CN103319342A - Method for synthesizing ethyl oleate - Google Patents
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Abstract
本发明公开了一种油酸乙酯的合成方法,其特点是该方法将油酸与乙醇在H2SO4/SiO2固载型催化剂下进行酯化反应,然后将反应液过滤,滤液经柱层析纯化或蒸馏得无色或淡黄色澄清液体为油酸乙酯;所述油酸与乙醇的摩尔比为1:1.5~5;所述催化剂与油酸的摩尔比为1:10~50。本发明与现有技术相比具有工艺简单、操作方便,生产成本低,产率高,反应条件更温和,进一步降低原材料消耗降低,产率可提高到95%以上,生产成本明显降低,而且催化剂可循环使用,不污染环境,是一种绿色环保和经济高效且很有应用前景的油酸乙酯的合成方法。The invention discloses a synthesis method of ethyl oleate, which is characterized in that the esterification reaction of oleic acid and ethanol is carried out under the H2SO4 / SiO2 immobilized catalyst, and then the reaction liquid is filtered, and the filtrate is passed through Purified by column chromatography or distilled to obtain a colorless or light yellow clear liquid which is ethyl oleate; the molar ratio of the oleic acid to ethanol is 1:1.5~5; the molar ratio of the catalyst to the oleic acid is 1:10~ 50. Compared with the prior art, the present invention has the advantages of simple process, convenient operation, low production cost, high yield, milder reaction conditions, further reduction of raw material consumption, yield can be increased to more than 95%, production cost is significantly reduced, and the catalyst The method can be recycled, does not pollute the environment, and is an environmentally friendly, cost-effective and promising method for synthesizing ethyl oleate.
Description
技术领域 technical field
本发明涉及有机化学合成技术领域,具体地说是一种油酸乙酯的合成方法。 The invention relates to the technical field of organic chemical synthesis, in particular to a method for synthesizing ethyl oleate.
背景技术 Background technique
油酸乙酯为淡黄色油状液体,主要用作表面活性剂、润滑剂、渗透剂、助溶剂、香精、抗水剂和树脂韧化剂,也用作香料。对于油酸乙酯的合成最典型的方法是以油酸和乙醇为原料,使用硫酸为催化剂进行加热回流10h,冷却后用甲醇钠中和至pH为8~9,然后用水洗至中性,最后用无水氯化钙干燥、过滤制得。(徐克勋.精细有机化工原料及中间体手册.北京:化学工业出版社1998,4:1~350)。该方法缺点是反应时间太长,同时产品后处理工序较长,工业成本较高。 Ethyl oleate is light yellow oily liquid, mainly used as surfactant, lubricant, penetrating agent, cosolvent, essence, water repellant and resin toughener, and also used as fragrance. The most typical method for the synthesis of ethyl oleate is to use oleic acid and ethanol as raw materials, use sulfuric acid as a catalyst to heat and reflux for 10 hours, neutralize with sodium methoxide to pH 8~9 after cooling, and then wash with water until neutral. Finally, it is obtained by drying with anhydrous calcium chloride and filtering. (Xu Kexun. Handbook of Fine Organic Chemical Raw Materials and Intermediates. Beijing: Chemical Industry Press 1998, 4:1~350). The disadvantage of this method is that the reaction time is too long, and the post-treatment process of the product is longer, and the industrial cost is higher.
另一种常用的方法是采用浸渍法制备负载型磷钨酸介孔炭作为催化剂(谭晓宇,杨丽娜,刘敬,徐俊博,负载型磷钨酸介孔炭催化合成油酸乙酯的研究.炭素,2011,1(145):25~28)。该方法反应温度为110℃,磷钨酸负载量为30%,反应时间4h,,油酸酯化率为89.34%。这一方法虽然比传统制备方法的反应时间有所缩短,但是反应温度较高,反应时间也较长,催化剂的制备成本较高且不可以回收重复使用。 Another commonly used method is to use the impregnation method to prepare supported mesoporous phosphotungstic acid carbon as a catalyst (Tan Xiaoyu, Yang Lina, Liu Jing, Xu Junbo, Research on the Catalytic Synthesis of Ethyl Oleate by Supported Phosphotungstic Acid Mesoporous Carbon. Carbon , 2011, 1(145):25~28). In this method, the reaction temperature is 110°C, the loading capacity of phosphotungstic acid is 30%, the reaction time is 4 hours, and the esterification rate of oil is 89.34%. Although the reaction time of this method is shorter than that of the traditional preparation method, the reaction temperature is higher and the reaction time is longer. The preparation cost of the catalyst is higher and cannot be recycled and reused.
综上所述,现有技术制备的油酸乙酯,合成工艺复杂,环境污染大,严重制约了的广泛应用。因此,有必要寻找一种体系更温和、更经济、绿色的油酸乙酯合成方法,这对于油酸乙酯在生产中的应用具有重要意义。 In summary, the ethyl oleate prepared by the prior art has a complex synthesis process and great environmental pollution, which seriously restricts its wide application. Therefore, it is necessary to find a method for the synthesis of ethyl oleate with a milder, more economical and green system, which is of great significance for the application of ethyl oleate in production.
发明内容 Contents of the invention
本发明的目的是针对现有技术的不足而提供的一种油酸乙酯的合成方法,采油酸与乙醇在H2SO4/SiO2固载型催化剂下进行酯化反应,合成油酸乙酯的反应体系温和,操作简便,原材料消耗降低,产率可提高到95%以上,生产成本明显降低,而且催化剂后处理简单可循环使用,不污染环境,是一种绿色环保和经济高效且很有应用前景的油酸乙酯合成方法。 The purpose of the present invention is to provide a kind of synthetic method of ethyl oleate for the deficiencies in the prior art, extracting oleic acid and ethanol carry out esterification reaction under H 2 SO 4 /SiO 2 solid-supported catalysts, synthetic ethyl oleate The reaction system of the ester is mild, easy to operate, the consumption of raw materials is reduced, the yield can be increased to more than 95%, the production cost is significantly reduced, and the post-treatment of the catalyst is simple and recyclable without polluting the environment. A promising method for the synthesis of ethyl oleate.
实现本发明目的的具体技术方案是:一种油酸乙酯的合成方法,其特点是该方法将油酸与乙醇在H2SO4/SiO2固载型催化剂下进行酯化反应,然后将反应液过滤去除催化剂,滤液经纯化得无色或淡黄色澄清液体为油酸乙酯,具体合成步骤如下: The specific technical scheme for realizing the object of the present invention is: a kind of synthetic method of ethyl oleate, it is characterized in that this method carries out esterification reaction with oleic acid and ethanol under H 2 SO 4 /SiO 2 solid-supported catalysts, and then The reaction solution was filtered to remove the catalyst, and the filtrate was purified to obtain a colorless or light yellow clear liquid which was ethyl oleate. The specific synthesis steps were as follows:
a、固体酸催化剂的制备 a, preparation of solid acid catalyst
将SiO2固体与无水甲醚和浓度为98%的硫酸按重量体积比为2g:4ml:1ml搅拌混合后,在130~140℃温度下干燥4~5h,得到浅棕色的细粉末为H2SO4/SiO2固载型催化剂; Mix SiO2 solid with anhydrous methyl ether and sulfuric acid with a concentration of 98% in a weight-to-volume ratio of 2g:4ml:1ml, and then dry at 130~140°C for 4~5h to obtain a light brown fine powder called H 2 SO 4 /SiO 2 solid-supported catalyst;
b、酯化反应 b. Esterification reaction
将油酸与乙醇按摩尔比为1:1.5~5混合,然后在上述制备的H2SO4/SiO2固载型催化剂下进行1~5小时的酯化反应,其反应温度为50~110℃;所述H2SO4/SiO2固载型催化剂与油酸的摩尔比为1:10~50; Mix oleic acid and ethanol at a molar ratio of 1:1.5~5, then carry out esterification reaction for 1~5 hours under the H 2 SO 4 /SiO 2 solid-supported catalyst prepared above, and the reaction temperature is 50~110 °C; the molar ratio of the H 2 SO 4 /SiO 2 solid-supported catalyst to oleic acid is 1:10~50;
c、提纯 c. Purification
将上述酯化的反应液中滤出催化剂,滤液经硅胶柱层析或减压蒸馏提纯,得到无色或浅黄色透明油状液体为油酸乙酯。 The catalyst was filtered out from the above-mentioned esterification reaction solution, and the filtrate was purified by silica gel column chromatography or vacuum distillation to obtain a colorless or light yellow transparent oily liquid as ethyl oleate. the
本发明与现有技术相比具有工艺简单、操作方便,反应条件温和,产率可提高到95%以上,进一步降低原材料消耗降低,生产成本明显降低,而且催化剂可循环使用,不污染环境,是一种绿色环保和经济高效且很有应用前景的油酸乙酯的合成方法。 Compared with the prior art, the present invention has simple process, convenient operation, mild reaction conditions, the yield can be increased to more than 95%, the consumption of raw materials is further reduced, the production cost is significantly reduced, and the catalyst can be recycled without polluting the environment. A green, cost-effective and promising synthetic method of ethyl oleate.
附图说明 Description of drawings
图1为本发明红外光谱图。 Fig. 1 is the infrared spectrogram of the present invention.
具体实施方式 Detailed ways
以下将通过具体的实施例对本发明做进一步的阐述: The present invention will be further elaborated below by specific embodiment:
实施例1 Example 1
a、固体酸催化剂的制备 a, preparation of solid acid catalyst
称取SiO2固体10.0g与20.0ml无水乙醚搅拌混合后缓慢滴加5ml浓度为98%的硫酸,滴加时需搅拌,滴加完后将其通风,让甲醚挥发后放置于烘箱中干燥,烘箱温度设置在135℃,干燥时间为4h,制得浅棕色的细粉末为H2SO4/SiO2固载型催化剂,待用。 Weigh 10.0g of SiO 2 solid and 20.0ml of anhydrous ether, stir and mix, then slowly add 5ml of sulfuric acid with a concentration of 98% dropwise, stirring is required during the dropwise addition, ventilate it after the dropwise addition, let the methyl ether volatilize, and then place it in an oven After drying, the oven temperature was set at 135° C., and the drying time was 4 hours. A light brown fine powder was obtained as a H 2 SO 4 /SiO 2 immobilized catalyst, which was ready for use.
b、酯化反应 b. Esterification reaction
将1.00ml油酸与0.55ml乙醇和0.013g上述制备的H2SO4/SiO2固载型催化剂搅拌混合,在搅拌下进行酯化反应,其反应温度为90℃,反应时间为2.5小时。 Stir and mix 1.00ml oleic acid with 0.55ml ethanol and 0.013g of the H 2 SO 4 /SiO 2 solid-supported catalyst prepared above, and carry out esterification reaction under stirring. The reaction temperature is 90°C and the reaction time is 2.5 hours.
c、提纯化 c. Purification
将上述酯化的反应液过滤,滤出的催化剂可循环使用,滤液经硅胶柱层析提纯,制得无色澄清液体的油酸乙酯0.981g,其产率为91.4%,测得折光率n20 D=1.4532。 The reaction solution of the above-mentioned esterification is filtered, and the catalyst filtered out can be recycled. The filtrate is purified by silica gel column chromatography to obtain 0.981 g of ethyl oleate, a colorless and clear liquid, with a yield of 91.4%. n 20 D =1.4532.
核磁谱测试数据如下: 1H-NMR(500MHz,CDCl3):δ(ppm) 5.34(m, 2H), 4.12(q,J= 7.2Hz, 2H), 2.28(t,J=7.5Hz,2H), 1.62(m, 2H), 1.24-1.31 (m,24H), 0.89(t, J=6.0Hz, 3H). The NMR test data are as follows: 1 H-NMR(500MHz,CDCl 3 ):δ(ppm) 5.34(m, 2H), 4.12(q,J=7.2Hz, 2H), 2.28(t,J=7.5Hz,2H ), 1.62(m, 2H), 1.24-1.31 (m,24H), 0.89(t, J=6.0Hz, 3H).
对上述所得产物油酸乙酯经检测、分析后可以确认为纯的目标产物。 After detecting and analyzing the above-mentioned obtained product ethyl oleate, it can be confirmed as a pure target product.
实施例2 Example 2
a、固体酸催化剂的制备 a, preparation of solid acid catalyst
称取SiO2固体10.0g与20.0ml无水乙醚搅拌混合后缓慢滴加5ml浓度为98%的硫酸,滴加时需搅拌,滴加完后将其通风,让甲醚挥发后放置于烘箱中干燥,烘箱温度设置在140℃,干燥时间为3.5h,制得浅棕色的细粉末为H2SO4/SiO2固载型催化剂,待用。 Weigh 10.0g of SiO 2 solid and 20.0ml of anhydrous ether, stir and mix, then slowly add 5ml of sulfuric acid with a concentration of 98% dropwise, stirring is required during the dropwise addition, ventilate it after the dropwise addition, let the methyl ether volatilize, and then place it in an oven After drying, the oven temperature is set at 140° C., and the drying time is 3.5 hours. A light brown fine powder is obtained as a H 2 SO 4 /SiO 2 immobilized catalyst, which is ready for use.
b、酯化反应 b. Esterification reaction
将50.0ml油酸与20.0ml乙醇和1.9g上述制备的H2SO4/SiO2固载型催化剂搅拌混合,在搅拌下进行酯化反应,其反应温度为110℃,反应时间为1.5小时。 Stir and mix 50.0ml oleic acid, 20.0ml ethanol and 1.9g of the H 2 SO 4 /SiO 2 solid-supported catalyst prepared above, and carry out esterification reaction under stirring. The reaction temperature is 110°C and the reaction time is 1.5 hours.
c、提纯 c. Purification
酯化反应结束后过滤反应体系,滤液经减压蒸馏得到淡黄色澄清液体油酸乙酯46.7g。(bp: 205~208℃/7mmHg)油酸乙酯理论产量为49.0g,故实验中油酸乙酯的产率为95.3%,测得样品折光率n20 D=1.4538。 After the esterification reaction was completed, the reaction system was filtered, and the filtrate was distilled under reduced pressure to obtain 46.7 g of ethyl oleate, a pale yellow clear liquid. (bp: 205~208℃/7mmHg) The theoretical yield of ethyl oleate is 49.0g, so the yield of ethyl oleate in the experiment is 95.3%. The measured refractive index of the sample n 20 D =1.4538.
参阅附图1,对上述所得产物油酸乙酯进行红外光谱检测,其数据如下:3006.67cm-1为油酸乙酯C=C双键上C-H的振动吸收峰;2926cm-1和2854.96cm-1为甲基和亚甲基的C-H伸缩振动吸收峰;1738.09cm-1为C=O酯羰基伸缩振动吸收峰;1178.78cm-1、1036.03cm-1为C-O-C键的非对称伸缩振动吸收峰;1462.38cm-1、1383.78cm-1为甲基和亚甲基的C-H弯曲振动吸收峰;980cm-1~650cm-1处的峰为多个CH2成直链时其C-H面外弯曲振动产生的吸收峰。实验所测得的红外光谱数据与文献(凌关庭,唐述潮,陶民强.食品添加剂手册[M].第三版.北京:化学工业出版社,2003.411-412)中油酸乙酯的主要基团红外特征吸收相一致,说明该产物为油酸乙酯。 Referring to accompanying drawing 1, carry out infrared spectrum detection to the above-mentioned product ethyl oleate, its data are as follows: 3006.67cm -1 is the vibrational absorption peak of CH on the C=C double bond of ethyl oleate; 2926cm -1 and 2854.96cm- 1 is CH stretching vibration absorption peak of methyl group and methylene group; 1738.09cm -1 is C=O ester carbonyl stretching vibration absorption peak; 1178.78cm -1 and 1036.03cm -1 are asymmetric stretching vibration absorption peaks of COC bond; 1462.38cm -1 and 1383.78cm -1 are the CH bending vibration absorption peaks of methyl and methylene groups; the peaks at 980cm -1 ~ 650cm -1 are the CH out-of-plane bending vibrations when multiple CH 2 are in a straight chain absorption peak. Infrared spectrum data measured in the experiment and literature (Ling Guanting, Tang Shuchao, Tao Minqiang. Food Additive Handbook [M]. Third Edition. Beijing: Chemical Industry Press, 2003.411-412) The infrared characteristic absorption of the main group of ethyl oleate Consistent, indicating that the product is ethyl oleate.
以上只是对本发明作进一步的说明,并非用以限制本专利,凡为本发明等效实施,均应包含于本专利的权利要求范围之内。 The above is only a further description of the present invention, and is not intended to limit this patent. All equivalent implementations of the present invention should be included in the scope of claims of this patent.
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| CN109942783A (en) * | 2019-02-22 | 2019-06-28 | 上海稻畑精细化工有限公司 | A kind of high stability polyurethane curing agent and preparation process thereof |
| CN110668944A (en) * | 2019-04-19 | 2020-01-10 | 江西阿尔法高科药业有限公司 | Refining method of ethyl oleate |
| CN115322090A (en) * | 2022-07-16 | 2022-11-11 | 江西益普生药业有限公司 | Method for preparing ethyl oleate |
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| CN109942783A (en) * | 2019-02-22 | 2019-06-28 | 上海稻畑精细化工有限公司 | A kind of high stability polyurethane curing agent and preparation process thereof |
| CN110668944A (en) * | 2019-04-19 | 2020-01-10 | 江西阿尔法高科药业有限公司 | Refining method of ethyl oleate |
| CN115322090A (en) * | 2022-07-16 | 2022-11-11 | 江西益普生药业有限公司 | Method for preparing ethyl oleate |
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Application publication date: 20130925 |