球形聚萘并噁嗪树脂酸催化酯化反应

研究了球形聚萘并GFDA1嗪树脂酸催化剂的制备方法,考察了其对酯化反应的催化活性. 萘并GFDA1嗪预聚体在甲基硅油中反相悬浮固化得到球形聚萘并GFDA1嗪树脂,再经磺化反应制得聚萘并FDA1嗪树脂酸,用扫描电子显微镜及其搭载的能谱仪(EDS)考察了催化剂的外貌特征和表面主要元素分布,用Tg分析了催化剂的热稳定性,通过催化冰醋酸与乙醇酯化反应评价了催化剂的活性. 结果表明,球形聚萘并GFDA1嗪树脂在300 ℃以下不发生热失重,45 ℃磺化得到的催化剂活性最高,树脂负载磺酸基团为4.29 mmol/g. 在反应时间2 h,催化剂用量为冰醋酸质量分数的3%和n(醇):n(酸)=2:1时,冰醋酸的转化率为77%.     

脂肪酶催化乳酸与乙醇合成乳酸乙酯的反应动力学

对脂肪酶催化乳酸与乙醇合成乳酸乙酯反应的动力学进行了研究,根据乒乓机制和双底物抑制的特性建立了反应速率方程.反应时间常数(tR)和扩散时间常数(tD)的计算结果表明,酯化反应速率未受到明显的限制.反应速率方程可以很好地预测实验结果,由非线性拟合得到的动力学参数中,乳酸(A)和乙醇(B)的抑制常数分别为KiA=10.7mmol/L和KiB=275.0mmol/L.这说明乳酸作为短链极性脂肪酸,对酶的失活作用远大于乙醇.乳酸在微液层中聚集并产生了使酶失活的低pH值环境,同时在酯化反应中存在竞争性抑制作用.     

NaA分子筛膜蒸汽渗透促进丙烯酸/乙醇的酯化反应

以对甲苯磺酸为催化剂,利用亲水性NaA分子筛膜蒸汽渗透过程,选择性地将丙烯酸和乙醇酯化反应产物中的水原位分离出反应器,打破反应平衡限制,使反应不断向右进行,反应15 h丙烯酸转化率达到100%。     

强酸性阳离子交换树脂催化酯化丙烯酸和甲醇合成丙烯酸甲酯的反应动力学

以丙烯酸和甲醇为原料,强酸性阳离子交换树脂Amberlyst-15为催化剂,对苯二酚为阻聚剂,合成丙烯酸甲酯。 考察了醇酸摩尔比、催化剂用量和温度对反应过程的影响,在实验范围内,随着温度或者催化剂用量的增加,反应速率加快,丙烯酸的转化率也不断提高。 醇酸摩尔比的增加能提高丙烯酸的转化率,反应速率出现先增加后减缓的现象。 与此同时,建立该催化酯化反应的Pseudo-Homogeneous（PH）的理想和非理想以及Langmuir-Hinshelwood（LH）反应动力学模型,辨识得到相应反应动力学方程。 经比较,采用活度替代物质的量浓度的LH模型的平均相对偏差(MRD)最小,计算值为1.466%,最适合实际反应。     

茂金属催化乙酸与丁醇酯化反应

以二茂铁、二茂钛、二茂锆和取代茂锆为催化剂用于催化酯化合成乙酸丁酯, 探讨了不同茂金属、反应时间和催化剂用量对反应性能的影响. 结果表明, 低含量的茂金属就可高效催化酯化反应. 当催化剂为二茂钛, 其含量为 0.049%(摩尔比)时, 反应 30 min 产物乙酸丁酯的分离收率达到 90%, 纯度达到 98%. 以 400 目不同温度活化的硅胶为载体, 考察了负载二茂锆催化剂的性能. 当硅胶在 400 ℃ 焙烧 4.0 h, 负载二茂锆催化剂用量为 Zr/丁醇 = 0.487% (摩尔比), 反应后乙酸丁酯收率为 90.6%, TOF = 318 h-1. 该反应的产物后处理不需要用水洗涤, 无废水排出, 催化剂易回收利用, 是一个绿色的反应过程.     

New Reaction of Dimethylformamide with Acrylic Acid

Russian Journal of Organic Chemistry - A new homogeneous reaction of dimethylformamide (DMF) with acrylic acid was studied. The reaction afforded previously unknown...     

Development of Kinetic Mechanism for the Esterification of Acrylic Acid with Hexanol Catalyzed by Ion‐Exchange Resin

The heterogeneous esterification reaction of acrylic acid with hexanol over three different cation‐exchange resins, Amberlyst 131, Amberlyst 15, and Dowex 50Wx‐400, was investigated. Surface area, pore volume, average pore diameter, and acid capacity analyses were carried out for these three catalysts. Amberlyst 131 gave the highest conversion, and therefore, further experiments were performed catalyzed by Amberlyst 131. The absence of external and internal mass transfer resistances was investigated for the esterification of acrylic acid with hexanol. Experiments showed that the reaction is controlled by chemical step rather than external and internal mass transfer steps. The effects of temperature, catalyst loading, and alcohol to acid molar ratio on the conversion of acrylic acid were determined. The activation energy and kinetic and adsorption constants were determined according to the Langmuir–Hinshelwood–Hougen–Watson mechanism.     

CTAB对H2O2氧化抗坏血酸反应动力学的影响

H₂O₂氧化抗坏血酸H₂A的反应为一复杂过程,其过程可用下面可逆连续反应来描述:HA－＋H₂O₂ A,本文用热导式热量计研究了该复杂反应在25 ℃和pH=7的磷酸缓冲溶液(离子强度μ=0.1 mol•L^－1)以及在阳离子表面活性剂十六烷基三甲基溴化铵(CTAB)存在下的反应动力学, 获得了不同CTAB浓度下该复杂反应的表观动力学参数k₁、k₂和k_－1.研究结果表明,表面活性剂CTAB单体分子对反应参数k_－1影响不大, 但却能催化第一步正向反应使k₁变大,而使k₂减小; 在临界胶束浓度cmc附近k₁达到最大值,随后又降低；低浓度胶束对k_-1影响不大,而使k₂增大；高浓度胶束则使k_-1增大而使k₂减小. 低浓度CTAB胶束对的活性影响不大, 而高浓度CTAB胶束将较显著地促进的歧化过程, 减缓的氧化过程. 胶束的静电效应、疏水效应和局部浓聚效应是影响上述反应的重要因素.     

杂多酸为催化剂的丙烯与醋酸气-液酯合成的反应模型初探

杂多酸对有机羧酸与低级烯烃的直接加成反应具有催化作用,但一般需在高压下进行。作者研究了较低压力(0.5～2.0 MPa)下的醋酸与丙烯、丁烯的加成酯化反应,结果较令人满意。本文初步探讨了醋酸与丙烯加成反应模型,为预测最佳反应条件提供了证据。     

壳聚糖席夫碱钯催化碘代苯与丙烯酸生成肉桂酸

壳聚糖席夫碱钯催化碘代苯与丙烯酸生成肉桂酸;壳聚糖;席夫碱钯催化剂;肉桂酸     

Kinetics of the Esterification Reaction Catalyzed by Lipase in W／O Microemulsions of Alkyl Polyglucoside

A novel kinetic mechanism of esterification reaction of 1-hexanoic acid with 1-butanol,catalyzed by lipase, was studied in water-in-oil microemulsions. The microemulsions were formed by alkyl polyglucoside C10G1.54/1-butanol/cyclohexane/phosphate buffer solution. The restult shows that when the ratio of mol concentration of 1-butanol to 1-hexanoic acid is about 3.0,the initial rate V0 get the maximum values. This phenomenon was explained by the modified fishlike phase diagrams.     

Theoretical and Experimental Insights of Benzimidazole Catalyzed by the Epoxy–Acrylic Acid Reaction

This study focuses on the experimental and molecular-level investigation of epoxy acrylate formation. Epoxy acrylate vinyl ester resin was prepared by a reaction of diglycidyl ether of bisphenol-A-based epoxy resin and acrylic acid, using benzimidazole as a catalyst. It was confirmed that benzimidazole can effectively catalyze this reaction. FTIR analysis of the product revealed a simple addition esterification reaction between the epoxide group and carboxylic group of acrylic acid excluding the side reactions (e.g., etherification). DFT computational studies were performed to theoretically explore the insights of reaction mechanisms. The calculations revealed that the benzimidazole-catalyzed reaction dominates the uncatalyzed reaction. A comparison of calculated activation energies showed that concerted mechanisms are less significant in such reactions owing to their high activation barriers.     

多种方法分析与评价乙酸乙酯合成实验中产物之纯度

采用气相色谱内标法、面积归一化法及NMR内标法3种方法对乙酸乙酯合成反应中的产物进行纯度分析.GC内标法可抵消由于操作条件的波动而带来的误差,只需内标物与待测组分在同样条件下出峰且分离度较好,定量精度高,测出的乙酸乙酯纯度最低;应用NMR内标法可同步完成纯度分析和结构鉴定,且无需引入校正因子,操作简便.     

Acid Catalyzed Reaction of Isocyanide with Epoxide

We have reported the acid–catalyzed cycloadditions of isocyanide with carbonyl compounds^1,2) and with Schiff bases,³⁾ in which the isocyanide component is incorporated as an imine group into the heterocyclic products. The cycloaddition of isocyanide with oxetane, four–membered cyclic ether, has also been realized with the aid of BF₃.Et₂o, which produces 1:1 cyclic adduct of 2–iminoterrahydrofuran.⁴⁾.     

Homogeneous Precipitation of Calcium Carbonates by Enzyme Catalyzed Reaction

Catalytic decomposition of urea by urease in aqueous calcium chloride solutions was used to rapidly prepare calcium carbonate polymorphs at room temperature. The nature of the resulting particles depended on the concentration of the enzyme and, in a strong manner, on the agitation of the reacting solutions. In an undisturbed system an amorphous precipitate is formed first, which readily crystallized to vaterite and upon aging changed to calcite. Under the influence of magnetic stirring, the amorphous phase could be not observed; instead smaller particles were initially obtained, which aggregated to vaterite and calcite. Similarly, the application of ultrasonic energy produced small vaterite particles at the early stages. It is apparent that enzyme macromolecules are important in the development of calcite faces and, as such, they exert significant influence on calcite morphology, without being present in detectable amounts in the resulting solids. Copyright 2001 Academic Press.     

Heterogeneous Solid Acid Catalysts for Esterification of Free Fatty Acids

Use of low-quality (and inexpensive) feedstock such as waste oils and animal fats for biodiesel synthesis has been continuously researched as a prospective means of improving the economic efficiency of the process. Pretreatment of free fatty acids by catalytic esterification is necessary for achieving this purpose. This paper reviews some relevant studies on heterogeneous acid catalysts that have been shown to be effective for this reaction.     

Activity-Based Models to Predict Kinetics of Levulinic Acid Esterification

The solvent is of prime importance in biomass conversion as it influences dissolution, reaction kinetics, catalyst activity and thermodynamic equilibrium of the reaction system. So far, activity-based models were developed to predict kinetics and equilibria, but the influence of the catalyst on kinetics has not been succesfully predicted by thermodynamic models. In this work, the thermodynamic model ePC-SAFT advanced was used to predict the activities of the reactants and of the catalyst at various conditions (temperature, reactant concentrations, γ-valerolactone GVL cosolvent addition, catalyst concentration) for the homogeneously acid-catalyzed esterification of levulinic acid (LA) with ethanol. Different kinetic models were applied, and it was found that the catalyst influence on kinetics could be predicted correctly by simultaneously solving the dissociation equilibrium of H₂SO₄ catalyst along the reaction coordinate and by relating reaction kinetics to proton activity. ePC-SAFT advanced model parameters were only fitted to reaction-independent phase equilibrium data. The key reaction properties were determined by applying ePC-SAFT advanced to one experimental kinetic curve for a set of temperatures, yielding the reaction enthalpy at standard state , activation energy and the intrinsic reaction rate constant k=0.011 s⁻¹ at 323 K, which is independent of catalyst concentration. The new procedure allowed an a-priori identification of the effects of catalyst, solvent and reactant concentration on LA esterification.     

层柱稀土盐催化合成乙二醇单烷基醚乙酸酯反应动力学

本文以Ce(SO4)2进行了酯化反应动力学进行研究,比其它类型催化剂具有较高的催化反应活性,通过Ce4 阳离子进行层间取代增大了层柱粘土催化剂的L酸及B酸位的数量和强度,酯化反应过程中生成的水受到Ce4 的诱导作用,进而造成L酸位向B酸位转换(B酸为主),导致催化剂表面产生较强的B酸酸强度.pH值测定提供了有力支持,结果表明:只有B酸位大于70%,并且在加人层柱粘土催化剂后乙二醇单烷基醚溶液pH值小于1时,在50～150℃的温度范围内才有良好的酯化反应活性和选择性.活性实验表明了层柱粘土催化剂可以重复使用,XRD也表明了新鲜的和重复使用的催化剂组成和晶相一样;同时对反应动力学作用用积分法进行研究,提出了这类反应本质的一般动力学方程.