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CN101024612B - A kind of acidic ionic liquid catalyzed alkyd esterification method - Google Patents

A kind of acidic ionic liquid catalyzed alkyd esterification method Download PDF

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CN101024612B
CN101024612B CN200710027186XA CN200710027186A CN101024612B CN 101024612 B CN101024612 B CN 101024612B CN 200710027186X A CN200710027186X A CN 200710027186XA CN 200710027186 A CN200710027186 A CN 200710027186A CN 101024612 B CN101024612 B CN 101024612B
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ionic liquid
alcohol
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CN101024612A (en
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黄宝华
汪艳飞
方岩雄
赵肃清
张焜
黎子进
史娜
周蓓蕾
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Guangdong University of Technology
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Abstract

本发明公开了一种酸性离子液体催化醇酸酯化方法,该方法采用α-吡咯烷酮阳离子与无机或有机阴离子构成的离子液体作为反应的催化剂、溶剂、脱水剂,离子液体加入量为醇和酸的总摩尔数的10~200%,在80~140℃,常压,反应0.5~8小时催化醇酸酯化反应生成酯;本发明与传统的酸催化法相比,酯化反应产物更容易分离,选择性更高,并具有高普适性;突出的特点是产物酯与催化剂可自动分相,而且离子液体经简单处理可重复使用,催化活性不变。The invention discloses an acidic ionic liquid catalyzed alkyd esterification method. The method uses an ionic liquid composed of α-pyrrolidone cations and inorganic or organic anions as a reaction catalyst, solvent, and dehydrating agent. 10-200% of the total moles, at 80-140°C, normal pressure, react for 0.5-8 hours to catalyze the esterification reaction of alkyd to generate ester; compared with the traditional acid-catalyzed method, the esterification reaction product is easier to separate, Higher selectivity and high universality; the outstanding feature is that the product ester and the catalyst can automatically separate phases, and the ionic liquid can be reused after simple treatment, and the catalytic activity remains unchanged.

Description

A kind of method for catalyzing alcohol acid esterization by acidic ion liquid
Technical field
The present invention relates to the organic chemical reactions method, particularly relate to a kind of method for catalyzing alcohol acid esterization by acidic ion liquid.
Background technology
Carboxylic acid ester compound has the wide industrial purposes, much is important chemical product.Traditional alcoholic acid esterification technology is used the inorganic acid as catalyst of severe corrosive such as the vitriol oil usually, exist that selectivity is low, product is coloured, be difficult to separate with product, problems such as etching apparatus and contaminate environment, it is therefore industrial that exploitation is had the novel alcoholic acid esterification system demand of environmental benefit and economic benefit is very urgent.Advantages such as the ionic liquid that is liquid state under the room temperature is the novel material that receives much attention in recent years, has good stability, and is non-volatile, and solvability and acidity are adjustable are showing excellent characteristic as novel green catalyst and solvent in a lot of acid catalyzed reactions.Deng You congruence (CN1247856) is used alkyl pyridine, the ionic liquid that phonetic azoles etc. contain nitric heterocyclic compound and metal or non-metallic halide formation carries out catalyst for esterification and solvent as alcohol and acid, realized the alcoholic acid esterification reaction, but shortcomings such as this class ionic liquid existence is stable inadequately to water and air, the stable deficiency of repeated use; (CN1405140 is CN1528733) with ionic liquid [Hmim] BF for He Mingyuan etc. 4, Fang Yanxiong etc. (CN1880295) is cationic ionic liquid with the pyrrolidone that the N-alkyl or alkenyl replaces, and as the catalyzer and the solvent of alcoholic acid esterification, successively realized the esterification of alcohol with acid.The small molecules ester of low carbon number is at [Hmim] BF 4System (CN1405140, CN1528733) in phase-splitting automatically, thereby can not prepare by separatory, must be by distillation preparation (CN1528733).The present invention is that the ionic liquid that constitutes with alpha-pyrrolidone positively charged ion and inorganic or organic anion is as alcoholic acid esterification catalyst for reaction, solvent, dewatering agent, have advantages of high catalytic activity and universality, just can realize automatic phase-splitting by simply being separated with esterification products, and can be recycled, catalytic activity is constant substantially, therefore is expected to substitute in chemical industry do not meet traditional severe corrosive acid catalytic materials such as the vitriol oil that Green Chemistry requires.
Summary of the invention
The objective of the invention is to replace the reaction of traditional inorganic acids catalyst alcoholic acid esterification, realize the alcoholic acid esterification of the green high-efficient under the mild reaction conditions with acidic ion liquid.
The present invention realizes by following scheme:
In the there-necked flask that magnetic stirring apparatus, thermometer, reflux condensing tube are housed, add the ionic liquid and the alcohol, sour of certain proportioning, through reacting by heating, cooling, standing demix while stirring, processes such as separatory realize esterification; Or ionic liquid mixed with alkyd, through after the reacting by heating while stirring, straight run distillation goes out ester products.Ionic liquid can be reused after simply dewatering and keep catalytic activity constant.
The inventive method feature is the ionic liquid that constitutes with alpha-pyrrolidone positively charged ion and inorganic or organic anion catalyzer, solvent, the dewatering agent as esterification, add-on is 10~200% of alcohol, a sour total mole number, 80~140 ℃ of temperature of reaction, normal pressure, 0.5~8 hour reaction times.
The described alpha-pyrrolidone cationic structural of the inventive method formula is as follows:
Figure S07127186X20070403D000011
The described inorganic or organic anion of the inventive method is chlorine, bromine, iodine, sulfate radical, bisulfate ion, nitrate radical, dihydrogen phosphate, acetate, tetrafluoroborate, tosic acid root, trifluoromethanesulfonic acid root, trifluoroacetic acid radical ion.
The described reactant alcohol of the inventive method is C 1~C 12The saturated or unsaturated fatty alcohol of the monobasic of straight or branched, aromatic alcohol, polyvalent alcohol, C 3~C 12Alicyclic ring alcohol.
The general formula of the described aromatic alcohol of the inventive method is:
Figure S07127186X20070403D000012
Wherein R is C 1~C 4Alkyl.
The described polyvalent alcohol of the inventive method is ethylene glycol, glycerol, tetramethylolmethane.
Monocarboxylic acid, di-carboxylic acid, lactic acid, citric acid that the described reactant acid of the inventive method is straight or branched, phenylformic acid, salicylic acid, m-Salicylic acid, P-hydroxybenzoic acid, 0-chloro-benzoic acid, m-chlorobenzoic acid, Chlorodracylic acid, o-bromobenzoic acid, m-bromobenzoic acid, parabromobenzoic acid.
The monocarboxylic general formula of the described straight or branched of the inventive method is R ' COOH, and R is H atom, C 1~C 17Alkyl, C 2~C 17Thiazolinyl; The general formula of di-carboxylic acid is HOOC (CH 2) nCOOH, n=O, 1-6.
In the method for the invention, the addition sequence in the reaction process between alcohol, acid and the ionic liquid three without limits.
In the method for the invention, stir reflux certain hour down in the reaction process, reaction afterreaction liquid leaves standstill separatory, tells upper organic phase and gets esterified prod; Or reaction afterreaction liquid directly distill esterified prod.
The inventive method is compared with background technology, and beneficial effect is:
1. used acidic ion liquid promotes medium as alcoholic acid esterification catalyst for reaction or reaction, the phase-splitting automatically of esterification reaction product and ionic liquid, and the purity height is simplified separation process.
2. transformation efficiency height, selectivity 100%.
3. reacted ionic-liquid catalyst can use repeatedly through simple vaccum dewatering, and catalytic activity is constant, and product is colourless.When the ionic liquid usage quantity is big, can dewater and use repeatedly continuously.
4. such ionic liquid is compared cheap with traditional imidazoles, pyridines ionic liquid.Because the ionic liquid steam forces down, and is non-volatile, so this catalyst system is eco-friendly.
5. universality is good.Saturated fatty acid, unsaturated fatty acids, alpha hydroxy acid, diprotic acid, aromatic acid, phenylformic acid, substituted benzoic acid can generate ester with above-mentioned reactant alcohol.
Embodiment
Following embodiment is to the further specifying of the inventive method, and is not limitation of the invention.
Embodiment one: take by weighing acetate 0.1mol respectively, ethanol 0.1mol, ionic liquid alpha-pyrrolidone hydrosulfate 0.1mol; Ionic liquid, ethanol, acetate are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, magnetic agitation, and 80 ℃ of heating reflux reactions 0.5 hour; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 90.3%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.
Embodiment two: take by weighing acetate 0.1mol respectively, propyl carbinol 0.1mol, ionic liquid alpha-pyrrolidone nitrate 0.02mol; Ionic liquid, propyl carbinol, acetate are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, and 100 ℃ of lower magnetic force stirring reactions 1 hour; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 75.8%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.
Embodiment three: take by weighing acetate 0.1mol respectively, n-Heptyl alcohol 0.1mol, ionic liquid alpha-pyrrolidone hydrochloride 0.01mol; Ionic liquid, n-Heptyl alcohol, acetate are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, magnetic agitation, and under 140 ℃, reacted 2 hours; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 71.7%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.
Embodiment four: take by weighing acetate 0.1mol respectively, lauryl alcohol (lauryl alcohol) 0.1mol, ionic liquid alpha-pyrrolidone hydrobromate 0.1mol; Ionic liquid, lauryl alcohol, acetate are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, magnetic agitation, and under 130 ℃, reacted 2 hours; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 65.2%, selectivity 100%.Ionic liquid is reused after vacuum hydro-extraction.
Embodiment five: take by weighing acetate 0.1mol respectively, phenylcarbinol 0.1mol, ionic liquid alpha-pyrrolidone hydriodate 0.05mol; Ionic liquid, phenylcarbinol, acetate are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, magnetic agitation, and under 110 ℃, reacted 2 hours; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 84.7%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.
Embodiment six: take by weighing acetate 0.1mol respectively, phenylpropyl alcohol 0.1mol, ionic liquid alpha-pyrrolidone acetate 0.02mol; Ionic liquid, phenylpropyl alcohol, acetate are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, magnetic agitation, and under 120 ℃, reacted 8 hours; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 73.2%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.
Embodiment seven: take by weighing acetate 0.1mol respectively, 4-phenyl-2-butanols 0.1mol, ionic liquid alpha-pyrrolidone trifluoroacetate 0.02mol; Ionic liquid, 4-phenyl-2-butanols, acetate are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, magnetic agitation, and under 140 ℃, reacted 8 hours; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 51.3%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.
Embodiment eight: take by weighing acetate 0.2mol respectively, ethylene glycol 0.1mol, ionic liquid alpha-pyrrolidone tosilate 0.02mol; Ionic liquid, ethylene glycol, acetate are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, magnetic agitation, and under 120 ℃, reacted 1 hour; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 67.1%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.
Embodiment nine: take by weighing propionic acid 0.1mol respectively, n-propyl alcohol 0.1mol, ionic liquid alpha-pyrrolidone fluoroform sulphonate 0.01mol; Ionic liquid, n-propyl alcohol, propionic acid are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, magnetic agitation, and under 90 ℃, reacted 2 hours; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 74.5%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.
Embodiment ten: take by weighing butanic acid 0.1mol respectively, ethanol 0.1mol, ionic liquid alpha-pyrrolidone hydrosulfate 0.02mol; Ionic liquid, ethanol, butanic acid are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, magnetic agitation, and under 80 ℃, reacted 2 hours; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 79.7%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.
Embodiment 11: take by weighing butanic acid 0.1mol respectively, propyl carbinol 0.1mol, ionic liquid alpha-pyrrolidone a tetrafluoro borate 0.2mol; Ionic liquid, propyl carbinol, butanic acid are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively magnetic agitation, and heating reflux reaction 1 hour; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 75.8%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.
Embodiment 12: take by weighing butanic acid 0.1mol respectively, the about 0.1mol of hexalin, ionic liquid alpha-pyrrolidone dihydrogen phosphate 0.04mol; Ionic liquid, hexalin, butanic acid are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, magnetic agitation, and under 120 ℃, reacted 2 hours; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 53.2%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.
Embodiment 13: take by weighing positive enanthic acid 0.1mol respectively, methyl alcohol 0.1mol, ionic liquid alpha-pyrrolidone tosilate 0.02mol; Ionic liquid, methyl alcohol, positive enanthic acid are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, magnetic agitation, and under 70 ℃ of stream temperature, reacted 4 hours; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 60.9%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.
Embodiment 14: take by weighing stearic acid (octadecanoic acid) 0.1mol respectively, ethanol 0.1mol, ionic liquid alpha-pyrrolidone hydrosulfate 0.1mol; Ionic liquid, ethanol, stearic acid are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, magnetic agitation, and under 90 ℃, reacted 8 hours; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 42.7%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.
Embodiment 15: take by weighing vinylformic acid 0.1mol respectively, propyl carbinol 0.1mol, ionic liquid alpha-pyrrolidone trifluoroacetate 0.05mol; Ionic liquid, propyl carbinol, vinylformic acid are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, magnetic agitation, and under 100 ℃, reacted 2 hours; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 82.5%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.
Embodiment 16: take by weighing oleic acid (Octadec-9-enoic Acid) 0.1mol respectively, propyl carbinol 0.1mol, ionic liquid alpha-pyrrolidone fluoroform sulphonate 0.05mol; Ionic liquid, propyl carbinol, oleic acid are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, magnetic agitation, and under 100 ℃, reacted 2 hours; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 61.8%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.
Embodiment 17: take by weighing oxalic acid 0.1mol respectively, ethanol 0.1mol, ionic liquid α-adjoin pyrrolidone hydriodate 0.1mol; Ionic liquid, ethanol, oxalic acid are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, magnetic agitation, and under 80 ℃, reacted 4 hours; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 71.3%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.
Embodiment 18: take by weighing Succinic Acid (succsinic acid) 11.8g (0.1mol) respectively, the about 9.260g of ethanol (0.1mol), ionic liquid alpha-pyrrolidone nitrate 0.1mol; Ionic liquid, ethanol, Succinic Acid are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, magnetic agitation, and under 80 ℃, reacted 2 hours; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 72.6%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.
Embodiment 19: take by weighing lactic acid (alpha-hydroxypropionic acid) 0.1mol respectively, propyl carbinol 0.1mol, ionic liquid alpha-pyrrolidone a tetrafluoro borate 0.05mol; Ionic liquid, propyl carbinol, lactic acid are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, magnetic agitation, and under 100 ℃, reacted 2 hours; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 67.5%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.
Embodiment 20: take by weighing phenylformic acid (M-nitro benzoic acid) 0.1mol respectively, ethanol 0.1mol, ionic liquid alpha-pyrrolidone hydrosulfate 0.1mol; Ionic liquid, ethanol, phenylformic acid are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, magnetic agitation, and under 80 ℃, reacted 4 hours; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 71.8%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.
Embodiment 21: take by weighing salicylic acid 0.1mol respectively, propyl carbinol 0.1mol, ionic liquid alpha-pyrrolidone tosilate 0.05mol; Ionic liquid, propyl carbinol, salicylic acid are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, magnetic agitation, and under 110 ℃, reacted 8 hours; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 64.6%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.
Embodiment 22: take by weighing adjacent bromobenzene formic acid 0.1mol respectively, propyl carbinol 0.1mol, ionic liquid alpha-pyrrolidone trifluoroacetate pyrrolidone hydrosulfate 0.05mol; Ionic liquid, propyl carbinol, adjacent bromobenzene formic acid are added in the round-bottomed flask that has agitator, thermometer, reflux condensing tube successively, magnetic agitation, and under 110 ℃, reacted 8 hours; Standing demix pipettes the upper strata esterification products, and transformation efficiency is 53.4%, selectivity 100%; Ionic liquid is reused after vacuum hydro-extraction.

Claims (9)

1.一种酸性离子液体催化醇酸酯化方法,其特征是以α-吡咯烷酮阳离子与无机或有机阴离子构成的离子液体作为反应的催化剂、溶剂、脱水剂;其中所述α-吡咯烷酮阳离子结构式为1. an acidic ionic liquid catalyzed alkyd esterification method is characterized in that the ionic liquid made of α-pyrrolidone cation and inorganic or organic anion is used as a catalyst, solvent, dehydrating agent for reaction; wherein said α-pyrrolidone cation structural formula is
Figure FSB00000208233100011
Figure FSB00000208233100011
上述离子液体加入量为醇和酸的总摩尔数的10~200%,反应温度80~140℃,常压,反应时间0.5~8小时。The addition amount of the above-mentioned ionic liquid is 10-200% of the total moles of alcohol and acid, the reaction temperature is 80-140° C., normal pressure, and the reaction time is 0.5-8 hours.
2.如权利要求1所述的方法,其特征在于所述无机或有机阴离子为氯、溴、碘、硫酸根、硫酸氢根、硝酸根、磷酸二氢根、醋酸根、四氟硼酸根、对甲苯磺酸根、三氟甲磺酸根、三氟乙酸根离子。2. the method for claim 1 is characterized in that described inorganic or organic anion is chlorine, bromine, iodine, sulfate radical, bisulfate radical, nitrate radical, dihydrogen phosphate radical, acetate radical, tetrafluoroborate radical, p-toluenesulfonate, trifluoromethanesulfonate, trifluoroacetate ions. 3.如权利要求1所述的方法,其特征在于上述反应物醇为C1~C12的直链或支链的一元饱和或不饱和脂肪醇、芳香醇、多元醇、C3~C12的脂环醇。3. The method according to claim 1, characterized in that the above-mentioned reactant alcohol is C 1 -C 12 linear or branched monovalent saturated or unsaturated fatty alcohol, aromatic alcohol, polyhydric alcohol, C 3 -C 12 of alicyclic alcohols. 4.如权利要求3所述的方法,其特征在于上述芳香醇的通式为:
Figure FSB00000208233100012
其中R为C1~C4的烷基。
4. method as claimed in claim 3 is characterized in that the general formula of above-mentioned aromatic alcohol is:
Figure FSB00000208233100012
Wherein R is a C1-C4 alkyl group.
5.如权利要求3所述的方法,其特征在于上述多元醇为乙二醇、丙三醇、季戊四醇。5. the method for claim 3 is characterized in that above-mentioned polyhydric alcohol is ethylene glycol, glycerol, pentaerythritol. 6.如权利要求1所述的方法,其特征在于上述反应物酸是直链或支链的一元羧酸、二元羧酸、乳酸、柠檬酸,苯甲酸、邻羟基苯甲酸、间羟基苯甲酸、对羟基苯甲酸、邻氯苯甲酸、间氯苯甲酸、对氯苯甲酸、邻溴苯甲酸、间溴苯甲酸、对溴苯甲酸。6. the method for claim 1 is characterized in that above-mentioned reactant acid is linear or branched monocarboxylic acid, dicarboxylic acid, lactic acid, citric acid, benzoic acid, o-hydroxybenzoic acid, m-hydroxybenzene Formic acid, p-hydroxybenzoic acid, o-chlorobenzoic acid, m-chlorobenzoic acid, p-chlorobenzoic acid, o-bromobenzoic acid, m-bromobenzoic acid, p-bromobenzoic acid. 7.如权利要求6所述的方法,其特征在于上述直链或支链的一元羧酸的通式为R′COOH,R′为H原子、C1~C17的烷基、C2~C17烯基;二元羧酸的通式为HOOC(CH2)nCOOH,n=0,1-6。7. The method according to claim 6, characterized in that the general formula of the above-mentioned linear or branched monocarboxylic acid is R'COOH, R' is an H atom, C 1 ~C 17 alkyl, C 2 ~ C 17 alkenyl; the general formula of dicarboxylic acid is HOOC(CH 2 ) n COOH, n=0, 1-6. 8.如权利要求1所述的方法,其特征在于上述反应过程中醇、酸与离子液体三者之间的加入顺序没有限制。8. The method according to claim 1, characterized in that there is no restriction on the order of adding alcohol, acid and ionic liquid in the above-mentioned reaction process. 9.如权利要求1所述的方法,其特征在于上述反应过程中搅拌下加热回流一定时间,反应后反应液静置分液,分出上层有机相得酯化产品;或反应后反应液直接进行蒸馏得酯化产品。9. method as claimed in claim 1, it is characterized in that in the above-mentioned reaction process, stirring under reflux for a certain period of time, after the reaction, the reaction solution is allowed to stand for liquid separation, and the upper organic phase is separated to obtain the esterification product; or after the reaction, the reaction solution is directly Esterification products are obtained by distillation.
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