用于丙烯气相一步氧化制环氧丙烷的Ag-MoO3/分子筛催化剂

用浸渍法制备了一系列以各种分子筛为载体、银及氧化钼为活性组分的负载型催化剂。在以分子氧为氧化剂，且原料气中不添加任何抑制剂的情况下，采用微反-色谱联合装置考察了催化剂对丙烯气相一步氧化制环氧丙烷的催化性能。结果表明，Ag含量、反应温度、载体及助剂对催化剂环氧化性能的影响非常明显。以MCM-41为载体的Ag-MoO3催化剂具有较好的催化性能，在300℃下，环氧丙烷的选择性和氧气的转化率可分别达到55．4％和2．2％；另外，0．1％NaCl改性的20％Ag5％MoO3/NaZSM-5催化剂在350℃下，环氧丙烷的选择性从未改性的9．1％提高到34．7％。     

以分子氧为氧源催化丙烯环氧化制环氧丙烷

综述了以分子氧为氧源催化丙烯环氧化制环氧丙烷近十年的研究进展。虽然目前这些方法还处于研究阶段,但作为具有最佳原子经济性清洁生产环氧丙烷的方法,该研究领域具有显著的工业化应用前景。     

A Self-Assembled Capsule for Propylene/Propane Separation

The development of energy-saving technology for the efficient separation of olefin and paraffin is highly important for the chemical industry. Herein, we report a self-assembled Fe₄L₆ capsule containing a hydrophobic cavity, which can be used to encapsulate and separate propylene/propane. The successful encapsulation of propylene and propane by the Fe₄L₆ cage in a water solution was documented by NMR spectroscopy. The binding constants K for the Fe₄L₆ cage toward propylene and propane were determined to be (5.0±0.1)×10³ M⁻¹ and (2.1±0.7)×10⁴ M⁻¹ in D₂O at 25 °C, respectively. Experiments and theoretical studies revealed that the cage exhibited multiple weak interactions with propylene and propane. The polymer-grade propylene (>99.5 %) can be obtained from a mixture of propylene and propane by using the Fe₄L₆ cage as a separation material in a U-shaped glass tube. This work provides a new strategy for the separation of olefin/paraffin.     

Dawson结构杂多酸盐催化合成碳酸丙烯酯

碳酸丙烯酯(PC)是一种性能优良的高沸点、高极性的有机溶剂,在有机合成、化妆品、电池电解质和脱碳溶剂等领域中具有重要应用.     

丙烯单体中硫化物的CGC-PFPD分析

报道了一种聚合级丙烯中多种硫化物的GC分析方法。样品在Gas Gaspro30m×0.317mm毛细管气相色谱柱分离,按程序升温操作,以脉冲火焰光度检测器(PF PD)检测器检测,CS2作外标,用PFPD检测器的原子响应特性测定了丙烯单体中ng/kg的硫化物含量。     

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).     

Au/Ti-MCM-41(H)催化丙烯气相直接环氧化

采用纳米组装法制备了一系列不同Ti含量的具有微孔-介孔复合结构(hybrid)的钛硅分子筛Ti-MCM-41(H)载体,继而用沉积-沉淀法制得纳米金催化剂.通过粉末X射线衍射(XRD)、氮气等温吸附-脱附、傅里叶变换红外(FT-IR)光谱、紫外-可见漫反射(DRUV-Vis)光谱、透射电镜(TEM)及等离子体原子发射光谱法(ICP-AES)对催化剂进行了表征,并考察了纳米金催化剂在氢气/氧气共存条件下丙烯气相直接氧化制环氧丙烷反应中的催化性能.结果表明:合成的微孔-介孔复合结构的钛硅分子筛Ti-MCM-41(H)具有典型的MCM-41结构,Ti(IV)以高分散的形式存在于分子筛的骨架结构中.在常压、423K反应温度下,以Ti/Si摩尔比为1%的Ti-MCM-41(H)为载体制备纳米金催化剂表现出了最佳的催化性能,反应30min,丙烯的转化率达5.4%,环氧丙烷的选择性为74.2%,环氧丙烷的生成速率为73.1g·h-1·kg-1;反应330min后,丙烯的转化率为4.9%,环氧丙烷的选择性为67.3%.     

Fe—Al配位催化环氧丙烷均聚

用于环氧丙烷开环聚合的催化剂为有机金属化合物和稀土络合物等,在对于铁系催化剂催化丁二烯聚合、马来酸酐与苯乙烯共聚和邻苯二甲酸酐与环氧丙烷共聚的研究基础上,我们首次将这一类催化剂用于环氧化物的开环均聚上,发现Fe(acac)3-Al(i-Bu）3催化剂具有良好的催化活性,并进行了产物结构和反应动力学的研究,结构分析表明Fe(acac)3-Al(i-Bu）3催化剂体系具有良好的立体定向性。     

丙烯直接环氧化Au/TiO2催化剂失活及再生研究

采用沉积沉淀法制得Au／TiO2负载型催化剂，研究了该催化剂的丙烯气相直接环氧化合成环氧丙烷的反应性能，对新鲜、失活和再生后的催化剂进行TG-DTA、FT-IR、吡啶-IR、TEM以及活性评价等表征．研究结果表明．催化剂的失活是由于吸附在催化剂表面酸性Ti位上的环氧丙烷产物发生副反应生成了大分子沉积物．该沉积物存在着两种类型，其含有长碳烷基和酯基．催化剂再生实验表明在空气和H2中再生时活性恢复良好，而在N2中的再生效果则很差．     

纳米薄层HZSM-5分子筛催化甲醇制丙烯

在合成系列硅铝比纳米薄层HZSM-5分子筛的基础上,研究了纳米薄层HZSM-5分子筛催化甲醇制丙烯(MTP)的反应性能.在固定床微反装置上详细考察了工艺条件对纳米薄层HZSM-5分子筛催化性能的影响,同时与纳米HZSM-5分子筛对MTP反应的催化性能进行了比较.结果表明,纳米薄层HZSM-5分子筛具有较高的目的产物选择性和较长的催化寿命.在适宜硅铝比(n(SiO2)/n(Al2O3)=213)和反应条件下(温度470°C,甲醇质量空速为3 h-1),丙烯的选择性达到46.7%,三烯(乙烯、丙烯和C4烯烃)选择性达到78.7%.其中,丙烯/乙烯的质量比可达到6.5,是纳米HZSM-5分子筛的2倍,而芳烃的选择性比纳米分子筛明显降低.这是因为纳米薄层HZSM-5分子筛比纳米HZSM-5分子筛具有较宽的(010)晶面、较大的外比表面积和介孔孔容.     

Polarity Effects of Propylene Carbonate on Breakdown Strength in Microsecond Range

We investigate the polarity effects of the propylene carbonate on the breakdown voltage using the needle-plate electrodes with gaps of 0.5, 1.0, and 2.0 mm. The devices used in this study involve a compact capacitive-energy-storage pulse power source with charging time varying from 5 ms to 20 ms and a test cell with the needle-plate electrodes. The breakdown voltage is recorded by a digital oscilloscope for each gap. The results of these three groups indicate that the positive breakdown voltage is higher than the negative one and the breakdown voltage of the PC increases with the ascending electrode gap. In addition, a simulation isconducted to support this experiment. Some explanations about the polarity effect of the PC are also given.     

丙烯的臭氧化反应动力学研究

使用自行研制的烟雾箱实验装置, 研究了模拟实际大气环境臭氧浓度下(最小浓度6.6×10−8)臭氧与丙烯的反应动力学. 结合Model 49C-O3 Analyzer与GC-FID对臭氧与丙烯在282~314 K温度范围内的速率常数进行了测定, 得到臭氧初始浓度为6.61×10−8、温度为282 K时臭氧与丙烯的反应速率常数为6.73×10−18 cm3•molecule−1•s−1. 并根据不同温度下测得的反应速率常数, 求得该反应的阿仑尼乌斯方程为k2=(5.8±1.2)×10−15e(−1907±53)/T. 对比前人结果, 我们测得的速率常数偏小, 活化能偏高, 但速率常数的最大误差仅为11%, 活化能的最大误差为5%. 说明我们的研究设备在实际大气条件下是可靠的, 可用于进一步深入研究臭氧有关的反应.     

Propylene Epoxidation by Dioxygen over Catalyst Copper-loaded TiO2

A copper-TiO2 based catalyst(Cu-OH-Cl-TiO2) was prepared through a slurry impregnation approach and the catalyst was found to be active and selective for the epoxidation of propylene by dioxygen. With a feed gas of 10% C3H6, 10% O2 and 80% N2 at a gas hourly space velocity(GHSV) of 4000 h–1, a propylene conversion of 4.8% and a propylene oxide(PO) selectivity of 38.9% were achieved over the obtained Cu-OH-Cl-TiO2 catalyst at a reaction temperature of 500 K. It revealed that Cu2+ provided by crystalline Cu2(OH)3Cl plays a key role in catalytic conversion of propylene to PO.     

Propylene/propane mixture adsorption on faujasite sorbents

The adsorption of propylene and propane on zeolite NaX with and without a saturated (36 wt%) amount of CuCl have been investigated. The single component adsorption isotherms could be well described with a Dual-Site Langmuir model. The dispersion of CuCl results in a decrease of the maximum adsorption capacity of the zeolite for both components. For propylene a strong adsorption via π-complexation with CuCl is present, increasing the adsorption selectivity of the zeolite. The binary mixture (50:50) adsorption was determined via breakthrough/desorption experiments at 318, 358 and 408 K with a partial pressure of the two components between 0.8–54 kPa. For NaX the mixture loading could be well described with the IAS-theory and the single component isotherms, both qualitatively and quantitatively. A transition from an enthalpy controlled adsorption at lower loadings to an entropy affected adsorption at higher loadings was observed. The IAS-theory could only qualitatively describe the trends in the observed mixture adsorption for the CuCl/NaX adsorbent. The dispersion of CuCl in NaX results in a modest improvement of the adsorption selectivity for propylene over propane (from 3–7 to 15–30) but at the expense of a reduced capacity.     

Ag-MoO3催化丙烯直接气相环氧化反应的原位红外研究

制备了对丙烯直接气相环氧化具有较好催化性能的Ag-MoO3催化剂, 采用原位FT-IR技术研究了丙烯、环氧丙烷及丙烯+氧气的混合气在Ag和Ag-MoO3催化剂表面上的吸附及反应行为. 研究表明, 丙烯在Ag和Ag-MoO3催化剂表面上吸附后, 均不发生化学反应, 而环氧丙烷吸附后在较高温度下则发生开环和聚合反应直至产生积炭. 与Ag催化剂相比, 在Ag-MoO3催化剂上, MoO3的加入在降低催化剂活性的同时, 在一定程度上抑制了产物环氧丙烷的开环及深度反应, 使环氧丙烷的选择性提高. 另外, 在较低的反应温度和较短的滞留时间下, 环氧丙烷发生深度反应的程度明显降低.     

SAPO-34分子筛催化丁烯转化制丙烯的研究

通过水热法合成SAPO-34分子筛,将其制成催化剂用于催化丁烯转化制取丙烯,考察了反应温度、空速和铝磷比等对催化性能的影响;还比较了SAPO-34分子筛与ZSM-5分子筛催化该反应的差异.结果表明,在实验范围内,反应温度升高会使得丁烯的转化率明显增高,且丙烯选择性提高;而空速增加,则丁烯的转化率和丙烯选择性降低;铝磷比越大,对丙烯的选择性越差.在有效的反应时间内,SAPO-34分子筛催化效果好于ZSM-5分子筛,但单程寿命较ZSM-5分子筛短.     

Isospecific Polymerization of Propylene By ansa-Zirconocene Diamide Compound Cocatalyzed by Mao

Abstract

The kinetics of propylene polymerization initiated by racemic ethylene-1,2-bis(1-indenyl) zirconium bis(dimethylamide) [rac-(EBI) Zr(NMe₂)₂(rac-1)] cocatalyzed by methylaluminoxane (MAO) were studied. The polymerization behaviors of rac-1/MAO catalyst investigated by changing various experimental parameters are quite different from those of rac-(EBI) ZrCl₂ (rac-2)/MAO catalyst, due to the differences in the generation procedure of cationic actives species of each metallocene by the reaction with MAO. The activity of rac-1/MAO catalyst showed maximum when [Al]/[Zr] is around 2000, when [Zr] is 137.1 μM, and when polymerization temperature is 30°C. The negligible activity of rac-1/MAO catalyst at a very low MAO concentration seems to be caused by the instability of the cationic active species. The meso pentad values of polymers produced by rac-1/MAO catalyst at 30°C are in the range of 82.8% to 89.7%. The rac-1/MAO catalyst lost stereorigid character at the polymerization temperature above 60°C. The molecular weight of polymer decreased as [Al]/[Zr] ratio, polymerization temperature, and [Zr] increased. The molecular weight distributions of all polymers are in the range of 1.8–2.3, demonstrating uniform active species present in the polymerization system.     

咪唑鎓离子液体协同催化苯酚与碳酸丙烯酯的反应

在离子液体1-丁基-3-甲基咪唑乙酸盐([bmim]OAc)催化下,苯酚和碳酸丙烯酯一步合成了丙二醇苯醚.系统考察了反应温度、反应时间及催化剂用量对反应性能的影响,在优化的反应条件下,丙二醇苯醚的收率达79%.同时研究了不同咪唑鎓离子液体的阴阳离子的种类对催化反应的影响,发现咪唑鎓中的C2-H对反应有极大的促进作用,咪唑鎓通过提供氢键能力活化反应底物碳酸丙烯酯;同时,离子液体的阴离子也对反应有很大的影响,阴离子通过接受氢键能力活化另一反应底物苯酚.离子液体阴阳离子通过提供和接受氢键协同催化苯酚与碳酸丙烯酯的反应.离子液体循环使用5次,其活性未见明显降低.     

稀土氯化物催化丙烯直接环氧化反应研究

以氯化稀土为催化剂,以锌粉为还原剂,对不同羧酸和溶剂条件下的丙烯直接用氧气环氧化进行了研究,并对它的催化反应机理进行了初步探讨,实验结果表明,氯化稀土中有EuCl3对丙烯直接环氧化起催化作用,并且要在锌粉和羧酸共同存在下才有效,所用羧酸中丙酸的效果最佳,使用有机溶剂比不用溶剂效果更好,但不能用碱性物质作为反应体系的溶剂。反应气压力越高越有利于 环氧丙烷（PO）的生成,但反应温度不宜过高,在EuCl3、锌粉、羧酸催化体系中,EuCl3起电子传递的桥梁作用,锌粉提供电子,羧酸提供质子,推测的反应机理与实验结果吻合。     

含桥式硫原子双酚盐配体的有机铋配合物的合成及其对CO2和环氧丙烷环加成反应催化性能的研究

合成分析了含有桥式硫原子二酚盐配体的新型有机铋配合物,并发现它们在亲核试剂(I-)存在下对CO2和环氧丙烷环加成反应合成碳酸丙烯酯表现出很高的催化活性和选择性.