溶剂对丙烯环氧化反应活性的影响

研究了溶剂对钛硅分子筛催化丙烯环氧化反应的影响．研究结果表明，随着溶剂极性增加，活性中间过渡态中的过氧键越易断裂，容易把氧原子传递给丙烯，因此丙烯环氧化反应活性增加．由于TS—1催化剂孔道狭小，产生空间位阻效应，醇溶剂分子越大，活性中间过渡态的形成越困难，反应活性越低．甲醇-丙醇混合溶剂中丙酮含量小于50％时，反应活性与纯甲酵做溶剂相近；混合溶剂中丙酮含量增加到80％时，反应活性略降低；丙酮含量进一步增加，反应活性急剧下降．     

等级孔介孔-微孔TS-1分子筛单晶的合成及催化氯丙烯环氧化性能

针对当前钛硅型分子筛存在的微孔孔道孔径限制导致的流通扩散性能差及催化效率低等关键瓶颈问题, 通过在微孔分子筛中构筑跨尺度贯通高物质传输性能的等级孔道结构, 对钛硅分子筛(TS-1)晶体内等级孔道结构的可控构筑及其催化环氧化进行了研究, 成功制备出具有富含介孔孔道的等级孔介孔-微孔TS-1分子筛单晶材料(HTS-1), 其在氯丙烯催化环氧化反应中表现出了优异的催化活性及稳定性能.     

钛硅分子筛TS-1催化氯丙烯环氧化反应动力学研究

 摘要：研究了钛硅分子筛催化氯丙烯环氧化反应的条件及动力学行为．\r\n结果表明，以钛硅分子筛为催化剂，氯丙烯可被高选择性地氧化为环氧\r\n氯丙烷．环氧化反应速度与分子筛中骨架钛的含量及分子筛的用量呈正\r\n比关系，是一级反应．对于氧化剂H2O2，只有当c（H2O2）＜0．4mol／\r\nL时，环氧化反应为一级反应；而c（H2O2）＞1．0mol／L时，为零级反\r\n应．对于氯丙烯，随着其浓度的变化，环氧化反应的级数在1和0之间．\r\n然而，只有当氯丙烯浓度很高时，环氧化反应的级数才有明显的降低．\r\n根据实验结果和Eley－Rideal单分子吸附方程，提出了氯丙烯环氧化反\r\n应的动力学模型．\r\n关键词：钛硅分子筛，氯丙烯，过氧化氢，环氧化，环氧氯丙烷，反应\r\n动力学     

Novel method for synthesis of titanium silicalite-1 (TS-1)

Titanium silicalite-1 (TS-1) was easily synthesized using inorganic silicon and titanium source, tetrapropylammonium bromide (TPABr) or TPAOH as templating molecule, NH3· H2O, HDA or TEAOH etc. as base sources. In this system, TPA cations (come from TPABr or TPAOH) served as tern-plating agents to direct the MFI structure. NH3H2O, TEAOH or HDA etc. provides the alkalinity necessary for crystallization. X-ray diffraction, UV-Vis, ER spectroscopies, SEM, 29 Si MAS NMR showed that the zeolites obtained possessed all the structural characteristics of TS-1, and titanium atoms were introduced into the framework in TS-1. This material was proved to have high crystallinity and high catalytic activity to allyl chloride epoxidation and propylene epoxidation. All the samples synthesized had similar catalytic properties with a standard TS-1 through compared inorganic reactant system with organic synthesis system using propylene epoxidation. The effects of silicon source and TPABr/SiO2 ratio were discussed.     

钛硅分子筛催化1-丁烯环氧化研究

自1983年Taramasso等报导TS-1的合成以来,钛硅分子筛的合成及应用一直是分子筛催化领域的热点。经典TS-1合成方法采用四丙基氢氧化铵（TPAOH）为模板剂,合成成本较高、条件苛刻,限制了其应用。用四丙基溴化铵（TPABr）为模板剂代替TPAOH,能够成功地合成TS-1。不同孔道结构的钛硅分子筛,如Ti-β、Ti-MCM-41、Ti-HMS等弥补了TS-1较小孔径的缺点,进一步扩大了钛硅分子筛的应用。本文以不同合成方法得到的TS-1及中孔Ti—HMS为催化剂,双氧水为氧化剂,1-丁烯环氧化合成1,2-环氧丁烷,研究了不同钛硅分子筛对1-丁烯环氧化反应的催化性能。     

钛硅分子筛催化1-丁烯环氧化反应溶剂效应和酸碱效应研究

研究了用双氧水为氧化剂，钛硅分子筛TS-1催化1-丁烯环氧化反应的溶剂效应．研究发现，在质子性溶剂中1-丁烯环氧化反应活性高于非质子性溶剂，而以甲醇为溶剂H2O2转化率最高．分别利用碱性添加物稀氨水溶液和酸性添加物稀盐酸溶液调变反应介质的pH值，考察了介质的pH值对1-丁烯环氧化反应的影响，结果表明，随pH值提高，1，2-环氧丁烷(B0)的选择性略提高，但是过量稀氨水的加入会导致催化剂失活，双氧水的转化率及利用率明显下降．与钛硅分子筛催化丙烯环氧化相比，酸性添加物的加入对反应结果的影响不大，随反应介质的pH值降低1，2-环氧丁烷的选择性没有明显下降．     

A quantum chemical study of comparison of various propylene epoxidation mechanisms using H2O2 and TS-1 Catalyst

We present a comparison of the following prominent propylene epoxidation mechanisms using H2O2/TS-1 at a consistent density functional theory (DFT) method: (1) the Sinclair and Catlow mechanism on tripodal site through Ti-OOH species, (2) the Vayssilov and van Santen mechanism on tetrapodal site without Ti-OOH formation, (3) the Munakata et al. mechanism involving peroxy (Ti-O-O-Si) species, (4) the defect site mechanism with a partial silanol nest, and (5) the defect site mechanism with a full silanol nest. We have reproduced the previously published (ethylene epoxidation) pathways (1-3) for propylene epoxidation using larger and SiH3-terminated cluster models of the T-6 crystallographic site of TS-1. Mechanism 5 is a new mechanism reported here for the first time. The use of a consistent level of theory for all the pathways allows for the first time a meaningful comparison of the energetics representing the aforementioned pathways. We have rigorously identified the important reaction intermediates and transition states and carried out a detailed thermochemical analysis at 298.15 K and 1 atm. On the basis of the Gibbs free energy of activation, the Sinclair and Catlow mechanism (Delta G(act) = 7.9 kcal/mol) is the energetically most favorable mechanism, which is, however, likely to operate on the external surface of TS-1 due to the tripodal nature of the Ti site in their model. The newly reported defect site mechanism (with a full silanol nest) is a competitive propylene epoxidation mechanism. There are two main steps: (1) hydroperoxy formation (Delta G(act) = 8.9 kcal/mol) and (2) propylene epoxidation (Delta G(act) = 4.6 kcal/mol). This mechanism is likely to represent the chemistry occurring inside the TS-1 pores in the liquid-phase epoxidation (H2O2/TS-1) process and could operate in direct gas-phase epoxidation (H2/O2/Au/TS-1) as well. If only the propylene epoxidation step is considered, then the Munakata peroxo intermediate (Si-O-O-Ti) is the most reactive intermediate, which can epoxidize propylene with a negligible activation barrier. However, formation of the Munakata intermediate is a very activated step (Delta G(act) = 19.8 kcal/mol). We also explain the trends in the activation barriers in different mechanisms using geometric and electronic features such as orientation of adsorbed H2O2 and propylene, hydrogen bonding, O1-Ti bond distance in the Ti-O1-O2-H intermediate, and O1-O2 stretching in the transition state. Implications of different Ti site models are also discussed in light of the nature of external/internal and nondefect/defect sites of TS-1.     

钛硅分子筛TS-1的快速合

quick synthesis, titanium silicalite-1, anatase titania, propylene, epoxidation, hydrogen peroxide     

TS-1 zeolite microengineered reactors for 1-pentene epoxidation

A zeolite-based microengineered reactor was fabricated and tested for 1-pentene epoxidation over titanium silicalite-1 (TS-1) catalyst, which has been selectively incorporated within the microreactor channel using a new synthesis procedure.     

Highly stereoselective epoxidation of O-protected 3-hydroxy-1-nitroalkenes

The diastereoselectivity of the nucleophilic epoxidation of O-protected 3-hydroxy-1-nitroalkenes was investigated. Epoxidation of the O-protected 3-hydroxy-1-nitroalkenes was highly stereoselective, giving rise to the anti isomer. The resulting nitroepoxides have been transformed into nitroaldols through hydrogenation. The nucleophilic epoxidation of nitroalkenes was found to be irreversible. Models to explain the observed stereoselectivities are proposed.     

无机钛硅原料体系合成TS-1催化丙烯环氧化反应

研究了无机钛硅原料体系合成的ＴＳ－１催化丙烯环氧化的反应,并与经典法、修正法制得样品的催化性能进行了比较。考察了搅拌、Ｎａ２ＣＯ３加入量、反应时间、反应温度、双氧水加量、催化剂量及溶剂等对丙烯环氧化反应的转化率、选择性等的影响,并初步探讨了无机钛硅原料合成的ＴＳ－１的再生性能。结果表明,对于丙烯环氧化反应,无机钛硅原料合成ＴＳ－１样品与经典法和修正法制取样品的催化性能相当;反应条件对丙烯环氧化反应     

Stereoselective synthesis of 2,3-difunctionalised thioesters using nucleophilic epoxidation of 1-arylthio-1-nitroalkenes

Stereoselective nucleophilic epoxidation of protected 3-amino and 3-hydroxy-substituted 1-arylthio-1-nitroalkenes, followed by intramolecular capture involving the amino and hydroxyl protecting groups, has led to the formation of isomeric oxazolidinones 5 and 7, and a cyclic carbonate 11. Together with the oxazolidinone precursor anti-alpha-bromo thioester 15a, the absolute and relative stereochemistry of these compounds has been determined by X-ray crystallography.     

Kinetic study of hydroperoxide epoxidation of 1‐octene in the presence of molybdenum disilicide as a catalyst in a low concentration range of olefin

The kinetic regularities of the influence of low 1‐octene concentrations on its epoxidation by tert‐butyl hydroperoxide in the presence of molybdenum disilicide (MoSi₂) as a catalyst were investigated. The minimum in the dependence of the initial rate of hydroperoxide consumption on 1‐octene concentration was observed. The kinetic scheme of epoxidation, which includes the competition between hydroperoxide and olefin for the catalytic active centers, was proposed. The equation for the reaction rate was derived according to the kinetic scheme. The kinetic parameters of epoxidation were calculated. © 2009 Wiley Periodicals, Inc. Int J Chem Kinet 41: 623–628, 2009     

丙烯环氧化反应中TS-1催化剂失活研究

采用丙烯气相进料，在预混段中先与双氧水的甲醇溶液混合后进入固定床反应器，考察了进料液中pH值、丙二醇单甲醚、乙硫醇以及铁锈等对丙烯环氧化连续反应中TS-1分子筛催化剂性能的影响。结果表明，进料液体pH值对催化剂的催化性能有影响，适宜的进料液体pH值在7左右；副产物丙二醇单甲醚含量的增加不会对催化剂性能产生影响；乙硫醇量的增加使环氧丙烷选择性下降，但不会引起催化剂的失活；而进料液体中铁锈的引入会导致催化剂中部分孔堵塞，使催化剂部分失活。当进料液中的pH值用0.1mol/L的氨水调节为7左右，在反应温度55℃,反应压力0.7MPa，TS-1催化剂具有较好的稳定性，经130h的连续试验考察，双氧水的转化率和环氧丙烷的选择性约为90%。     

Synthesis and solution conformational analysis of 2,3-anhydro-3-C-[(1R)-2,6-anhydro-1-deoxy-1-fluoro-D-glycero-D-gulo-heptitol-1-C-yl]-beta-D-gulo-furanose: first example of a monofluoromethylene-linked C-disaccharide.

Condensation of 2,3,4,6-tetra-O-benzyl-beta-D-glucopyranosylcarbaldehyde with isolevoglucosenone induced by Et(2)AlI, followed by epoxidation, gave an aldol that was fluorinated into a monofluoromethylene C-glucopyranoside that was converted into the title C-disaccharide 1. Its conformational behavior in water has been studied by using a combination of NMR spectroscopy (J and NOE data) and molecular mechanics calculations.     

Biphasic epoxidation of 1-octene with H2O2 catalyzed by amphiphilic fluorinated Ti-loaded zirconia

A series of amphiphilic fluorinated zirconia containing titanium was prepared by titanium impregnation followed by fluorination and alkylsilylation of zirconium oxide. Physical properties of the resulting samples were characterized by XRD analysis, UV-vis spectroscopy, BET surface area analysis and EDAX analysis. The effects of fluorine and alkylsilane groups on the samples were studied by the epoxidation of 1-octene with aqueous hydrogen peroxide. The epoxidation of alkenes is one of the most important methods of functionalizing simple hydrocarbons. The amphiphilic fluorinated catalysts were more active and more efficient than the conventional titania-silica and zirconia-silica mixed oxides in linear alkene epoxidation; enhanced by the presence of alkylsilane and fluorine groups in the catalysts. Modification with alkylsilane successfully induces the hydrophobic behavior of zirconia which is hydrophilic in nature; whereas fluorine was chosen for its electron-withdrawing effect which further activates the titanium active sites.     

合成条件对TS-1结构及其催化氯丙烯环氧化的影响

采用水热法合成了TS-1分子筛，根据XRD、FT-IR、FT-Raman和UV-Vis的表征结果计算了TS-1的相对结晶度和骨架钛相对含量，并以氯丙烯环氧化反应为探针反应，研究了合成条件对TS-1的结构和催化性能的影响，结果表明，TS-1的结晶度随合成液中Si／Ti比和TPAOH／Si比的增大呈先增大后减小的趋势，TS-1的骨架钛相对含量也随合成液中钛含量的减少呈先增大后减小的趋势，随TPAOH含量的增加TS-1的骨架钛相对含量和非骨架钛含量一直增加，且非骨架钛的类型有所改变．具有较高结晶度和骨架钛含量及较低非骨架钛含量的TS-1的催化性能较好．较好的氯丙烯的转化率和环氧氯丙烷的选择性分别为92．1％和87．5％．     

碱金属碳酸盐改性对Au/TS-1催化剂的丙烯气相环氧化活性和稳定性的提升作用研究

制备了不同碱金属碳酸盐（Na₂CO₃、K₂CO₃、Rb₂CO₃和Cs₂CO₃）超声浸渍改性的Au/TS-1催化剂，采用XRD、ICP、XPS、UV-vis、NH₃-TPD、FT-IR和HAADF-STEM等手段对催化剂结构性质进行了表征，研究了碱金属碳酸盐改性对Au/TS-1催化剂的丙烯气相环氧化活性和稳定性的影响。结果表明，碱金属碳酸盐改性可以降低Au/TS-1催化剂的表面酸性，减缓环氧丙烷（PO）在催化剂表面吸附引起的积炭失活，抑制金颗粒粒径的增大；此外，Cs₂CO₃和Rb₂CO₃改性还可减少Au/TS-1催化剂上的骨架外Ti含量。碱金属碳酸盐改性后的Au/TS-1的催化活性和稳定性都得到明显的改善，其中，Cs₂CO₃改性的Au/TS-1表现出最佳的催化活性，丙烯转化率为6.2%，环氧丙烷选择性为86.2%，氢气利用效率为26.2%。相关研究为提高Au/TS-1催化剂的丙烯气相环氧化活性和稳定性提供了新的思路。     

多级孔TS-1用于油酸甲酯高效绿色环氧化

当今时代,资源短缺、环境污染等问题日益严峻,生物质资源化学转化利用成为各国研究重点,以生物质资源代替化石资源、以生物基材料代替石化材料,为发展绿色经济、循环经济奠定了基础.植物油资源由于其广泛的可获得性、固有的生物可降解性、低成本及突出的环境效益受到广泛关注.其中,环氧化的植物油作为可再生原材料应用于生产热塑材料的增塑剂和稳定剂、生物润滑油、涂料、粘合剂、化妆品及各种聚合物材料 (聚酯、聚氨酯、聚酰胺等).目前,工业上生产环氧化植物油通常采用 Prilezhaev 过程,即在无机强酸如 H2SO4,HCl,HNO3等的催化作用下,过氧化氢与甲酸或乙酸作用原位生成过氧甲酸或过氧乙酸作为环氧化试剂用于环氧化反应.但就该反应过程而言,强酸的存在会带来一系列问题:(1) 强酸的存在容易引发一系列副反应,如环氧环开环生成二醇、二聚物等; (2) 产物分离问题,反应完毕后产物需经碱洗、水洗和减压蒸馏才能得到最后产品,工艺过程复杂且可能造成环境污染,不符合绿色化学理念; (3) 强酸存在引起的设备腐蚀问题.因而开发新型高效的催化技术降低生产成本,解决生产过程中的污染问题,实现植物油的绿色高效利用,是我们当前迫切要解决的问题.寻找安全无污染且具有高效催化性能的非均相催化剂也迫在眉睫.因此,各过渡金属如 MoIV,WVI,NbV和 TiIV复合物催化剂得到广泛研究.其中,钛硅分子筛 TS-1 由于其良好的稳定性及优异的环氧化催化性能受到关注,然而其狭窄的孔道尺寸使得它在大分子反应物参与的反应中受到显著的扩散限制,因而需合成含有介孔及大孔的多级孔 TS-1 用于植物油环氧化反应中.本课题组多年从事钛硅分子筛的制备及催化氧化研究工作.本文以聚季铵盐-6 作为介孔模板剂合成了多级孔TS-1(HTS-1),将其作为催化剂,油酸甲酯作为模型化合物,H2O2作为氧化剂,系统研究了反应条件 (H2O2与双键摩尔比、氧化剂浓度与用量、反应温度与时间) 对油酸甲酯环氧化反应的影响.采用响应曲面分析法 (RSM) 优化反应条件,获取环氧化油酸甲酯的最大收率,并对各因素对油酸甲酯环氧化影响的显著性及各因素之间的交互作用进行探究.结果发现,H2O2与双键摩尔比及催化剂用量对油酸甲酯环氧化的影响较大,在优化的反应条件下环氧化产物的收率可高达 94.9%.而HTS-1 表现出的优异催化性能主要归结于其良好的疏水性能和高活性且可供大分子接触反应的钛物种.     

Dimethyldioxirane epoxidation of 3‐aryl‐1‐(3‐coumarinyl)propen‐1‐ones

Regioselective epoxidation of 3‐aryl‐1‐(3‐coumarinyl)propen‐1‐ones 1–10 by isolated dimethyldioxirane afforded the appropriate epoxides 11–20 in high (76–87%) yields.