螯合树脂负载钯催化剂的合成及研究

聚苯乙烯树脂经8-氨基喹啉处理,再与氯化钯反应制得高分子负载钯铬合物。与不同还原剂(H_2,SnCl_2,NaBH_4,LiAlH_4,CH_3OH-H_2O-OH~-和H_2NNH_2)反应后分别制成高分子负载的铬合钯催化剂、胶态钯催化剂和混合价态钯催化剂。文中比较了它们对己烯-1和1,5,9-环十二碳三烯的催化加氢活性和选择性。实验表明用还原能力适中的还原剂作用制得的混合价态钯催化剂具有很高的催化活性和选择性。同时发现增加钯在载体表面的分散度和降低反应所用溶剂的极性可减少贵金属的流失。     

芳基碘化物[聚(4-乙烯基吡啶)]钯(0)催化下的乙烯基化反应

前文报道了聚[(苯乙烯)联吡啶]钯(0)催化剂在芳基碘化物乙烯基化反应中的应用,其催化剂的活性较高,但连续使用三次后,活性明显降低.本文继续报道能用于芳基碘化物乙烯基化反应的高分子负载钯催化剂的合成和应用.据文献报道能用于芳基碘化物乙烯基化的高分子负载钯催化剂,都是通过多步反应将配体导入聚苯乙烯骨架上合成的,操作比较复杂.为了简化催化剂的制备方法,我们探索了用聚(4-乙烯基吡啶)作高分子载体的可能性.将4 乙烯基吡啶与苯乙烯共聚,加入2%二乙烯基苯作交联剂,生成的共聚物用醋酸钯处理后,加氢化铝锂还原,得到每克含钯7.0mg、氮33.7mg的催化剂,并研究了它在芳基碘化物与苯乙烯、丙烯酸和丙烯酰胺的反应中的催化性能.     

钯盐中负离子对聚合物载钯催化剂加氢性能的影响

将三种钯盐（Ｐｄ（ＯＡｃ）２，ＰｄＣｌ２，ＰｄＩ２）分别与聚乙烯苄二甲胺反应，然后将其还原制成三种不同的高分子负载钯金属催化剂，考察了起始钯盐中负离子的不同对所合成的高分子催化剂表面上钯粒子大小，钯粒子分布状况的影响及催化剂的催化性能。研究结果表明，由Ｐｄ（ＯＡｃ）２制备的高分子载钯催化剂具有最好的催化活性和使用寿命。     

高分子负载咪唑啉钯催化剂的合成及其对Heck反应的催化性能研究

以普通商品聚丙烯腈(PAN)为原料, 合成了四种功能基化的纤维高分子载体, 挑选出其中一种与金属钯盐反应合成出了高分子负载钯催化剂. 利用元素分析、红外光谱、原子吸收光谱、SEM及XPS等手段对其结构进行了表征. 研究了该催化剂对碘代苯与丙烯酸乙酯反应的催化性能及循环使用性能.     

氧化镁负载三聚氰胺缩甲醛高分子钯配合物催化剂催化加氢制备葡辛胺的研究

以氧化镁负载三聚氰胺缩甲醛高分子钯配合物为催化剂, 对葡萄糖与正辛胺催化加氢制备葡辛胺进行了研究. 结果表明在以60 mL乙醇为溶剂, 三乙胺为添加剂(1.0 mL), 于60 ℃的反应温度, 1.5 MPa反应氢压, 0.7 g催化剂用量下反应6 h, 37.2 mmol葡萄糖与31 mmol正辛胺催化加氢可得产率为57.6%的葡辛胺. 相对于雷内镍催化剂, 该催化剂制备简单,制备过程无污染、对环境友好,产物纯度高,并具有适当的可重复使用,因此氧化镁负载三聚氰胺缩甲醛高分子钯配合物是葡辛胺制备的良好催化剂.     

由直链聚苯乙烯制备的负载型钯催化剂的加氢性能

聚苯乙烯(PS)是匀相催化剂多相化研究中常用的高分子载体,但通常涉及的均是交联聚苯乙烯(CPS)。本文制备了不同链长的直链聚苯乙烯(LPS)负载钯催化剂(LPSN-Pd);将其与相应的交联聚苯乙烯负载的钯催化剂(CPSN-Pd)对比,考察了这类催化剂对不饱和烃类加氢反应的活性、选择性以及起始载体链长对催化刑加氢性能的影响。     

淀粉负载钯催化剂的制备及对Heck反应的催化性能

淀粉负载钯催化剂的制备及对Heck反应的催化性能;淀粉;钯;负载型催化剂;Heck反应     

高分子负载催化剂中金属流失的研究 Ⅱ．活性中心金属的影响

通过测定加氢反应后反应溶液中金属的溶出量,考察了高分子负载催化剂的稳定性,研究了活性中心金属的种类、价态及分散程度对催化剂稳定性的影响。实验表明,在聚苯乙烯苄基氨茴酸树脂载体上,不同金属物种的催化剂稳定性次序为:Pd混合价态钯>二价钯。随着载体表面钯分散度的增大,钯盐中配体En值的减小,溶剂极性的减弱,钯的流失量也呈下降趋势。     

高分子负载贵金属类催化剂及其在有机反应中的最新应用

高分子负载金属催化剂与传统的均相催化剂相比,具有较高的催化活性、立体选择性、较好的稳定性和重复使用性能,并且后处理简单,在反应完成后可方便地借助固-液分离方法将高分子催化剂与反应体系中其他组分分离、再生和重复使用,可降低成本和减少环境污染。本文综述了近五年来高分子负载贵金属类催化剂在有机反应中的最新应用,根据金属不同将其分为钌、钯、银、金四大类,并分类介绍了其在不同固相反应中的应用。本文介绍的负载贵金属类催化剂中的负载物均为不溶性聚合物,但不包括二氧化硅、可溶性聚合物和树枝状大分子等。     

有机硅聚合物负载硫、膦混合双齿钯配合物的合成与催化性能

负载型钯催化剂;混合双齿高分子配体;羰基化;芳基卤化物;聚合物;有机硅聚合物负载硫、膦混合双齿钯配合物的合成与催化性能     

Ethylene polymerization with porous polystyrene spheres supported Cp2ZrCl2 catalyst

A catalyst with porous polystyrene beads supported Cp₂ZrCl₂ was prepared and tested for ethylene polymerization with methylaluminoxane as a cocatalyst. By comparison, the porous supported catalyst maintained higher activity and produced polyethylene with better morphology than its corresponding solid supported catalyst. The differences between activities of the catalysts and morphologies of the products were reasonably explained by the fragmentation processes of support as frequently observed with the inorganic supported Ziegler–Natta catalysts. Investigation into the distribution of polystyrene in the polyethylene revealed the fact that the porous polystyrene supported catalyst had undergone fragmentation during polymerization. © 2003 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem 41: 3313–3319, 2003     

L-脯氨酸稳定的铱催化苯乙酮及其衍生物不对称加氢反应

以L-脯氨酸为稳定剂制备了负载型金属铱催化剂, 并用于苯乙酮及其衍生物不对称加氢反应. 考察了载体以及L-脯氨酸的量对催化剂性能的影响, 以透射电镜(TEM)和X射线光电子能谱(XPS)对催化剂进行了表征. 结果表明L-脯氨酸对金属铱粒子具有较好的分散和稳定作用. 通过考察反应条件发现: 碱金属离子对反应有较大影响; L-脯氨酸与手性修饰剂对催化活性和对映选择性存在一定的协同促进作用. 在手性二胺(1S,2S)-1,2- 二苯基乙二胺 ((1S,2S)-DPEN) 修饰下, 催化剂 5% (w, 质量分数)Ir/15( 脯氨酸与铱的摩尔比)(L-Proline)-γ-Al2O3催化苯乙酮不对称加氢获得了71.3%的对映选择性(ee), 2?-(三氟甲基)苯乙醇的对映选择性达到了79.8%. 该催化剂制备方法简单, 不需要膦配体做稳定剂, 催化剂性能稳定, 通过简单的离心分离可循环使用5次而无明显的活性和对映选择性降低.     

SBA-15 固载离子液体功能化脯氨酸的制备及其催化 Knoevenagel 缩合反应

 以 L-脯氨酸为原料合成了离子液体功能化脯氨酸前驱体 (IL-Pro), 并将其固载到 SBA-15 介孔分子筛上, 制得 IL-Pro/SBA-15 催化剂. 用红外光谱、热重、N2 吸附-脱附、X 射线衍射和透射电镜等手段表征了 IL-Pro/SBA-15 催化剂, 并考察了该催化剂在 Knoevenagel 缩合反应中的催化性能. 结果表明, 固载离子液体功能化脯氨酸没有破坏 SBA-15 的有序介孔结构, 但孔体积、孔径和比面表积有所下降; IL-Pro/SBA-15 的失重峰在 250~360 oC (峰值为 310 oC). 在以苯甲醛和丙二腈为底物的 Knoevenagel 反应中, IL-Pro/SBA-15 催化剂表现出较高的活性, 缩合产物收率高达 94%; 经简单分离后催化剂可重复使用 7 次以上而活性基本保持不变.     

PVP-PdCl2-CuCl2/SiO2-PEG600催化芳氯化物水相脱氯研究

PVP(聚乙烯吡咯烷酮)负载双金属催化剂催化芳香氯化物脱氯已有报道[1～3];利用双金属的协同作用,可以大大提高催化剂的脱氯活性和选择性[4]. 但是,这些研究多是在有机相中进行的,催化剂在水相中则会降低甚至失去活性,且难以回收和重复利用. 然而,难溶于水的有毒芳香氯化物,常存在于工业或生活排放的废水中. 由于治理环境的需要,研究芳香氯化物催化水相脱氯,则是极具挑战性的课题. 本文把起相转移作用的聚乙二醇(PEG)键合到硅胶上作为固相载体,制成双负载双金属水相脱氯催化剂PVP-PdCl2-CuCl2/SiO2-PEG600,成功地用于难溶于水的芳香氯化物的水相脱氯. 研究结果表明,这种催化剂对于芳香氯化物有良好的催化脱氯性能,使用中便于分离并能重复利用. 同时,用IR,TEM和XPS等手段对催化剂进行了表征,探讨了催化剂中各组分在催化脱氯中的作用.     

Synthesis of Higher Alcohols from Syngas over Alkali Promoted K-Co-Mo Catalysts Supported on Multi-walled Carbon Nanotubes

A series of carbon nanotubes-supported K-Co-Mo catalysts were prepared by a sol-gel method combined with incipient wetness impregnation.The catalyst structures were characterized by X-ray diffraction,N₂ adsorption-desorption,transmission electron microscopy and H₂-TPD,and its catalytic performance toward the synthesis of higher alcohols from syngas was investigated.The as-prepared catalyst particles had a low crystallization degree and high dispersion on the outer and inner surface of CNTs.The uniform mesoporous structure of CNTs increased the diffusion rate of reactants and products,thus promoting the reaction conversion.Furthermore,the incorporation of CNTs support led to a high capability of hydrogen absorption and spillover and promoted the formation of alkyl group,which served as the key intermediate for the alcohol formation and carbon chain growth.Benefiting from these characteristics,the CNTs supported Mo-based catalyst showed the excellent catalytic performance for the higher alcohols synthesis as compared to the unsupported catalyst and activated carbon supported catalyst.     

Supported bis(indenyl)– and bis(fluorenyl)–chromium catalysts for ethylene polymerization

Silica-supported bis(indenyl)– and bis(fluorenyl)–chromium catalysts show good activity in ethylene polymerization. For maximum productivity with the indenyl chromium catalyst, the silica must be dried, with higher dehydration temperatures giving a significant increase in polymerization activity. Less deactivation on thermal aging of the supported bis(indenyl)–chromium catalyst allows ethylene polymerization to proceed for many hours, which provides polyethylenes of low residual chromium content. In contrast to the behavior of supported chromocene catalysts, the indenyl–and fluorenyl–chromium catalysts require a higher hydrogen/ethylene ratio to achieve a specific polymer melt index. Nevertheless, highly saturated polyethylenes are produced with these new catalysts. This result indicates that chain transfer to hydrogen remains the major chain transfer reaction. Addition of cyclopentadiene to a supported indenyl–chromium catalyst provided a catalyst with a much higher transfer response to hydrogen. This result suggests that ligand exchange occurred, producing a supported chromocene catalyst. These overall results are consistent with an active-site model which comprises a supported divalent chromium center attached to an indenyl or fluorenyl ligand during the polymerization process. Polymerization is believed to occur by a coordinated anionic mechanism of the type previously discussed for a supported chromocene catalyst.     

微波辅助催化氧化苯高性能催化剂实验研究

采用传统浸渍法制备分子筛负载过渡金属和稀土元素催化剂,通过微波辅助催化氧化苯性能实验考察其催化活性。研究表明,天津科密欧的5A分子筛为优良的催化剂载体,分子筛负载铜-锰-铈催化剂对苯的完全燃烧温度为230℃,铜(Cu)锰(Mn)双金属催化剂中晶相与非晶相Cu_1.5Mn_1.5O₄尖晶石提高了催化剂的催化活性,稀土铈(Ce)的助催化效果显著;30 h的连续性实验表明,Cu-Mn-Ce/分子筛催化剂具有良好的稳定性和高的催化活性。催化剂的比表面积和表面形貌表征表明,催化剂比表面积和孔径受高温煅烧和氧化反应而增大,从而有助于苯的吸附与氧化降解;X射线衍射表明,实验前后分子筛结构未发生明显变化,铜锰主要以二价和三价的氧化物形态分布于催化剂表面。     

Selective Hydrogenation of Citral over a Carbon‐titania Composite Supported Palladium Catalyst

A novel carbon‐titania composite material, C/TiO₂, has been prepared by growing carbon nanofibers (CNFs) on TiO₂ surface via methane decomposition using Ni‐Cu as a catalyst. The C/TiO₂ was used for preparing supported palladium catalyst, Pd/C/TiO₂. The support and Pd/C/TiO₂ catalyst were characterized by BET, SEM, XRD and TG‐DTG. Its catalytic performance was evaluated in selective hydrogenation of citral to citronellal, and compared with that of activated carbon supported Pd catalyst. It was found that the Pd/C/TiO₂ catalyst contains 97% of mesopores. And it exhibited 88% of selectivity to citronellal at citral conversion of 90% in citral hydrogenation, which was much higher than that of activated carbon supported Pd catalyst. This result may be attributed to elimination of internal diffusion limitations, which were significant in activated carbon supported Pd catalyst, due to its microporous structure.     

Novel Ru - K/Carbon Nanotubes Catalyst for Ammonia Synthesis

Since 1970s alkali metal-promoted ruthenium was found to be an active catalyst forammonia synthesis under atmospheric pressure, ruthenium catalysts come to beconsidered as a second-generation-catalyst for ammonia synthesis after the iron-basedcatalyst'-=. We have reported the activity of ammonia synthesis of ruthenium-basedcatalysts on various supports previously and found that fullerene was the best support'.Recently, we used the carbon nanotubes, which have metallic or semiconductingproperti…     

New Rh—ZnO／Carbon Nanotubes Catalyst for Methanol Synthesis

A new catalyst for methanol synthesis,ZnO-promoted rhodium supported on carbon nanotubes,was developed.It was found that the Rh-ZnO/CNTs catalyst had high activity of 411.4mg CH3OH/g/cat/h and selectivity of 96.7% for methanol at 1 MPa and 523 K.The activity of this catalyst is much higher than that of NC 207 catalyst at the same reaction conditions.It was suggested that the multi-walled strueture CNTs favored both the couple transfer of the proton and clectron over the surface of the catalyst and the uptake of hydrogen which was favorable to methanol synthesis.