负载型铜系分子筛催化剂在苯酚羟基化反应中的应用

以介孔分子筛MCM-41、MCM-48和AIMCM-41以及微孔分子筛Naβ和MOR为载体,分别采用有机官能团化法和分步水热合成法制备了系列负载型催化剂,考察了其在苯酚羟基化反应中的活性;得到了不同载体类型、不同负载方法及不同助剂与反应活性的对应关系．结果表明：以微孔分子筛为载体的催化剂对副产物有明显的抑制作用．介孔分子筛AIMCM-41,MCM-41,MCM--48为载体时,催化剂在苯酚羟基化反应中的活性顺序为AIMCM-41〉MCM-48〉MCM-41,助剂镧和钴的引入可以有效抑制副产物的产生．     

介孔分子筛MCM-41表面的有机胺功能化及其应用

采用γ-胺丙基三甲氧基硅烷与表面硅羟基的反应,对介孔分子筛MCM-41进行了有机胺功能化.并对其进行了表征.XRD、比表面积测定、元素分析、TG、FT-IR和TEM的测定结果均表明,MCM-41表面成功地接枝上了有机胺功能基团而六方结构特征基本保持.在有机胺功能化的MCM-41上固载Ru基催化剂,并将其用于CO2加H2合成HCOOH反应,所显示的活性优于相应的均相催化剂,并且该催化剂具有较好的回收再用性能.     

MCM-41负载手性Salen-Mn(Ⅲ)配合物的制备及其对不对称环氧化的催化性能

 三乙氧基硅丙胺与介孔分子筛MCM-41表面的羟基在甲苯中回流反应得到氨丙基官能团化的MCM-41, 再利用氨基与Salen-Mn(Ⅲ)上的活性酯基生成酰胺键,将手性Salen-Mn(Ⅲ)配合物负载到MCM-41上,实现了手性均相催化剂的多相化. 分别利用FT-IR, DR UV-Vis, XRD, ICP和N2吸附等手段对负载型催化剂进行了表征. 结果表明,手性Salen-Mn(Ⅲ)配合物成功负载到MCM-41上,但MCM-41和手性Salen-Mn(Ⅲ)配合物固有的结构保持不变. 以次氯酸钠和间氯过氧苯甲酸为氧化剂,考察了负载型催化剂对1,2-二氢萘不对称环氧化反应的催化性能,结果表明,负载型催化剂的催化活性比相应均相催化剂的低,但对映体选择性有所提高. 在NaClO/PyNO氧化剂体系中20 ℃反应12 h, 1,2-二氢萘环氧化物的收率达45.9%, 对映体过量值为84.3%. 负载型催化剂在循环使用5次后Mn的流失达34%.     

乙二胺基和2，4-戊二酮官能化介孔分子筛固载钼（Ⅵ）：新型的环己烯环氧化催化剂

通过对介孔分子筛HMS和MCM-41表面修饰，将乙二胺基和2，4-戊二酮引入到介 孔分子筛孔道内，制备出乙二胺基和戊二酮官能化介孔分子筛。首次将烯烃环氧化 均相催化剂MoO_2(acac)_2固载到乙二胺基和戊二酮官能化介孔分子筛孔道内，制 备出新型的、易回收、可重复使用的烯烃环氧化多相催化剂。环已烯催化环氧化表 明，该催化剂的催化活性与均相催化剂MoO_2(acac)_2相当，选择性大于80%。     

AlCl3/MCM-41催化剂上桥式四氢双环戊二烯异构化反应

 分别采用介孔 MCM-41 和 SiO2 为载体制备了固载化 AlCl3 催化剂, 考察了其催化桥式四氢双环戊二烯异构化生成挂式四氢双环戊二烯反应性能. 结果表明, 180 °C 时 AlCl3/MCM-41 催化剂上挂式四氢双环戊二烯选择性可达 95.7%, 而在 AlCl3/SiO2 上仅为 86.3%. 采用 N2 吸附-脱附、Hammett 指示剂法、吡啶吸附红外光谱和化学分析等方法对催化剂进行了表征. 结果表明, AlCl3/MCM-41 催化剂较弱的表面酸性和一维孔结构有利于挂式四氢双环戊二烯的生成.     

苯基化纳米MCM-41材料的制备与表征

以苯基三甲氧基硅烷为偶联剂对纳米MCM-41分子筛进行了有机改性,制备了苯基改性的纳米MCM-41分子筛MCM-41(m)。利用元素分析、粉末XRD、傅里叶变换红外光谱、氮气吸附-解吸附、扫描电镜和差热-热重分析对制备产物进行了表征。粉末XRD结果表明,改性过程中,分子筛骨架未被破坏,并且所制备MCM-41(m)分子筛结晶度依然很高;傅里叶变换红外光谱表明苯官能团已经成功地接枝到了分子筛的孔道表面,且所得产物的骨架依然完好;低温氮气吸附-解吸附分析结果表明,MCM-41(m)分子筛孔道具有高度有序性,改性的纳米MCM-41分子筛孔道内的硅羟基与苯基三甲氧基硅烷发生了硅烷化反应,苯基成功地接枝到了分子筛的孔道表面。扫描电镜结果表明, 制得的苯基改性纳米MCM-41平均尺寸为110 nm。差热-热重分析结果说明了所制备的苯基化的纳米MCM-41样品具有良好的热稳定性,骨架稳定温度为823 ℃。苯基化的纳米MCM-41材料具有作为催化剂材料的潜在应用前景。     

杂化材料Eu(Phen)2Cl3/MCM-41的荧光性能及热稳定性研究

采用超声波辅助,将稀土配合物Eu(Phen)2Cl3装入中孔分子筛MCM-41孔道,合成了不同组装量的杂化材料Eu(Phen)2Cl3/MCM-41。运用XRD、N2吸附-脱附、FTIR、荧光光谱等手段对杂化材料进行了表征,研究表明稀土配合物已进入分子筛孔道,且随着配合物嵌入量的增加,杂化材料的荧光发射也逐渐增强。当Eu(Phen)2Cl3的组装量达到饱和(7.17%)时,其荧光强度最大。与纯配合物Eu(Phen)2Cl3相比,Eu(Phen)2Cl3/MCM-41的热稳定性提高了约100°C。     

MCM-41-HY复合分子筛的合成及其在深度加氢脱硫中的应用

在水热条件下合成了包覆型MCM-41-HY复合分子筛.采用XRD、N2气吸附和SEM等方法对其进行了表征.结果表明,MCM-41-HY复合分子筛和MCM-41与H型Y沸石(HY)的机械混合物明显不同,在复合分子筛MCM-41-HY中,中孔相MCM-41附晶生长在HY沸石上,将HY包覆起来.以二苯并噻吩为模型化合物,考察了该材料担载NiMo催化剂的加氢脱硫活性.结果表明,MCM-41-HY复合分子筛与MCM-41和HY的机械混合物担载NiMo催化剂的加氢脱硫(HDS)活性相当,但MCM-41-HY复合分子筛担载NiMo催化剂的裂化活性较低.其裂化活性不同的原因在于其载体孔道结构和酸性位的分布不同.     

通过接枝苄基磺酸在MCM-41上固载手性Mn(salen)配合物

首先通过两步后合成处理,在MCM-41上接枝苄基磺酸;然后,以苄基磺酸为过渡产物,用手性Mn(salen)配合物修饰处理,得到了苄基磺酸轴向负载手性Mn(salen)配合物的MCM-41;实现了在廉价且温和条件下均相手性Mn(salen)催化剂的非均相化。采用X射线衍射(XRD)、低温N₂吸附-脱附、红外光谱、热重-差示扫描量热(TG-DSC)分析、电感耦合等离子体发射光谱(ICP)和酸度滴定等对样品进行了表征。结果表明,手性Mn(salen)配合物成功固载在MCM-41上,且MCM-41的介孔结构和Mn(salen)配合物的手性特征仍然保留。以间氯过氧苯甲酸为氧化剂,考察了所得固载型催化剂对α-甲基苯乙烯的不对称环氧化催化性能,结果表明在0 ℃反应2 h,催化剂用量为0.02 mmol,无需加入轴向配体N-甲基吗啉氮氧化物(NMO)的条件下对映体过量(enantiomeric excess,e.e.)值可达99%以上,转化率为77%。归因于苄基磺酸基起到了很好的轴向配体作用。经适当处理,固载型催化剂在循环使用5次后e.e.值依然有71%,表现出较好的活性和重复使用性能。     

通过接枝苄基磺酸在MCM-41上固载手性Mn(salen)配合物

首先通过两步后合成处理,在MCM-41上接枝苄基磺酸;然后,以苄基磺酸为过渡产物,用手性Mn(salen)配合物修饰处理,得到了苄基磺酸轴向负载手性Mn(salen)配合物的MCM-41;实现了在廉价且温和条件下均相手性Mn(salen)催化剂的非均相化。采用X射线衍射(XRD)、低温N2吸附-脱附、红外光谱、热重-差示扫描量热(TG-DSC)分析、电感耦合等离子体发射光谱(ICP)和酸度滴定等对样品进行了表征。结果表明,手性Mn(salen)配合物成功固载在MCM-41上,且MCM-41的介孔结构和Mn(salen)配合物的手性特征仍然保留。以间氯过氧苯甲酸为氧化剂,考察了所得固载型催化剂对α-甲基苯乙烯的不对称环氧化催化性能,结果表明在0℃反应2 h,催化剂用量为0.02 mmol,无需加入轴向配体N-甲基吗啉氮氧化物(NMO)的条件下对映体过量(enantiomeric excess,e.e.)值可达99%以上,转化率为77%。归因于苄基磺酸基起到了很好的轴向配体作用。经适当处理,固载型催化剂在循环使用5次后e.e.值依然有71%,表现出较好的活性和重复使用性能。     

PtSn/Al2O3/MCM-41催化剂的丙烷脱氢催化性能

用微型催化反应装置评价, 并结合X射线粉末衍射(XRD)、表面积和孔结构测试、程序升温还原(TPR)、氢化学吸附和热重分析等方法研究了负载型PtSn/γ-Al2O3, PtSn/MCM-41和PtSn/Al2O3/MCM-41催化剂的丙烷脱氢反应催化性能. 发现PtSn/Al2O3/MCM-41催化剂具有较PtSn/MCM-41催化剂高的丙烷脱氢反应活性和较PtSn/γ-Al2O3催化剂高的反应稳定性. 实验结果表明, 纯硅MCM-41载体表面的锡物种因与载体相互作用较弱故易被还原, 导致铂金属分散度和催化剂的丙烷脱氢活性较低. 用Al2O3修饰MCM-41可以增强Sn物种与Al2O3/MCM-41载体之间的相互作用, 提高PtSn/Al2O3/MCM-41催化剂铂金属分散度和丙烷脱氢催化活性. 并且, 积炭后的PtSn/Al2O3/MCM-41催化剂具有较高的铂金属表面裸露度, 故具有较高的丙烷脱氢反应稳定性. PtSn/Al2O3/MCM-41催化剂优良的丙烷脱氢催化性能可能不仅与Sn-载体Al2O3/MCM-41较强的相互作用有关, 而且与Al2O3/MCM-41载体的介孔结构有关.     

过渡金属改性MCM-41的结构及对苯催化氧化的研究

制备了Ti,Fe,Cr,Ni改性的MCM-41,采用XRD、低温N₂吸附及TPD手段研究了改性MCM-41的结构特征和表面性质.过渡金属可同品取代骨架Si,同品取代的能力与过渡金属离子半径有关.过渡金属改性MCM-41均具有较好的长程有序结构、均一的孔径分布和较高的比表面积.引入不同的过渡金属可以改变MCM-41表面酸性和亲水/憎水性.考察了改性MCM-41对苯氧化的催化性能.     

Influence of the pore structure of MCM-41 and SBA-15 silica fibers on atomic layer chemical vapor deposition of cobalt carbonyl

Mesoporous high surface area MCM-41 and SBA-15 type silica materials with fibrous morphology were synthesized and used as support materials for the ALCVD (atomic layer chemical vapor deposition) preparation of Co/MCM-41 and Co/SBA-15 catalysts. Co/MCM-41 and Co/SBA-15 catalysts were prepared by deposition of Co2(CO)8 from the gas phase onto the surfaces of preheated support materials in a fluidized bed reactor. For both silica materials, two different kinds of preparation methods, direct deposition and a pulse deposition method, were used. Pure silica supports as well as supported cobalt catalysts were characterized by various spectroscopic (IR) and analytical (X-ray diffraction, Brunauer-Emmett-Teller, elemental analysis) methods. MCM-41 and SBA-15 fibers showed considerable ability to adsorb Co2(CO)8 from the gas phase. For MCM-41 and SBA-15 silicas, cobalt loadings of 13.7 and 12.1 wt % were obtained using the direct deposition method. The cobalt loadings increased to 23.0 and 20.7 wt % for MCM-41 and SBA-15 silicas, respectively, when the pulse deposition method was used. The reduction behavior of silica-supported cobalt catalysts was found to depend on the catalyst preparation method and on the mesoporous structure of the support material. Almost identical reduction properties of SBA-15-supported catalysts prepared by different deposition methods are explained by the structural properties of the mesoporous support and, in particular, by the chemical structure of the inner surfaces and walls of the mesopores. Pulse O2/H2 chemisorption experiments showed catalytically promising redox properties and surface stability of the prepared MCM-41- and SBA-15-supported cobalt catalysts.     

Oxime carbapalladacycle covalently anchored to high surface area inorganic supports or polymers as heterogeneous green catalysts for the Suzuki reaction in water

An oxime carbapalladacycle known as an extremely active homogeneous catalyst for the Suzuki coupling in water has been conveniently modified and anchored on high surface area SiO(2), MCM-41, and polystyrene-divinylbenzene and ethylenglycol dimethylacrylate polymers. The resulting solids were characterized by analytical and spectroscopic (UV-vis and IR) techniques and tested as catalysts for the reaction of 4-chloroacetophenone with phenylboronic acid in water, dioxane, and a mixture of both. Differences in activity depending on the support were remarkable, the palladium complex being more active for the reactions in water when supported on SiO(2) or MCM-41. The catalysts were truly heterogeneous (no leached palladium) and when anchored on SiO(2) were reused seven times without loosing activity. Palladium complex anchored in SiO(2) was also tested as Suzuki catalyst for a wide range of bromo-, chloro-, and even fluoroaromatics.     

Encapsulation of a chiral MnIII(salen) complex in ordered mesoporous silicas: an approach towards heterogenizing asymmetric epoxidation catalysts for non-functionalized alkenes

Two immobilized chiral Mn^III(salen) complexes covalently anchored on modified MCM-41 (50 Å) and SBA-15 (75 Å) were prepared using 3-aminopropyltriethoxysilane as a reactive surface modifier to afford comparable or even higher enantioselectivity than homogeneous catalysts for the enantioselective epoxidation of a series of smaller to bulkier alkenes. The catalyst immobilized in silica with larger pore diameters was found to be more active. Compared to homogeneous catalysts, the heterogenized catalysts are more stable and can be recycled four times with retention of enantioselectivity.     

Carbonylation of Alkynes,Alkenes and Alcohols using Metal Complex Catalysts

Carbonylation of olefins, alcohols and halides using homogeneous as well as heterogeneous catalysts has been discussed. Highlights of contributions on the activity, selectivity and stability of catalysts for carbonylation reactions are discussed. Kinetics and mechanism including characterization of the intermediate catalytic species has also been reviewed. The performance of anchored Pd complexes on mesoporous supports (MCM-41 and MCM-48), water soluble Pd complexes and supported Pd catalysts in carbonylation of aryl alcohols and olefins has been discussed in the context of catalyst-product separation. Some aspects of kinetic modelling and reaction engineering of these multiphase catalytic reactions have also been reviewed.     

载体性质对Pd催化剂加氢脱硫性能的影响

以Si O2、全硅MCM-41(Si-MCM-41)、通过机械混合Si-MCM-41与ZSM-5得到的Z-MCM-41-M以及通过在ZSM-5外部包覆MCM-41制备得到的Z-MCM-41四种材料为载体,制备了四种负载型Pd催化剂。采用XRD、HRTEM、N2吸附-脱附、NH3-TPD手段对Pd催化剂进行了表征;以二苯并噻吩(DBT)为模型化合物,在固定床反应器上对四种催化剂的加氢脱硫(HDS)活性、加氢路径选择性和加氢裂化活性进行了考察,研究了不同类型载体对Pd催化剂加氢脱硫性能的影响。结果表明,载体的性质会显著影响负载型Pd催化剂的加氢脱硫性能。载体的比表面积对负载型Pd催化剂加氢脱硫活性影响不大,但是HYD路径的选择性与载体的孔道结构有关;具有介孔孔道结构有利于加氢路径选择性的提高。酸性载体负载的Pd催化剂表现出较好加氢脱硫活性和加氢选择性,这与氢溢流有关。介孔材料的孔道结构与微孔沸石的酸性有机结合,所得到的Z-M CM-41复合材料是是潜在的贵金属Pd加氢脱硫催化剂优良载体,可有效提升其加氢脱硫活性。     

Dicyano-functionalized MCM-41 anchored-palladium complexes as recoverable catalysts for Heck reaction

Palladium(II,0) complexes were anchored on dicyano-functionalized MCM-41, producing new heterogeneous catalysts of the Heck reaction, which were synthesized via two-step surface modification of mesoporous molecular sieve MCM-41. The developed catalysts demonstrated easy separation after reaction, and reusability. BET, XRD, FT-IR, ICP-AES, H₂ chemisorption as well as XPS techniques were employed to characterize the catalytic materials.     

Comparison of Ta–MCM-41 and Ti–MCM-41 as catalysts for the enantioselective epoxidation of styrene with TBHP

Chiral Ti–MCM-41 and Ta–MCM-41 catalysts have been prepared by grafting of Ti(OⁱPr)₄ and Ta(OEt)₅ and the modification with R-(+)-diethyl l-tartrate or R-(+)-diisopropyl l-tartrate. In general, the solid catalysts are more active and selective than their homogeneous counterparts in the epoxidation of styrene with tert-butyl hydroperoxide. The enantioselectivities depend on both the nature of the chiral ligand and the calcination temperature of the support, as it is supposed this controls the type of surface species that are formed. The best result of 71% ee is obtained with DIPT–Ta–MCM₅₅₀ and is the first example of the use of a Ta catalyst for the enantioselective epoxidation of unfunctionalized alkenes. Nonetheless, the recovered Ta catalysts are less active and selective.