丙烯环氧化反应中失活钛硅分子筛的无氧脱附研究

采用无氧脱附方法对丙烯环氧化中失活的薄层钛硅分子筛(即Spent EPO-4)和环氧丙烷(PO)与丙二醇单甲醚(MME)浸渍的TS-1催化剂(即PO／TS-1和MME／TS-1)进行了研究，脱附产物由气相色谱定性分析，无氧脱附后的催化剂以丙烯环氧化为探针反应进行再生性能评价，同时在无氧条件下考察了TS-1在300℃时催化裂化PO反应．实验结果表明：PO浸渍TS-1可使其活性明显下降，PO在TS-1上不是简单的弱吸附，存在着化学强吸附和自聚．失活催化剂(Spent EPO-4和PO／TS-1)经无氧脱附后，其催化活性可显著恢复．通过对失活催化剂脱附产物的比较，推测了丙烯环氧化反应过程中钛硅分子筛失活原因．     

Au/NTS-1催化丙烯气相直接环氧化(英文)

以高温氨气处理制得含氮微孔钛硅分子筛(NTS-1)为载体,用沉积-沉淀法制得了一系列纳米金催化剂.考察了纳米金催化剂在氢气和氧气共存下催化丙烯气相环氧化制环氧丙烷反应中的催化性能.结果表明,高温氨气处理钛硅分子筛(TS-1)载体降低了其酸性,提高了纳米金催化剂制备中金的利用率和纳米金催化剂中金的分散度,显著提高纳米金催化剂的催化活性.载体酸性降低和载体表面–NH2配位效应增强了催化剂活性.     

无机钛硅原料合成TS-1催化氯丙烯环氧化反应

采用无机钛硅原料体系合成出了TS-1分子筛,并对TS-1分子筛催化氯丙烯环氧化反应进行了研究.在以甲醇为溶剂的体系中考察了反应时间、反应温度、催化剂用量、氯丙烯与双氧水的摩尔比对反应的影响,得到了无机钛硅原料体系合成的TS-1催化氯丙烯环氧化反应的最优条件:反应时间为60 min,反应温度为45℃,催化剂用量为22.5 g L-1,氯丙烯与双氧水的摩尔比n(AC):n(H2O2)=1.8,并对无机钛硅原料体系合成的TS-1进行了修饰改性,评价了其催化性能.     

硅烷化TS-1对环己烷均相氧化反应的促进作用

考察了钛硅分子筛(TS-1)以及硅烷化钛硅分子筛(TS-1-S)上环烷酸钴(Co-nap)催化环己烷氧化反应性能.结果表明,TS-1和TS-1-S对该反应均具有显著的促进作用,环己烷转化率由无TS-1时的3.6%分别提高至6.4%和7.9%,产物选择性保持在80%左右,反应时间由300 min可缩短为130min.进一...     

硅胶微球负载钛硅分子筛TS-1催化剂的制备及对苯氧化合成苯酚的催化性能

将硅胶微球浸渍于钛硅分子筛（TS-1）合成液中,经晶化、焙烧制得负载TS-1分子筛硅胶微球催化剂。 用XRD、IR和SEM测试技术对其进行表征,将其用于过氧化氢氧化苯合成苯酚的反应中。 结果显示,TS-1分子筛能够很好地负载于硅胶表面,晶化温度160 ℃,晶化时间72 h,焙烧温度550 ℃,焙烧时间6 h时,获得的催化剂显示良好的催化性能。 在苯和H2O2初始原料量分别为0.5和0.1 mol、催化剂加入量为8 g、反应温度为60 ℃条件下,经过3 h的反应,苯的转化率达到10.32%,苯酚选择性达到97.12%。 9次重复使用后的苯转化率为9.42%,苯酚选择性为93.14%。     

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%。     

Ti-MWW催化烯丙基氯环氧化高效合成环氧氯丙烷

 研究了具有MWW结构的新一代钛硅分子筛Ti-MWW催化剂对烯丙基氯液相环氧化高效合成环氧氯丙烷的催化性能. 结果表明, Ti-MWW的催化活性以及产物选择性均优于传统的钛硅分子筛TS-1. 对于Ti-MWW,合适的溶剂为非质子性溶剂丙酮和乙腈,在该溶剂中环氧化物不易发生溶剂化开环反应; 而对于TS-1,合适的溶剂是质子性溶剂甲醇,但甲醇可导致醇醚副产物的生成. 在Ti-MWW催化剂上烯丙基氯的转化率和环氧氯丙烷的选择性都能达到99%以上.     

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     

Sn改性的Au/TS-1催化剂上丙烯气相环氧化反应研究

以Sn改性的TS-1分子筛为载体,利用沉积沉淀法制备了金催化剂,用于在氢气氧气共存下丙烯直接环氧化反应,并比较了不同Sn掺杂量对催化剂结构及其催化性能的影响.X射线衍射与红外光谱结果表明,Sn掺杂进入TS-1骨架中.反应活性结果表明,Sn的改性使催化剂上丙烯的转化率由1.6提高到2.5%,环氧丙烷的选择性由87上升到90%,活性的增加可能是由于Sn的掺入引起的配位效应(ligand effect).     

多级孔钛硅分子筛的制备及应用进展

以钛硅分子筛(TS-1)为催化剂的选择性催化氧化工艺具有反应条件温和、产物选择性高及环境污染小等特点,促进了烃类催化氧化反应的绿色化发展.但常规TS-1分子筛狭窄的孔道限制了其在大分子催化氧化反应中的应用.多级孔TS-1分子筛为包含不同尺度的孔道结构的晶体沸石,兼具微孔分子筛晶体优异的水热稳定性和介孔材料优异的扩散传输性能,因此其受到国内外众多专家学者的广泛关注.多级孔TS-1分子筛的制备方法很多,主要有直接合成法和后处理法,其中直接合成法包括硬模板法、软模板法和自组装法,而后处理制备主要为碱处理法.我们在对多级孔TS-1分子筛制备方法进行归纳总结的基础上,探讨不同制备方法对分子筛中钛硅物种分布、孔道结构及催化烃类选择性氧化反应性能的影响.结合目前TS-1分子筛应用现状,对其未来发展进行展望.     

One-pot Synthesis of Dimethyl Carbonate in the Presence of a Two-component Catalyst

The one-pot synthesis of dimethyl carbonate（DMC） with co-production of propy-lene carbonate（PC） and propylene glycol（PG） from propylene oxide（ PO）, carbon dioxide and methanol as the starting materials was investigated. The catalyst adopted here was a mixture of tetrabutyl ammonium bromide and sodium methoxide. It was found that un- der the reaction conditions of t = 150 ℃, p =3-4 MPa and 2 h, the PO conversion could reach 100%, the DMC, PC and the PG selectivities were 49. 7%, 42. 7% and 49. 8%, respectively, and the selectivity of by-products was below 10%.     

Reaction of inorganic cyanates with halides. II. Reactions of chlorohydrins

The reaction of ethylene and trimethylene chlorohydrins with cyanate ion in anhydrous dimethylformamide (DMF) forms 2-oxazolidinone and tetrahydro-2H-1, 3-oxazin-2-one, respectively. These are the major products over a wide concentration range, and at initial chlorohydrin concentration of 1 M and lower, the yields are high enough to make the reaction useful for synthesis of oxazine and oxazolidine derivatives. The corresponding reaction with tetramethylene chlorohydrin gave tetrahydrofuran as the major product with the by-products being polymeric. Pentamethylene and hexamethylene chlorohydrins yield linear polyurethanes when allowed to react with cyanate in DMF. Examination of the relative rates of reaction of these chlorohydrins indicate that the mechanism by which urethanes are formed (both cyclic and polymeric) is an S_N2 displacement of chloride by cyanate ion to give an isocyanate intermediate which then reacts with an alcohol group to form urethane.     

Ionic telomerization of 1-chloro-2,3-epoxypropane with allyl alcohol and properties of products obtained

Ionic telomerization of 1-chloro-2,3-epoxypropane with allyl alcohol in the presence of boron trifluoride etherate as a route to halogenated epoxy oligoethers was studied. Selective chlorination or bromination of the intermediate oligo(chlorohydrin), followed by dehydrochlorination (epoxidation) of the intermediate oligohalohydrins with NaOH, was performed. The synthesized products are effi cient as active diluents for a compound based on ED-20 resin.     

TS-1/尿素/过氧化氢体系中的丙烯环氧化反应

 研究了TS-1/尿素/过氧化氢体系中的丙烯环氧化反应,考察了尿素用量和过氧化氢浓度对反应的影响. 结果表明,加入适量尿素可以显著提高环氧丙烷选择性和过氧化氢的利用率,而提高过氧化氢浓度不利于丙烯环氧化反应. 在尿素用量为31.2 g/L和过氧化氢浓度为0.09 mol/L时,过氧化氢转化率可达90.00%,环氧丙烷选择性可达96.12%,过氧化氢利用率可达98.46%.     

Preferential Adsorption of Ethylene Oxide on Fe and Chlorine on Ni Enabled Scalable Electrosynthesis of Ethylene Chlorohydrin

Industrial manufacturing of ethylene chlorohydrin (ECH) critically requires excess corrosive hydrochloric acid or hypochlorous acid with dealing with massive by-products and wastes. Here we report a green and efficient electrosynthesis of ECH from ethylene oxide (EO) with NaCl over a NiFe₂O₄ nanosheet anode. Theoretical results suggest that EO and Cl preferentially adsorb on Fe and Ni sites, respectively, collaboratively promoting the ECH synthesis. A Cl radical-mediated ring-opening process is proposed and confirmed, and the key Cl and carbon radical species are identified by high-resolution mass spectrometry. This strategy can enable scalable electrosynthesis of 185.1 mmol of ECH in 1 h with 92.5 % yield at a 55 mA cm⁻² current density. Furthermore, a series of other chloro- and bromoethanols with good to high yields and paired synthesis of ECH and 4-amino-3,6-dichloropyridine-2-carboxylicacid via respectively loading and unloading Cl are achieved, showing the promising potential of this strategy.     

Fluoro-ketones IV. Synthesis of phenylperfluoroalkyl ketones - mechanism of reaction between phenyllithium and fluoroesters

Although fluorine containing ketones (R_fC(O)R_f and R_fC(O)R, R_f = perfluoroalkyl) have been prepared from the reaction between organolithium reagents and perfluoroalkyl esters, the reaction has not found general applicability. Variable yields of ketones and co-production of secondary and tertiary alcohol by-products have in most instances been experienced. We have examined in more detail the factors e.g., temperature, mode of addition and perfluoroalkyl ester structure which influence ketone product and by-products formation. By controlling experimental conditions excellent yields of C₆H₅C(O)R_f compounds can be attained. A lithium salt of a hemiketal (II) has been isolated and shown to be the active intermediate in the production of the ketone. The stability of the salt and its potential reaction with the solvent dictates the type of reaction products. Low temperature favors stability of the lithium salt of the hemiketal whereby high yields of ketones are produced on hydrolysis.     

丙烯直接环氧化Cu基催化剂的研究进展与挑战

作为一种重要的化工原料,环氧丙烷年产量近千万吨,然而目前工业上制备环氧丙烷的方法仍然面临着成本高、副产物多以及污染严重等问题。直接氧气氧化法进行丙烯环氧化因为具有原子经济、环保等优点受到了越来越多的关注。但是,催化过程中丙烯的α-H和环氧丙烷都具有很高的活性,使得在高转化率的条件下提升环氧丙烷选择性成为一个巨大的挑战。研究者们发现相较于其他币族金属,Cu基催化剂表现出更优异的丙烯直接环氧化反应性能。本综述总结梳理了近年来关于Cu基催化剂催化丙烯直接环氧化反应的研究成果,聚焦于Cu基催化剂改性方法,并对Cu基催化剂依然存在的问题和挑战进行深入探讨。     

Über den Technologiewandel in der Propylenoxid‐Herstellung

Propylene oxide (PO) is one of the most important intermediates for the chemical industry. It is used for the manufacture of materials such as insulating foams, solvents, deicing fluids among others and has, thus, become essential for our modern life. The first industrial production route for PO and today still the most important one is the so called chlorhydrine process. With the renouncement of chlorine, the SM‐PO and MTBE‐PO processes provide more environmentally friendly routes for the production of PO. However, Styrene and MTBE are obtained as secondary coproducts. The economic feasibility of these processes is determined not only by PO. It is also influenced by the demand of the coproducts. The CU‐PO process has been developed as a coproduct‐free variant of the SM‐PO process. The development of the highly selective catalyst titansilicalit‐1 (TS‐1) together with the vast expansion of the availability of hydrogen peroxide paved the way for the industrial realization of the coproduct‐free HPPO technology at various sites worldwide. Excellent yields and selectivities and water as an environmentally friendly byproduct characterize this new process for the production of PO. The application of homogeneous catalysts or the direct synthesis using air/oxygen and propylene are only of academic importance so far.     

混合溶剂系统中固定化脂肪酶对酮基布洛芬的催化酯化反应

以硅藻土吸附的脂肪酶为催化剂,对外消旋酮基布洛芬[2-(3-苯甲酰苯基)丙酸]进行对映选择性酯化反应;考察了不同的脂肪酶制剂,固定化时所加缓冲液的体积与pH值,酰基受体(醇)的种类以及混合溶剂系统的组成等因素对酶活性的影响.结果表明,在所考察的7种脂肪酶中,以LipaseOF的酪化活性最高;用硅藻土吸附固定化酶时,缓冲溶液的最适pH为7.0左右,每克酶粉加1.0mL缓冲溶液为最佳;固定化酶催化酯化的活性比游离的脂肪酶高.在酮基布洛芬与不同酰基受体(醇)的酶促酯化反应中,以丙醇的反应速度为最快.在由一种主溶剂与一种助溶剂组成的混合溶剂系统中,酶促酯化的速度要比在单一的主溶剂或助溶剂系统中快.当以1gP值较大的环己烷或异辛烷等为主溶剂,甲苯为助溶剂时,脂肪酶催化酮基布洛芬酯化反应的活性最高.     

Synthesis of collagen-like sequential polypeptides containing O-phospho-L-hydroxyproline and preparation of electrospun composite fibers for possible dental application

A synthetic route is described for collagen-like polypeptides constructed from O-phospho-L-hydroxyproline [Hyp(PO(3)H(2))] residues. Using the synthetic polypeptides and a natural protein, gelatin, fine fibers and their network structures (ESNWs) were prepared via electrospinning. The composite ESNWs can induce the mineralization of calcium phosphate. The phosphoryl groups of the Hyp(PO(3)H(2)) residues affect both the crystalline phase and amount of the calcium phosphate, depending on the chemical structure in the repeating sequence. The composite ESNWs can be developed as a biocompatible replacement of the extracellular matrix of hard tissues, and thus can be applied as dental materials for restoration of dental cavities or as a sealant for pits and fissures.