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1.
磷钨酸催化合成三醋酸甘油酯   总被引:18,自引:0,他引:18  
张敏  袁先友 《合成化学》2001,9(5):469-472
以磷钨酸为催化剂,对冰醋酸与甘油的酯化反应进行了研究。考察了催化剂用量、酸醇比和带水剂对酯化反应的影响,探讨其最佳反应条件为:催化剂用量为反应物质量的3.8%,油浴温度为135℃-155℃,反应时间7h,酯收率达84.6%。  相似文献   

2.
磷钨酸催化合成氯乙酸异丙酯   总被引:5,自引:0,他引:5  
研究了磷钨酸催化氯乙酸与异丙醇合成氯乙酸异丙酯的反应 ,讨论了影响合成的因素 ,找出了最佳合成条件 ,收率达到 90 %。  相似文献   

3.
磷钨酸催化合成乙酸戊酯   总被引:2,自引:0,他引:2  
以磷钨酸为催化剂,冰醋酸和戊醇为原料,催化合成了乙酸戊酯.探讨了催化剂用量、醇酸比、反应时间等对酯化反应的影响.研究结果表明:取冰醋酸40mL,正戊醇25mL,磷钨酸2.0g,反应时间为2h时,酯的产率大于80%.  相似文献   

4.
磷钨酸催化合成己二酸二乙酯的研究   总被引:22,自引:0,他引:22  
己二酸二乙酯是无色油状液体 ,溶于乙醇和其它有机溶剂 ,不溶于水 ,主要用于作溶剂和有机合成中间体 ,还可用于日用化学工业和食品工业。目前工业上大多采用以硫酸为催化剂的合成方法 [1-2 ] ,但硫酸腐蚀性很强 ,化学性质很活泼 ,反应中副反应多 ,以致碳化、聚合、重排等现象时有发生 ,而且后处理麻烦 ,污染环境。近几年已有固体酸作催化剂合成酯的报道 [3 -5 ] ,其特点是活性高 ,选择性好 ,但反应需高温活化 ,处理麻烦。杂多酸 (盐 )化合物是一类含有氧桥的多核高分子化合物 ,具有较强的酸性和适中的氧化还原性 ,可作为酸型和氧化还原型催…  相似文献   

5.
活性炭负载磷钨酸催化合成季戊四醇缩酮(醛)   总被引:5,自引:0,他引:5  
季戊四醇双缩酮(醛)可作为杀虫剂[1]、塑料的抗氧化剂及表面活性剂的消泡剂等[2,3];其单缩酮(醛)是有机合成的重要中间体。其合成反应常用无机酸催化剂(如H2SO4、HCl、H3PO4等)[4],副反应多、腐蚀性强和易污染。近年来,采用脱铝超稳Y沸石和对甲苯磺酸等作催化剂[5-7],效果良好。本文以活性炭负载磷钨酸作催化剂合成了12种季戊四醇缩酮(醛),催化剂用量少、反应速率快、产率高,催化剂可回收使用。其结构经元素分析、IR及1HNMR等表征。1 实验部分1 1 仪器与试剂Kofler熔点仪,温度计未经校正;美国NICO LETAVATAR 360FT光谱仪…  相似文献   

6.
以磷钨酸为催化剂 ,乙酰乙酸乙酯和乙二醇为原料 ,甲苯为带水剂合成了苹果酮。结果表明 ,磷钨酸催化剂具有活性高、选择性好、后处理简单的优点  相似文献   

7.
Dawson结构磷钨酸银催化绿色合成阿司匹林   总被引:1,自引:0,他引:1  
曹小华 《化学通报》2015,78(10):928-932
通过沉淀法制备出Dawson结构磷钨酸银(Ag3H3P2W18O62·n H2O),采用FT IR、EDX对其进行了表征,并将其用于催化乙酸酐和水杨酸合成阿司匹林。研究了催化剂用量、水杨酸和乙酸酐摩尔比、反应温度、反应时间等因素对反应的影响。结果表明,所制磷钨酸银在多次使用后仍保持Dawson结构不变。在优化条件下,即n(水杨酸)∶n(乙酸酐)=1∶1.75,反应温度为90℃,催化剂用量为3.2%(以反应物质量计),反应时间为20min,阿司匹林收率为90.1%。催化剂重复使用5次,阿司匹林收率仍可保持为82.4%。  相似文献   

8.
磷钨酸镧催化合成缩醛(酮)的研究   总被引:2,自引:0,他引:2  
以磷钨酸镧为催化剂催化合成了苯甲醛乙二醇缩醛、苯甲醛1,2-丙二醇缩醛及环己酮乙二醇缩酮.较系统研究了反应物料配比、催化剂用量、反应时间、催化剂重复使用性能等因素对反应的影响.结果表明:在醛(酮)/二元醇(乙二醇、1,2-丙二醇)=1.0:1.5(mol/mol),催化剂用量为反应物料总质量的1.0%,环己烷为带水剂,在反应温度86~96℃条件下,反应时间2.0h,苯甲醛乙二醇缩醛收率为78.5%,苯甲醛1,2-丙二醇缩醛收率为76.1%,环己酮乙二醇缩酮收率为79.5%.  相似文献   

9.
磷钨酸催化合成癸二酸二丁酯   总被引:5,自引:0,他引:5  
朱静  戴波  钟梅英 《合成化学》2003,11(5):450-452
用磷钨酸催化合成癸二酸二丁酯,考察了诸因素对酯化率的影响,产品经IR鉴定。确定酯化反应的最佳条件为:癸二酸50mmol,n(癸二酸):n(正丁醇)=l:4,催化剂0.5g(反应物总质量的1.7%),反应时间2h,酯化率达96.46%。  相似文献   

10.
通过在300℃下焙烧2h制备了磷酸钛固载15%磷钨酸H3PW12O40(简记为HPW)非均相酯化催化剂HPW/Ti3(PO4)4;采用红外光谱仪分析了催化剂的结构;基于异戊酸与正己醇的酯化反应考察了催化剂用量、n(正己醇)∶n(异戊酸)、反应时间、带水剂种类和催化剂重复使用性能等因素对酯化率的影响.结果表明,该催化剂催化合成异戊酸己酯的适宜反应条件为:0.2mol异戊酸,催化剂用量0.6g,n(正己醇)∶n(异戊酸)=1.6∶1,反应时间4.5h,环己烷10mL;相应的酯化率达95.1%.与此同时,该催化剂循环利用6次后酯化率不低于84%.  相似文献   

11.
对甲苯磺酸催化合成乙酸正丁酯   总被引:8,自引:0,他引:8  
李继忠 《合成化学》2003,11(5):457-458
用对甲苯磺酸作冰乙酸和正丁醇的酯化催化剂,成功地合成了乙酸正丁酯,考察了影响反应的因素,探讨并找到了较好的反应条件:乙酸l00mmol,n(冰乙酸):n(正丁醇):n(催化剂)=1:3:0.006,反应时间1.5h,不另加带水剂,产率达99.14%。  相似文献   

12.
Free radical bulk copolymerizations of conjugated linoleic acid (CLA)/styrene (Sty) and CLA/butyl acrylate (BA) were performed at 80°C. Copolymers were characterized for composition, conversion, molecular weights and glass transition temperature (Tg). A pseudo-kinetic model was developed and validated with experimental data. Reactivity ratios estimations were performed and one impurity commonly found in CLA, oleic acid, influenced the reaction kinetics significantly. The Tg of CLA homopolymer was predicted to be 5°C.  相似文献   

13.
Cooperative enamine-metal Lewis acid catalysis has emerged as a powerful tool to construct carbon-carbon and carbon-heteroatom bond forming reactions. A concise synthetic method for asymmetric synthesis of chromans from cyclohexanones and salicylaldehydes has been developed to afford tricyclic chromans containing three consecutive stereogenic centers in good yields (up to 87 %) and stereoselectivity (up to 99 % ee and 11 : 1 : 1 dr). This difficult organic transformation was achieved through bifunctional enamine-metal Lewis acid catalysis. It is believed that the strong activation of the salicylaldehydes through chelating to the metal Lewis acid and the bifunctional nature of the catalyst accounts for the high yields and enantioselectivity of the reaction. The absolute configurations of the chroman products were established through X-ray crystallography. DFT calculations were conducted to understand the mechanism and stereoselectivity of this reaction.  相似文献   

14.
The reactivity ratios for the bulk free‐radical copolymerization of n‐butyl acrylate (BA)/n‐butyl methacrylate (BMA) are estimated at 80 °C. By performing a series of low conversion runs including replicate runs, the reactivity ratios are estimated as rBA = 0.460 and rBMA = 2.008. Runs to high conversions are then conducted at three different feed compositions (fBMA = 0.2, 0.5, and 0.8) to validate the reactivity ratios. The composition data from the high conversion experiments show good agreement with the estimated reactivity ratios in the integrated form of the Mayo–Lewis model. The molecular weight, gel content, and glass transition temperature of BA/BMA copolymers are also determined.

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15.
活性炭负载硅钨酸催化合成乙酸正丁酯   总被引:8,自引:0,他引:8  
以活性炭负载硅钨酸为催化剂,乙酸和正丁醇为原料合成乙酸正丁酯.优化的反应条件如下:在冰乙酸0.253mol、正丁醇0.22mol、催化剂用量为反应物总量的1.5%(质量分数)、反应温度115℃,反应时间为90min的条件下,酯化率可达97.8%.产品纯度>98%,并且催化剂可以多次使用活性没有明显下降.  相似文献   

16.
Branch lengths resulting from both backbiting and intermolecular chain transfer to polymer are examined for the solution polymerization of butyl acrylate, using a rate‐equation model and ordinary differential equations. Backbiting is allowed to generate branches of varying length, according to a cumulative distribution function obtained from a lattice kinetic Monte Carlo simulation. About 8% of the branches produced by backbiting are 10 mers or longer. In contrast to common assumptions about the origins of short‐chain and long‐chain branches, the model indicates that nearly all of the long‐chain branches may be produced by backbiting, rather than intermolecular chain transfer to polymer.

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17.
Summary: High temperature semibatch free radical solution copolymerizations of n-butyl acrylate (BA) and styrene (ST) were carried out over a range of copolymer composition. The significant increase in experimental polymer weight-average molecular weight with time, as well as the shift in the entire polymer molecular weight distribution, is explained by assuming fast β-scission of BA midchain radicals with an adjacent styrene unit, followed by subsequent addition of the resultant macromonomer to growing radicals. A mechanistic model including backbiting and β-scission, macronomer incorporation, long-chain branching, and propagation and termination penultimate effects was constructed in Predici; the model provides a good representation of the experimental data using rate coefficients taken from literature.  相似文献   

18.
In this work, secondary reactions involved in the free radical polymerization of butyl acrylate are investigated using quantum chemistry. First, various backbiting reactions are studied by adopting a simplified molecular model suitable for treating long polymer chains. The predicted reaction kinetics suggest the possibility of a radical migration along the poly(butyl acrylate) (PBA) chain as a consequence of subsequent j:j + 4 hydrogen abstractions, which are characterized by a low activation energy. Moreover, branching propagation and β‐scission reactions originating from mid‐chain radicals are investigated using a complete PBA model composed of five monomer units. The reaction kinetics involving short‐branch radicals are also examined, and a novel backbiting step leading to the formation of short branches is proposed.

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19.
20.
High‐pressure atom transfer radical polymerization (ATRP) of n‐butyl acrylate (BA) is performed in acetonitrile (MeCN) with CuIBr/TPMA [TPMA: tris(2‐pyridylmethyl)‐amine] as the catalyst up to 5 kbar. Increasing either pressure or temperature significantly enhances the rate of polymerization, while retaining control over the polymerization. The polymerizations under high pressure could be efficiently performed with very low levels of Cu catalyst in the absence of any reducing agents. For example, 100 ppm Cu is sufficient to catalyze the polymerization of BA with targeted degree of polymerization (DPT) = 1000. The conversion reached 79% in 3.0 h at 80 °C providing PBA with M n = 112 000, M w/M n = 1.12. Since the initial CuI‐to‐initiator molar ratio is 0.05:1, the molar percentage of terminated chains should remain <5%. For DPT = 10 000 using only 50 ppm Cu catalyst, a polymer with molecular weight M n = 612 000 (DP = 4800) was obtained at 67% conversion.

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