CN1687001A - Method for esterifying organic acid - Google Patents
Method for esterifying organic acid Download PDFInfo
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- CN1687001A CN1687001A CN 200510049588 CN200510049588A CN1687001A CN 1687001 A CN1687001 A CN 1687001A CN 200510049588 CN200510049588 CN 200510049588 CN 200510049588 A CN200510049588 A CN 200510049588A CN 1687001 A CN1687001 A CN 1687001A
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Abstract
The present invention relates to an esterification method of organic acid. Said invention uses organic acid and alcohol as raw material, and uses inorganic acid as catalyst, and makes the organic acid and alcohol react at 20-250 deg.C in fluorine solvent, and makes after-treatment so as to obtain organic ester. The described fluorine solvent is perfluoroalkane or perfluoroalkene or perfluoroarene of C1-C15 or their mixture with any form.
Description
(I) technical field
The invention relates to an organic acid esterification method.
(II) background of the invention
Organic esters are important products or intermediates in the chemical industry and in pharmaceuticals. In organic synthesis, esterification is one of the most common and most widely used reactions. From the preparation of natural products to the large-scale production of bulk chemicals, many esterification processes have been successfully employed. The most important preparation method of carboxylic acid esters is the direct esterification of the free acid and the alcohol.
Since the reaction of carboxylic acid and alcohol is generally very slow due to low carbonyl activity, the addition of inorganic acids such as sulfuric acid, anhydrous hydrogen chloride, and p-toluenesulfonic acid can greatly accelerate the esterification reaction. The esterification reaction is a reversible reaction, and carboxylic acid and alcohol react to generate ester and water; and the alcohol and the acid can be obtained by the action of the ester and the water. When carboxylic acids and alcohols in equivalent amounts participate in the esterification reaction, only two thirds of the theoretical yield of ester is obtained. According to the law of mass action, one of the reactants, for example the carboxylic acid, must be in excess in order to shift the equilibrium in the direction of the product ester. However, when the carboxylic acid is more expensive than the alcohol, an excess of the alcohol is used. The chemical equilibrium will only be shifted sufficiently towards esters when the reactants are in excess, e.g. 5-10 times excess (handbook of organic chemistry, Liqueen, Van. Lin compiled, Shanghai science publishers, first edition 1981, page 327). Thus, after the reaction is finished, excessive reactants need to be recovered, and partial material loss and energy consumption are caused. Another method is to distill off the ester or water formed in the reaction and break the equilibrium continuously, so that the equilibrium moves towards the product.
The simplest method is to use an acid (sulfuric acid or hydrochloric acid) as a catalyst to bind the water produced by the reaction, but the amount of acid used will be large. After the reaction, the acid-containing wastewater must be neutralized by alkali, which causes resource waste and increases production cost. Azeotropic distillation dehydration, which is particularly suitable for the esterification of reactive compounds, is often preferred, since in this case only small amounts of acid catalyst are used. The dehydrating agent is generally selected by selecting the boiling point of the lowest boiling component of the reaction mixture. Benzene, chloroform or carbon tetrachloride are commonly used for the preparation of ethyl esters and propyl esters, where there is a problem of toxicity of the dehydrating agent, and where benzene is used as the dehydrating agent, the ratio of water and alcohol distilled off at the same time is not ideal. The process of distilling off the ester is often limited by the relatively high boiling point of the ester. Esterification is often carried out in organic solvents, and benzene and toluene are mostly used as solvents for esterification. The separation of the organic solvent and the product after the reaction inevitably results in loss of the solvent.
The greening of esterification reactions is the direction of effort. Fraga-Dubreuil et al reported esterification in hydrogen sulfate ionic liquids of 1-hexyl-3-methylimidazole (Catal. Commun., 2002, 3, 185)) The reaction product ester is not dissolved in the ionic liquid and is conveniently separated, the product water is dissolved in the ionic liquid, the product water is separated from the reaction system, the reaction balance is shifted to the right, the yield and the selectivity are both high, and the ionic liquid is a green solvent for the esterification reaction. However, the preparation of the ionic liquid is complicated, volatile organic solvents are used in the preparation and recycling, and the conversion rate of most reactants is lower than 60%. Lynnette A. et al, using supercritical CO2As a solvent for the esterification reaction, an esterification reaction of acetic acid and ethanol (Green Chemistry, 2001, 3, 17-19). Because the product ethyl acetate can be dissolved in supercritical CO2The equilibrium position of the reversible reaction is shifted to the direction of ester formation, and the equilibrium conversion rate of the esterification reaction is improved from 63% to 72% compared with the conventional organic solvent. But supercritical CO2As a solvent, the reaction pressure is up to 5.9MPa, the requirements on equipment and operation control are high, and the application range is limited.
Disclosure of the invention
The invention aims to provide an organic acid esterification method with simple reaction conditions, low cost and high yield.
The organic acid esterification method takes organic acid and alcohol as raw materials and comprises the following steps: reacting organic acid and alcohol in a fluorine solvent at 20-250 ℃ by taking inorganic acid as a catalyst, and performing post-treatment to obtain organic ester; the fluorine solvent is C1～C15Of perfluoroalkanes or perfluoroolefins or perfluoroaromatics or mixtures thereof in any form, preferably C6～C12And (3) perfluoroalkanes or perfluoroolefins or perfluoroaromatics such as perfluorononene, perfluorotoluene, perfluorocyclohexane, and the like, more preferably perfluorononene.
The organic acid is especially C1～C20The 1-to 2-membered fatty acid, alicyclic acid or aromatic acid is preferably acetic acid or benzoic acid. The alcohol is in particular C1～C20The 1-3-membered aliphatic alcohol or alicyclic alcohol or phenol is preferably ethanol, n-propanol or n-butanol.
The inorganic acid is preferably one of the following: sulfuric acid, hydrochloric acid, p-toluenesulfonic acid, and the like, concentrated sulfuric acid is preferred.
The reaction temperature is preferably 20 to 150 ℃, and the stirring reaction is preferably performed for 1 to 20 hours.
In the reaction system, the ratio of the organic acid to the alcohol functional group can be 1: 0.8-1.2, and the optimal ratio is 1: 1; the mass ratio of the fluorine solvent to the reactant (organic acid + alcohol) is 0.1-10: 1, preferably 2-4: 1; the using amount of the inorganic acid accounts for 1-20% of the mass of the reactants (organic acid and alcohol);
when the product organic ester is a liquid, the post-treatment steps can be as follows: separating the reaction solution to remove a water phase, standing for layering, recovering a lower fluorine solvent layer, washing an upper organic layer to be neutral by using a sodium carbonate solution, washing by using saturated saline solution, drying by using anhydrous sodium sulfate, and filtering to obtain a product organic ester; the post-treatment is preferably carried out using a 10% sodium carbonate solution.
When the product organic ester is a solid, the post-treatment step may be: and standing the reaction solution, separating a water layer and a fluorine solvent layer, recrystallizing the residual solid, and purifying to obtain the product organic ester.
Compared with the prior art, the invention does not need a water-carrying agent, does not need to evaporate a product or water in the reaction process, and has the ratio of organic acid to alcohol functional groups close to or equal to 1; the conversion rate is high; the separation and the solvent recovery are very simple and convenient, and the recovered solvent can be directly used without purification. Simple operation, high resource utilization rate and less three wastes.
(IV) detailed description of the preferred embodiments
The present invention is further illustrated by the following examples, but the scope of the invention is not limited thereto.
Example 1
Adding 7.5 g of acetic acid, 5.8 g of absolute ethyl alcohol and 33.0 g of perfluorononene into a 100 ml four-neck flask (provided with a reflux device and a mechanical stirrer) in sequence, stirring and heating, dropwise adding 1.3 ml of concentrated sulfuric acid under vigorous stirring, after dropwise adding within 10 minutes, heating to 72 ℃, starting reflux, and continuing to react for 1.5 hours under the conditions. Standing for a moment, separating out a water phase, cooling to room temperature, separating out a lower fluorine solvent layer, washing an upper organic solution with 10% sodium carbonate to control the pH value to be 7, washing with equal volume of saturated saline solution twice, drying the treated organic solution with anhydrous sodium sulfate, and filtering to obtain an ethyl acetate solution with the content of 99.3%. The reaction conversion rate was 100%.
Example 2
60.0 g of acetic acid, 60 g of n-propanol and 330.0 g of perfluorononene are sequentially added into a 1000 ml four-neck flask (provided with a reflux device and a mechanical stirrer), stirred and heated, 10.0 ml of concentrated sulfuric acid is dropwise added under vigorous stirring, the temperature is raised to 72 ℃ after the dropwise addition is finished within 1 hour,the reflux is started, and the reaction is continued for 1.5 hours under the condition. Standing for a moment, separating a water phase, cooling to room temperature, separating a lower fluorine solvent layer, washing an upper organic solution with 10% sodium carbonate to control the pH value to be 7, washing with equal volume of saturated saline solution twice, drying the treated organic solution with anhydrous sodium sulfate, and filtering to obtain the product with the n-propyl acetate content of 97.9% and the reaction conversion rate of 97%.
Example 3
The alcohol was changed to 74.0 g of n-butanol, and the other reactions and workup were the same as in example 2.
The content of n-butyl acetate is 98.9 percent. The reaction conversion was 95%.
Example 4
Adding 8.0 g of benzoic acid, 3.0 g of absolute ethyl alcohol and 30.0 g of perfluorononene into a 250 ml four-neck flask provided with a reflux device and a mechanical stirrer, stirring and heating, dropwise adding 1.0 ml of concentrated sulfuric acid under vigorous stirring, after dropwise adding within 15 minutes, heating and refluxing, and continuing to react for 3 hours under the condition. Standing, separating water phase, cooling to 10 deg.C, recovering fluorine solvent, washing the residual organic solution with 10% sodium carbonate aqueous solution to neutrality, washing with equal volume of saturated sodium chloride solution twice, drying with anhydrous sodium sulfate, and filtering to obtain ethyl benzoate with content of 98.8%. The reaction conversion rate was 100%.
Example 5
40.0 g of benzoic acid, 20.0 g of n-propanol and 150.0 g of perfluorononene are added into a 500 ml four-neck flask provided with a reflux device and a mechanical stirrer, stirred and heated, 3.0 ml of concentrated sulfuricacid is dropwise added under vigorous stirring, the dropwise addition is completed within 15 minutes, the temperature is increased for reflux, and the reaction is continued for 3 hours under the condition. Standing, separating out water phase, cooling to 10 deg.C, recovering fluorine solvent, washing the residual organic solution with 10% sodium carbonate aqueous solution to neutrality, washing with equal volume of saturated sodium chloride solution twice, drying with anhydrous sodium sulfate, and filtering to obtain n-propyl benzoate with content of 98.3% and reaction conversion rate of 98.0%.
Example 6
40.0 g of benzoic acid, 31.0 g of phenol and 150.0 g of perfluorononene are added into a 500 ml four-neck flask provided with a reflux device and a mechanical stirrer, stirred and heated, 3.0 ml of concentrated sulfuric acid is dropwise added under vigorous stirring, the dropwise addition is finished within 15 minutes, the temperature is increased for reflux, and the reaction is continued for 3 hours under the condition. Standing and separating out a water phase, cooling to room temperature, filtering, and layering the filtrate to recover the fluorine solvent. The solid is crystallized and purified to obtain the product with benzoic acid phenyl ester content of 99.7% and reaction conversion rate of 98.0%.
Example 7
Adding 10.0 g of octadecanoic acid, 1.6 g of absolute ethyl alcohol and 30.0 g of perfluorononene into a 100 ml four-neck flask (provided with a reflux device and a mechanical stirrer) in sequence, stirring and heating, dropwise adding 1.0 ml of concentrated sulfuric acid under vigorous stirring, after dropwise adding within 10 minutes, heating to 70 ℃, and reacting for 2.5 hours under the conditions. Standing for a moment, cooling to room temperature, separating out a water layer and a fluorine solvent layer, recrystallizing and purifying the residual solid, wherein the content of the ethyl octadecanoate is 99.8%. The reaction conversion was 99.1%.
Example 8
75.0 g of sebacic acid, 34.1 g of ethanol and 150.0 g of perfluorocyclohexane are added into a 500 ml four-neck flask provided with a reflux device and a mechanical stirrer, stirred and heated, 3.0 ml of concentrated sulfuric acid is dropwise added under vigorous stirring, the dropwise addition is completed within 15 minutes, the temperature is raised and the reflux is carried out, and the reaction is continued for 3 hours under the condition. Standing, separating out a water phase, cooling to room temperature, recovering the fluorine solvent, washing the remaining organic solution with a 10% sodium carbonate aqueous solution to be neutral, washing with an equal volume of saturated saline solution twice, drying with anhydrous sodium sulfate, and filtering to obtain the product with the diethyl sebacate content of 98.6% and the reaction conversion rate of 99.5%.
Example 9
32.0 g of oxalic acid, 42.6 g of n-propanol and 110.0 g of perfluorononene are added into a 500 ml four-neck flask provided with a reflux device and a mechanical stirrer, stirred and heated, 2.0 ml of concentrated sulfuric acid is added dropwise under vigorous stirring, the dropwise addition is finished within 15 minutes, the temperature is increased for reflux, and the reaction is continued for 3 hours under the condition. Standing, separating out a water phase, cooling to 10 ℃, recovering the fluorine solvent, washing the remaining organic solution with a 10% sodium carbonate aqueous solution to be neutral, washing with an equal volume of saturated saline solution twice, drying with anhydrous sodium sulfate, and filtering to obtain the dipropyl oxalate with the content of 98.9% and the reaction conversion rate of 99.2%.
Example 10
100.0 g of phthalic acid, 55.4 g of ethanol and 150.0 g of perfluorotoluene are added into a 500 ml four-neck flask provided with a reflux device and a mechanical stirrer, stirred and heated, 10.0 ml of concentrated sulfuric acid is dropwise added under vigorous stirring, the dropwise addition is completed within 15 minutes, the temperature is raised and the reflux is carried out, and the reaction is continued for 3 hours under the condition. Standing, separating out a water phase, cooling to 10 ℃, recovering the fluorine solvent, washing the remaining organic solution with a 10% sodium carbonate aqueous solution to be neutral, washing with an equal volume of saturated saline solution twice, drying with anhydrous sodium sulfate, and filtering to obtain the product with the diethyl phthalate content of 98.6% and the reaction conversion rate of 98.9%.
Example 11
32.0 g of oxalic acid, 31.0 g of 1, 4-butanediol and 110.0 g of perfluorononene are added into a 500 ml four-neck flask provided with a reflux device and a mechanical stirrer, stirred and heated, 2.0 ml of concentrated sulfuric acid is added dropwise under vigorous stirring, the dropwise addition is completed within 15 minutes, the temperature is increased for reflux, and the reaction is continued for 3 hours under the condition. Standing, separating out water phase, cooling to 10 deg.C, recovering fluorine solvent, washing the residual organic solution with 10% sodium carbonate aqueous solution to neutrality, washing with equal volume of saturated saline solution twice, drying with anhydrous sodium sulfate, and filtering to obtain succinic diacid ester with content of 98.1% and reaction conversion rate of 99.2%.
Example 12
Adding 46.4 g of stearic acid, 5.0 g of glycerol and 150 g of perfluorononene into a 500 ml four-neck flask provided with a reflux device and a mechanical stirrer,stirring and heating, dropwise adding 3.0 ml of concentrated sulfuric acid under vigorous stirring, after dropwise adding within 15 minutes, heating and refluxing, and continuing to react for 4 hours under the condition. Standing for a moment, cooling to room temperature, separating out a water layer and a fluorine solvent layer, recrystallizing and purifying the remaining solid to obtain the glycerol tristearate with the content of 99.2 percent and the stearic acid conversion rate of 96 percent.
Example 13
100.0 g of eicosanoic acid, 10.2 g of methanol and 150 g of perfluorocyclohexane are added into a 500 ml four-neck flask provided with a reflux device and a mechanical stirrer, stirred and heated, 3.0 ml of concentrated sulfuric acid is dropwise added under vigorous stirring, the dropwise addition is completed within 15 minutes, the temperature is raised and the reflux is carried out, and the reaction is continued for 3 hours under the condition. Standing for a moment, cooling to room temperature, separating out a water layer and a fluorine solvent layer, recrystallizing and purifying the residual solid to obtain the eicosane methyl ester with the content of 99.6 percent and the eicosanoic acid conversion rate of 98 percent.
Claims (10)
1. An organic acid esterification method takes organic acid and alcohol as raw materials, and is characterized by comprising the following steps: reacting organic acid and alcohol in a fluorine solvent at 20-250 ℃ by taking inorganic acid as a catalyst, and performing post-treatment to obtain organic ester; the fluorine solvent is C1～C15Or a perfluoroalkene or a perfluoroarene or any mixture thereof.
2. The method of esterifying an organic acid according to claim 1, wherein the organic acid is C1～C20The alcohol is C, 1-2-membered fatty acid or alicyclic acid or aromatic acid1～C201-3-membered aliphatic alcohol or alicyclic alcohol or phenol.
3. The method of esterifying an organic acid according to claim 2, wherein the organic acid is acetic acid or benzoic acid, and the alcohol is ethanol, n-propanol or n-butanol.
4. The method of esterifying an organic acid according to claim 1, wherein the inorganic acid is one of: sulfuric acid, hydrochloric acid, p-toluenesulfonic acid.
5. The method of esterifying an organic acid according to claim 4, wherein the inorganic acid is concentrated sulfuric acid.
6. The method of esterifying an organic acid according to claim 1, wherein the fluorine solvent is C6～C12Or a perfluoroalkene or a perfluoroarene or any mixture thereof.
7. The method of esterifying an organic acid according to claim 6, wherein the fluorosolvent is perfluorononene.
8. The method for esterifying an organic acid according to any one of claims 1 to 7, wherein the ratio of the organic acid to the alcohol functional group is 1: 0.8 to 1.2, the mass ratio of the fluorine solvent to the reactant is 0.1 to 10: 1, and the mass ratio of the inorganic acid to the reactant is 1% to 20%; the reaction temperature is 20-120 ℃.
9. The method for esterifying an organic acid according to claim 8, wherein the molar ratio of the organic acid to the functionalgroup of the alcohol is 1: 1, and the mass ratio of the fluorine solvent to the reactant is 2 to 4: 1.
10. The method of esterifying an organic acid according to claim 8, wherein: when the product organic ester is liquid, the post-treatment steps are as follows: separating the reaction solution to remove a water phase, standing for layering, recovering a lower fluorine solvent layer, washing an upper organic layer to be neutral by using a sodium carbonate solution, washing by using saturated saline solution, drying by using anhydrous sodium sulfate, and filtering to obtain a product organic ester; when the product organic ester is a solid, the post-treatment steps are as follows: and standing the reaction solution, separating a water layer and a fluorine solvent layer, recrystallizing the residual solid, and purifying to obtain the product organic ester.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN102442930A (en) * | 2011-11-02 | 2012-05-09 | 江苏宇翔化工有限公司 | Preparation method of DL-p-methylsulfonylphenyl serine ethyl ester |
| CN103695053A (en) * | 2013-12-25 | 2014-04-02 | 济南开发区星火科学技术研究院 | Synthetic method of diesel oil cetane number improver |
| CN110372505A (en) * | 2019-08-30 | 2019-10-25 | 锦西化工研究院有限公司 | A kind of preparation method of dibutyl oxalate |
| CN114073923A (en) * | 2021-11-26 | 2022-02-22 | 江苏云华新材料科技有限公司 | Low-dielectric-constant aliphatic alkane and preparation method thereof |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI529159B (en) | 2012-05-09 | 2016-04-11 | China Petrochemical Dev Corp Taipei Taiwan | Method for continuously preparing carboxylic acid esters |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| DE3042695A1 (en) * | 1979-11-13 | 1981-05-27 | Union Carbide Corp., 10017 New York, N.Y. | METHOD FOR PRODUCING ESTERS |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102442930A (en) * | 2011-11-02 | 2012-05-09 | 江苏宇翔化工有限公司 | Preparation method of DL-p-methylsulfonylphenyl serine ethyl ester |
| CN103695053A (en) * | 2013-12-25 | 2014-04-02 | 济南开发区星火科学技术研究院 | Synthetic method of diesel oil cetane number improver |
| CN103695053B (en) * | 2013-12-25 | 2015-11-18 | 济南开发区星火科学技术研究院 | A kind of synthetic method of diesel cetane-number improver |
| CN110372505A (en) * | 2019-08-30 | 2019-10-25 | 锦西化工研究院有限公司 | A kind of preparation method of dibutyl oxalate |
| CN114073923A (en) * | 2021-11-26 | 2022-02-22 | 江苏云华新材料科技有限公司 | Low-dielectric-constant aliphatic alkane and preparation method thereof |
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