硼酸保护羟基法合成甘油单月桂酸酯

研究了以甘油、月桂酸为原料,用硼酸保护羟基进行酯化反应合成甘油单月桂酸酯的新方法。最佳合成条件是：ｍｏｌ甘油：ｍｏｌ硼酸：ｍｏｌ月桂酸＝２：１：２,对甲苯磺酸（催化剂）用量为月桂酸用量的１．２０％（ｗｔ％）,在２３０℃反应１ｈ,产品收率为９１．２％,单酯含量为９４．８％,产品经ＩＲ分析。     

微波辅助酶促月桂酸淀粉酯的合成

以天然玉米淀粉和月桂酸为原料,脂肪酶Novozym 435为催化剂,研究了微波辐照下月桂酸淀粉酯的酶促合成.通过对淀粉进行预处理活化来提高淀粉的酯化反应活性,并主要考察了微波功率、月桂酸用量、脂肪酶Novozym 435用量及反应时间等参数对酶促月桂酸淀粉酯合成的影响.采用气相色谱法进行取代度的测定,并以取代度为考察指标,确定了最佳的反应条件.结果表明,淀粉的最佳预处理方法为NaOH/尿素混合溶液法,经该法处理后淀粉的酯化反应活性大大提高;微波辐照技术的应用大大缩短了反应时间,并提高了月桂酸淀粉酯的取代度.适宜的工艺条件为:微波功率为240 W,月桂酸用量为30%,酶加入量为7%,反应时间26 min.     

微波辅助酶促月桂酸淀粉酯的合成

以天然玉米淀粉和月桂酸为原料,脂肪酶Novozym 435为催化剂,研究了微波辐照下月桂酸淀粉酯的酶促合成。通过对淀粉进行预处理活化来提高淀粉的酯化反应活性,并主要考察了微波功率、月桂酸用量、脂肪酶Novozym 435用量及反应时间等参数对酶促月桂酸淀粉酯合成的影响。采用气相色谱法进行取代度的测定,并以取代度为考察指标,确定了最佳的反应条件。结果表明,淀粉的最佳预处理方法为NaOH/尿素混合溶液法,经该法处理后淀粉的酯化反应活性大大提高;微波辐照技术的应用大大缩短了反应时间,并提高了月桂酸淀粉酯的取代度。适宜的工艺条件为：微波功率为240W,月桂酸用量为30%,酶加入量为7%,反应时间26min。在上述反应条件下可以制得取代度为 0.0311的月桂酸玉米淀粉酯。     

无溶剂系统中固定化脂肪酶催化废油脂转酯生产生物柴油

 探讨了无溶剂系统中固定化脂肪酶Novozym 435催化餐饮业废油脂转酯生产生物柴油. 反应副产物甘油可吸附在固定化酶载体表面,采用丙酮洗涤除去甘油可提高酶的稳定性. 适宜的醇/油摩尔比、酶用量、反应温度和摇床转速分别为1, 6.6 U/g, 35～40 ℃和150 r/min,不宜加水到反应体系中. 采用分步加入甲醇的方式可减轻甲醇对酶的毒害作用. 分别在反应进行到6和14 h时用丙酮除去酶表面的甘油,然后按醇/油摩尔比为1的比例加入甲醇继续反应,反应30 h后产物中的脂肪酸甲酯含量为88.6%. 连续反应300 h后,酶活性基本没有下降.     

对甲苯磺酸与碘协同催化合成月桂酸甲酯

以甲醇(1)和月桂酸(2)为原料,碘和对甲苯磺酸协同催化合成了月桂酸甲酯(3),其结构经IR确证。考察了催化剂、反应时间、反应温度和物料比r[n(1)∶n(2)]对3产率的影响。结果表明:在最优反应条件(2 10mmol,r=15∶1,3 mol%TsOH,6 mol%I2,于60℃反应90 min)下,3产率93.5%。     

酶催化和不对称催化及多位催化理论在其中的应用

在简单或复杂结构的有机化合物的催化影响下进行的反应,在化学实践中获得了日益重大的意义。生物催化剂——酶——在有机催化剂中占有特殊的地位,这是生物机体的细胞所制造出的复杂物质。在酶的催化作用下,在生物界中完成着无数的有机物质的转化过程。酶能够迅速而充分地进行在实验室或生产条件下难以实现的许多有机反应。例如,二羟基丙酮的合成这一比较简单的反应,在实验室条件下很难实现,然而,将甘油进行生物化学氧化时,却     

均相介质中脂肪酶催化沙丁鱼油甘油解反应的动力学研究（英文）

多不饱和脂肪酸(PUFAs)的生产多集中在酶催化,与无机催化相比,酶催化具有定向性和更温和的反应条件,因而酶催化制取多不饱和脂肪酸的路线在最近几年引起人们极大的兴趣.本文以优化量的叔丁醇为有机溶剂,研究了脂肪酶Lipozyme~435催化沙丁鱼油甘油解反应生成PUFA(多以甘油一酯或二酯(DAGs,MAGs)的形式存在).首先分析了反应系统的传质影响,考察了脂肪酶载量、温度和进料浓度等因素的影响.采用一个基于甘油酯甘油解和水解这对可逆基元反应的半经验动力学模型,成功地关联了实验的动力学数据.结果表明,温度为323 K,甘油与油的摩尔比为3:1时,生成的MAG可达84 wt%以上.还考察了其他甘油解体系,并在MAG收率、反应速率和动力学参数意义等方面进行了比较.     

手性Salen-Co(Ⅱ)络合物催化芳香酮的不对称还原反应 ——推荐一个综合化学实验

介绍以Salen—Co（Ⅱ）络合物为金属有机催化剂的不对称芳香酮还原反应实验。通过本实验可了解有关手性、金属配合物催化剂的设计合成、催化机理、产率、选择性等基本概念，提高在手性化合物拆分及不对称催化方面的操作能力，加强在有机、无机合成、仪器分析、催化、手性分离及化合物表征等方面的综合能力。讨论了该实验在高年级本科生综合化学实验教学工作中的实践效果。     

均相介质中脂肪酶催化沙丁鱼油甘油解反应的动力学研究

多不饱和脂肪酸(PUFAs)的生产多集中在酶催化,与无机催化相比,酶催化具有定向性和更温和的反应条件,因而酶催化制取多不饱和脂肪酸的路线在最近几年引起人们极大的兴趣。本文以优化量的叔丁醇为有机溶剂,研究了脂肪酶Lipozymeò435催化沙丁鱼油甘油解反应生成PUFA (多以甘油一酯或二酯(DAGs, MAGs)的形式存在)。首先分析了反应系统的传质影响,考察了脂肪酶载量、温度和进料浓度等因素的影响。采用一个基于甘油酯甘油解和水解这对可逆基元反应的半经验动力学模型,成功地关联了实验的动力学数据。结果表明,温度为323 K,甘油与油的摩尔比为3：1时,生成的MAG可达84 wt%以上。还考察了其他甘油解体系,并在MAG收率、反应速率和动力学参数意义等方面进行了比较。     

可透皮吸收的白藜芦醇月桂酸单酯的合成与纯化

以白藜芦醇(Res)、月桂酰氯(LC)为原料,在催化剂4-二甲氨基吡啶(DMAP)的作用下,合成白藜芦醇月桂酸酯。实验结果指出:白藜芦醇与月桂酰氯摩尔比为0.8、催化剂为白藜芦醇质量的5%、pH值为11、反应时间为4 h为合成白藜芦醇月桂酸酯的最佳工艺。因素Res/LC摩尔比对白藜芦醇的转化率影响极显著,催化剂添加量和反应体系pH值为较显著。以半制备高效液相色谱分离纯化白藜芦醇月桂酸单酯的条件为:C18柱;检测波长:306nm;柱温:25℃;进样量:18mL;流速:18mL·min~(-1);时间程序:0～30min,甲醇/水(mL·mL~(-1))由50∶50梯度变化至70∶30,30～45min,甲醇与水体积比恒定为70∶30;将半制备分离物进行无水甲醇重结晶,纯度达99.3%。LC-MS、~1H NMR分析表明:该合成物为白藜芦醇月桂酸单酯。透皮实验结果指出:白藜芦醇月桂酸单酯在0.5 h内可全部透过皮肤。     

Enzymatic synthesis of medium chain monoglycerides in a solvent-free system

The synthesis of monocaprin, monolaurin, and monomyristin in a solvent-free system was conducted by mixing a commercial immobilized lipase with the organic reactants (glycerol and fatty acids) in a 20-mL batch reactor with constant stirring. The effects of temperature, fatty acid/glycerol molar ratio, and enzyme concentration on the reaction conversion were determined. The addition of molecular sieves in the assays of monomyristin synthesis was also evaluated. The reactions were carried out for 5 to 6 h and the nonpolar phase was analyzed by gas chromatography. The best results in terms of selectivity and conversion (defined as the percentage of fatty acid consumed) were achieved when the stoichiometric amount of reagents (molar ratio=1) and 9% (w/w) commercial enzyme were used and the reaction was performed at 60°C. The addition of molecular sieves did not improve the synthesis of monomyristin. Conversions as high as 80%, with monoglycerides being the major products, were attained. After 5 h of reaction, the concentration of monoglyceride was about twice that of diglyceride, and only trace amounts of triglyceride were found. The results illustrate the technical possibility of producing medium chain monoglycerides in a solvent-free medium using a simple batch reactor.     

Glycerol mediated synthesis of 5-substituted 1H-tetrazole under catalyst free conditions

We have developed simple,cost effective and environmentally benign protocol for the synthesis of 5-substituted 1H-tetrazoles via[2,3]cycloaddition reaction from organic nitriles and sodium azide in glycerol under catalyst free condition.The corresponding 5-substituted 1H-tetrazoles were obtained with good to excellent yields(68-95%).     

溶剂量子化学特性对鱼油多不饱和脂酰甘油酯非水相酶促合成作用的影响

鱼油多不饱和脂酰甘油酯非水相酶促合成率与底物摩尔比例、反应温度、溶剂分子性质及溶剂系统中的最初水分含量有密切关系。溶剂分子的量子化学特性对非水相酶促酯化反应具有极为重要的影响。酯化率依溶剂分子最高占有轨道能量的增高及前沿轨道能差的减少而增加。溶剂分子电荷密度、静电势及前沿轨道系数对酯化率无显著影响。说明溶剂分子内不存在作用中心，溶剂分子主要是为非水相酶促酯化反应提供易于形成酶一底物电荷转移复合物的诱导场环境。     

Room temperature synthesis of glycerol carbonate catalyzed by N-heterocyclic carbenes

N-Heterocyclic carbenes were used as efficient organocatalysts for the synthesis of glycerol carbonate from glycerol and dimethyl carbonate. The reaction takes place in a liquid mixture of reactants without solvent at room temperature. It provides glycerol carbonate in high yield using 2.6–4 mol % of catalyst in a reaction period of 20–30 min.     

Study of the reaction of methyl 4‐nitrobenzenesulfonate and Br− in water–glycerol cationic micellar solutions

The reaction of methyl 4‐nitrobenzenesulfonate (MNB) and Br^? has been studied in water–glycerol (GLY) alkyltrimethylammonium bromide micellar solutions, with the weight percentage of glycerol up to 50%. A pseudophase kinetic model was used for quantitatively discussing the kinetic data. Results showed that the equilibrium‐binding constant for the organic substrate molecules to the cationic micelles decreases upon increasing the amount of glycerol present in the micellar reaction media. The second‐order rate constant of the reaction in the micellar pseudophase is practically independent of wt% of GLY. Similar results were found in other water–organic solvent alkyltrimethylammonium bromide micellar solutions for the same process. However, the dependence of the reaction rate, for a given surfactant concentration, on the wt% of organic solvent is weaker for glycerol than for the other organic solvents. This was explained by considering that the cationic micellar ionization degree is nearly independent of wt% GLY. As a consequence, bromide ions concentration in the interfacial region (the reaction site) does not change by varying wt% of GLY. © 2008 Wiley Periodicals, Inc. Int J Chem Kinet 40: 845–582, 2008     

Process development for production of medium chain triglycerides using immobilized lipase in a solvent-free system

The synthesis of tricaprylin, tricaprin, trilaurin, and trimyristin in a solvent-free system was conducted by mixing a commercial immobilized lipase with the organic reagents (glycerol and fatty acid) in a 20-mL batch reactor with constant stirring. The effects of temperature, fatty acid/glycerol molar ratio, and enzyme concentration on the reaction conversion were determined. The reactions were carried out for 26 h and the nonpolar phase was analyzed by gas chromatography. Appreciable levels of medium chain triglycerides were achieved, except for tricaprylin. The higher selectivity values for the production of triglycerides were attained under the following conditions: a fatty acid/glycerol molar ratio of 5; enzyme concentration of 5 or 9% (w/w); and temperatures of 70°C (tricaprin), 80°C (trilaurin), and 90°C (trimyristin). After completion of the esterification reaction under these conditions, the recovery of the triglyceride and fatty acids, and the reusability of the enzyme were studied. The unreacted fatty acid and the produced triglyceride were satisfactorily recovered. The commercial immobilized lipase was used in 10 consecutive batch reactions at 80°C, with 100% selectivity in the trilaurin and trimyristin synthesis. The possibility of enzyme reuse and the recovery of residual fatty acid are relevant results that contribute to increasing the viability of the process.     

甘油作溶剂、微波促进苯并噁唑类化合物的合成

苯并噁唑类化合物在医药、化工、有机合成等方面应用广泛,其合成具有重要意义。以邻氨基苯酚与苯甲醛类化合物为原料,物质量的比为1∶1,用绿色试剂甘油做溶剂,微波加热促进合成苯并噁唑类化合物。聚焦微波功率为20W,反应温度110℃。在此条件下,以80%~91%的产率得到相应的目标产物。该方法具有溶剂无污染、反应条件温和、操作简便、产率较高、反应底物易得,反应快速简便等优点,为现有方法提供了有益和重要的补充。     

Enzymatic synthesis of medium-chain triglycerides in a solvent-free system

The synthesis of tricaprylin, tricaprin, trilaurin, and trimyristin in a solvent-freesystem was conducted by mixing a commercial immobilized lipase (Lipozyme IM 20, Novo Nordisk, Bagsvaerd, Denmark) with the organic reactants (glycerol and fatty acids) in a 20-mL batch reactor with constant stirring. In a first set of experiments, the effect of water concentration (0–6%) on the reaction conversion was shown to be negligible. In a second set of experiments, the effects of temperature (70–90°C), fatty acid/glycerol molar ratio (1–5), and enzyme concentration (1–9%[w/w]) on the reaction conversion were determined by the application of a 3×3 experimental design. The reactions were carried out for 26 h and the nonpolar phase was analyzed by gas chromatography (GC). Appreciable levels of medium-chain triglycerides were achieved, except for tricaprylin. For the triglyceride production, higher selectivity was attained under the following conditions: molar ratio of 5, enzyme concentration of 5 or 9% (w/w) and temperatures of 70°C (Tricaprin), 80°C (trilaurin), and 90°C (trimyristin). Statistical analysis indicated that the fatty acid/glycerol molar ratio was the most significant variable affecting the synthesis of triglycerides.     

Synthesis of Microporous Silica Spheres

Spherical microporous silica powders with a narrow size distribution have been prepared by a precipitation technique involving the hydrolysis reaction of a silicon alkoxide in ethanol. The formation of the important microporosity has been investigated following two templating methods: the co-hydrolysis and condensation of two alkoxides, one of which presents porogen function, and the adsorption of an organic compound (glycerol) as the porogen. In both processes, the organic porogen is removed by a simple calcination. In the first method, the addition of more than 20 mol% of the porogen alkoxide, necessary for generating enough microporosity, disturbs completely the condensation process resulting in microporous, nonuniform silica particles of large size distribution. The best result has been obtained with the glycerol method where submicrometer-sized silica spheres with a very narrow size distribution and about 40 vol% porosity have been synthesized. The presence of glycerol during the synthesis considerably affects the precipitation mechanism, resulting in a larger mean particle size. The use of an aggregative growth model has successfully been employed to explain the effect of the porogen during particle formation. The precipitation mechanism of silica involves the aggregation between particles of similar size until a critical size is reached, resulting in a uniform particle size distribution. In the presence of glycerol, it has been shown that a second aggregative growth between still-nucleating primary particles and large particles occurred with increasing reaction time. This second aggregative growth appears at an intermediate stage of the precipitation process and is due to both the precipitation of smaller primary particles and the destabilization of the colloidal stability of the system. This explains why the final particle size reached in this system is larger compared to silica particles synthesized without glycerol and shows how glycerol is incorporated in the silica particles. The synthesis of silica microporous spheres of narrow size distribution, by varying particle size and porosity, should yield a wide range of aqueous silica slurries for particular chemical mechanical polishing applications. Copyright 2000 Academic Press.     

Process intensification for synthesis of triglycerides of capric acid using green approaches

The present research focuses on intensified synthesis of tricaprin by esterification reaction between capric acid and glycerol catalysed by dry amberlyst-15 using ultrasonication approach. Effect of several reaction conditions like molar ratio, reaction temperature, and amberlyst-15 loading on the rate of conversion has been studied. Effect of ultrasonic conditions like duty cycle and irradiation time on the intensified synthesis is investigated. Recyclability of amberlyst-15 is studied to make process more economical. It is investigated that the optimum reaction conditions which gave maximum conversion of 95% were molar ratio of capric acid: glycerol as 3:5, reaction temperature 90 ​°C, 4% amberlyst −15 loading. It was further investigated that ultrasonic conditions which gave intensified synthesis were 70% duty cycle and irradiation time of 120 ​min. The ultrasonic assisted process was compared with conventional synthesis. Conventional synthesis gave 30% yield in 120 ​min and 82% in 18 ​h. Amberlyst-15 was successfully reused for 13 cycle without any change in the conversion (%) of reaction.