水溶性纳米ni催化氢化氯代硝基苯制备氯代苯胺

水溶性纳米镍;催化加氢;氯代硝基苯;氯代苯胺     

负载型纳米Ni催化剂用于对氯硝基苯选择加氢

以TiO2为载体,N iB为诱导剂,粉末化学镀法制备了负载型纳米N i催化剂.通过TEM、HRTEM、XRD和ICP技术对催化剂物性进行了表征.结果表明,碱性镀液可使载体表面均匀负载微晶结构纳米N i团簇,尺度为35nm左右.该负载型纳米N i在对氯硝基苯选择加氢反应中表现出很高催化加氢活性,并能有效抑制脱氯,达到了工业骨架镍水平.由酸性镀液得到的负载型非晶态纳米N i-P合金具有较弱的催化对氯硝基苯加氢活性.反应温度对反应时间和脱氯率有明显影响.     

金属有机骨架材料负载镍纳米颗粒催化硝基苯加氢

以MIL-53(Al)、MIL-96(Al)和MIL-120(Al)(MIL： Material Institute of Lavorisier)三种金属有机骨架材料为载体,采用浸渍法制备了负载廉价金属镍纳米颗粒的催化剂。将其用于催化硝基苯加氢合成苯胺反应,发现以MIL-53(Al)为载体制得的催化剂表现出优异的催化性能。采用不同的镍前驱体,如硝酸镍、醋酸镍、乙二胺合镍,制备了一系列Ni/MIL-53(Al)催化剂。通过X射线衍射、傅里叶变换红外光谱、电感耦合等离子体、N2物理吸附、H2程序升温还原、透射电镜等技术对其进行了表征,研究了镍前驱体对金属-载体相互作用、镍颗粒尺寸以及分散程度的影响。结果表明：以乙二胺合镍为镍前驱体制得的催化剂具有金属-载体相互作用适中、镍纳米颗粒更小(4-5 nm)和分布更均匀的特点,在硝基苯加氢反应中表现出优异的催化性能,硝基苯转化率达到100%。回收重复使用5次后,此催化剂仍保持催化活性,硝基苯转化率达92%。     

纳米碳管负载金属镍催化叶绿素加氢反应

用等体积浸渍法制备了纳米碳管负载金属镍催化剂，采用电镜(TEM）、红外光谱（IR）对催化剂的形貌、结构进行了表征.并考察了常温常压下不同Ni负载量的催化剂对叶绿素加氢反应的性能.结果表明，纳米碳管负载镍催化剂在催化反应过程中保持高分散态，不会发生团聚.而经过硝酸氧化后的纳米碳管负载镍催化剂在催化反应中表现出高的活性.当Ni负载量为7％时，催化活性最好，叶绿素分子开环生成各种小分子.     

纳米碳管负载金属镍催化叶绿素加氯反应

用等体积浸渍法制备了纳米碳管负载金属镍催化剂，采用电镜（TEM）、红外光谱（IR）对催化剂的形貌、结构进行了表征，并考察了常温常压下不同Ni负载量的催化剂对叶绿素加氢反应的性能。结果表明，纳米碳管负载镍催化剂在催化反应过程中保持高分散态，不会发生团聚，而经过硝酸氧化后的纳米碳管负载镍催化剂在催化反应中表现出高的活性，当Ni负载量为7％时，催化活性最好，叶绿素分子开环生成各种小分子。     

磁场诱导合成一维金属镍线的形貌控制

以镍盐与水合肼为起始原料,采用外加磁场辅助的水热法合成了表面具有纳米级刺状结构的一维金属镍线.向体系中引入十六烷基三甲基溴化铵(CTAB)作为包裹剂,可以合成表面光滑的金属镍线.对比大块镍,金属镍线的矫顽力得到了显著的增强.研究结果表明,外加磁场是线状结构形成的关键,而在镍核表面的CTAB吸附是控制表面形貌的重要因素.以甲基异丁基甲酮加氢制备甲基异丁基甲醇为探针反应,考察了所合成材料的加氢催化性能.结果表明,金属镍材料的一维结构与表面的纳米级刺状结构均有助于提高镍基催化剂的加氢催化活性.     

负载型纳米镍铈催化剂的表征及其选择性催化加氢活性(英文)

采用氢电弧等离子体法制备了具有储氢性能的镍铈纳米颗粒,通过扫描电镜、透射电镜、X光电子能谱、X射线粉末衍射、程序升温还原等手段对比表征了氧化铝负载的纳米镍铈催化剂和工业用负载镍催化剂,并以裂解汽油一段加氢反应为模型反应研究了它们的催化性能.研究结果表明,纳米镍铈催化剂的催化活性和储氢性能与催化剂表面的镍铈合金有关,负载性纳米镍铈催化剂的优良选择性与其特殊的制备方法有关.     

漆原镍催化剂用于硝基化合物催化加氢

采用锌粉还原氯化镍制备了漆原镍催化剂,并将其用于催化间二硝基苯加氢制间苯二胺和2,5-二氯硝基苯加氢制2,5-二氯苯胺反应.运用X射线衍射、电感耦合等离子体发射光谱和透射电子显微镜等技术对催化剂进行了表征.考察了锌粉、展开剂和制备温度对催化剂活性的影响,以及压力、溶剂等对加氢反应速率的影响,确定了适宜的催化剂制备条件.结果表明,在间二硝基苯和2,5-二氯硝基苯加氢反应中,漆原镍催化剂表现出很高的活性和选择性,在乙醇溶剂中加入适量的水能够大大提高反应速率,适量的脱氯抑制剂能够有效加快2,5-二氯硝基苯加氢速率并提高2,5-二氯苯胺选择性.漆原镍催化剂重复使用5次后其性能基本保持不变.     

马来酸-苯乙烯共聚物-钯络合物催化剂在加氢反应中的变化及钯的回收利用

马来酸-苯乙烯共聚物-钯络合物在催化加氢过程中,络合在高分子配体上的钯离子易被还原为Pd(0),而部分地脱落下来,这可从XPS及电镜分析证实。催化活性中心可能是高分子络合(或隔离保护)的Pd(0)微粒。本文研究了高分子钯催化剂在硝基苯加氢过程中,钯的用量范围,溶剂对催化活性的影响,催化剂的回收与其活性及金属钯的回收与再利用。此外还测定了硝基苯催化加氢的活化能。     

常温常压下吡咯及其衍生物的镍催化加氢反应考察

为进一步研究常温常压下吡咯及其衍生物的镍催化加氢反应,我们对试剂吡咯、吡咯烷和吡咯烷酮做了相应的催化加氢实验。并采用电镜（TEM-HREM）、X射线衍射（XRD）对Ni基催化剂的形貌、结构、加氢活性和超声波对其影响进行了检测,同时还用紫外吸收光谱、气相色谱等对加氢产物进行了分析考察。结果表明超声波能促进镍基催化剂活性,使镍微晶(111)晶面间距增大1.5%、并保持高分散态。常温常压下纳米镍基催化剂对吡咯、吡咯烷和吡咯烷酮的加氢反应显示一定的催化活性;吡咯加氢首先生成吡咯烷,进而使环打开生成低碳烃、氨等产物,总反应为零级,符合表面接触反应特征。     

利用乙醇重整制氢进行硝基苯原位液相加氢合成苯胺

 利用乙醇液相催化重整制得的氢直接进行硝基苯原位液相加氢合成苯胺. 考察了不同催化剂、反应温度及反应时间等因素的影响. 在以Pt/Al2O3为催化剂,反应温度220 ℃和反应时间3 h的条件下,硝基苯的转化率可达99.3%, 苯胺的选择性为99.8%, 催化剂表现出较高的加氢活性和选择性.     

Selectivity in the Phase Transfer Catalytic Hydrogenation of Nitrobenzene by Transition VIII Metals

The phase transfer hydrogenation of nitrobenzene to p-aminophenol has been investigated for the catalysts Pt, Pd, Rh and Ru. The influence of factors such as surfactant concentration, sulfuric acid concentration, hydrogen pressure and temperature on the reaction was determined. It was found that the rate-determining step for the catalytic hydrogenation of nitrobenzene is the catalytic process by which the hydrogen atom is absorbed on the metal surface. A reaction model is suggested which accounts for the observed hydrogenation selectivity and explains how these factors affect product composition and yield. It is shown that Pt favors p-aminophenol production, while Pd favors aniline production.     

复合氧化物催化剂(Cu)CeO2上硝基苯加氢反应的研究

 基于用FT－IR表征H2与硝基苯在催化剂（Cu）CeO2上的吸附和反\r\n应行为，对硝基苯加氢反应进行了研究．结果表明，氢在催化剂表面的\r\n吸附主要为解离吸附，硝基苯的吸附也主要为化学吸附；两种吸附物种\r\n在催化剂上进行表面反应生成易脱附的苯胺，避免了产物与反应物间的\r\n竞争吸附，有利于反应物完全转化．在（Cu）CeO2催化剂上，硝基苯加\r\n氢反应机理为朗格缪尔－欣谢伍德型，即表面反应为控制步骤．     

HYDROGENATION OF NITROBENZENE TO FORM ANILINE IN LIQUID PHASE AT ATMOSPHERIC PRESSURE

Aromatic amine compounds and their derivatives are important intermediates of fine chemicals like dye and medicine.The former hydrogenation catalyst has many problems,such as environment pollution caused by old technology,strict reaction condtion,complicated equipment,bad property of catalyst and so on.Holy ^[1] firstly reported the hydrogenation of nitrobenzene on modified polystyrene Pd catalyst.But how to improve the activity,selectivity and stability of the polymer suppoorter catalyst needs to studyfurther.We prepared a series of polymer supported catalysts by the methods of adsorption and mechanical mixting ,selected a high active catalyst Pd-Ah-1 by observing the hydrogenation of nitrobenzene.     

HYDROGENATION OF NITROBENZENE TO FORM ANILINE IN LIQUID PHASE AT ATMOSPHERIC PRESSURE*

1. EXPERIMENT SECTION1.1 Reagent and InstrumentNitrobenzene (chemical purity), alcohol (medical), hydrogen (electrolytic method 99.8%), anion exchange resin AH-1 PdCl2, 2H20 (Pd containing 59%), NaCl, LXM-80-type vapor-liquid chromatograph (made in Russia), ZD-2-type potentiometer (made in Russia). 1.2 Catalyst PreparationThere are two methods of catalyst preparation, one of which is adsorption: putting PdCl2?2H2O, AH-1, NaCl and distilled water in oscillating hydrogenation re…     

Controllable synthesis of VSB-5 microspheres and microrods: growth mechanism and selective hydrogenation catalysis

Nanoporous VSB-5 nickel phosphate molecular sieves with relatively well controllable sizes and morphology of microspheres assembled from nanorods were synthesized at 140 degrees C over a short time in the presence of hexamethylenetetramine (HMT) by a facile hydrothermal method. The pH value, reaction time, and ratio of HMT to NaHPO2.H2O crucially influence the morphology and quality of the final products. By adjusting the pH value of the initial reaction solution, the morphology changes from disperse rods to microspheres assembled from rods and finally to a large quantity of fibers, and the diameters of the VSB-5 rods can be varied. The catalytic activity of VSB-5 in selective hydrogenation of several unsaturated organic compounds was tested. Nickel(II) in VSB-5 can selectively catalyze hydrogenation of C=C in trans-cinnamaldehyde and 3-methylcrotonaldehyde. In addition, since nitrobenzene (NB) and 2-chloronitrobenzene could be reduced to aniline (AN) and 2-chloroaniline with high selectivity, VSB-5 could have potential applications in synthesizing dyes, agrochemicals, and pharmaceuticals.     

PVA‐encapsulated Palladium Nanoparticles: Eco‐friendly and Highly Selective Catalyst for Hydrogenation of Nitrobenzene in Aqueous Medium

In aqueous medium without any other additives, palladium (Pd) nanoparticles with water‐soluble polyvinyl alcohol (PVA) as stabilizer were synthesized for the catalytic hydrogenation of nitrobenzene. Under the optimum experimental conditions, the nitrobenzene conversion and the selectivity for aniline were 99.3 % and 100 %, respectively. Comprehensive characterization methods, including TEM, UV/Vis, confocal laser scanning microscopy (CLSM), XRD and XPS allowed a better understanding of the role of PVA aggregates and the properties of Pd nanoparticles. The nitrobenzene conversion exceeded 80 % even after 6 cycles without any treatment of the catalyst. A mechanism about the hydrogenation of nitrobenzene catalyzed by Pd/PVA system was proposed. The Pd/PVA catalyst also exhibited excellent activity and selectivity, particularly to ortho‐fluoronitrobenzene and ortho‐nitrotoluene. This research can provide a reference for the environmentally friendly catalysis for hydrogenation of nitrobenzene and other substituted nitrobenzene compounds.     

One pot synthesis of N-ethylaniline from nitrobenzene and ethanol

A novel method for the one pot synthesis of N-alkyl arylamines from nitro aromatic compounds and alcohols is proposed through the combination of the aqueous-phase reforming of alcohol for hydrogen production, the reduction of nitro aromatic compounds for the synthesis of aromatic amine and the N-alkylation of aromatic amine for the production of N-alkyl arylamine over an identical catalyst under the same conditions of temperature and pressure in a single reactor. In this process, hydrogen generated from the aqueous-phase reforming of alcohols was used in-situ for the hydrogenation of nitro aromatic compounds for aromatic amine synthesis, followed by N-alkylation of aromatic amine with alcohols to form the corresponding N-alkyl arylamines at a low partial pressure of hydrogen. For the system composed of nitrobenzene and ethanol, under the conditions of 413 K and PN2 = 1 MPa, the conversion degrees of nitrobenzene and aniline were 100%, the selectivity to N-ethylaniline and N, N-diethylaniline were 85.9% and 0%-4%, respectivity, after reaction for 8 h at the volumetric ratio of nitrobenzene:ethanol:water = 10:60:0. The selectivity for N, N-diethylaniline production is much lower than that through the traditional method. In this process, hydrogen and aromatic amines generated from the aqueous-phase reforming of alcohols and hydrogenation of nitro aromatic compounds, respectively, could be promptly removed from the surface of the catalyst due to the occurrence of in-situ hydrogenation and N-alkylation reactions. Thus, this may be a potential approach to increase the selectivity to N-alkyl arylamine.