辛弗林衍生物的合成

以苯甲醚为起始原料,与乙酰氯发生付-克酰基化后脱甲基得到4-羟基苯乙酮,然后与液溴进行α-溴代得到2-溴-1-(4-羟苯基)乙酮,再与叔丁胺进行胺化得到1-(4-羟基苯基)-2-(叔丁基氨基)乙酮,最后用氢硼化钠还原合成目标产物1-(4-羟基苯基)-2-(叔丁基氨基)乙醇,总收率约为42.3%。     

NaBF4催化合成二吲哚甲烷类化合物

在乙醇水溶液中,以Na BF4为催化剂,通过吲哚与芳香醛间的串联反应合成了二吲哚甲烷衍生物。考察了催化剂种类、反应介质、温度、反应时间等因素对反应的影响,在优化条件下以较高产率得到了一系列目标产物。     

炭黑负载Pt-Sn双金属催化剂对乙醇的电催化氧化性能

采用一步还原法(乙二醇为还原剂)与两步还原法(在聚乙烯吡咯烷酮PVP保护下,先用硼氢化钠还原制备Sn溶胶,沉积Pt后用乙二醇还原)制备了炭黑负载Pt-Sn双金属催化剂,利用循环伏安法和计时电流法考察了催化剂制备方法、Pt/Sn原子比、溶液p H值、PVP/Sn质量比、反应介质等对乙醇室温电催化氧化活性和稳定性的影响.以X光衍射、透射电镜及电化学活性面积测定对所得催化剂进行了表征.发现引入Sn明显提高了Pt催化剂对乙醇的电催化活性与稳定性,两步还原法得到的Pt3Sn/C催化剂具有更小的颗粒尺寸,更大的电化学活性面积及更高的乙醇氧化活性与稳定性.与酸性介质相比,该催化剂在碱性介质中的电化学活性更好.     

聚乙二醇和液体石蜡介质对完全液相法制Cu-Zn-Al催化剂结构及CO加氢催化性能的影响

催化剂的形成和使用环境对催化剂的结构和性能会产生重要的影响.我们采用完全液相法,以PEG-400和液体石蜡分别作为热处理介质制备Cu-Zn-Al催化剂,用X射线粉末衍射、H2程序升温还原、N2吸附、X射线光电子能谱对其进行表征,考察热处理介质对催化剂结构的影响;以相应的热处理介质作为浆态床反应介质,考察介质对CO加氢催化反应性能的影响.结果表明,PEG-400作为热处理介质有助于提高催化剂的比表面积、Zn O的分散度和表面铜含量,催化剂中存在难还原的Cu+,有利于形成Cu+-Cu0之间的协同作用;在反应过程中,PEG-400作为反应介质可以抑制铜晶粒的长大,有利于乙醇的生成及C5烃选择性的提高,但催化剂的结构和表面组成会发生较大的变化.     

配体对钯纳米催化剂的形成及其电活性的影响

分别在EDTA,甘氨酸(Gly)和木质素磺酸钠(Ls)存在下,以硼氢化钠为还原剂,将Pd²⁺还原为Pd纳米颗粒并负载在多壁碳纳米管(MWCNT)表面。采用扫描电镜(SEM),透射电镜(TEM)和X射线衍射(XRD)对纳米Pd催化剂的形貌和微结构进行了表征。结果表明:EDTA存在时,所形成的Pd纳米颗粒(Pd-EDTA/MWCNT)的粒径更小,在MWCNT上的分散度更高。采用循环伏安(CV)和计时伏安技术(CA),研究了催化剂在碱性环境中对乙醇的电催化活性。在碱性溶液中对乙醇氧化的电化学研究表明:在Pd-EDTA/MWCNT催化剂上,乙醇氧化反应的起始电位较低,电流密度最大,电子传递阻力较小,反应速率较大,并且对乙醇氧化的电催化活性保持稳定。     

不同提取方法对所得稻壳基木质素的影响研究

本文以稻壳这种在我国来源十分丰富的农业副产物为原料,采用三种方法(乙二醇法、乙醇法、碱法)提取稻壳中的木质素,考察相应处理条件下的木质素提取率、羟基含量来确定提取适宜条件。乙二醇提取法所得木质素的羟基值和产率可以分别达到275.2mg/g和45.2%;乙醇法在适宜的提取条件下得到稻壳基木质素羟基值和产率分别为269.1mg/g和51.1%;碱溶液提取法可获得羟基值和产率分别为324.7mg/g和64.1%的碱木质素,无论何种木质素都富含活性官能团为后续再利用提供条件。     

植物还原法制备负载型金纳米催化剂催化乙醇选择氧化反应

采用侧柏叶提取液还原氯金酸制备负载型金纳米催化剂,通过乙醇选择氧化反应,筛选出催化性能较好的TiO2载体。以TiO2载体为载体,考察了Au负载量、焙烧温度、催化剂用量、碳酸氢钠添加量及催化剂反应条件(时间、温度、压力)等因素对乙醇选择氧化反应的影响。结果表明,1.5%Au/TiO2催化剂(Au负载量为1.5%,质量分率,下同)催化乙醇选择氧化反应性能最佳,产物为乙醛、乙酸乙酯和缩醛,0.5%碳酸氢钠添加剂可抑制缩醛的生成,并可显著提高乙醇转化率和乙酸乙酯选择性。通过优化催化反应条件(1.5%Au/TiO2催化剂焙烧温度为400℃、用量为0.4 g、反应温度为100℃、氧气压力为3 MPa、反应时间为3 h时),乙醇转化率为47.9%,乙酸乙酯选择性为89.1%。     

Four-Component Domino Reaction for the Synthesis of 1-(1H-Indol-2-yl)-1H-pyrazolo[1,2-b]phthalazine-5,10-diones

Facile, efficient, four-component domino reaction of dialkylphthalates, hydrazine hydrate, indole-3-carboxaldehydes, and malononitrile/ethyl cyanoacetate leads to the formation of 1-(1H-indol-2-yl)-1H-pyrazolo [1,2-b] phthalazine-5,10-diones in the presence of InCl₃ as catalyst in refluxing ethanol for 1 h in good yields. This four-component domino reaction transformation presumably proceeds via sequential addition, dehydration, condensation, and cyclization steps.     

Equilibrium solubility of carbon dioxide in 2(methylamino)ethanol

In this paper the equilibrium solubility of carbon dioxide in 1.0 M, 2.0 M and 4.0 M 2(methylamino)ethanol (MAE) is measured at 303, 313 and 333 K, and at CO₂ partial pressures ranging from 1 to 100 kPa using stirred cell reactor. The Kent-Eisenberg model was used to predict the solubility of carbon dioxide in MAE solutions. The equilibrium constant representing hydrolysis of carbamate ion is correlated with temperature, CO₂ partial pressure and amine concentration by non-linear regression, using experimental results of carbamate ion concentrations. The model predicted results showed good agreement with the experimental solubility results. The solubility profile of CO₂ in MAE showed better performance when compared with other commercial amines.     

Combined chemical and phase equilibrium for the hydration of ethylene to ethanol calculated by means of the Peng-Robinson-Stryjek-Vera equation of state and the Wong-Sandler mixing rules

Due to the economics of the ethylene market and the subsidized production of fermentation-based ethanol in some countries, use of the ethylene hydration process to make ethanol has been steadily declining. The economics of this process might improve by combining the reaction and separation in a reactive distillation column, whose conceptual design requires a study of the combined chemical and phase equilibrium (CPE) of the reacting system. In this work, the Peng-Robinson-Stryjek-Vera equation of state was combined with the UNIQUAC activity coefficient model through the Wong-Sandler (WS) mixing rules in order to correlate the available experimental data for the vapor-liquid equilibria (VLE) of the ethylene-water, ethylene-ethanol, and ethanol-water binary systems at 200 °C. The interaction energies of the UNIQUAC model and the binary interaction coefficient of the WS mixing rules were used as the fitting parameters. From the optimum values of these parameters, both the VLE and the combined CPE of the ethylene-water-ethanol ternary system were predicted at 200 °C and various pressures. At this temperature, the catalytic activity of a H-pentasil zeolite has already been reported to exhibit a maximum for ethylene hydration, and also the experimentally measured two-phase region of the ternary system is sufficiently wide. By means of the reactive flash method, the chemical equilibrium compositions of the liquid and vapor phases were determined for several pressures, and the equilibrium conversion and the vapor fraction were calculated as functions of the ethylene to water feed mole ratio. It turns out that the vapor-liquid mixed-phase hydration of ethylene achieves equilibrium conversions much higher than those computed for a vapor-phase reaction that would hypothetically occur at the same conditions of pressure and feed mole ratio. It was found that the reactive phase diagram of the ternary system exhibits a critical point at 200 °C and 155 atm.