CN113292423A - Synthesis method of o-methyl cyclohexyl acetate - Google Patents

Synthesis method of o-methyl cyclohexyl acetate Download PDF

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Publication number
CN113292423A
CN113292423A CN202110605025.4A CN202110605025A CN113292423A CN 113292423 A CN113292423 A CN 113292423A CN 202110605025 A CN202110605025 A CN 202110605025A CN 113292423 A CN113292423 A CN 113292423A
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synthesis
acetate
methyl cyclohexyl
cyclohexyl acetate
synthesis method
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CN113292423B (en
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陈建
宋青明
李军峰
许蓉
杨红军
李闯
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Wuhan University of Technology WUT
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Wuhan University of Technology WUT
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C67/00Preparation of carboxylic acid esters
    • C07C67/08Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides with the hydroxy or O-metal group of organic compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/0215Sulfur-containing compounds
    • B01J31/0225Sulfur-containing compounds comprising sulfonic acid groups or the corresponding salts
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/0215Sulfur-containing compounds
    • B01J31/0225Sulfur-containing compounds comprising sulfonic acid groups or the corresponding salts
    • B01J31/0227Sulfur-containing compounds comprising sulfonic acid groups or the corresponding salts being perfluorinated, i.e. comprising at least one perfluorinated moiety as substructure in case of polyfunctional compounds
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C69/00Esters of carboxylic acids; Esters of carbonic or haloformic acids
    • C07C69/003Esters of saturated alcohols having the esterified hydroxy group bound to an acyclic carbon atom
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C69/00Esters of carboxylic acids; Esters of carbonic or haloformic acids
    • C07C69/02Esters of acyclic saturated monocarboxylic acids having the carboxyl group bound to an acyclic carbon atom or to hydrogen
    • C07C69/12Acetic acid esters
    • C07C69/14Acetic acid esters of monohydroxylic compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2231/00Catalytic reactions performed with catalysts classified in B01J31/00
    • B01J2231/40Substitution reactions at carbon centres, e.g. C-C or C-X, i.e. carbon-hetero atom, cross-coupling, C-H activation or ring-opening reactions
    • B01J2231/49Esterification or transesterification
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2601/00Systems containing only non-condensed rings
    • C07C2601/12Systems containing only non-condensed rings with a six-membered ring
    • C07C2601/14The ring being saturated
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/584Recycling of catalysts

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Abstract

The invention relates to the field of chemical industry, and discloses a synthesis method of o-methyl cyclohexyl acetate. The synthesis method of o-methyl cyclohexyl acetate greatly shortens the reaction time by sulfonic acid catalysts, and the obtained product has high purity.

Description

Synthesis method of o-methyl cyclohexyl acetate
Technical Field
The invention relates to the field of chemical industry, in particular to a synthesis method of o-methyl cyclohexyl acetate.
Background
At present, most of hydrogen peroxide is produced by an anthraquinone method. However, the production of hydrogen peroxide by the anthraquinone process suffers from low yield and poor product quality. Therefore, the method for solving the performance problem of the working solution is an important method for improving the yield of the hydrogen peroxide.
By adding 2-MCA into the working solution, the performance of the working solution can be effectively improved. The synthesis of o-methylcyclohexyl acetates from acetic anhydride and o-methylcyclohexanol is known.
Chinese patent (published: 10/13/2004, publication No. CN1240663C) discloses a preparation method of o-methylcyclohexyl acetate, wherein a catalyst for synthesizing 2-MCA is trimethylchlorosilane (CTMS), and the CTMS is used to reduce the operation risk coefficient, but the reaction time is too long, and the yield is low.
Therefore, a catalyst with good catalytic effect and low risk coefficient is urgently needed to improve the synthesis process of 2-MCA, so as to improve the reaction efficiency and shorten the reaction time.
Disclosure of Invention
The invention aims to overcome the defects of the prior art and provide a method for synthesizing o-methylcyclohexyl acetate, which greatly shortens the reaction time by using a sulfonic acid catalyst and obtains a product with high purity.
In order to achieve the purpose, the synthesis method of the o-methyl cyclohexyl acetate provided by the invention comprises the step of reacting o-methyl cyclohexanol with acetic anhydride under the catalysis of a sulfonic acid catalyst to generate the o-methyl cyclohexyl acetate.
Preferably, the sulfonic acid-based catalyst includes methanesulfonic acid, p-toluenesulfonic acid, benzenesulfonic acid, and trifluoromethanesulfonic acid.
Preferably, the reaction temperature is 30-60 ℃.
Preferably, the reaction time is 1 to 3 hours.
Preferably, the molar ratio of the o-methyl cyclohexanol to the acetic anhydride is 1: 1.0 to 1.5.
Preferably, the dosage of the sulfonic acid catalyst is 0.01-0.1% of the mass of the o-methylcyclohexanol.
Compared with the prior art, the invention has the following advantages:
1. simple operation, high catalytic efficiency and low catalyst consumption;
2. the yield of the finally obtained product is more than 98 percent, and the purity of the obtained product is high;
3. compared with the prior catalyst, the catalyst has more development potential and process prospect.
Detailed Description
The present invention will be described in further detail with reference to specific examples.
Example 1
50 g of o-methylcyclohexanol and 52.7 g of acetic anhydride are added into a reactor, 0.005 g of trifluoromethanesulfonic acid is added into the reactor, the reaction temperature is controlled at 50 ℃, the reaction time is 2 hours, and the yield of o-methylcyclohexyl acetate is 98%.
Example 2
50 g of o-methylcyclohexanol and 57.9 g of acetic anhydride are added into a reactor, 0.025 g of trifluoromethanesulfonic acid is added into the reactor, the reaction temperature is controlled at 60 ℃, the reaction time is 2 hours, and the yield of o-methylcyclohexyl acetate is 98%.
Example 3
50 g of o-methylcyclohexanol and 57.9 g of acetic anhydride are charged into a reactor, 0.05 g of p-toluenesulfonic acid is charged into the reactor, and stirring is carried out until it is dissolved. The reaction temperature is controlled at 60 ℃, the reaction time is 2 hours, and the yield of the o-methylcyclohexyl acetate is 99 percent.
The synthesis method of o-methyl cyclohexyl acetate has the advantages of simple and convenient operation, high catalytic efficiency and low catalyst consumption; the yield of the finally obtained product is more than 98 percent, and the purity of the obtained product is high; compared with the prior catalyst, the catalyst has more development potential and process prospect.

Claims (6)

1. A method for synthesizing o-methyl cyclohexyl acetate is characterized in that: the o-methyl cyclohexanol and acetic anhydride react under the catalysis of sulfonic acid catalyst to produce o-methyl cyclohexyl acetate.
2. The process for the synthesis of o-methylcyclohexyl acetate as claimed in claim 1, wherein: the sulfonic acid catalyst includes methanesulfonic acid, p-toluenesulfonic acid, benzenesulfonic acid and trifluoromethanesulfonic acid.
3. The process for the synthesis of o-methylcyclohexyl acetate as claimed in claim 1, wherein: the reaction temperature is 30-60 ℃.
4. The process for the synthesis of o-methylcyclohexyl acetate as claimed in claim 1, wherein: the reaction time is 1-3 hours.
5. The process for the synthesis of o-methylcyclohexyl acetate as claimed in claim 1, wherein: the mol ratio of the o-methyl cyclohexanol to the acetic anhydride is 1: 1.0 to 1.5.
6. The process for the synthesis of o-methylcyclohexyl acetate as claimed in claim 1, wherein: the dosage of the sulfonic acid catalyst is 0.01-0.1% of the mass of the o-methylcyclohexanol.
CN202110605025.4A 2021-05-31 2021-05-31 Synthesis method of o-methyl cyclohexyl acetate Active CN113292423B (en)

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CN202110605025.4A CN113292423B (en) 2021-05-31 2021-05-31 Synthesis method of o-methyl cyclohexyl acetate

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CN113292423B CN113292423B (en) 2023-12-12

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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050010065A1 (en) * 2001-11-15 2005-01-13 Alexander Wartini Method for producing (meth) acrylic acid esters of polyhydric alcohols
CN104557526A (en) * 2014-11-27 2015-04-29 浙江金科过氧化物股份有限公司 Method for preparing ortho-methylcyclohexyl acetate under solvent-free conditions
CN105315156A (en) * 2014-07-31 2016-02-10 广西田东达盛化工科技有限公司 Synthesis method for 2-methylcyclohexyl acetate

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050010065A1 (en) * 2001-11-15 2005-01-13 Alexander Wartini Method for producing (meth) acrylic acid esters of polyhydric alcohols
CN105315156A (en) * 2014-07-31 2016-02-10 广西田东达盛化工科技有限公司 Synthesis method for 2-methylcyclohexyl acetate
CN104557526A (en) * 2014-11-27 2015-04-29 浙江金科过氧化物股份有限公司 Method for preparing ortho-methylcyclohexyl acetate under solvent-free conditions

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
向德轩 等: "甲基丙烯酸八氟戊酯的合成", 《精细石油化工》 *
周扬志 等: "三氟甲磺酸催化合成柠檬酸酯", 《现代化工》 *
李玉文 等: "三氟甲磺酸催化合成阿司匹林", 《应用化工》 *
李玉文: "三氟甲磺酸催化便捷高效合成2,4-滴丁酯除草剂", 《应用化工》 *

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