Mo的引入方式对CeO2脱硝性能的影响

固定源排放的氮氧化物(NOx)导致了严重的环境污染问题,NH3选择性催化还原(NH3-SCR)被认为是目前控制NOx排放的最有效技术,已广泛应用于电力行业的烟气排放治理.然而,我国非电行业的NOx减排仍然面临着重大挑战,因为其排放的废气温度通常低于300oC,且含有一定量的SO2,传统的钒基SCR催化剂因活性温度(300～400oC)较高而无法有效发挥作用.因此,亟待开发新型的高效低温SCR催化剂.铈基催化剂由于氧化铈(CeO2)的优异储氧能力(OSC)和良好的氧化还原能力而显示出较好的低温(80～300oC)脱硝性能,如Mn-Ce,W-Ce,Ta-Ce,Cu-Ce和Nb-Ce等.但这些铈基催化剂易被烟气中的SO2毒化而导致催化活性降低.因此,提高铈基SCR催化剂抗硫中毒能力是其产业化应用的关键.已有研究发现,通过构筑结构保护层或添加另一种金属来保护活性组分是提高SCR催化剂抗硫性能的一种可行策略.氧化钼(MoO3)通常被用做传统V2O5/TiO2催化剂的促进剂以提高其水热稳定性和表面酸性.研究表明,在V/Ti催化剂中引入钼物种不仅可以提高其SCR活性,而且提高了V/Ti催化剂的抗SO2性能,这是由于VMo/Ti表面较少的V–O–V键削弱了对SO2的氧化作用.Tang等开发了一种Fe2O3/MoO3纳米片催化剂,显示出比纯Fe2O3更好的抗SO2能力,主要是由于层状结构的MoO3能阻止NH4+在硫酸氢铵中的沉积.目前关于Mo的引入方式即催化剂的制备方法对铈基催化剂物化性能和NH3-SCR催化性能(特别是抗SO2能力)的影响的研究还比较少.本文分别采用浸渍法和沉淀法在CeO2中引入钼物种,制备了Mo-CeO2和MoCe-cp催化剂来探究制备方法对MoCe催化剂的脱硝性能及抗SO2中毒能力的影响.结果表明,引入Mo可以显著地提高CeO2的低温脱硝性能,其中Mo-CeO2催化剂在150 oC即可达到80％以上的脱硝效率,同时抗SO2中毒性能也得到了显著提高.对催化剂结构、氧化还原能力、表面酸度和反应物分子的吸附脱附性质进行了表征,并与MoCe催化剂脱硝性能和抗硫性能相关联.结果表明,Mo-CeO2和MoCe-cp催化剂的物理化学性质和脱硝性能有明显区别.首先,Mo-CeO2中的钼物种主要存在于CeO2表面,而MoCe-cp中的钼物种主要存在于CeO2体相,其为Mo-CeO2表面带来大量的Br?nsted酸位并抑制了硝酸盐的吸附,促使NH3-SCR反应按照Eley-Rideal机理进行,进而表现出优于MoCe-cp的低温活性.其次,Mo-CeO2表面更多的Mo物种抑制了SO2的吸附,从而使Mo-CeO2表现出更好的抗SO2性能.本文为具有实际应用前景的铈基NH3-SCR催化剂的设计提供了参考.     

金团簇二十面体结构融合过程中其催化活性的演变

近年来,由有机配体保护的原子精确金属团簇在合成方面已取得了重要进展,其独特的原子结构对一些化学反应产生独特的催化效果.原子精确的团簇催化剂明显不同于纳米颗粒催化剂和单原子催化剂,是一种关联均相和多相的、原子数目确定、尺寸均一、结构精确的新型催化剂.从原子尺度上精确构筑团簇催化剂,探究亚纳米尺度的微观结构对催化性能的影响,为常规催化剂所未能解决的关键科学问题提供解决的机会,为在分子尺度上揭示催化作用机制以及准确关联催化剂结构与催化性能提供新的研究体系,具有重要的科学研究意义.本文设计和使用了三种结构精确的金团簇催化剂,即Au25(PPh3)10(SC2H4Ph)5Cl2,Au38(SC2H4Ph)24和Au25(SC2H4Ph)18,分别由二十面体结构的Au13单元通过中心顶点融合、面融合、体相融合形成的(简写为Auvf、Auff和Aubf),详细研究了这三个金团簇催化剂在二十面体Au13单元的结构融合过程中,其催化活性的演变规律.在催化吡咯烷与O2反应制备γ-丁内酰胺反应中,金团簇催化剂的催化活性顺序为Aubf>Auff>Auvf,表明这三个金团簇中Au13单元的结构随着点、面、体的融合,其催化活性随之增加.同时研究发现,对于同一个Au团簇催化剂,其表面硫醇配体的烷基链越短,其催化活性越高,这主要是由于短链硫醇分子的空间位阻较小,吡咯烷分子更容易进入催化剂的金表面,接触到活性位点,进行催化反应.实验表明,三个团簇金原子均带正电荷,正价金物种可能是催化吡咯烷与O2反应的催化活化物种.研究发现,Aubf团簇表面的活性位数目高于Auff和Auvf团簇的,因此Aubf的催化活性最高;同时,团簇表面配体的烷基链越短,其表面活性位数目也越多,这也进一步解释了表面硫醇配体的烷基链越短,其相应的金团簇催化剂的催化活性越高的原因.吡咯烷与O2在金团簇上反应的可能路径为O2在Au活性位上裂解的O原子和吡咯烷β-H转移至Au活性位的β-H反应脱水后形成亚胺,亚胺经过水解进一步氧化得到产物.这项研究将为在原子层次上调变金属团簇催化剂的结构进而改变其催化性能提供新的思路,对精准设计和构筑高效催化剂具有一定的科学指导意义.     

KIT-6负载CeO2催化CO2和甲醇合成碳酸二甲酯

采用不同老化温度(80、100、120和150℃)合成了一系列KIT-6载体,并通过浸渍法制备了相应的CeO_2/KIT-6催化剂。结合X射线衍射、N_2物理吸附、NH_3程序升温脱附、CO_2程序升温脱附、透射电子显微镜、傅里叶变换红外光谱和X射线光电子能谱等表征结果,详细考察了老化温度对KIT-6结构以及CeO_2/KIT-6催化剂直接催化CO_2和甲醇合成碳酸二甲酯(DMC)反应活性的影响。结果表明,不同老化温度下制备的KIT-6均保持其独特的三维孔道结构。随着老化温度升高,KIT-6比表面积先增大后减小,当老化温度为100℃时,KIT-6比表面积达到最大(683 m~2·g~(-1))。KIT-6较高的比表面积有利于提高CeO_2分散度,进而提高暴露的活性位点数量,催化活性随催化剂表面中等碱/酸性吸附位数量和Ce~(3+)含量的增加而逐渐提高。其中,CeO_2/100-KIT-6催化剂中CeO_2颗粒尺寸最小(5.9 nm),暴露的活性位数量最高,催化活性最佳。随后,考察了反应温度和压力对CeO_2/100-KIT-6催化活性的影响。随着反应温度提高,催化活性先升高后降低,当反应温度为140℃时,催化活性最高;且催化活性随反应压力的提高而逐渐增加。在反应温度为140℃、压力为6.8 MPa条件下,催化剂经6次循环后,DMC收率由15 mmol·g_(CeO_2)~(-1)逐渐降低至2.8 mmol·g_(CeO_2)~(-1),原因归结为反应过程中CeO_2纳米颗粒发生团聚,使暴露出的活性位数量减少。     

An Aluminophosphate Molecular Sieve with 36 Crystallographically Distinct Tetrahedral Sites

The structure of the new medium‐pore aluminophosphate molecular sieve PST‐6 is determined by the combined use of rotation electron diffraction tomography, synchrotron X‐ray powder diffraction, and computer modeling. PST‐6 was prepared by calcination of another new aluminophosphate material with an unknown structure synthesized using diethylamine as a structure‐directing agent, which is thought to contain bridging hydroxy groups. PST‐6 has 36 crystallographically distinct tetrahedral sites in the asymmetric unit and is thus crystallographically the most complex zeolitic structure ever solved.     

Counting of Oxygen Defects versus Metal Surface Sites in Methanol Synthesis Catalysts by Different Probe Molecules

Different surface sites of solid catalysts are usually quantified by dedicated chemisorption techniques from the adsorption capacity of probe molecules, assuming they specifically react with unique sites. In case of methanol synthesis catalysts, the Cu surface area is one of the crucial parameters in catalyst design and was for over 25 years commonly determined using diluted N₂O. To disentangle the influence of the catalyst components, different model catalysts were prepared and characterized using N₂O, temperature programmed desorption of H₂, and kinetic experiments. The presence of ZnO dramatically influences the N₂O measurements. This effect can be explained by the presence of oxygen defect sites that are generated at the Cu‐ZnO interface and can be used to easily quantify the intensity of Cu‐Zn interaction. N₂O in fact probes the Cu surface plus the oxygen vacancies, whereas the exposed Cu surface area can be accurately determined by H₂.     

过渡金属/氮掺杂石墨的制备及电催化氧还原

用简单的化学方法制备了过渡金属(TM)壳聚糖水杨醛席夫碱配合物,然后以此配合物为金属源和N源、以硝酸预处理石墨为载体,经热处理后制备了过渡金属/氮掺杂石墨催化剂TM-N-C-t(TM=Co,Ni,Cu;t=200,400,600,800,1 000℃).以此催化剂为修饰剂制备了玻碳修饰电极,并用循环伏安法(CV)和旋转圆盘电极(RDE)伏安法研究了催化剂TM-N-C-t的电化学行为和电催化氧还原(ORR)的催化性能,催化剂的组成和结构采用TG,FT-IR,XRD,XPS等技术进行了表征.研究结果表明,催化剂TM-N-C-t对ORR均显示不同程度的催化活性,其中以1 000℃热处理的钴基催化剂Co-N-C-1000的催化活性最好,其活性已接近相同条件下的商用催化剂JM 20%Pt/C,催化活性位主要为Co—N—C.根据扩散控制的不可逆反应的循环伏安行为,计算得到了TM-N-C-t催化剂电催化ORR的动力学参数,并以此提出了氧还原催化反应的机理,在活性最好的催化剂Co-N-C-1000修饰电极上,氧气以4e转移途径被还原为水.     

Effects of acid etching on the structure of PtNi catalyst and total exposed active sites

The integration technology of hydrogen preparation–hydrogen storage not only can utilize hydrogen energy efficiently but also can improve the selectivity of the electrode maximally. In the present work, the structure and composition of the PtNi catalyst was characterized by X-ray diffraction (XRD); and its electrochemical properties, morphology, and surface binding energy were analyzed by cyclic voltammetry (CV) and linear scanning voltammetry (LSV), scanning electron microscopy equipped with energy-dispersive spectrometry (SEM-EDS), and X-ray photoelectron spectroscopy (XPS), respectively. The effects of different acid etching treatments (e.g., etching time, etchant concentration, and etching temperature) on the structure and surface active sites were investigated by the orthogonal experiment. The experimental results reveal that after etching with 0.5 mol/L of perchloric acid for 0.5 h at 60°C, the electrode weight loss of the PtNi catalyst is mainly attributed to the large loss of Ni atoms in film layer. This results in the reduced alloy phase in film layer and the appearance of Pt characteristic diffraction peak. The relative content of Pt on the surface of the film electrode increases significantly, and the total number of active sites also increases correspondingly. The binding energy of Pt4f_7/2 decreases by 0.19 eV, and the number of active sites involved in hydrogen release decreases, indicative of the reduced promotion effect of the PtNi catalyst on hydrogen release.     

Dual Metal Active Sites in an Ir1/FeOx Single-Atom Catalyst: A Redox Mechanism for the Water-Gas Shift Reaction

Herein, we report a theoretical and experimental study of the water-gas shift (WGS) reaction on Ir₁/FeO_x single-atom catalysts. Water dissociates to OH* on the Ir₁ single atom and H* on the first-neighbour O atom bonded with a Fe site. The adsorbed CO on Ir₁ reacts with another adjacent O atom to produce CO₂, yielding an oxygen vacancy (O_vac). Then, the formation of H₂ becomes feasible due to migration of H from adsorbed OH* toward Ir₁ and its subsequent reaction with another H*. The interaction of Ir₁ and the second-neighbouring Fe species demonstrates a new WGS pathway featured by electron transfer at the active site from Fe³⁺−O⋅⋅⋅Ir²⁺−O_vac to Fe²⁺−O_vac⋅⋅⋅Ir³⁺−O with the involvement of O_vac. The redox mechanism for WGS reaction through a dual metal active site (DMAS) is different from the conventional associative mechanism with the formation of formate or carboxyl intermediates. The proposed new reaction mechanism is corroborated by the experimental results with Ir₁/FeO_x for sequential production of CO₂ and H₂.     

Pt/CexZr1-xO2催化剂上丙烷完全氧化性能研究

采用沉淀法制备了ZrO2,CeO2和Ce0.7Zr0.3O2载体,并用浸渍法制备负载型Pt催化剂。考察了500和900℃焙烧催化剂的丙烷完全氧化性能和水汽对丙烷氧化反应的影响。对于500℃焙烧的催化剂,催化剂的丙烷氧化活性顺序为:Pt/ZrO2-500>Pt/CeO2-500>Pt/Ce0.7Zr0.3O2-500;而经900℃焙烧的催化剂活性顺序为:Pt/ZrO2-900>Pt/Ce0.7Zr0.3O2-900>Pt/CeO2-900。反应气氛中水汽的存在对两种Pt/ZrO2催化剂的活性均有抑制作用(T50温度均提高了10~15℃);而对于Pt/CeO2-500催化剂有抑制作用(T50温度提高10℃),但对Pt/CeO2-900催化剂活性有促进作用(T50温度下降25℃);对于两种Pt/Ce0.7Zr0.3O2催化剂活性具有促进作用(T50温度均下降5~25℃)。表征结果表明催化剂的活性与其表面Pt物种价态密切相关,催化剂表面上Pt0物种有利于活性的提高。Pt/Ce0.7Zr0.3O2-500催化剂中只含有氧化态Pt物种(Pt^2+),而Pt/Ce0.7Zr0.3O2-900催化剂中则含有部分金属态Pt物种,因此其活性高于Pt/Ce0.7Zr0.3O2-500催化剂。