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SnCl_(2)促进的Pt1/PS-PPh_(2)催化剂高选择性催化高碳烯烃氢甲酰化反应
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作者 虞周楠 张磊磊 +7 位作者 谈源龙 井日峥 曹宏晨 楼才溢 格日乐 王军虎 王爱琴 张涛 《Chinese Journal of Catalysis》 SCIE CAS CSCD 2024年第5期316-326,共11页
氢甲酰化作为工业上制备醛、醇等含氧化合物的重要反应,广泛应用于制备洗涤剂、增塑剂、表面活性剂和香料等.目前,氢甲酰化反应主要使用HCo(CO)_(4),HCo(CO)_(3)(PR_(3))和HRh(CO)(PPh_(3))_(2)等配合物作为催化剂.尽管Co基催化剂可以... 氢甲酰化作为工业上制备醛、醇等含氧化合物的重要反应,广泛应用于制备洗涤剂、增塑剂、表面活性剂和香料等.目前,氢甲酰化反应主要使用HCo(CO)_(4),HCo(CO)_(3)(PR_(3))和HRh(CO)(PPh_(3))_(2)等配合物作为催化剂.尽管Co基催化剂可以将高碳烯烃、内烯烃以及支链烯烃高选择性地转化为直链醛,但其反应条件(5-30 MPa,140-200℃)较苛刻,且容易发生烯烃加氢等副反应.相比之下,Rh催化剂的活性比Co基催化剂高1-2个数量级,且反应条件较为温和.但Rh储量稀少,价格昂贵,而且对于高碳烯烃氢甲酰化反应,Rh催化剂难以分离和循环使用.因此,研究者开展了其他金属催化剂的研究,其中Pt-Sn催化剂因其出色的区域选择性而备受关注.但目前Pt-Sn催化剂多局限于均相催化体系,而且Sn助剂的作用尚不明确.本文采用商业化三苯基膦嫁接的聚苯乙烯小球为载体,通过浸渍法制备了SnCl_(2)-Pt_(1)/PS-PPh_(2)单原子催化剂,考察了其在长链-烯烃氢甲酰化反应中的催化性能,并研究了Sn的促进作用.首先,以1-己烯氢甲酰化为探针反应,对催化剂的组成以及反应条件进行了优化.当Pt/P/Sn=1/2/5时,催化剂表现出最高的催化活性,在90-120℃和4-6 MPa合成气条件下,催化剂转化频率(TOF)为40 h^(-1),产物醛的正异比>42.随后,考察了催化剂的底物适用性.结果表明,C6-C12的高碳烯烃均可被高选择性地转化为相应的醛(正异比>20).然而,在循环使用实验中,由于SnCl_(2)不能稳定锚定在载体上,第二次循环时催化活性降低.但通过补加SnCl_(2),催化活性可以完全恢复.高压热过滤实验及元素检测结果表明,反应过程中Pt没有流失.X射线吸收光谱(XAFS)表征结果表明,反应后Pt仍以单原子形式存在,说明Pt1/PS-PPh_(2)具有良好的稳定性.通过准原位X-射线吸收谱、Mössbauer谱和红外光谱表征对反应过程中Pt和Sn的电子性质和配位结构进行了研究.结果表明,SnCl_(2)在反应过程中逐渐转化为Sn(dioxane)Cl3-物种(1,4-二氧六环为反应溶剂),并与Pt原子形成Pt-Sn键.当反应体系中没有Sn时,Pt(II)会被合成气过度还原并发生团聚.当没有膦配体时,Pt原子也会发生聚集,而且SnCl_(2)会在Pt(II)的催化作用下发生水解生成SnO.因此Sn(dioxane)Cl3-与膦配体共同抑制了Pt(I)在反应过程中的还原与聚集.最后,通过XAFS表征深入研究了反应机理.分析结果表明,CO在催化剂上具有较强的吸附作用,而H_(2)则可能以异裂的方式在催化剂上被活化.据此提出可能的反应机理:首先,H_(2)在催化剂上活化先形成Pt-H物种;随后,烯烃插入Pt-H,形成Pt-烷基物种;接着,CO迁移并插入,生成Pt-酰基物种;最后,经过还原消除步骤,得到最终的产物醛.综上,本文制备了一种对高碳烯烃氢甲酰化反应具有良好催化性能的SnCl_(2)-Pt1/PS-PPh_(2)单原子催化剂,为低成本非Rh基催化剂的开发提供借鉴.同时,揭示了催化体系中Sn的促进作用,为通过Lewis酸来调控催化剂的性能提供了参考. 展开更多
关键词 氢甲酰化反应 铂-锡催化剂 高碳烯烃 区域选择性 单原子催化剂
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氧化还原驱动的高活性Pd/PdO表面界面促进低温甲烷燃烧
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作者 谈源龙 张亚峰 +10 位作者 高雅 马静远 赵晗 顾青青 苏杨 徐晓燕 王爱琴 杨冰 张国旭 刘晓艳 张涛 《Chinese Journal of Catalysis》 SCIE CAS CSCD 2024年第5期242-252,共11页
天然气汽车尾气中尚未充分燃烧的甲烷是一种典型的温室气体之一,其温室效应远超二氧化碳,达到后者的20倍以上.因此,减少甲烷的排放对于有效应对气候变化至关重要.目前,以Pd/Al_(2)O_(3)为基础催化剂的催化燃烧反应,已被证实为减少甲烷... 天然气汽车尾气中尚未充分燃烧的甲烷是一种典型的温室气体之一,其温室效应远超二氧化碳,达到后者的20倍以上.因此,减少甲烷的排放对于有效应对气候变化至关重要.目前,以Pd/Al_(2)O_(3)为基础催化剂的催化燃烧反应,已被证实为减少甲烷排放的最为切实可行的技术手段.深入了解钯基催化剂的活性结构不仅有助于合理设计高效的催化体系,还能在很大程度上减少贵金属钯的使用量.然而,在甲烷燃烧反应过程中,由于氧化还原气氛的复杂性,Pd金属的表面容易转变为不同结构,这增加了研究其活性结构的难度.此外,催化剂的制备方法、载体的性质、预处理的气氛以及温度等因素均会对Pd的价态和粒径效应产生影响,使得Pd基催化剂在甲烷燃烧反应中的活性结构至今仍存在争议.为了深入研究这一问题,本文选用商业化的纳米级γ-Al_(2)O_(3)作为载体,采用易于工业化应用的浸渍法制备了Pd/Al_(2)O_(3)催化剂,并研究其在低温(200-400℃)贫燃条件下的活性结构.球差电镜结果表明,催化剂中的Pd纳米颗粒在不同气氛中经800℃高温预处理后呈现出不同的结构特点.氦气处理后的催化剂中,Pd以完全金属态的形式存在;氧气处理后的催化剂中,Pd以PdO的形式存在;甲烷燃烧反应气处理后的催化剂中,PdO大颗粒上存在金属Pd小颗粒,呈现出“荔枝型”Pd/PdO结构.准原位X射线光电子能谱和原位X射线吸收谱等结果表明,“荔枝型”Pd/PdO结构是在甲烷燃烧反应中受氧化还原气氛诱导形成的.该独特的“荔枝型”Pd/PdO结构的催化剂在300℃甲烷燃烧反应中,表现出337.8μmol gPd^(-1) s^(-1)的反应速率,分别是纯金属Pd和PdO型催化剂反应速率的10.7倍和15.5倍.进一步研究表明,无论催化剂中Pd的初始状态为金属态或是氧化态,高活性的“荔枝型”Pd/PdO结构都可以在较低温度(500℃)的长时间(12 h)甲烷燃烧反应中缓慢生成.通过调节预处理气氛中甲烷与氧气的相对浓度,可以实现689.2μmol gPd-1 s^(-1)的反应速率,高于文献已报道的Pd基催化剂在相似反应条件下的活性.密度泛函理论计算结果表明,相对于金属Pd和PdO,甲烷在Pd/PdO界面处表现出最低(0.40 eV)的自由能势垒,这表明由于界面处金属Pd和PdO的协同作用,甲烷断裂第一个C-H键的解离活化过程更容易发生,从而解释了“荔枝型”Pd/PdO结构高催化活性的来源.综上,本文通过先进的球差电镜和原位光谱表征技术,为深入认识甲烷燃烧钯基催化剂活性结构提供了新的角度.研究发现,反应过程中因气氛诱导而生成的高活性结构可能是重要的活性中心,这一观点不仅有助于理解甲烷燃烧反应的机理,而且可以为其他氧化还原催化体系的研究以及工业催化剂的设计制备提供参考. 展开更多
关键词 原位表征 纳米颗粒 甲烷燃烧 界面
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乙炔选择加氢反应中碳化钯的动态精细调控: 气氛和氧化锌助剂的作用
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作者 陈欢 虞周楠 +8 位作者 杨冰 张亚峰 车春霞 刘晓艳 张峰 韩伟 温翯 王爱琴 张涛 《Chinese Journal of Catalysis》 SCIE CAS CSCD 2024年第5期190-200,共11页
碳化钯通常被认为是乙炔选择加氢反应中原位生成的活性相,其生成有助于抑制次表面非选择性的氢化钯物种,从而实现高选择性乙炔加氢制乙烯的目标.次表面上碳化钯和氢化钯物种之间的竞争很大程度上决定了乙炔加氢反应的选择性.然而,由于... 碳化钯通常被认为是乙炔选择加氢反应中原位生成的活性相,其生成有助于抑制次表面非选择性的氢化钯物种,从而实现高选择性乙炔加氢制乙烯的目标.次表面上碳化钯和氢化钯物种之间的竞争很大程度上决定了乙炔加氢反应的选择性.然而,由于实际反应环境的复杂性,反应环境下的两种物种之间的动态转化过程和竞争关系尚不清晰.特别是,反应环境(比如氢气组分)对碳化钯物种的调控机制仍不明确,也使得对碳化钯活性物种的精准调控变得困难.此外,氧化锌助剂作为乙炔选择加氢反应中最常用的助剂之一,存在典型的金属-氧化物界面相互作用,也会对渗碳过程产生重要影响.因此,从动态视角理解碳化钯物种的原位形成过程,对于精准设计和合成高性能乙炔选择加氢钯基催化剂具有重要的科学意义.近年来,先进原位表征光谱技术的不断发展使得从原子、分子层面理解原位过程机制成为可能.本文旨在通过先进的原位表征技术揭示乙炔选择加氢反应中碳化钯物种的动态生成过程,并进一步探究气氛环境、温度、助催化剂等参数对碳化钯物种的动态调控机制,从而为高性能乙炔选择加氢催化剂的精准设计和合成提供有力支撑.原位研究结果表明,在氢气升温还原条件下,空气焙烧后新鲜催化剂中氧化钯相首先转变为氢化钯相;随着还原温度升高,氢化钯相的含氢量逐渐降低.当切换至乙炔选择加氢反应原料气时,氢化钯相迅速分解为金属钯,并随着恒温碳化时间的延长,烃类裂解产生的碳原子逐渐渗入钯的体相,最终形成稳定的碳化钯活性相.通过移除乙炔加氢反应原料气氛中的氢气,考察了反应气中的氢气组分对碳化钯形成的调控机制.实验发现,在仅有乙炔和乙烯存在时,碳化过程仍能发生;而引入少量氢气(体积分数2.2%)后,碳化程度显著增强,C/Pd原子比从0.136提升至0.154.相变机理研究表明,氢气的引入促进了氢化钯物种的形成,并通过晶格扩张作用促进渗碳过程.此外,还研究了氧化锌助剂对原位渗碳过程的影响,揭示了氧化锌助剂对碳化钯的抑制作用.结合原位CO吸附漫反射红外光谱、准原位X射线光电子能谱分析发现,低温氢气还原下Pd-ZnO界面作用促进了微量表面PdZn合金的生成,从而抑制了碳的渗入.这种现象在不含氢气的碳化气氛中尤为显著,碳含量降低一个数量级(C/Pd原子比仅为0.019).在此基础上,通过调节反应条件,实现了对碳化钯物种碳含量的精准调控,并与反应活性关联,揭示了碳化钯含量与乙炔选择加氢反应活性之间的线性关系.电子结构表征和同位素实验进一步表明,Pd-C的电子相互作用促进了向Pd中心原子的电子转移,从而提高了氢气的活化解离能力和乙炔加氢反应活性.综上,本工作原位解析了碳化钯的动态形成过程,阐明了氢气辅助插碳和ZnO抑制插碳的微观机制,实现了碳化钯活性物种的精准调控,揭示了碳化程度与反应活性的线性关系,为高性能乙炔选择加氢催化剂设计提供了参考. 展开更多
关键词 乙炔选择加氢 碳化钯 渗碳过程 原位光谱 动态机制
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Biomass-based production of trimellitic and trimesic acids
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作者 Lin Yuan Yancheng Hu +6 位作者 Guangyi Li Fengan Han aiqin wang Yu Cong Tao Zhang Feng wang Ning Li 《Green Energy & Environment》 SCIE EI CAS CSCD 2024年第8期1267-1278,共12页
The production of industrial chemicals with renewable biomass feedstock holds potential to aid the world in pursuing a carbon-neutral society.Trimellitic and trimesic acids are important commodity chemicals in industr... The production of industrial chemicals with renewable biomass feedstock holds potential to aid the world in pursuing a carbon-neutral society.Trimellitic and trimesic acids are important commodity chemicals in industry that are prepared by the oxidation of petroleum-derived trimethylbenzene.To reduce the dependence on the limited oil source,we develop a potential sustainable alternative towards trimellitic and trimesic acids using biomass-based 2-methyl-2,4-pentandiol(MPD),acrylate and crotonaldehyde as starting materials.The process for trimellitic acid includes dehydration/D-A reaction of MPD and acrylate,flow aromatization over Pd/C catalyst,hydrolysis and catalytic aerobic oxidation(60%overall yield).The challenging regioselectivity issue of D-A reaction is tackled by a matched combination of temperature and deep eutectic solvent ChCl/HCO_(2)H.Crotonaldehyde can also participate in the reaction,followed by Pd/C-catalyzed decarbonylation/dehydrogenation and oxidation to provide trimesic acid in 54%overall yield.Life cycle assessment implies that compared to conventional fossil process,our biomass-based routes present a potential in reducing carbon emissions. 展开更多
关键词 BIOMASS Trimellitic acid Trimesic acid Deep eutectic solvent Dehydration/D-A reaction
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Sn1Pt单原子合金催化剂在丙烷脱氢反应中的应用 被引量:2
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作者 邢亚楠 康磊磊 +10 位作者 马静远 蒋齐可 苏杨 张盛鑫 徐晓燕 李林 王爱琴 刘智攀 马思聪 刘晓艳 张涛 《Chinese Journal of Catalysis》 SCIE EI CAS CSCD 2023年第5期164-174,共11页
丙烯是生产聚丙烯、各类丙烷氧化物、丙烯腈的重要化工原料.近年来,随着丙烯需求量日益增长,作为一种专产丙烯的生产方式,丙烷脱氢(PDH)受到了越来越多的关注.PtSn/Al_(2)O_(3)是一种典型的工业丙烷脱氢催化剂,其特征是催化活性会随反... 丙烯是生产聚丙烯、各类丙烷氧化物、丙烯腈的重要化工原料.近年来,随着丙烯需求量日益增长,作为一种专产丙烯的生产方式,丙烷脱氢(PDH)受到了越来越多的关注.PtSn/Al_(2)O_(3)是一种典型的工业丙烷脱氢催化剂,其特征是催化活性会随反应时间的推移而下降,因此需要反复再生以保证丙烯产率.提高PtSn催化剂的稳定性,需要明确反应状态下PtSn的催化性能与其结构之间的关系.然而,Pt和Sn的价态及其相互作用,对制备方法、预还原条件、载体类型等因素非常敏感,此外,从Pt-Sn二元相图来看,二者在高温(~600℃)还原性反应气氛下可形成多种合金结构,因此,PtSn在丙烷脱氢中的活性位结构的认识颇具挑战,目前文献报道结果仍存在争议.本文选用商业化的纳米级γ-Al_(2)O_(3)作为载体,通过利用纳米载体上只能担载有限数量的金属原子和加入过量的第二金属Sn稀释活性金属Pt的方式,得到高分散的PtSn/nano-Al_(2)O_(3)催化剂.当Pt和Sn的负载量分别为0.1 wt%和1 wt%时,其初始丙烯产率可达到47.6 molC_(3)H_(6)gPt^(-1)h^(-1),高于文献已报道的PtSn双金属催化剂,该催化剂经3-10 h活性快速下降期(k_(d-3h):0.11h^(-1))后,表现出较好的稳定性(k_(d-10~40h):0.0026 h^(-1)).球差电镜(AC-HAADF-STEM)表征结果显示,该催化剂经500℃焙烧后,Pt及Sn在Al_(2)O_(3)载体上均呈单原子分散状态;经600℃氢气还原后,Pt团聚为平均直径约0.85 nm的纳米颗粒;通过对其进行能谱点扫分析,发现Pt纳米颗粒上分布有少量的Sn原子,而剩余大量的Sn原子则继续以单原子形式分布在载体上.进一步原位X射线光电子能谱和原位X射线吸收能谱结果证明,该催化剂中纳米颗粒的具体组成为Sn单原子分散在Pt纳米颗粒表面,形成S_(n1)Pt表面单原子合金结构.密度泛函理论理论计算证明了S_(n1)Pt表面单原子合金结构的稳定性及其在丙烷脱氢中的高活性.最后结合原位CO吸附的漫反射红外光谱等表征,揭示了催化剂反应初期活性下降及后期高稳定性的内在原因:催化剂经还原后形成了高活性的S_(n1)Pt表面单原子合金结构,在反应过程中,该结构演变为纯相Pt_(3)Sn金属间化合物,其与周围呈单分散的SnOx物种协同作用,抑制和转移在活性中心上的积碳,进而实现了高稳定性.这种通过单原子表面合金演变得到的Pt_(3)Sn金属间化合物,与传统Pt与Pt_(3)Sn等金属化合物混相共存的工业催化剂相比,可以避免丙烯在催化剂表面单金属Pt平台位点上的深度脱氢和积碳,进而提高了催化剂稳定性.综上,本文从原子水平上为PDH反应中PtSn/Al_(2)O_(3)催化剂的活性位结构及其演化过程提供了新的见解,并为工业催化剂的设计制备提供了理论参考. 展开更多
关键词 丙烷脱氢 丙烯 Pt-Sn催化剂 结构重构 单原子合金
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Sub-nanometer Pt_(2)In_(3) intermetallics as ultra-stable catalyst for propane dehydrogenation
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作者 Yanan Xing Guiyue Bi +11 位作者 Xiaoli Pan Qike Jiang Yuanlong Tan Yang Su Leilei Kang Bonan Li Lin Li aiqin wang Jingyuan Ma Xiaofeng Yang Xiao Yan Liu Tao Zhang 《Journal of Energy Chemistry》 SCIE EI CAS CSCD 2023年第8期304-312,I0009,共10页
Pt-based catalysts are the typical industrial catalysts for propane dehydrogenation(PDH),which still suffer from insufficient lo ng-term durability due to the structu ral instability and coke deposition.A commercial ... Pt-based catalysts are the typical industrial catalysts for propane dehydrogenation(PDH),which still suffer from insufficient lo ng-term durability due to the structu ral instability and coke deposition.A commercial γ-Al_(2)O_(3) supported thermally robust sub-nanometer Pt2In3intermetallic catalyst with atomically ordered structure and rigorously separated Pt single atoms was fabricated,which showed outstanding robustness in 240 h long-term operation at 600℃ with the deactivation rate constant kdas low as0.00078 h^(-1), ranking among the lowest reported values.Based on various in situ characterizations and theoretical calculations,it was proved that the catalyst stability not only resulted from the separated Pt single-atom sites but also significantly affected by the distance of adjacent Pt atoms.An increasing distance to 3.25 A in the Pt_(2)In_(3)could induce a weak π-adsorption configuration of propylene on Pt sites,which facilitated the desorption of propylene and restrained the side reactions like coking. 展开更多
关键词 Propane dehydrogenation PROPYLENE Pt-In catalyst Intermetallic compounds Pt_(2)ln_(3)
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Enhanced adsorption of Methylene Blue from aqueous solution by chitosan-g-poly(acrylic acid)/vermiculite hydrogel composites 被引量:31
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作者 Yi Liu Yian Zheng aiqin wang 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2010年第4期486-493,共8页
A series of chitosan-g-poly (acrylic acid)/vermiculite hydrogel composites were synthesized and used as adsorbents for the investigation of the effect of process parameters such as vermiculite content, pH of dye sol... A series of chitosan-g-poly (acrylic acid)/vermiculite hydrogel composites were synthesized and used as adsorbents for the investigation of the effect of process parameters such as vermiculite content, pH of dye solution, contact time, initial concentration of dye solution, temperature, ionic strength and concentration of surfactant sodium dodecyl sulfate on the removal of Methylene Blue (MB) from aqueous solution. The results showed that the adsorption capacity for dye increased with increasing pH, contact time and initial dye concentration, but decreased with increasing temperature, ionic strength and sodium dodecyl sulfate concentration in the present of the surfactant. The adsorption kinetics of MB onto the hydrogel composite followed pseudo second-order kinetics and the adsorption equilibrium data obeyed Langmuir isotherm. By introducing 10 wt.% vermiculite into chitosan-g-poly (acrylic acid) polymeric network, the obtaining hydrogel composite showed the highest adsorption capacity for MB, and then could be regarded as a potential adsorbent for cationic dye removal in a wastewater treatment process. 展开更多
关键词 hydrogel composites VERMICULITE Methylene Blue adsorption kinetics adsorption isotherms
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Removal of Methyl Violet from aqueous solutions using poly (acrylic acid-co-acrylamide)/attapulgite composite 被引量:14
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作者 Yongshengwang Li Zeng +2 位作者 Xuefeng Ren Hai Song aiqin wang 《Journal of Environmental Sciences》 SCIE EI CAS CSCD 2010年第1期7-14,共8页
The adsorption of Methyl Violet (MV) cationic dye from aqueous solution was carried out by using crosslinked poly (acrylic acid-coacrylamide)/attapulgite (Poly(AA-co-AM)/ATP) composite as adsorbent. The factor... The adsorption of Methyl Violet (MV) cationic dye from aqueous solution was carried out by using crosslinked poly (acrylic acid-coacrylamide)/attapulgite (Poly(AA-co-AM)/ATP) composite as adsorbent. The factors influencing adsorption capacity of the composite such as pH, concentration of the dye, temperature, contact time, adsorbent dosage, ionic strength and surfactant were systematically investigated. The equilibrium data fitted very well to the Langmuir isotherm and the maximum adsorption capacity reached 1194 mg/g at 30℃. The thermodynamic parameters including △G0, △H0 and △S0 for the adsorption processes of MV on the composite were also calculated, and the negative △H0 and △G0 confirmed that the adsorption process was exothermicand spontaneous. The kinetic studies showed that the adsorption process was consistent with the pseudo second-order kinetic model and the desorption studies revealed that the regeneration of the composite adsorbent can be easily achieved. 展开更多
关键词 COMPOSITE Methyl Violet adsorption kinetics ISOTHERM
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Selective hydrogenolysis of glycerol to 1,3-propanediol over Pt-W based catalysts 被引量:10
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作者 Jia wang Man Yang aiqin wang 《Chinese Journal of Catalysis》 SCIE EI CAS CSCD 北大核心 2020年第9期1311-1319,共9页
The selective hydrogenolysis of glycerol to 1,3-propanediol(1,3-PDO)is an attractive reaction due to the high demand for valorization of huge excess amounts of glycerol supply as well as the important application of 1... The selective hydrogenolysis of glycerol to 1,3-propanediol(1,3-PDO)is an attractive reaction due to the high demand for valorization of huge excess amounts of glycerol supply as well as the important application of 1,3-PDO in polyester industry.Nevertheless,the formation of 1,3-PDO is thermodynamically less favorable than 1,2-PDO,which necessitates the development of efficient catalysts to manipulate the reaction kinetics towards the 1,3-PDO formation.Among others,Pt-W based catalysts have shown promising activities and selectivities of 1,3-PDO although the reaction mechanism is not well addressed at the molecular level.In this short review,we have compared the performances of different Pt-W based catalysts and discussed the key factors influencing the activity and selectivity.Three possible reaction mechanisms have been discussed in terms of the synergy between Pt and WO_x and the origin of acid sites.Finally,the long-term stability of the Pt-W catalysts has been discussed.We hope this review will provide useful information for the development of more efficient catalysts for this important reaction. 展开更多
关键词 GLYCEROL HYDROGENOLYSIS 1 3-propanediol Pt-W based catalysts
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Effect of IB-metal on Ni/SiO2 catalyst for selective hydrogenation of acetylene 被引量:9
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作者 Hua Liu Mengqian Chai +5 位作者 Guangxian Pei Xiaoyan Liu Lin Li Leilei Kang aiqin wang Tao Zhang 《Chinese Journal of Catalysis》 SCIE EI CAS CSCD 北大核心 2020年第7期1099-1108,共10页
The IB metal(Au,Ag and Cu)alloyed Pd single atom catalysts had been proved to be efficient in promoting the selectivity for hydrogenation of acetylene to ethylene.As a base metal in the same group as Pd,the Ni-based c... The IB metal(Au,Ag and Cu)alloyed Pd single atom catalysts had been proved to be efficient in promoting the selectivity for hydrogenation of acetylene to ethylene.As a base metal in the same group as Pd,the Ni-based catalysts are also active for hydrogenation reactions.Herein,the effects of the IB metals on the Ni/SiO2 catalyst for the selective hydrogenation of acetylene were systematically studied.Different from the Pd/SiO2 catalyst,the monometallic Ni/SiO2 catalyst is not active at low temperatures.The addition of the IB metals to the Ni/SiO2 catalysts can greatly enhance the activity.Besides,the catalytic activity of the AuNix/SiO2 and CuNix/SiO2 catalysts increase with the reduction temperature,while the AgNix/SiO2 catalysts are not sensitive to the pretreatment temperature.The origin of the effect of the different IB metals on the Ni-based catalysts for selective hydrogenation of acetylene is discussed based on the characterizations by XRD,TPR and microcalorimetric measurements. 展开更多
关键词 ACETYLENE Selective hydrogenation ETHYLENE Ni IB metals
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Pt/Nb‐WO_x for the chemoselective hydrogenolysis of glycerol to 1,3‐propanediol: Nb dopant pacifying the over‐reduction of WO_x supports 被引量:10
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作者 Man Yang Xiaochen Zhao +4 位作者 Yujing Ren Jia wang Nian Lei aiqin wang Tao Zhang 《Chinese Journal of Catalysis》 SCIE EI CAS CSCD 北大核心 2018年第6期1027-1037,共11页
Selective hydrogenolysis of glycerol to 1,3‐propanediol(1,3‐PD) is an important yet challenging method for the transformation of biomass into value‐added chemicals due to steric hindrance and unfavorable thermody... Selective hydrogenolysis of glycerol to 1,3‐propanediol(1,3‐PD) is an important yet challenging method for the transformation of biomass into value‐added chemicals due to steric hindrance and unfavorable thermodynamics. In previous studies, chemoselective performances were found de‐manding and sensitive to H2 pressure. In this regard, we manipulate the chemical/physical charac‐teristics of the catalyst supports via doping Nb into WOx and prepared 1D needle‐, 2D flake‐, and 3D sphere‐stack mesoporous structured Nb‐WOx with increased surface acid sites. Moreover, Nb dop‐ing can successfully inhibit the over‐reduction of active W species during glycerol hydrogenolysis and substantially broaden the optimal H2 pressure from 1 to 5 MPa. When Nb doping is 2%, sup‐ported Pt catalysts showed promising performance for the selective hydrogenolysis of glycerol to 1,3‐PD over an unprecedentedly wide H2 pressure range, which will guarantee better catalyst sta‐bility in the long run, as well as expand their applications to other hydrogen‐related reactions. 展开更多
关键词 Nb‐doped WOx Glycerol 1 3‐propanediol Selective HYDROGENOLYSIS
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Effect of promoters on the selective hydrogenolysis of glycerol over Pt/W-containing catalysts 被引量:7
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作者 Jia wang Nian Lei +3 位作者 Chaojun Yang Yang Su Xiaochen Zhao aiqin wang 《Chinese Journal of Catalysis》 SCIE EI CAS CSCD 北大核心 2016年第9期1513-1520,共8页
Diverse promoters,including noble metals(such as Ru,Ir and Rh) and transition metal oxides(such as Re,La,Fe,Zr,Sn and Ce oxides) were introduced into Pt/WOx and Pt/WOx/Al2O3 catalysts to investigate the ability of... Diverse promoters,including noble metals(such as Ru,Ir and Rh) and transition metal oxides(such as Re,La,Fe,Zr,Sn and Ce oxides) were introduced into Pt/WOx and Pt/WOx/Al2O3 catalysts to investigate the ability of these promoters to modify activity and selectivity during glycerol hydrogenolysis to 1,3-propanediol.Among these,La exhibited the greatest promotional effect;the introduction of 0.1% La to the Pt/WOx improved activity,selectivity and stability,although the significant increase in selectivity came at the cost of a slight activity loss in the case of the Pt/WOx/Al2O3 catalyst.Transmission electron microscopy,high angle annular dark field scanning tunneling electron microscopy and NH3-temperature programmed desorption all demonstrated that the introduction of La generates a greater quantity of acidic sites on the catalyst surface,and that the majority of the La species are associated with Pt particles.Most of the other additives resulted in only minimal improvements or even detrimental effects with regard to both activity and selectivity,although some appear to improve the stability of the catalyst. 展开更多
关键词 GLYCEROL HYDROGENOLYSIS 1 3-propanediol Tungsten oxide PROMOTER
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Amine formylation with CO2 and H2 catalyzed by heterogeneous Pd/PAL catalyst 被引量:8
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作者 Xingchao Dai Bin wang +1 位作者 aiqin wang Feng Shi 《Chinese Journal of Catalysis》 SCIE EI CAS CSCD 北大核心 2019年第8期1141-1146,共6页
For the first time, Pd supported on natural palygorskite was developed for amine formylation with CO2 and H2. Both secondary and primary amines with diverse structures could be converted into the desired formamides at... For the first time, Pd supported on natural palygorskite was developed for amine formylation with CO2 and H2. Both secondary and primary amines with diverse structures could be converted into the desired formamides at < 100 °C, and good to excellent yields were obtained. 展开更多
关键词 FORMYLATION Carbon dioxide AMINE Heterogeneous palladium catalyst FORMAMIDE
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Understanding the deactivation behavior of Pt/WO3/Al2O3 catalyst in the glycerol hydrogenolysis reaction 被引量:7
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作者 Nian Lei Zhili Miao +4 位作者 Fei Liu Hua wang Xiaoli Pan aiqin wang Tao Zhang 《Chinese Journal of Catalysis》 SCIE EI CAS CSCD 北大核心 2020年第8期1261-1267,共7页
The selective hydrogenolysis of glycerol to 1,3-propanediol is a highly important reaction for both improving the profitability of biodiesel and valorization of biomass.While intensive research efforts have been devot... The selective hydrogenolysis of glycerol to 1,3-propanediol is a highly important reaction for both improving the profitability of biodiesel and valorization of biomass.While intensive research efforts have been devoted to enhancing the catalytic activity and selectivity,little is focused on the stability although the latter is of paramount importance to practical applications.In this work,we investigated the stability of Pt/WO3/Al2O3 and observed a continuous deactivation trend during a 700 h time-on-stream run.Neither the leaching of active W nor the coking was responsible for the deactivation.Instead,XRD,HAADF-STEM and CO chemisorption results clearly showed the occurrence of significant aggregation of Pt particles,which caused a remarkable decrease of Pt-WOx interfacial sites.As a consequence,strong Br?nsted acid sites which were in situ formed by H2 dissociation at the Pt-WOx interfacial sites were reduced,leading to the deactivation of the catalyst. 展开更多
关键词 GLYCEROL HYDROGENOLYSIS 1 3-PROPANEDIOL DEACTIVATION Aggregation/agglomeration
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Chemoselective hydrogenolysis of tetrahydrofurfuryl alcohol to 1,5-pentanediol over Ir-MoO_x/SiO_2 catalyst 被引量:6
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作者 Zhiqiang wang Boonrat Pholjaroen +6 位作者 Mengxia Li Wenjun Dong Ning Li aiqin wang Xiaodong wang Yu Cong Tao Zhang 《Journal of Energy Chemistry》 SCIE EI CAS CSCD 2014年第4期427-434,共8页
In this work, MoOx promoted Ir/SiO2 catalysts were prepared and used for the selective hydrogenolysis of tetrahydrofurfuryl alcohol (THFA) to 1,5-pentanediol in a continuous flow reactor. The effects of different no... In this work, MoOx promoted Ir/SiO2 catalysts were prepared and used for the selective hydrogenolysis of tetrahydrofurfuryl alcohol (THFA) to 1,5-pentanediol in a continuous flow reactor. The effects of different noble metals (Ir, Pt, Pd, Ru, Rh), supports and Ir contents were screened. Among the investigated catalysts, 4 wt%Ir-MoOx/SiO2 with a Mo/Ir atomic ratio of 0.13 exhibited the best catalytic performance. The synergy between Ix particles and the partially reduced isolated MoOx species attached on them is essential for the excellent catalytic performance of Ix-MoOx/SiO2. The catalyst exhibited a better hydrogenolysis efficiency of THFA with the selectivity of 1,5-pentanediol of 65%-74% at a conversion of THFA of 70%-75% when the initial THFA concentration is ranging from 20 wt% and 40 wt%. And higher system pressure was also in favor of the conversion of THFA. During a stability test, the conversion of THFA and 1,5-pentanediol yield over Ix-MoOz/SiO2 decreased with reaction time, which can be explained by the leaching of Mo species during the reaction. 展开更多
关键词 selective hydrogenolysis tetrahydrofurfuryl alcohol (THFA) 1 5-pentanediol Ir-MoOz catalyst biomass refinery
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On the mechanism of H2 activation over single-atom catalyst: An understanding of Pt1/WOx in the hydrogenolysis reaction 被引量:6
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作者 Maoxiang Zhou Man Yang +6 位作者 Xiaofeng Yang Xiaochen Zhao Lei Sun Weiqiao Deng aiqin wang Jun Li Tao Zhang 《Chinese Journal of Catalysis》 SCIE EI CAS CSCD 北大核心 2020年第3期524-532,共9页
Owing to the atomic dispersion of active sites via electronic interaction with supports,single-atom catalysts(SACs)grant maximum utilization of metals with unique activity and/or selectivity in various catalytic proce... Owing to the atomic dispersion of active sites via electronic interaction with supports,single-atom catalysts(SACs)grant maximum utilization of metals with unique activity and/or selectivity in various catalytic processes.However,the stability of single atoms under oxygen-poor conditions,and the mechanism of hydrogen activation on SACs remain elusive.Here,through a combination of theoretical calculation and experiments,the stabilization of metal single atoms on tungsten oxide and its catalytic properties in H2 activation are investigated.Our calculation results indicate that the oxygen defects on the WO3(001)surface play a vital role in the stabilization of single metal atoms through electron transfer from the oxygen vacancies to the metal atoms.In comparison with Pd and Au,Pt single atoms possess greatly enhanced stability on the WOx(001)surface and carry negative charge,facilitating the dissociation of H-2 to metal-H species(Hδ-)via homolytic cleavage of H2 similar to that occurring in metal ensembles.More importantly,the facile diffusion of Pt-H to the WOx support results in the formation of Bronsted acid sites(Hδ+),imparting bifunctionality to Pt1/WOx.The dynamic formation of Br?nsted acid sites in hydrogen atmosphere proved to be the key to chemoselective hydrogenolysis of glycerol into 1,3-propanediol,which was experimentally demonstrated on the Pt1/WOx catalyst. 展开更多
关键词 Single-atom catalyst Pt Density function theory Hydrogen dissociation Tungsten oxide
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Highlights of the major progress in single-atom catalysis in 2015 and 2016 被引量:15
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作者 Bing Han Rui Lang +2 位作者 Botao Qiao aiqin wang Tao Zhang 《Chinese Journal of Catalysis》 CSCD 北大核心 2017年第9期1498-1507,共10页
The idea that single metal atoms dispersed on a solid support can act as an efficient heterogeneous catalyst was raised in2011when single Pt atoms on an FeOx surface were reported to be active for CO oxidation and pre... The idea that single metal atoms dispersed on a solid support can act as an efficient heterogeneous catalyst was raised in2011when single Pt atoms on an FeOx surface were reported to be active for CO oxidation and preferential oxidation of CO in H2.The last six years have witnessed tremendous progress in the field of single‐atom catalysis.Here we introduce the major achievements on this topic in2015and2016.Some particular aspects of single‐atom catalysis are discussed in depth,including new approaches in single‐atom catalyst(SAC)synthesis,stable gold SACs for various reactions,the high selectivity of Pt and Pd SACs in hydrogenation,and the superior performance of non‐noble metal SACs in electrochemistry.These accomplishments will encourage more efforts by researchers to achieve the controllable fabrication of SACs and explore their potential applications. 展开更多
关键词 Single‐atom catalysis Catalyst synthesis CO oxidation HYDROGENATION ELECTROCATALYSIS
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SiO_2-supported Au-Ni bimetallic catalyst for the selective hydrogenation of acetylene 被引量:8
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作者 Mengqian Chai Xiaoyan Liu +6 位作者 Lin Li Guangxian Pei Yujing Ren Yang Su Hongkui Cheng aiqin wang Tao Zhang 《Chinese Journal of Catalysis》 EI CSCD 北大核心 2017年第8期1338-1346,共9页
Supported Au catalysts have been reported to exhibit high ethylene selectivity in the hydrogenation of acetylene,but the conversion is relatively low.Adding a second metal to Au has proven to be a promising approach t... Supported Au catalysts have been reported to exhibit high ethylene selectivity in the hydrogenation of acetylene,but the conversion is relatively low.Adding a second metal to Au has proven to be a promising approach to enhance its catalytic performance in acetylene hydrogenation.In this work,SiO2‐supported Au‐Ni bimetallic catalysts were synthesized and investigated in the selective hydrogenation of acetylene.The Au‐Ni bimetallic catalysts exhibited much higher catalytic performance than that of the corresponding monometallic Au or Ni catalysts.By tuning the reduction temperature and/or Ni loading,we obtained an Au‐Ni/SiO2catalyst with optimal performance.The results of transmission electron microscopy imaging revealed that the Au‐Ni bimetallic particles were highly dispersed on the SiO2support.Meanwhile,analysis of the bimetallic catalyst by energy‐dispersive X‐ray spectroscopy,high‐resolution transmission electron microscopy,and in situ diffuse reflectance infrared Fourier transform spectroscopy demonstrated the formation of Au‐Ni alloy,which contributed to the synergistic effect between Au and Ni in the hydrogenation of acetylene. 展开更多
关键词 GOLD NICKEL Bimetallic catalyst Synergistic effect Acetylene hydrogenation
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Dehydration of xylose to furfural over niobium phosphate catalyst in biphasic solvent system 被引量:4
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作者 Boonrat Pholjaroen Ning Li +2 位作者 Zhiqiang wang aiqin wang Tao Zhang 《Journal of Energy Chemistry》 SCIE EI CAS CSCD 2013年第6期826-832,共7页
Phosphoric acid treated niobic acid(NbP)was used for the dehydration of xylose to furfural in biphasic solvent system,which was found to exhibit the best performance among the tested catalysts.The excellent performanc... Phosphoric acid treated niobic acid(NbP)was used for the dehydration of xylose to furfural in biphasic solvent system,which was found to exhibit the best performance among the tested catalysts.The excellent performance of NbP could be explained by the better synergistic cooperation between Bro¨nsted and Lewis acid sites.Moreover,NbP showed good stability and no obvious deactivation or leaching of Nb could be observed after six continuous recycles. 展开更多
关键词 XYLOSE FURFURAL DEHYDRATION biphasic solvent system solid acid catalyst niobium phosphate
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Inhibiting effect of tungstic compounds on glucose hydrogenation over Ru/C catalyst 被引量:3
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作者 Junying Zhang Baolin Hou +3 位作者 Xuefei wang Zhenlei Li aiqin wang Tao Zhang 《Journal of Energy Chemistry》 SCIE EI CAS CSCD 2015年第1期9-14,共6页
The effect of acid component including various conventional acids and tungstic compounds on glucose hydrogenation over a series of binary catalyst system containing Ru/C catalyst was investigated. The results showed t... The effect of acid component including various conventional acids and tungstic compounds on glucose hydrogenation over a series of binary catalyst system containing Ru/C catalyst was investigated. The results showed that HC1, H2SO4, H3BO3, H3PO4, and HNO3 had negligible effect, while all the tungstic compounds imposed inhibiting effects on the hydrogenation of glucose over Ru/C catalyst, and the suppressing effect followed the order of H2WO4〉HPW〉WO3〉AMT〉HSiW. This order is the same as the order of ethylene glycol (EG) yields in the one-pot conversion of glucose to EG, suggesting the important role of competition between glucose hydrogenation and retro-aldol condensation in controlling the selectivity of EG. 展开更多
关键词 glucose hydrogenation binary catalyst system suppressing effect retro-aldol condensation ethylene glycol tungstic compounds Ru/C cata-lyst
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