无碱条件下Au/ZnO选择性催化氧化1,3-丙二醇合成3-羟基丙酸甲酯

采用溶胶-沉积法合成了高选择性的Au/ZnO催化剂,用于1,3-丙二醇选择性氧化酯化为3-羟基丙酸甲酯的反应.研究了保护剂PVA用量、金溶胶合成温度、金负载量及催化剂循环利用对反应的影响,且优化了反应温度和反应压力,并对催化剂进行了XRD和TEM表征.结果表明,PVA∶Au(m/m)=1∶4、金溶胶合成温度25℃、金负载量1%的Au/ZnO对目标反应的催化活性最好,在100℃和Po2=2MPa的条件下1,3-丙二醇的转化率达82.8%,产物3-羟基丙酸甲酯的选择性达95.4%.Au纳米粒子的粒径影响催化性能,在Au平均粒径为2.8~6.1nm的范围内,产物选择性随Au纳米粒子的粒径的减小而增大,平均粒径在2.8~4.8nm的范围内时,催化剂具有较好的产物选择性(大于90%);Au/ZnO催化剂循环利用4次后催化性能(转化率和选择性)无明显下降;并推测了无碱条件下Au/ZnO选择性催化氧化1,3-丙二醇合成3-羟基丙酸甲酯的反应机制.     

Pd/PMO-SBA-15 催化剂催化苯甲醇选择氧化反应性能

 研究了 PMO-SBA-15 材料负载的金属钯纳米粒子 (Pd/PMO-SBA-15) 在水相中催化苯甲醇选择氧化制苯甲醛的反应. 考察了纳米粒子种类、氧化剂用量、反应时间和反应温度等对苯甲醇转化率及苯甲醛选择性的影响. 结果表明, 以水为溶剂, 以 H2O2 (30%) 为氧化剂时, 可得到较高的苯甲醇转化率和苯甲醛选择性. 当以 0.05 g 的 2%Pd/PMO-SBA-15 为催化剂, H2O2 用量为 1.5 ml, 反应温度为 80 oC, 反应 4 h 时, 苯甲醇转化率和苯甲醛选择性分别达到 97.1% 和 100.0%. 对该催化体系的重复使用性能进行了考察. 结果发现, 随着使用次数的增加, 苯甲醇转化率有所下降, 但苯甲醛选择性保持不变.     

铜基催化剂上甘油脱水制备羟基丙酮

采用共沉淀法制备了一系列铜基催化剂,在N2中于高压釜中,考察了其催化甘油脱水制备羟基丙酮的反应性能.结果表明,Cu/SiO2催化剂具有较高的催化甘油脱水活性,但目的产物羟基丙酮易与反应产生的H2生成1,2-丙二醇,使得羟基丙酮选择性不高.因此,在固定床反应器上详细考察了在优选的Cu/SiO2催化剂上反应气氛、温度和空速...     

KF/Al2O3催化剂上苯脲醇解合成苯氨基甲酸甲酯的研究

采用浸渍法制备负载KF固体碱催化剂,应用于苯脲和甲醇制备苯氨基甲酸甲酯的反应,考察了氧化物载体、卤化钾种类对催化剂性能的影响,KF/Al₂O₃催化剂显示出良好的催化活性和苯氨基甲酸甲酯的选择性。通过对KF/Al₂O₃催化剂中KF的负载量和催化剂焙烧温度的研究发现,在500 ℃焙烧4 h、负载质量分数50%KF的催化剂能够更好地促进MPC生成,苯脲转化率和苯氨基甲酸甲酯选择性分别达到96.5%和86.3%。XRD分析表明,KF与Al₂O₃之间存在较强的相互作用,部分转化为K₃AlF₆。KF与K₃AlF₆分别对甲醇的活化和苯脲的选择性起促进作用,两者的协同效应共同促进了目标产物苯氨基甲酸甲酯的生成。     

乙酸选择性加氢制乙醇反应性能研究

在固定床反应器上考察了反应温度、反应压力、乙酸(HAC)液体进料空速、H_2/HAC(总气体空速GHSV或H_2流量)对乙酸选择性加氢制乙醇反应的影响,研究了乙酸转化率、产物选择性、乙醇时空收率的变化规律,验证了自主开发催化剂的稳定性。结果表明,副产物的选择性受反应条件的影响,选择合适的反应条件可以抑制乙酸乙酯和丙酮的生成。原料与催化剂床层接触时间小于5s时,可以避免发生乙酸加氢分解脱羰反应生成甲烷气相产物,也避免了乙醇的进一步反应生成乙烷。在反应温度为280℃,反应压力为2.5 MPa,乙酸进料液时空速为0.72 h~(-1),H_2/HAC(mol ratio)为16的条件下,乙酸乙酯选择性为6%。900 h长周期实验表明,自主开发催化剂具有较好的工业应用前景。     

磷钼杂多酸对纤维素水解产物分布及水解过程的影响

本文用自制玉米秸秆纤维素作为原料，以Wells Dawson型磷钼杂多酸H₆P₂Mo₁₈O₆₂(Phosphomolybdic acid, PMA)作为催化剂，在水热条件下降解纤维素，考察反应温度、反应时间、料液比和催化剂用量对纤维素转化率及液化产物分布的影响，并探究PMA在水解过程中发挥的机理作用，得到最佳反应条件：反应温度220℃,反应时间60 min,料液比1∶50,催化剂用量1 g,此条件下羟基乙酸、乳酸、甲酸和乙酰丙酸产率分别达到13.69%、4.15%、4.83%和4.34%。结果表明，PMA在纤维素水解实验中表现出很大的潜力，可作为非均相固体酸催化剂用于羟基乙酸生产。     

Pt改性分子筛催化剂上丙烷与苯的烷基化反应

研究了不同分子筛负载的Pt催化剂上丙烷与苯的烷基化反应.结果表明,Pt/HZSM-5具有较好的催化性能.在0~0.3%范围内提高Pt负载量可以提高催化剂的催化活性和生成C9以及C10 芳烃的选择性,降低非芳烃产物的选择性.较低的反应温度、较高的苯/丙烷摩尔比和较高的空速有利于烷基芳烃的生成.     

高Cu含量MCM-41在苯直接羟基化反应中的催化性能

 考察了高铜含量(最高达26.0%)且铜原子主要处于中孔骨架的Cu-MCM-41在苯/过氧化氢直接羟基化制备苯酚反应中的催化性能,研究了铜含量、催化剂用量、溶剂种类、反应物摩尔比、温度以及时间等对催化剂活性的影响. 结果表明,该催化剂在苯直接羟基化反应中具有良好的催化活性,在最佳反应条件下,可使苯转化率达52.9%, 苯酚选择性达58.9%, 苯酚收率达31.2%, 优于文献报道的低铜含量中孔分子筛的催化结果. 另外,从反应机理对影响反应的因素进行了初步探讨.     

不同晶粒ZSM-5沸石分子筛对合成气羰基化反应性能的影响

对沸石分子筛而言,分子筛的孔道、孔径、孔容和微孔等物理性质和酸性影响它的活性.通过调节和控制以上物理性质能够提高产物选择性和收率,降低副产物,从而促进反应性能提高活性.我们考察了ZSM-5分子筛的晶粒度和硅铝比对合成气羰基化反应性能的影响.结果表明,晶粒度小及具有一定比例的中强酸中心的ZSM-5沸石分子筛对反应有利,但晶粒度比较大即1和3μm的ZSM-5沸石分子筛目标产物选择性比较低.纳米级的ZSM-5沸石分子筛催化剂在反应中表现出较高的活性及较低的副产物选择性,是适宜的合成气羰基化反应催化剂载体.温度考察结果可知,反应温度为300℃时,效果为最佳.其中, 30～50 nm的ZSM-5沸石分子筛催化剂CO转化率为55%,乙酸甲酯和甲酸甲酯选择性之和为52%,而晶粒度3μm时, CO转化率仅为25%,乙酸甲酯和甲酸甲酯选择性之和为20%,是30～50 nm沸石分子筛的一半.当反应继续升温时,副产物的选择性也随之增加,是因为所生成的中间产物和甲醇等继续进行各种反应生成二甲醚、芳烃、烷烃以及裂解生成CO_2等干气.     

TiO2负载Co2+、Cu2+催化剂的制备及其对甲酚催化氧化性能

用浸渍法制备了一系列以TiO2为载体的负载型催化剂,利用XRD和IR分析测试技术研究了负载Co2+与Cu2+后催化剂的表面结构,催化剂用于对甲酚氧化制备对羟基苯甲醛的反应中。 结果表明,n(Co2+)∶n(Cu2+)=1∶0.5时,催化剂的催化效果最佳。 在反应优化条件下,对甲酚的转化率可达100%,对羟基苯甲醛的选择性达95.2%。     

Catalytic Performance of Amorphous Ti/SiO2 in the Gas-Phase Epoxidation of Propylene with H2O2

The epoxidation of propylene with dilute H₂O₂ aqueous solution over titanium silicalite-1 (TS-1) zeolite catalyst is a green chemical reaction for propylene oxide (PO) production. Carrying out the reaction in gas-phase can get rid of problems caused by using methanol solvent. This paper reports an attempt of using non-zeolite catalyst for the gas-phase epoxidation. Amorphous Ti/SiO₂, obtained by grafting amorphous SiO₂ with TCl₄ in ethanol solvent in a chemical liquid-phase deposition (CLD) process, has been used as the catalyst. Results show that the CLD Ti/SiO₂ with appropriate Si/Ti molar ratio is an active catalyst for gas-phase epoxidation, achieving 9.8 % propylene conversion and 66.9 % PO selectivity with 40.3 % H₂O₂ utilization, which indicates that this amorphous Ti/SiO₂ catalyst deserves extensive studies in the future.     

Synthesis of p-Hydroxybenzaldehyde by Liquid-phase Catalytic Oxidation of p-Cresol over PVDF Modified Cobalt Pyrophosphate

The influence of the wettability of a catalyst on the performance of the liquid phase oxidation of p-cresol was investigated. It was found that the surface hydrophobicity of a catalyst, which can be changed by modification with various loadings of polyvinylidene fluoride(PVDF), has a promotion effect on the catalytic performance. At the same time, the reaction parameters such as oxygen pressure, molar ratio of NaOH to p-cresol, reaction temperature and time on the catalytic performance in the liquid-phase oxidation of p-cresol were optimized. As a result, 10%(mass fraction) PVDF modified cobalt pyrophosphate gave the highest conversion of 94.2% of p-cresol with a selectivity of 94.4% for p-hydroxybenzaldehyde at 348 K and a molar ratio of 4:1 of NaOH/p-cresol and an oxygen pressure of 1.0 MPa for 3 h.     

Review of Acetic Acid Synthesis from Various Feedstocks Through Different Catalytic Processes

Acetic acid (AA) has been largely used with a wide range of applications such as a raw material for a synthesis of vinyl acetate monomer, cellulose acetate or acetate anhydrate, acetate ester and a solvent for a synthesis of terephthalic acid and so on. The present paper briefly summarizes the commercialized chemical processes with their Rh or Ir-based catalytic systems in a liquid-phase carbonylation reaction such as Monsanto, Cativa and Acetica processes. In addition, some alternative catalytic systems such as heterogeneous catalysts to produce AA by direct oxidation or indirect carbonylation of dimethyl ether through BP-SaaBre process in a gas-phase reaction to solve some problems such as a difficult separation of homogeneous catalysts in a corrosive reaction medium. Some home-made heterogeneous catalysts such as a rhodium incorporated graphitic carbon nitride (Rh-g-C₃N₄) and some heterogenized homogeneous catalysts using the supports of tungsten carbide, iron oxide or graphitic carbon nitride containing rhodium complexes were also introduced for the synthesis of AA through a liquid-phase methanol carbonylation reaction to effectively solve the leaching problem of active rhodium metal as well as to mitigate the separation problem of homogeneous catalysts.     

Critical re-evaluation of the O-H bond dissociation enthalpy in phenol

The gas-phase O-H bond dissociation enthalpy, BDE, in phenol provides an essential benchmark for calibrating the O-H BDEs of other phenols, data which aids our understanding of the reactivities of phenols, such as their relevant antioxidant activities. In a recent review, the O-H BDE for phenol was presented as 90 +/- 3 kcal mol(-1) (Acc. Chem. Res. 2003, 36, 255-263). Due to the large margin of error, such a parameter cannot be used for dynamic interpretations nor can it be used as an anchor point in the development of more advanced computational models. We have reevaluated the existing experimental gas-phase data (thermolyses and ion chemistry). The large errors and variations in thermodynamic parameters associated with the gas-phase ion chemistry methods produce inconsistent results, but the thermolytic data has afforded a value of 87.0 +/- 0.5 kcal mol(-1). Next, the effect of solvent has been carefully scrutinized in four liquid-phase methods for measuring the O-H BDE in phenol: photoacoustic calorimetry, one-electron potential measurements, an electrochemical cycle, and radical equilibrium electron paramagnetic resonance (REqEPR). The enthalpic effect due to solvation, by, e.g., water, could be rigorously accounted for by means of an empirical model and the difference in hydrogen bond interactions of the solvent with phenol and the phenoxyl radical. For the REqEPR method, a second correction is required since the calibration standard, the O-H BDE in 2,4,6-tri-tert-butylphenol, had to be revised. From the gas-phase thermolysis data and three liquid-phase techniques (excluding the electrochemical cycle method), the present analysis yields a gas-phase BDE of 86.7 +/- 0.7 kcal mol(-1). The O-H BDE was also estimated by state-of-the-art computational approaches (G3, CBS-APNO, and CBS-QB3) providing a range from 86.4 to 87.7 kcal mol(-1). We therefore recommend that in the future, and until further refinement is possible, the gas-phase O-H BDE in phenol should be presented as 86.7 +/- 0.7 kcal mol(-1).     

Does electrospray ionization produce gas-phase or liquid-phase structures?

Electrospray ionization of tyrosine from a 3:1 (v:v) CH3OH/H2O solution is found to afford an M - H ion which is a 70:30 mixture of phenoxide and carboxylate ions. This corresponds to the gas-phase equilibrium composition and not the liquid-phase proportions. In contrast, the carboxylate is produced as the dominant ion (approximately 95%) from anhydrous CH3CN and CH3CN/H2O mixtures. The addition of small amounts of CH3OH to the solvent, however, convert the M - H ion back into the gas-phase isomeric ratio. The isomeric structure therefore depends on the solvent system from which an ion is sprayed.     

Near-ultraviolet chemiluminescence from the reaction of ammonia with hypobromite in aqueous solution

The chemiluminescence arising from the oxidation of ammonium chloride by sodium hypobromite in aqueous alkaline solution includes a series of peaks in the near-ultraviolet, which is not commonly observed in liquid-phase chemiluminescence. The dominant peak in that region has an intensity maximum at 292 nm and smaller peaks are observed at 313, 334 and 356 nm. The emitted photons are of similar energy to the Vergard-Kaplan transition of molecular nitrogen, a major product of this reaction. However, the spectral distribution is different to that of previously reported gas-phase chemiluminescence attributed to the Vergard-Kaplan transition.     

Pd催化糠醛加氢反应中溶剂依赖效应的理论计算

糠醛催化加氢反应工艺主要分为气相、液相以及催化转移加氢等.相比于糠醛气相加氢,液相加氢为反应提供了更多的可持续性和自由度,但其中溶剂依赖现象对糠醛定向催化转化的影响机制尚不清晰.针对上述问题,本文选用3种溶剂(甲醇、水和环己烷)为研究对象,采用密度泛函方法,从理论计算角度探究了Pd催化糠醛加氢反应中溶剂效应对反应活性和选择性的重要作用.结果表明,在糠醛加氢反应过程中,溶剂一方面能够形成氢键网络促进质子穿梭,另一方面能够稳定反应物、中间体以及生成物,有效降低C=O加氢的能垒.自由能计算结果表明,在液态水、甲醇和环己烷中,随着溶剂极性的降低(水>甲醇>环己烷),第一步C=O氢化的能垒逐渐降低(0.70 eV>0.68 eV>0.44 eV).在水和甲醇介导的糠醛加氢反应过程中,第一步C=O加氢的反应势垒进一步降低为0.47和0.41 eV.差分电荷密度以及Bader电荷分析表明,反应过程中存在糠醛和Pd催化剂之间的电荷转移.分波态密度(PDOS)分析表明,溶剂的加入使d带中心向靠近费米能级的方向移动,表明Pd催化剂的催化活性得到提高.     

Low-temperature synthesis of anatase-brookite composite nanocrystals: the junction effect on photocatalytic activity

Anatase-brookite composite nanocrystals have successfully been synthesized at 50 degrees C using a simple liquid-phase process. The photocatalytic activity of the sample for the gas-phase oxidation of CH3CHO is 5.4 times greater than that of a single-phase anatase sample with comparable crystallite size and surface area. Electron energy loss spectra suggest that this high activity results from junction between anatase and brookite crystals.     

Methanol dehydrogenation in the liquid phase with Ru/active carbon catalyst

In contrast to the gas-phase reaction, the liquid-phase reaction of methanol with Ru/C catalyst scarcely gave methane. Product distribution strongly depended on reaction conditions even under atmospheric pressure.     

The role of pressure in partial oxidation of methane

Analysis of experimental data and results of kinetic simulation throw light on the reasons for which the pressure exerts influence on the partial oxidation of methane to methanol. Among the most important factors are a crucial transition of the reaction to the steady-state chain-branched regime, an increase in the role of nonlinear gas-phase reactions, and a change in the relative contribution of heterogeneous transformations to the overall process.