient CO-mediated eliminative deoxygenation of epoxides catalyzed by supported gold nanoparticles

Supported gold nanoparticles (NPs), which are well-known epoxidation catalysts, were found to be exceptionally active for the selective deoxygenation of epoxides into alkenes using cheap and easily accessible CO and H(2)O as the reductant.     

镍掺杂对氧化铝纳米片负载金催化剂在CO氧化反应中的促进作用（英文）

负载型金催化剂在CO氧化反应中具有良好的低温活性,受到了研究者的广泛关注,其催化性能与载体的性质密切相关.氧化铝具有廉价易得、比表面积大和热稳定性好等优点.然而,作为一种非还原性载体,氧化铝提供活性氧物种的能力差,与还原性载体相比催化剂的CO氧化活性较低.理论计算和实验结果表明,在金催化剂中引入过渡金属镍能够有效促进氧分子在催化剂表面的吸附和活化,从而提升金催化剂活性.此外,过渡金属的存在能够提高金的分散度,增加活性位数目,防止在高温预处理过程中金颗粒的烧结,从而提高催化剂的活性和稳定性.基于上述考虑,本文在氧化铝纳米片合成过程中原位引入硝酸镍,以实现对氧化铝载体的改性,然后负载金并应用于CO氧化反应.结果表明,当载体中的Ni/Al摩尔比为0.05,金负载量为1wt%时,采用还原性气氛对催化剂进行预处理可以得到具有CO氧化性能优良的金催化剂, 20 oC下CO转化率即可达100%.预处理气氛能够显著影响催化活性,采用还原性气氛预处理后催化剂活性明显优于氧化性气氛预处理.采用X射线衍射(XRD)、高分辨透射电镜(HRTEM)、氢气程序升温还原(H2-TPR)、氧气程序升温脱附(O2-TPD)、CO吸附原位红外光谱(CO-DRIFT)和X射线光电子能谱(XPS)等表征手段进一步研究了镍掺杂对Au/Al2O3催化剂上CO氧化反应的促进作用机制.XRD测试未观察到明显的金或镍衍射峰,表明金或镍物种均为高分散.HRTEM结果进一步证实,引入镍物种后金颗粒的粒径由3.6 nm减小为2.4 nm,表明镍掺杂有助于提高金的分散度.而XPS结果显示,镍掺杂催化剂中金与镍存在电子转移,而镍仍以Ni O为主.H2-TPR结果表明,镍掺杂的催化剂前驱体中的金物种更容易被还原.O2-TPD结果证实,镍掺杂催化剂能够引入更多的氧空位,促进氧分子的吸附和活化,从而促进CO氧化反应的进行.CO-DRIFT结果表明,相比于氧化性气氛,采用还原性气氛预处理后金物种的电子云密度增加, CO吸附增强.而对于镍掺杂的催化剂,金物种吸附CO分子的能力进一步提高,有利于CO氧化反应的进行.综上,镍掺杂能够有效提高催化剂中金的分散度,增强催化剂对CO的吸附,促进氧气分子的吸附和活化,从而提高了催化剂的CO氧化活性.     

Supported Ru catalysts prepared by two sonication-assisted methods for preferential oxidation of CO in H2

The preferential oxidation (PROX) of CO in the presence of H(2) is an important step in the production of pure H(2) for industrial applications. In this report, two sonochemical methods (S1 and S2) were used to prepare highly dispersed Ru catalysts supported on mesoporous TiO(2) (TiO(2)(MSP)) for the PROX reaction, in which a reaction gas mixture containing 1% CO + 1% O(2) + 18% CO(2) + 78% H(2) was used. The supported Ru catalysts performed better than the supported Au and Pt catalysts, and the S1 and S2 methods are superior to the impregnation method. The Ru/TiO(2)(MSP) catalysts were active for the PROX reaction below 200 °C and good for the methanation reactions of CO and CO(2) above 200 °C. The presence of residual chlorine in the catalysts severely suppressed their PROX reaction activity, and a higher dispersion of Ru particles led to better catalytic performances. The addition of Au in the Ru/TiO(2)(MSP) catalyst also caused a poorer catalytic activity for both the PROX and the methanation reactions. TPR results showed that in the active catalysts prepared by the S1 and S2 methods, the well dispersed Ru particles, after calcination in air, had a stronger interaction with the support than those in the catalyst prepared by the impregnation method and in the Au-Ru/TiO(2)(MSP) catalyst. In situ CO absorption experiments performed with the diffusion reflectance Fourier transform infra red (DRIFT) method showed that the bridged adsorbed CO species on isolated Ru(0) sites correlated with the catalytic performances, indicating that these isolated Ru(0) sites are the most active sites of the Ru/TiO(2)(MSP) catalysts in the PROX reaction.     

An Os(II)--bisbipyridine--4-picolinic acid complex mediates the biocatalytic growth of au nanoparticles: optical detection of glucose and acetylcholine esterase inhibition

The complex Os(II)-bisbipyridine-4-picolinic acid, [Os(bpy)(2)PyCO(2)H](2+) (1), mediates the biocatalyzed growth of Au nanoparticles, Au NPs, and enables the spectroscopic assay of biocatalyzed transformations and enzyme inhibition by following the Au NP plasmon absorbance. In one system, [Os(bpy)(2)PyCO(2)H](2+) mediates the biocatalyzed oxidation of glucose and the growth of Au NPs in the presence of glucose oxidase, GOx, AuCl(4) (-), citrate and Au NP seeds. The mechanism of the Au NPs growth involves the oxidation of the [Os(bpy)(2)PyCO(2)H](2+) complex by AuCl(4) (-) to form [Os(bpy)(2)PyCO(2)H](3+) and Au(I). The [Os(bpy)(2)PyCO(2)H](3+) complex mediates the GOx biocatalyzed oxidation of glucose and the regeneration of the mediator 1. Citrate reduces Au(I) and enlarges the Au seeds by the catalytic deposition of gold on the Au NP seeds. In the second system, the enzyme acetylcholine esterase, AChE, is assayed by the catalytic growth of the Au NPs. The hydrolysis of acetylcholine (2) by AChE to choline is followed by the [Os(bpy)(2)PyCO(2)H](3+) mediated oxidation of choline to betaine and the concomitant growth of the Au NPs. The mediated growth of the Au NPs is inhibited by 1,5-bis(4-allyldimethylammonium-phenyl)pentane-3-one dibromide (3). A competitive inhibition process was demonstrated (K(M)=0.13 mM, K(I)=2.6 microM) by following the growth of the Au NPs.     

沉积-沉淀法和沉积-还原法制备Nb2O5负载的金纳米粒子及其催化CO氧化活性

采用不同的沉积法制备了氧化铌(Nb2O5)负载的金纳米粒子催化剂,即沉积-沉淀(DP)法、尿素辅助的DP法、沉积-还原(DR)法和一步法制备了1 wt%Au/Nb2O5催化剂.在众多类型Nb2O5(包括商业Nb2O5)中,采用水热法制备的层间型Nb2O5(Nb2O5(HT))最适合用作载体.结果表明,较大比表面积的Nb2O5(HT)使得金以纳米颗粒形式分散于其上.在优化的条件下,以DP和DR法沉积于Nb2O5(HT)上的金纳米粒子平均粒径为5 nm.采用DR法制备的Au/Nb2O5(HT)催化剂上CO转化率为50%时的温度为73oC.不沉积金的条件下,即使在250oC, Nb2O5(HT)对CO氧化反应也没有催化活性.因此,金的沉积对活性的促进作用非常明显.该简易Au/Nb2O5催化剂将金催化剂的类型扩展到酸性载体,这将增加新的应用.     

光致热效应促进的全光谱光催化CO2还原

以半导体等为催化剂,在太阳能作用下将CO2和H2O转化为可再生燃料与氧气的“人工光合作用”有望同时解决目前面临的严峻能源和环境问题,因而备受关注.但半导体催化剂光谱响应范围较窄、表面反应动力学缓慢,从而导致目前仍无法获得可观的太阳能-燃料转换效率.已有很多研究采用了晶面调控、元素掺杂和异质结构建等方法,以提高半导体光催化剂的太阳能-燃料转换效率,但效果仍不令人满意,主要原因是半导体光催化剂很难在吸收带边-氧化还原能力和活性-稳定性这两种关系中取得较好的平衡.此外,光催化反应中的动力学也是主要问题之一,尤其在人工光合作用反应中,CO2还原半反应和H2O氧化半反应的动力学均较困难, 这已成为共识, 而解决这个问题, 将有助于我们从一新的角度理解光催化过程, 从而提升光催化反应性能.本文以Au NP/金红石为模型催化剂, 纯金红石为参照, 证明了存在太阳光中的红外光致热和可见光诱导的等离激元热效应等两类光致热效应, 它们均可以促进人工光合作用反应. 研究发现, 人工光合作用反应与其他许多化学反应一样, 表观活化能为正, 从而表明动力学因素在该反应中起着重要作用. 此外, 根据不同反应温度下的结果, 通过计算Au NP/金红石和纯金红石上生成CO和CH4的表观活化能, 发现在这二种样品上CH4的表观活化能均高于CO, 这就从动力学上解释了热力学上更容易得到的CH4在绝大多光催化CO2还原反应中的产率均低于CO. 此外, 无论是对于CO还是CH4, Au NP/金红石的催化表观活化能均低于纯金红石的. 因此, 本文从实验上提供了贵金属纳米粒子改善人工光合作用动力学的实验证据,并从动力学角度解释了人工光合作用反应中的活性和选择性问题. 本研究证明了动力学因素在光催化反应, 尤其是人工光合作用反应中的重要性, 并提出了从动力学角度提升人工光合作用反应的新方法, 即利用太阳光的光致热效应加速反应, 这不仅有助于提升太阳能转化效率, 也有望减少反应设备成本, 从而促进其大规模应用.     

Highly efficient asymmetric epoxidation of alkenes with a D(4)-symmetric chiral dichlororuthenium(IV) porphyrin catalyst.

A dichlororuthenium(IV) complex of 5,10,15,20-tetrakis[(1S,4R,5R,8S)-1,2,3,4,5,6,7,8-octahydro-1,2:5,8-dimethanoanthrance-9-yl]porphyrin, [Ru(IV)(D(4)-Por)Cl(2)] (1), was prepared by heating [Ru(II)(D(4)-Por)(CO)(MeOH)] (2) in refluxing CCl(4). Complex 1 is characterized by (1)H NMR (paramagnetically shifted pyrrolic protons at delta(H) = -52.3 ppm), FAB-mass spectroscopies, and magnetic susceptibility measurement (mu(eff) = 3.1 mu(B)). The ruthenium complex exhibits remarkable catalytic activity toward enantioselective alkene epoxidation using 2,6-dichloropyridine N-oxide (Cl(2)pyNO) as terminal oxidant. The Ru(IV)-catalyzed styrene epoxidation is achieved within 2 h (versus 48 h for the 2-catalyzed reaction), and optically active styrene oxide was obtained in 69% ee and 84% yield (875 turnovers). Likewise, substituted styrenes and some conjugated cis-disubstituted alkenes (e.g., cis-beta-methylstyrene, cis-1-phenyl-3-penten-1-yne, 1,2-dihydronaphthalene, and 2,2-dimethylchromenes) are converted effectively to their organic epoxides in 50-80% ee under the Ru(IV)-catalyzed conditions, and more than 850 turnovers of epoxides have been attained. When subjecting 1 to four repetitive uses by recharging the reaction mixture with Cl(2)pyNO and styrene, styrene oxide was obtained in a total of 2190 turnovers and 69% ee. UV-vis and ESI-mass spectral analysis of the final reaction mixture revealed that a ruthenium-carbonyl species could have been formed during the catalytic reaction, leading to the apparent catalyst deactivation. We prepared a heterogeneous chiral ruthenium porphyrin catalyst by immobilizing 1 into sol-gel matrix. The heterogeneous catalyst is highly active toward asymmetric styrene epoxidation producing styrene oxide in 69% ee with up to 10,800 turnovers being achieved. The loss of activity of the Ru/sol-gel catalyst is ascribed to catalyst leaching and/or deactivation. On the basis of Hammett correlation (rho(+) = -1.62, R = 0.99) and product analysis, a dioxoruthenium(VI) porphyrin intermediate is not favored.     

Carbon Monoxide Oxidation by Polyoxometalate‐Supported Gold Nanoparticulate Catalysts: Activity,Stability, and Temperature‐ Dependent Activation Properties

Nanoparticulate gold supported on a Keggin‐type polyoxometalate (POM), Cs₄[α‐SiW₁₂O₄₀]⋅n H₂O, was prepared by the sol immobilization method. The size of the gold nanoparticles (NPs) was approximately 2 nm, which was almost the same as the size of the gold colloid precursor. Deposition of gold NPs smaller than 2 nm onto POM (Au/POM) was essential for a high catalytic activity for CO oxidation. The temperature for 50 % CO conversion was −67 °C. The catalyst showed extremely high stability for at least one month at 0 °C with full conversion. The catalytic activity and the reaction mechanism drastically changed at temperatures higher than 40 °C, showing a unique behavior called a U‐shaped curve. It was revealed by IR measurement that Au^δ+ was a CO adsorption site and that adsorbed water promoted CO oxidation for the Au/POM catalyst. This is the first report on CO oxidation utilizing Au/POMs catalysts, and there is a potential for expansion to various gas‐phase reactions.     

Carbon Monoxide Oxidation by Polyoxometalate‐Supported Gold Nanoparticulate Catalysts: Activity,Stability, and Temperature‐ Dependent Activation Properties

Nanoparticulate gold supported on a Keggin‐type polyoxometalate (POM), Cs₄[α‐SiW₁₂O₄₀]?n H₂O, was prepared by the sol immobilization method. The size of the gold nanoparticles (NPs) was approximately 2 nm, which was almost the same as the size of the gold colloid precursor. Deposition of gold NPs smaller than 2 nm onto POM (Au/POM) was essential for a high catalytic activity for CO oxidation. The temperature for 50 % CO conversion was ?67 °C. The catalyst showed extremely high stability for at least one month at 0 °C with full conversion. The catalytic activity and the reaction mechanism drastically changed at temperatures higher than 40 °C, showing a unique behavior called a U‐shaped curve. It was revealed by IR measurement that Au^δ+ was a CO adsorption site and that adsorbed water promoted CO oxidation for the Au/POM catalyst. This is the first report on CO oxidation utilizing Au/POMs catalysts, and there is a potential for expansion to various gas‐phase reactions.     

Synthesis of hollow and nanoporous gold/platinum alloy nanoparticles and their electrocatalytic activity for formic acid oxidation

In this work, hollow Au/Pt alloy nanoparticles (NPs) with porous surfaces were synthesized in a two-step procedure. In the first step, tri-component Ag/Au/Pt alloy NPs were synthesized through the galvanic replacement reaction between Ag NPs and aqueous solutions containing a mixture of HAuCl₄ and H₂PtCl₄. In the second step, the Ag component was selectively dealloyed with nitric acid (HNO₃), resulting in hollow di-component Au/Pt alloy NPs with a porous surface morphology. The atomic ratio of Au to Pt in the NPs was easily tunable by controlling the molar ratio of the precursor solution (HAuCl₄ and H₂PtCl₆). Hollow, porous Au/Pt alloy NPs showed enhanced catalytic activity toward formic acid electrooxidation compared to the analogous pure Pt NPs. This improved activity can be attributable to the suppression of CO poisoning via the “ensemble” effect.     

Activation of Au/TiO2 catalyst for CO oxidation

Changes in a Au/TiO(2) catalyst during the activation process from an as-prepared state, consisting of supported AuO(x)(OH)(4-2x)(-) species, were monitored with X-ray absorption spectroscopy and FTIR spectroscopy, complemented with XPS, microcalorimetry, and TEM characterization. When the catalyst was activated with H(2) pulses at 298 K, there was an induction period when little changes were detected. This was followed by a period of increasing rate of reduction of Au(3+) to Au(0), before the reduction rate decreased until the sample was fully reduced. A similar trend in the activation process was observed if CO pulses at 273 K or a steady flow of CO at about 240 K was used to activate the sample. With both activation procedures, the CO oxidation activity of the catalyst at 195 K increased with the degree of reduction up to 70% reduction, and decreased slightly beyond 80% reduction. The results were consistent with metallic Au being necessary for catalytic activity.     

Identifying the active photocatalytic H2-production sites on TiO2-supported Pt nanoparticles by the in-situ infrared spectrum of CO

Identifying the active catalytic centers on catalyst surface is significant for exploring the catalytic reaction mechanism and further guiding the synthesis of high-performance catalysts.However,it remains a challange in developing the site-specific technology for the identification of the active catalytic centers.Herein,in-situ infrared spectroscopy of adsorbed CO,photocatalytic hydrogen evolution reaction(HER) test and theoretical simulation were used to distinguish and quantify the different surface sites and their H2-production catalytic activity on TiO_2-supported Pt nanoparticles(Pt NPs).Two different types of surface Pt sites,tip Pt(Pt_(tip)) and edge/terrace Pt_(edge/terrace),on TiO_2-supported Pt nanoparticles(Pt NPs) were identified.The photocatalytic H2-production activity of TiO_2-supported Pt NPs shows a linear functional relationship with the number of Pt_(tip) sites.However,the number of Pt_(edge/terracesites) produced little effect on the activity of TiO_2-supported Pt NPs.First-principle simulations confirmed that H2-evolution at the Pttipsites owns a lower energy barrier than that at Pt_(edge/terrace).This findings would be helpful for the fabrication of high-performance Pt catalysts.     

A study of [Co2(alkyne)(binap)(CO)4] complexes (BINAP=(1,1'-binaphthalene)-2,2'-diylbis(diphenylphosphine))

Understanding the interaction of chiral ligands, alkynes, and alkenes with cobaltcarbonyl sources is critical to learning more about the mechanism of the catalytic, asymmetric Pauson-Khand reaction. We have successfully characterized complexes of the type [Co2(alkyne)(binap)(CO)4] (BINAP=(1,1'-binaphthalene)-2,2'-diylbis(diphenylphosphine)) and shown that diastereomer interconversion occurs under Pauson-Khand reaction conditions when alkyne=HC[triple bond]CCO2Me. Attempts to isolate [Co2(alkyne)(binap)(CO)x] complexes with coordinated alkenes led to the formation of cobaltacyclopentadiene species.     

Cryogenic CO oxidation on TiO(2)-supported gold nanoclusters precovered with atomic oxygen

Bulk gold has long been regarded as a noble metal, having very low chemical and catalytic activity. However, metal oxide-supported gold particles, particularly those that are less than 5 nm in diameter, have been found to have remarkable catalytic properties. In this study we show that impinging gas-phase CO molecules react readily with oxygen adatoms preadsorbed on Au/TiO(2)(110) to produce CO(2) even under conditions in which the sample is cryogenically cooled. Gold particle size seems to have little effect on the CO oxidation reaction when oxygen adatoms are preadsorbed. We also show that as the oxygen adatom coverage increases, the rate of CO oxidation decreases on Au/TiO(2) at cryogenic temperatures.     

Novel deoxygenation reaction of epoxides by indium

[reaction: see text] A novel, mild, ecofriendly protocol for the deoxygenation of epoxides to alkenes using indium metal and indium(I) chloride or ammonium chloride in alcohol has been developed. It was necessary for the presence of good radical-stabilizing groups adjacent to the oxirane ring for the deoxygenation reaction to occur. It is proposed that this reaction occurs through an SET process with indium as an electron donor.     

Au/Ag2O与Ag掺杂的Au粉催化剂上CO氧化反应：Au-Ag双金属催化剂活性位

有关用于各种氧化反应中Au-Ag双金属催化剂存在显著协同效应的来源有两种观点：(1) AgOx块与体相Au表面的接触界面起重要作用,体相Au的表面是催化活性位;(2) Au-Ag双金属催化剂中形成的Au-Ag合金中电荷从Ag转移到Au上,可能对催化剂活性起作用。因此,确定Au表面上Ag是以氧化物还是以金属合金形式存在可能是深度理解该协同效应的关键。
　　为了检测和验证催化剂活性的增加是由于Ag2O与Au纳米粒子的紧密接触,在密闭循环反应体系中比较研究了Au/Ag2O和Ag2O催化剂上CO氧化反应。将CO/O2摩尔比为2的混合气通入到这二个催化剂上来跟踪压力降低的速率。因而检测了气体的消耗量和CO2的生成量。结果发现,在稳态下Au/Ag2O和Ag2O催化剂的压力降低的速率不存在差别。这两个催化剂上压力的降低是由于Ag2O中表面晶格氧被混合气中CO的还原所致。 Au/Ag2O催化剂上得到的结果与以前研究的具有氧化表面的Ag掺杂的Au粉末(Ag/Au-b)上的一致,也表明AgOx块与体相Au表面界面周边不大可能是CO氧化反应催化活性位。基于具有稳态表面的Ag/Au-b样品上的研究结果,我们认为AgOx物种被还原为0价态Ag而形成的Ag-Au合金很可能是催化活性位。     

Room-temperature regioselective C-H/olefin coupling of aromatic ketones using an activated ruthenium catalyst with a carbonyl ligand and structural elucidation of key intermediates

Mechanistic studies of the ruthenium-catalyzed reaction of aromatic ketones with olefins are presented. Treatment of the original catalyst, RuH(2)(CO)(PPh(3))(3), with trimethylvinylsilane at 90 °C for 1-1.5 h afforded an activated ruthenium catalyst, Ru(o-C(6)H(4)PPh(2))(H)(CO)(PPh(3))(2), as a mixture of four geometric isomers. The activated complex showed high catalytic activity for C-H/olefin coupling, and the reaction of 2'-methylacetophenone with trimethylvinylsilane at room temperature for 48 h gave the corresponding ortho-alkylation product in 99% isolated yield. The activated catalyst was thermally robust and showed excellent catalytic activity under refluxing toluene conditions. (1)H and (31)P NMR studies of the C-H/olefin coupling at room temperature suggested that an ortho-ruthenated complex, P,P'-cis-C,H-cis-Ru(2'-(6'-MeC(6)H(4)C(O)Me))(H)(CO)(PPh(3))(2), participated in the reaction as a key intermediate. Isotope labeling studies using acetophenone-d(5) indicated that the rate-limiting step was the C-C bond formation, not the C-H bond cleavage, and that each step prior to the reductive elimination was reversible. The rate of C-H/olefin coupling was found to exhibit pseudo first-order kinetics and to show first-order dependence on the ruthenium complex concentration.     

用辛烷基硫醇单层保护Au纳米粒子制备CO氧化催化剂Au/γ-Al2O3

采用两相法合成出含活性组分Au的辛烷基硫醇单层保护Au纳米粒子(C8AuNPs)的正己烷溶胶, 用“逐次浸润”法将C8AuNPs负载在γ-Al2O3上, 经真空干燥及活化处理制得Au/γ-Al2O3催化剂. 所制得的Au催化剂前体C8AuNPs/γ-Al2O3表面Au粒子平均粒径可控制在2-3 nm范围内, 且分布比较单一; 催化剂活性评价600 h后, 其表面Au的粒径仍主要分布在2-4 nm范围内; 真空干燥温度影响Au催化剂的粒子尺寸和催化活性, 随着真空干燥温度的提高, Au纳米粒子的粒径增大. 将所制备的催化剂用于低温CO氧化反应, 催化活性评价结果表明, 经25 ℃真空干燥制得的2.5%(质量分数, w)Au/γ-Al2O3具有较高的活性和长期稳定性, 其催化CO完全转化的最低温度为-19 ℃, 在15 ℃下CO完全转化时Au/γ-Al2O3的单程寿命至少900 h; 4.0%(w) Au/γ-Al2O3在15 ℃和进料中含水条件下对CO完全氧化的单程寿命不低于2000 h, 可见催化剂具有强的抗潮湿中毒特性. 综合上述实验结果, 讨论了影响Au/γ-Al2O3催化剂活性的可能因素.     

金属载体强相互作用增强Au/TiO2催化剂在3-硝基苯乙烯选择性加氢反应的活性

自Haruta与Hutchings于上世纪八十年代末发现金纳米催化剂优异的反应活性以来,科研人员对金催化的应用领域进行了广泛而深入地研究.对金催化科学和应用领域的研究一直在进行.大量的研究表明,金催化剂在各种选择性氧化反应中具有优异的催化性能(高活性和高选择性).然而,在催化加氢反应中,尽管金催化剂相比于铂族金属显示出优越的选择性,但是由于金催化剂选择性加氢反应的活性较差,使其在选择性催化加氢反应中的应用受到了极大的限制.研究表明,金催化剂较弱的活化氢气能力是其催化加氢反应活性低的主要原因.研究发现,氢气活化的活性中心可能是界面、负价金、低配位的金原子等.金催化剂具有明显的载体效应,金属-载体之间的相互作用能够显著地改变金催化剂的催化性能.Tauster等研究发现,铂族金属与还原性载体之间存在强相互作用,能够引发载体包覆金属表面,并且使得电子从载体向金属迁移,导致金属带负电.受金属-载体强相互作用(SMSI)效应的启发,本文探究了Au/TiO2催化剂中SMSI对金催化剂加氢性能的影响.在H2或O2气氛下高温焙烧Au/TiO2,获得一系列金催化剂(Au/TiO2-TA,T为焙烧温度(oC):300、400、500和600;A为气氛:H2或O2).对比在3-硝基苯乙烯(3-NS)选择性加氢反应中的活性发现,Au/TiO2-500H的TOF值是Au/TiO2-500O的3.3倍;动力学测试表明,Au/TiO2-500H和Au/TiO2-500O的反应表观活化能分别为79.5和105.1 kJ/mol.这表明两类催化剂催化活性中心的结构存在差异.X射线光电子能谱测试结果表明,Au/TiO2-H样品中Au带部分负电,而Au/TiO2-O中Au显示为金属态.HAADF-STEM和EELS显示,Au/TiO2-H中Au NPs的表面有TiOx物种,增加了Au-TiO2的界面.EPR结果表明,Au/TiO2-H中存在表面Ti3+物种,而Au/TiO2-O样品中则没有.为确认加氢反应的活性中心到底是界面还是负价金物种,本文探究了不同温度下氢气处理的Au/TiO2的结构与性能的关系,发现Au/TiO2-300H/400H/500H催化剂都显示出较好的催化3-NS加氢活性,而Au/TiO2-600H虽然具有更多的负价金物种,但是3-NS选择性加氢反应的活性反而降低,因此,负价金不是活性中心.这是因为不同温度处理的Au/TiO2-H样品中,SMSI的强弱不同,在300、400、500 oC下,SMSI能够增加Au-TiO2的界面长度,从而增强了3-NS加氢反应的活性;而温度达到600 oC,SMSI效应太强,Au NPs被包覆更密实,导致Au/TiO2-600H的3-NS选择性加氢反应的活性下降.密度泛函理论计算表明,Au/TiO2-H样品具有更低的H2解离活化能以及氢转移活化能.氢氘交换反应也进一步验证了SMSI有利于H2的活化.     

纳米Pd和Au催化CO2还原粒径效应的密度泛函理论计算研究

以可再生能源为能量来源,在水溶液中进行的光(电)催化CO₂还原生成高附加值化学品和燃料是解决能源危机与环境污染的有效途径之一.CO是一种简单却很重要的CO₂还原产物,它可以作为水煤气变换反应与费托合成的重要原料.具有较高CO选择性的贵金属纳米颗粒催化剂(如Au和Pd)一直受到研究者的广泛关注.一般来说,金属颗粒催化剂的催化性能与粒径大小密切相关,即所谓的粒径效应.然而在实际的理论计算研究中,由于受到计算能力的限制,催化剂模型都仅局限于简单的周期性模型或小的金属团簇模型,无法准确描述真实颗粒上复杂的反应位点的性质,导致了对催化行为的误解.因此,建立更加真实的颗粒模型对探究纳米颗粒催化剂上活性位点的性质,解释其粒径效应至关重要.本文旨在阐述Au与Pd纳米颗粒催化剂不同活性位点上CO₂还原反应与产H2副反应的竞争机制,并解释Au与Pd纳米颗粒催化剂在CO₂电还原中表现出不同粒径效应的原因.本文基于密度泛函理论,采用VASP软件,BEEF-vdW泛函进行计算.分别建立了原子数为55,147,309和561的颗粒模型和高CO^*覆盖度模型,避免了传统周期性模型的局限性,探究了金属颗粒催化剂不同反应位点上的CO选择性.结果表明,对于颗粒模型来说,(100)位点对CO的选择性优于边缘位点;但对于周期性模型来说,Au(211)对CO的选择性则优于Au(100).产生这种反差的主要原因在于Au颗粒的边缘位点对H*的吸附过强.通过对比,我们直观地展现了颗粒模型上平面位点和Edge位点与相对应的周期性模型上CO选择性的区别,突出了模型选择对揭示活性位点性质的重要性.在此基础上,通过计算理论CO法拉第效率,发现Au颗粒随着粒径的减小,CO选择性降低,与实验的趋势一致.对于Pd催化剂来说,低覆盖度模型无法正确预测活性位点的性质;而高CO覆盖度的情况下,Pd颗粒的边缘位点对COOH^*吸附能更强,这是导致边缘位点上CO选择性更高的主要原因.同样通过计算理论CO法拉第效率,发现随着粒径的减小,Pd颗粒上CO选择性升高.本文不仅成功揭示了Au与Pd颗粒催化剂上活性位点的性质,对粒径效应做出了合理解释,也强调了合理的计算模型是理论研究的基础.