阳离子交换树脂催化氯乙酸和甲醇酯化反应动力学

以强酸性阳离子交换树脂为催化剂合成氯乙酸甲酯，研究催化反应的动力学，研究确定为表观正、逆向二级反应，求得其表观活化能为Ｅａ＋＝３４．２０１ＫＪ／ｍｏｌ，Ｅａ＝４８．３０５ＫＪ／ｍｏｌ。     

磺酸型阳离子交换树脂催化合成肉桂酸甲酯

以磺酸型阳离子交换树脂为催化剂，由肉桂酸和甲醇合成了肉桂酸甲酯。考察了反应条件对酯化反应的影响和树脂的催化稳定性。结果表明，肉桂酸的转化率可达９５．５％，且催化剂的性能稳定。     

阳离子交换树脂催化合成巯基乙酸酯

使用阳离子交换树脂Ｄ６１、Ｄ７２为催化剂，合成了七种巯基乙酸酯。文中对影响反应的诸因素进行了讨论。酯收率为９０％左右。     

微波辐射下阳离子交换树脂催化合成1-萘乙酸甲酯

以阳离子交换树脂732、NKC-9、D072和D061为催化剂,在微波条件下使用1-萘乙酸和甲醇合成1-萘乙酸甲酯.研究了微波法及常规法活化阳离子交换树脂的催化性能.实验结果表明,微波法活化阳离子交换树脂的催化性能好,酯化反应时间只需30min,酯产率就高达99.05%;使用过的催化剂用微波法处理活化后,催化酯化的产率最高也达97.16%.     

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。     

强酸性阳离子交换树脂催化合成醋酸正丁酯的动力学研究

以强酸性阳离子交换树脂Amberlyst 15作为催化剂,研究了醋酸与正丁醇合成醋酸正丁酯的反应动力学;考察了搅拌速度、催化剂粒径、温度、催化剂用量,以及酸醇物质的量之比对醋酸转化率的影响;建立了拟均相动力学模型,对实验数据进行了拟合,并估算了相应的动力学参数.结果表明,由拟均相动力学模型得到的计算值与实验值吻合较好.     

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。     

金属离子负载修饰阳离子树脂在酯化反应中的研究

将催化精馏中常用作催化填料的强酸性阳离子交换树脂用金属离子负载修饰后，考察了树脂催化性能的改变及树脂结构对催化性能的影响。实验表明，经修饰后树脂的催化能力都高于原树脂，在不分水的情况下，合成乙酸乙酯时乙酸的转化率最高可达73％，具有很好的选择性，金属离子能与树脂的磺酸基团产生络合，提高了树指的催化性能，所形成的新酸中心不会被阳离子交换而失活。     

应用阳离子交换树脂催化水解蔗糖Ⅰ.蔗糖非均相催化水解反应动力学

实验选用两种H+型强酸性阳离子交换树脂为催化剂，研究蔗糖在离子交换树脂柱内的非均相催化反应动力学。结果表明，温度每升高10℃，蔗糖在两种离子交换树脂柱内的水解速度分别增加到2．1和3．3倍；蔗糖在两种离子交换树脂柱内水解反应的表观活化能分别为64．96kJ／mol和79．59kJ／mol，其水解反应有明显的扩散控制。     

强酸阳离子交换树脂催化性能的研究

通过叔丁醇脱水生成异丁烯的反应研究对比了国内外常见种类的凝胶型和大孔型强酸阳离子交换树脂的催化性能，并对树脂的性质，预处理方法，以及其用量和再生程度等因素对树脂催化活性的影响进行了研究。在此基础上，合成了具有较高催化活性的新型大孔强酸阳离子交换树脂。     

Specific features of solketal synthesis on KU-2-8 cation-exchange resin

Technological specific features of the solketal synthesis on a KU-2-8 cation-exchange resin were improved. Data are presented on the mutual solubility of the components in the glycerol–acetone–water and glycerol–acetone–water–ethanol systems. It is shown that use of ethanol for homogenization of the starting reagents is more than twice more efficient than performing the process with delivery of an emulsion of the reagents or reaching a full solubility of glycerol in acetone due to the 20-fold excess of the latter at 35°C. It is shown that the delivery of a glycerol emulsion in acetone to an immobile bed of a heterogeneous catalyst working in the falling-film mode leads to flooding of the reactor at spraying densities exceeding 0.15 m³ m^–2 h^–1.     

Structure and catalytic properties of chromium complexes on cation-exchange resin surfaces

The type of bonding of Cr(III) on the surface of cation-exchange resins has been studied. The complexes of Cr(III) with ethylenediamine were obtained by direct synthesis on the surface. Coordination to nitrogen bases increases the catalytic activity of Cr(III) ions in hydrogen peroxide decomposition.

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Cr(III) . Cr(III) . Cr(III) .

     

Kinetics of esterification of palmitic acid with isobutyl alcohol on ion-exchange resin pellets

Cylindrical pellets were made by mixing ion-exchange resin particles with binding powders and heating to 140°C. To compare catalytic activities of these resin pellets with those of resin particles and sulfuric acid, the esterification of palmitic acid with isobutyl alcohol was carried out in a batch reactor. The rate equation for sulfuric acid could be applied to ion-exchange resins although the values of parameters were different.     

Kinetics and molecular orbital calculations of desulfonation of strong acid cation-exchange resin

This paper deals with the desulfonation properties of some strong acid cation-exchange resins. The sulfate concentration in solution is continuously increased when a strong acid cation-exchange resin is mixed with water. The leaching of sulfate results from the desulfonation of the fixed group, and the amount of leached sulfate depends on the counter ion charge, the crosslinking degree and the exchanger matrix. The effects of the counter ion charge on the desulfonation rate suggested that the counter ion induces the nucleophilic attack of a water molecule on the sulfo group. This interpretation was supported by semiempirical molecular orbital calculations for the C₆H₅SO₃⁻M^m+ (M^m+ = Na⁺, Mg²⁺ and Al³⁺) systems, and the transition state of the Na⁺ system was successfully predicted by DFT calculations. The crosslinking degree influenced the desulfonation rate, which can be related to the decreasing hydration number of each counter ion in the resin phase with the increasing crosslinking degree. Furthermore, different exchanger matrices produced the differences in the rates, which may be derived from the electron-density donation from the exchanger matrix to the sulfo group. The desulfonation is governed by the electron-density of the sulfur atom and the water activity in the solid phase.     

Kinetics and mechanism of esterification of epoxy resin in presence of triphenylphosphine

The kinetics of esterification of bisphenol‐A based epoxy resin with acrylic acid in presence of triphenylphosphine has been studied. The reaction exhibits a first‐order rate dependence with respect to [Epoxy] and [Catalyst]. A first‐order dependence of rate with respect to [Acid] has been observed during a particular kinetic run. However, a retarding effect of [Acid] on the rate has been observed by increasing the initial concentration of acid. A suitable mechanism consistent with the kinetic data is proposed and discussed. © 2004 Wiley Periodicals, Inc. Int J Chem Kinet 36: 280–285, 2004     

聚苯乙烯二乙醇胺树脂催化合成丙酸苄酯的研究

应用聚苯乙烯二乙醇胺树脂（PSDEA）催化苄氯与丙酸的酯化反应，合成了丙 酸苄酯。研究结果表明，聚苯乙烯二乙醇胺树脂具有较高的催化活性。考察了丙酸 ／苄氯摩尔比、催化剂用量和反应时间对酯产率的影响，在典型反应条件（丙酸： 苄氯摩尔比＝1．25：1，16．7gPSDEA／摩尔苄氯，80℃浴温，反应4．0h）下，所 得丙酸苄酯的产率为95．5％，该催化剂易于回收且可重复使用、具有良好的活性 稳定性。