富氧条件下Ir催化NO反应

用浸渍法制备了系列Ir催化剂, 研究了富氧条件下Ir催化NO的反应, 考察了催化剂的催化反应性能及负载量和载体对催化活性的影响. 结果表明, 在Ir催化剂上不仅发生了NO氧化反应, 同时也发生了NO还原反应; Ir催化剂对NO反应有催化作用, 催化活性随Ir负载量的增加而增强. 载体对催化剂活性有一定的影响, 负载量低于0.1%(w)时, 催化NO氧化的活性顺序为Ir/ZSM-5>Ir/γ-Al2O3>Ir/SiO2, 这主要受载体自身性质的影响; 负载量高于0.1%时, 催化NO氧化的活性顺序为Ir/ZSM-5>Ir/SiO2>Ir/γ的活性顺序为Ir/γ-Al2O3>Ir/SiO2>Ir/ZSM-5, 这主要由于载体吸附作用促进了NO2在Ir催化剂上吸附分解. 与Pt催化剂相比, Ir催化剂更有利于促进NO还原.     

室温条件下硝酸羟胺的催化分解

 采用等体积浸渍法制备了一系列以Al2O3和SiO2为载体的负载型贵金属催化剂. 用热重法考察了催化剂对80%硝酸羟胺推进剂的分解活性. 结果表明, Ir/SiO2催化剂能够在室温以下(20.7 ℃)催化分解80%硝酸羟胺,显示出该催化体系在环境友好的单组元推进器上具有很大的应用潜力. H2化学吸附实验表明, Ir/SiO2 具有比 Ir/Al2O3更大的Ir颗粒,这可能是造成前者活性比后者高的原因之一.     

贵金属铱对氨分解用镍基催化剂的促进作用研究

用湿式浸渍法制备了不同贵金属质量分数的镍-铱双金属催化剂,以氨分解为模型反应对其催化性能进行考察.结果表明,贵金属铱的添加提高了10%Ni/γ-Al2O3的低温活性.在铱的质量分数不高于1%时,氨分解反应活性随铱质量分数的增加出现最大值(相应的Ir质量分数为0.7%),对应的10%Ni-0.7%Ir/γ-Al2O3催化剂在400 ℃时,氨分解率为43.55%,较单组分的Ni催化剂高40.0%.用H2-TPR、H2-TPD 、BET和XRD表征方法对催化剂进行了表征.结果表明,Ir与活性组分Ni之间存在协同作用.铱的添加促进了活性组分的分散、减小了镍的晶粒尺寸,且增加了催化剂活性位的数量,从而提高了催化剂的氨分解性能.     

助剂Fe对Ir/SiO2催化剂的巴豆醛选择性加氢性能的影响

以SiO2为载体采用分步浸渍法制备了Fe/Ir/SiO2催化剂,考察了助剂Fe对Ir/SiO2催化剂气相巴豆醛选择性加氢性能的影响.采用X射线粉末衍射(XRD)、CO化学吸附、H2-程序升温还原(H2-TPR)和拉曼光谱(Raman)等技术对催化剂进行了表征.结果表明,助剂Fe能有效提高Ir/SiO2催化剂的巴豆醛转化率和巴豆醇选择性.Fe含量为0.087%的0.087Fe/Ir/SiO2催化剂的反应性能最佳,反应进行9 h的巴豆醛转化率36.9%,巴豆醇选择性83%.随着催化剂CO吸附量的下降(Fe覆盖的增加),催化剂的转换频率(turn over frequency,TOF)明显增加,这表明Fe促进Ir/SiO2催化剂表面活性位的加氢活性.然而,Fe的掺杂使得Ir/SiO2催化剂存在明显的活性下降现象,归因于Fe导致Ir/SiO2催化剂表面积炭和CO中毒.     

Pd基催化剂上H2快速选择催化还原 NOx

 首次研究了 Pd 基催化剂上氢快速选择催化还原 NOx 反应 (快速 H2-SCR 反应). 结果表明, Pd/Al2O3 和 Pd/SiO2 催化剂表现出极高的活性, 在 200 oC 以上时 NOx 转化率可达 100%; 但 Pd/MgO 催化剂在整个考察温度范围均没有活性, 这表明载体对催化剂快速 H2-SCR 活性有决定性作用. 与常规 H2-SCR 反应相比, 快速 H2-SCR 反应明显提高了 NOx 的消除效率. 原位漫反射红外光谱结果表明, 快速 H2-SCR 反应活性的提高来源于加速生成的氨物种以及后续反应速率的加快.     

Ir/SiO2上甲烷部分氧化制合成气反应的原位时间分辨红外和原位Raman光谱表征

采用原位时间分辨红外光谱和原位显微Raman光谱技术对Ir/SiO2上甲烷部分氧化(POM)制合成气反应的初级产物和反应条件下催化剂表面物种进行了跟踪考察，实验结果表明，在H2预还原的新鲜Ir/SiO2表面，CO是V(CH4)：V(O2)：V(Ar)=2：1：45混合气反应的初级产物，因而甲烷的直接氧化过程是CO生成的主要途径；而在稳态反应条件下，CO生成的途径可能主要来自CO2和H2O与催化剂表面积碳物种(CHx)和／或CH4的反应.催化剂上生成的积碳可能是导致稳态条件下Ir/SiO2上POM反应机理不同于H2预还原的新鲜催化剂的主要原因.     

金红石型氧化钛负载的铱在催化分解N_2O推进剂反应中的应用（英文）

氧化亚氮(N_2O)是一种性能独特优越的新型绿色推进剂,分解后可以生成高温富氧燃气,实现自增压式多种模式推进,是小卫星推进系统理想的推进剂选择,因而具有广阔的应用前景.在标准状态下,N_2O热分解反应活化能为250 k J/mol,致使其非催化热分解温度高达600 ℃,显然小卫星的能源系统无法满足,必须采取催化分解的手段,改变反应路径、降低反应活化能,使N_2O能够在较低的温度下分解.有关N_2O分解催化剂的报道很多,如纯相或复合氧化物、金属交换分子筛和负载贵金属等,但是这些催化剂仍然存在活性较低等问题,难以满足N_2O推进系统的应用需求.氧化钛是光催化和金催化常用的催化剂,经还原后能够形成氧缺陷,可以为涉氧反应提供电子,而N_2O分解会产生大量氧,氧脱附是其速率控制步骤,因而以氧化钛为载体,有望促进氧脱附及N_2O分解.与此同时,氧化铱具有较高的N_2O分解活性,而且与金红石型氧化钛晶格相似,相似的晶格参数可能会促进其在氧化钛表面的分散,进一步提高N_2O分解性能.基于此,本文以金红石氧化钛(r-TiO_2)为载体,采用匀相沉积沉淀法制备了不同载量的金红石氧化钛负载铱催化剂(Ir/r-TiO_2),并制备了锐钛矿型氧化钛、混合晶相P25和γ-Al_2O_3负载铱催化剂作为对比.通过活性测试我们发现,Ir/r-TiO_2催化剂显示了非常优异的N_2O分解活性,N_2O转化率明显高于参比催化剂,在250℃就能够开始分解,在300 ℃可以分解完全,而且当Ir含量降低到0.1%时,催化剂仍然保持与2 wt%Ir/γ-Al_2O_3相当的催化活性.随后我们采取多种表征手段对Ir/r-TiO_2的活性本质和N_2O分解机理进行了探究.首先利用BET、HAADF-STEM和XRD对催化剂的基本物性进行了测试,发现Ir/r-TiO_2具有较低的比表面积,但金属铱在金红石氧化钛表面表现出较高的分散度,平均粒径仅为1.25 nm.采用H-2-TPR和O 1s XPS考察了催化剂的电子特性和还原特性,发现Ir/r-TiO_2催化剂上高分散的Ir与氧的结合能较弱,易于还原,有助于N_2O的分解和生成氧的脱附.进一步采用原位N_2O-DRIFT对N_2O分解过程进行了研究,发现了桥式过氧物种,并据此提出了N_2O在Ir/r-TiO_2催化剂上的分解机理.     

(1S,2S)-1,2-二苯基乙二胺修饰Ir/SiO_2催化苯乙酮及其衍生物不对称加氢(英文)

不添加任何稳定剂,在碱性条件下制备了5%Ir/SiO2催化剂,并用于催化苯乙酮的不对称加氢反应中,详细考察了碱和手性修饰剂种类、氢气压力、反应温度、(1S,2S)-1,2-二苯基乙二胺((1S,2S)-DPEN)浓度对反应的影响.在优化反应条件下,5%Ir/SiO2催化剂表现出较好的反应活性和对映选择性.其中,苯乙酮不对称加氢反应的对映选择性达70%.该催化剂不需要任何稳定剂,制备方法简单,催化性能稳定,通过简单的离心分离即可循环使用.     

(1S,2S)-1,2-二苯基乙二胺修饰Ir/SiO2催化苯乙酮及其衍生物不对称加氢（英文）

不添加任何稳定剂,在碱性条件下制备了5%Ir/SiO2催化剂,并用于催化苯乙酮的不对称加氢反应中,详细考察了碱和手性修饰剂种类、氢气压力、反应温度、(1S,2S)-1,2-二苯基乙二胺((1S,2S)-DPEN)浓度对反应的影响.在优化反应条件下,5%Ir/SiO2催化剂表现出较好的反应活性和对映选择性.其中,苯乙酮不对称加氢反应的对映选择性达70%.该催化剂不需要任何稳定剂,制备方法简单,催化性能稳定,通过简单的离心分离即可循环使用.     

高硫化氢合成气制甲硫醇新型钼基催化剂研究

研究了一系列负载型钼基催化剂催化含高硫化氢合成气制甲硫醇的性能 ,用XPS和ESR对其进行表征 .活性测试显示 ,钾促进的钼基催化剂催化的反应产物中甲硫醇成为主导产物 .几种钼基催化剂合成甲硫醇的活性大小顺序 :K2 MoO4/CoO/SiO2 >K2 MoO4/SiO2 >MoO3 /K2 CO3 /SiO2 >K2 MoS4/SiO2 >MoS2 /K2 CO3 /SiO2 .ESR表征显示 ,反应后的催化剂可以检测到“oxo Mo(V)”和“thio Mo(V)”物种 .XPS表征显示反应后催化剂中的Mo包含着Mo4+ ,Mo5+ 和Mo6+ ,S包含着S2 -,(S—S) 2 -和S6+ 三种价态 .添加CoO后 ,“oxo Mo(V)”含量减少 ,而“thio Mo(V)”含量增加 ,(S—S) 2 -物种的生成得到抑制 ,S2 -物种的量增多 .(Mo4+ +Mo5+ ) /Mo6+ 峰强度比为 0 75以及S2 -/(S—S) 2 -接近 1有利于甲硫醇的生成 .本文提出甲硫醇的合成与“Mo S K”相关联的反应机理     

SARS冠状病毒E蛋白的结构研究及功能预测

结合生物信息学方法及分子模拟手段,选择较高准确度的方法,预测了SARSE蛋白的分子结构并探讨其潜在的生物学活性和功能.研究结果表明,SARSE蛋白跨膜区25个疏水的氨基酸形成α-螺旋结构,包埋于病毒外壳磷脂双分子层中;N端10个氨基酸残基位于膜外;C端41个残基则附着于磷脂双分子膜内侧.同时发现,C端由9个氨基酸组成的劈裂是一个可能的活性部位.对分子进行进一步静电势分析证实,E蛋白C端可能的活性部位具有较大的静电势,可能的活性残基具有最大电荷密度,故有较强的结合受体或与其它蛋白相互作用的能力.     

Decomposition of ammonia and hydrogen on Ir surfaces: structure sensitivity and nanometer-scale size effects

The adsorption and decomposition of ammonia and hydrogen have been studied on surfaces of clean planar Ir(210) and clean nanoscale-faceted Ir(210), which are prepared from the same crystal in situ. We find evidence for structure sensitivity in recombination and desorption of H2 and in thermal decomposition of NH3 on clean planar Ir(210) versus clean faceted Ir(210). Moreover, the decomposition kinetics of NH3 on faceted Ir(210) exhibit size effects on the nanometer scale, which is the first observation of size effects in surface chemistry on an unsupported monometallic catalyst with controlled and well-defined structure and size.     

铜对Mn/Al_2O_3氨还原SO_2到单质硫催化性能的影响

ＳＯ2 是危害最为严重的大气污染物之一 ,也是造成酸雨的元凶。将ＳＯ2 选择性还原为单质硫 ,既能消除ＳＯ2 对环境的污染 ,又能回收单质硫 ,具有特别重要的意义。根据所用的还原剂的不同 ,催化还原ＳＯ2 到单质硫可分为Ｈ2 、炭、烃类 (主要是ＣＨ4 )、ＣＯ和ＮＨ3还原法[1] 。氨还原法是基于氨的催化分解生成Ｎ2 和Ｈ2 混合气 ,其中的Ｈ2 再还原ＳＯ2 到硫和Ｈ2 Ｓ ,然后进行高温Ｃｌａｕｓ反应生成单质硫。Ｐａｉｋ[2 ] 等以第四周期过渡金属硫化物载于Ａｌ2 Ｏ3 作为催化剂 ,研究了Ｈ2 还原ＳＯ2 为单质硫的反应 ,认为过渡金属硫化物是…     

Distinct thermodynamics for the formation and cleavage of N-H bonds in aniline and ammonia. Directly-observed reductive elimination of ammonia from an isolated amido hydride complex

The reactions of aryl and alkylamines with the (PCP)Ir fragment (PCP = 1,3-di-tert-butylphosphinobenzene) were studied to determine the reactivities and stabilities of amine and amido hydride complexes relative to C-H activation products. Reaction of aniline with the (PCP)Ir unit generated from (PCP)IrH2 and norbornene resulted in the N-H oxidative addition product (PhNH)(H)Ir(PCP) (1a). In contrast, reaction of this fragment with ammonia gave the ammonia complex (NH3)Ir(PCP) (2). The amido hydride complex that would be formed by oxidative addition of ammonia, (PCP)Ir(NH2)(H) (1b), was generated independently by deprotonation of the ammonia complex (NH3)Ir(H)(Cl)(PCP) (3) with KN(SiMe3)2 at low temperature. This amido hydride complex underwent reductive elimination at room temperature to form the ammonia complex 2. Addition of CO to anilide complex 1a gave (PCP)Ir(PhNH)(H)(CO) (4a). Addition of CNtBu to terminal amido complex 1b formed (PCP)Ir(NH2)(H)(CNtBu) (4b), the first structurally characterized iridium amido hydride. Complexes 4a and 4b underwent reductive elimination of aniline and ammonia; parent amido complex 4b reacted faster than anilide 4a. These observations suggest distinct thermodynamics for the formation and cleavage of N-H bonds in aniline and ammonia. Complexes 1a, 2, 4a, and 4b were characterized by single-crystal X-ray diffraction methods.     

表面酸性对Ni/SiO_2-Al_2O_3催化剂催化1,4-丁炔二醇高压加氢性能的影响

通过浸渍法分别在Al(OH)_3和Al_2O_3中引入SiO_2,经焙烧后制备具有不同表面酸性质的SiO_2-Al_2O_3载体,以上述SiO_2-Al_2O_3及Al_2O_3为载体,采用等体积浸渍法制备Ni负载量为15%的Ni/SiO_2-Al_2O_3催化剂(分别为Ni/SA-1和Ni/SA-2)与Ni/Al_2O_3.采用N2物理吸附、Py-FTIR、NH3-TPD、XRD、H2-TPR和H2-TPD手段对催化剂进行表征,考察了表面酸性质对催化剂催化1,4-丁炔二醇高压加氢性能的影响.结果表明,SiO_2引入方式会影响Ni/Al_2O_3催化剂表面酸性质及活性组分Ni在载体表面的分散行为.在Al(OH)3中引入SiO_2时,Ni/SA-1催化剂不仅活性组分具有高分散度,而且表面具有丰富的L酸位点,L酸位点与Ni活性中心协同作用有效提高了催化剂的高压加氢性能.而在Al_2O_3中直接引入SiO_2时,SiO_2覆盖了Al_2O_3表面的L酸位点,催化剂活性组分分散度较低,表现出低的加氢活性.     

Activation and coordination of ammonia at [cp*ir(h)(2) ]: NMR and matrix isolation studies

(1) H?NMR exchange spectroscopy of a reaction mixture of [Cp*Ir(H)(4) ] (1; Cp*=1,2,3,4,5-pentamethylcyclopentadienyl) and ammonia suggests an exchange of hydrogen atoms between the hydrido ligands and ammonia. Treatment of 1 with ND(3) led to an H/D exchange between ND(3) and the hydrido ligands of 1. Subsequent studies showed that photolysis of 1 isolated in frozen argon matrices leads to the formation of the iridium compounds [Cp*Ir(H)(2) ] (2) and [Cp*Ir(H)(3) ] (4), as it was confirmed by IR spectroscopy. In the presence of water the aqua complex [Cp*Ir(H)(2) (OH(2) )] (3) was generated simultaneously. Accordingly, photolysis of 1 in an argon matrix doped with ammonia gave rise to the ammine complex [Cp*Ir(H)(2) (NH(3) )] (5). IR assignments were supported by calculations of the gas-phase IR spectra of 1-5 by DFT methods.     

Surface properties of Ni-Pt/SiO2 catalysts for N2O decomposition and reduction by H2

The surface properties of bimetallic Ni-Pt/SiO2 catalysts with variable Ni/Ni + Pt atomic ratio (0.75, 0.50, and 0.25) were studied using N2O decomposition and N2O reduction by hydrogen reactions as probes. Catalysts were prepared by incipient wetness impregnation of the silica support with aqueous solutions of the metal precursors to a total metal loading of 2 wt %. For both model reactions, Pt/SiO2 catalyst was substantially more active than Ni/SiO2 catalyst. Mean particle size by TEM was about the same (in the range 6-8 nm) for all catalysts and truly bimetallic particles (more than 95%) were evidenced by EDS in the Ni-Pt/SiO2 catalysts. CO adsorption on the bimetallic catalysts showed differences in the linear CO absorption band as a function of the Ni/Pt atomic ratio. Bimetallic Ni-Pt/SiO2 catalysts showed, for the N2O decomposition, a catalytic behavior that points out an ensemble-size sensitive behavior for Ni-rich compositions. For the N2O + H2 reaction, the bimetallic catalysts were very active at low temperature. The following activity order at 300 K was observed: Ni75Pt25 > Ni25Pt75 approximately Ni50Pt50 > Pt. TOF values for these catalysts increased 2-5 times compared to the most active reference catalyst (Pt/SiO2). The enhancement of the activity in the Ni75Pt25 bimetallic catalysts is explained in terms of the presence of mixed Ni-Pt ensembles.     

Influence of Preparation Conditions on the Catalytic Performance of MoNx/SBA-15 for Ammonia Decomposition

The influence of preparation conditions (e.g. H2-N2 ratios, final nitriding temperatures) on the performance of MoNx/SBA-15 catalysts for ammonia decomposition was investigated. The variation of catalytic activity with H2-N2 ratios may be attributed to the variation of surface compositions and particle sizes of the active components. The variation of nitriding temperatures leads to the formation of molybdenum nitride domains of varying compositions, which are responsible for the difference in their catalytic performance with respect to ammonia decomposition. At 923 K. ammonia could be completely decomposed using 15800 ml/h·gcat of GHSVNH,, which shows high performance for the catalytic decomposition of ammonia.     

Activation and Coordination of Ammonia at [Cp*Ir(H)2]: NMR and Matrix Isolation Studies

¹H NMR exchange spectroscopy of a reaction mixture of [Cp*Ir(H)₄] ( 1 ; Cp*=1,2,3,4,5‐pentamethylcyclopentadienyl) and ammonia suggests an exchange of hydrogen atoms between the hydrido ligands and ammonia. Treatment of 1 with ND₃ led to an H/D exchange between ND₃ and the hydrido ligands of 1 . Subsequent studies showed that photolysis of 1 isolated in frozen argon matrices leads to the formation of the iridium compounds [Cp*Ir(H)₂] ( 2 ) and [Cp*Ir(H)₃] ( 4 ), as it was confirmed by IR spectroscopy. In the presence of water the aqua complex [Cp*Ir(H)₂(OH₂)] ( 3 ) was generated simultaneously. Accordingly, photolysis of 1 in an argon matrix doped with ammonia gave rise to the ammine complex [Cp*Ir(H)₂(NH₃)] ( 5 ). IR assignments were supported by calculations of the gas‐phase IR spectra of 1 – 5 by DFT methods.