WO2019019808A1 - Method for synthesizing carvacrol by catalyzing dihydrocarvone isomerization - Google Patents

Method for synthesizing carvacrol by catalyzing dihydrocarvone isomerization Download PDF

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WO2019019808A1
WO2019019808A1 PCT/CN2018/089942 CN2018089942W WO2019019808A1 WO 2019019808 A1 WO2019019808 A1 WO 2019019808A1 CN 2018089942 W CN2018089942 W CN 2018089942W WO 2019019808 A1 WO2019019808 A1 WO 2019019808A1
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carvacrol
dihydrocarvone
catalyst
isomerization
catalyzing
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PCT/CN2018/089942
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French (fr)
Chinese (zh)
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刘晓涛
刘建国
万猛
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淮安万邦香料工业有限公司
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/56Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by isomerisation

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  • the invention belongs to the field of chemistry, and in particular relates to a method for chemical synthesis of carvacrol.
  • Carvacrol is a commonly used food additive and fragrance that has been approved as a safe food additive in the United States and Europe. It is a colorless to pale yellow thick oily liquid with the same odor as thymol, with low toxicity and natural characteristics.
  • Carvacrol has a very high application value, it inhibits bacteria, yeasts, fungi, insects and cockroaches by destroying and changing the cell membrane structure of the pathogenic bacteria, or the structure of the mycelium, or effectively inhibiting the activity of the conidia. It grows with good antibacterial and insecticidal effects. It is also an effective component of thyme's blood circulation and phlegm. It can realize platelets by mediating the signal transduction pathway of anti-thromboxin by G13 protein-linked RhoA/Rho-kinase. Activation is a natural antibacterial preservative that can be used in food, medicine, cosmetics and other fields.
  • the current preparation methods and problems of carvacrol are as follows:
  • PEG-400 or PEG-600 as a cocatalyst to promote intramolecular rearrangement of carvone to form carvacrol, which will produce 5-isopropyl-2-methyl -2,4-cyclohexadienone, 5-isopropenyl-2-methyl-2,6-cyclohexadienol and other by-products, difficult to separate from carvone, complicated subsequent processing, increasing production costs And time, and the product yield is low.
  • the copper is supported on activated carbon as a catalyst to dehydroisomerize carvone to carvacrol.
  • the catalyst particles in this method are small and easy to adhere, but after the reaction, the catalyst is not easily separated from carvacrol. It is not conducive to the recovery of the catalyst, and the reaction conversion rate is low.
  • the invention provides a method for isomerization of dihydrocarvone to form carvacrol, and the active copper is supported on a chromium material to form a catalyst of the method, the process is simple, the green is pollution-free, the catalyst is easy to recycle, and is suitable for industrial scale. Production.
  • the dihydrocarvone undergoes a dehydroisomerization reaction under the action of the catalyst Cu/Cr. After the reaction is completed, the Cu/Cr is repeatedly removed by filtration, and the organic phase is subjected to vacuum distillation to obtain carvacrol.
  • the reaction equation is as follows:
  • the catalyst Cu/Cr is a catalyst formed by supporting active copper on a chromium material with a Cu/Cr molar ratio of 5:1.
  • dihydrocarvone and Cu/Cr catalyst were added separately, stirred uniformly, heated to 160-200 ° C, reacted for 4-5 h, cooled to room temperature, filtered to remove catalyst Cu/Cr for recycling, organic phase decompression Rectification to obtain carvacrol.
  • the mass ratio of dihydrocarvone to active Cu is from 500 to 1000:2 to 50.
  • the invention adopts Cu/Cr to catalyze the dehydroisomerization of dihydrocarvone to synthesize carvacrol, the catalyst particles are slightly larger than the copper carbon catalyst, the adhesion of the reaction raw materials to the catalyst is high, and after the reaction, the catalyst particles and products are obtained. Easy to separate, can be recycled many times and the catalytic efficiency is basically unchanged, the reaction conversion rate is high, no industrial waste is produced; in addition, the catalyst in the invention is cheap and easy to obtain, the process is simple, the green is pollution-free, and is more suitable for industrial scale production. Carvacrol.
  • Catalyst reuse The Cu/Cr catalyst recovered by filtration was flushed to the reaction vessel with 500 g of dihydrocarvone, and the temperature was raised to 160 ° C for about 4 hours. After the GC showed that the reaction was completed, the Cu/Cr catalyst was continuously recovered by filtration, and the filtrate was decompressed. Rectification yielded 342 g of carvacrol with a content of 99.2%, an effective yield of 68.4%, and a yield of 99% of tetrahydrocarvone 156 g, a yield of 31.2%. By repeating this application 6 times, the catalyst efficiency was not significantly lowered.
  • Catalyst reuse The Cu/Cr catalyst recovered by filtration was flushed to the reaction vessel with 500 g of dihydrocarvone, and heated to 180 ° C for about 4.5 h. After GC showed that the reaction was over, the Cu/Cr catalyst was recovered by filtration, and the filtrate was reduced. Press distillation was carried out to obtain 355 g of carvacrol having a content of 99.1%, an effective yield of 71.2%, and at the same time, 143 g of tetrahydrocarvone having a content of 99% was obtained in a yield of 28%. When the application was repeated 7 times, the catalyst efficiency was not significantly lowered.

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Abstract

The present invention discloses a method for synthesizing carvacrol by catalyzing dihydrocarvone isomerization, wherein Cu/Cr is used to catalyze the dehydroisomerization of dihydrocarvone so as to synthesize carvacrol; after the reaction is finished, the catalyst particles and the product are easy to separate, and same can be recycled many times and the catalytic efficiency thereof stays basically unchanged; and the reaction conversion rate is high, and none of the industrial three wastes are produced. In addition, the catalyst in the invention is cheap and easy to obtain, the process is simple, green and non-polluting, and same is more suitable for the industrial-scale production of carvacrol.

Description

一种催化二氢香芹酮异构化合成香芹酚的方法Method for catalyzing isomerization of dihydrocarvone to carvacrol 技术领域Technical field
本发明属于化学领域,具体涉及一种香芹酚的化学合成方法。The invention belongs to the field of chemistry, and in particular relates to a method for chemical synthesis of carvacrol.
技术背景technical background
香芹酚是一种常用的食品添加剂及芳香剂,在美国和欧洲被批准为安全的食品添加剂。它是无色至淡黄色稠厚油状液体,有着和麝香草酚相同的气味,具有低毒性、天然性的特点。Carvacrol is a commonly used food additive and fragrance that has been approved as a safe food additive in the United States and Europe. It is a colorless to pale yellow thick oily liquid with the same odor as thymol, with low toxicity and natural characteristics.
香芹酚有着极高的应用价值,它通过破坏及改变致病菌的细胞膜结构、或菌丝体的结构、或有效抑制分生孢子的活性,从而抑制细菌、酵母菌、真菌、昆虫及螨类的生长,具有良好的抑菌、杀虫效果;同时它也是百里香活血化瘀的有效成分,通过介导抗血栓素经G13蛋白藕联的RhoA/Rho-激酶的信号转导途径,实现血小板活化,是一种天然的抑菌防腐剂,可应用于食品、药品、化妆品等领域。目前香芹酚常用的制备方法以及存在的问题如下:Carvacrol has a very high application value, it inhibits bacteria, yeasts, fungi, insects and cockroaches by destroying and changing the cell membrane structure of the pathogenic bacteria, or the structure of the mycelium, or effectively inhibiting the activity of the conidia. It grows with good antibacterial and insecticidal effects. It is also an effective component of thyme's blood circulation and phlegm. It can realize platelets by mediating the signal transduction pathway of anti-thromboxin by G13 protein-linked RhoA/Rho-kinase. Activation is a natural antibacterial preservative that can be used in food, medicine, cosmetics and other fields. The current preparation methods and problems of carvacrol are as follows:
(1)以邻甲基苯酚为原料,采用三氯化铝或者三氯化铁作为催化剂促进邻甲基苯酚与2-氯丙烷反应合成香芹酚的方法,该方法会产生大量的铝盐和铁盐固体废弃物,造成环境污染,限制了其在生产上的大规模应用。(1) A method for synthesizing carvacrol by reacting o-methylphenol with 2-chloropropane using o-methylphenol as a raw material and using aluminum trichloride or ferric chloride as a catalyst, which produces a large amount of aluminum salt and Iron salt solid waste, causing environmental pollution, limits its large-scale application in production.
(2)以有机酸或者无机酸为主催化剂,PEG-400或PEG-600为辅催化剂促进香芹酮分子内重排合成香芹酚,该方法会产生5-异丙基-2-甲基-2,4-环己二烯酮、5-异丙烯基-2-甲基-2,6-环己二烯醇等副产物,不易与香芹酮分离,后续处理复杂,增加了生产成本和时间,且产品 产率低。(2) Using organic acid or inorganic acid as main catalyst, PEG-400 or PEG-600 as a cocatalyst to promote intramolecular rearrangement of carvone to form carvacrol, which will produce 5-isopropyl-2-methyl -2,4-cyclohexadienone, 5-isopropenyl-2-methyl-2,6-cyclohexadienol and other by-products, difficult to separate from carvone, complicated subsequent processing, increasing production costs And time, and the product yield is low.
(3)将铜负载在活性炭上作为催化剂,使香芹酮脱氢异构化合成香芹酚,该方法中的催化剂颗粒较小,易于附着,但反应结束后,催化剂不易与香芹酚分离,不利于催化剂的回收,且反应转化率低。(3) The copper is supported on activated carbon as a catalyst to dehydroisomerize carvone to carvacrol. The catalyst particles in this method are small and easy to adhere, but after the reaction, the catalyst is not easily separated from carvacrol. It is not conducive to the recovery of the catalyst, and the reaction conversion rate is low.
本发明提供一种二氢香芹酮异构化合成香芹酚的方法,将活性铜负载在铬材料上形成该方法的催化剂,工艺简单,绿色无污染,催化剂易回收利用,适合于工业规模化生产。The invention provides a method for isomerization of dihydrocarvone to form carvacrol, and the active copper is supported on a chromium material to form a catalyst of the method, the process is simple, the green is pollution-free, the catalyst is easy to recycle, and is suitable for industrial scale. Production.
发明内容Summary of the invention
为了实现上述目的,本发明所采用的技术解决方案为:In order to achieve the above object, the technical solution adopted by the present invention is:
二氢香芹酮在催化剂Cu/Cr的作用下发生脱氢异构化反应,反应结束后,过滤除去Cu/Cr重复利用,有机相减压精馏,得到香芹酚,反应方程式如下:The dihydrocarvone undergoes a dehydroisomerization reaction under the action of the catalyst Cu/Cr. After the reaction is completed, the Cu/Cr is repeatedly removed by filtration, and the organic phase is subjected to vacuum distillation to obtain carvacrol. The reaction equation is as follows:
Figure PCTCN2018089942-appb-000001
Figure PCTCN2018089942-appb-000001
优选地,催化剂Cu/Cr为活性铜负载在铬材料上形成的催化剂,Cu/Cr摩尔比为5:1。Preferably, the catalyst Cu/Cr is a catalyst formed by supporting active copper on a chromium material with a Cu/Cr molar ratio of 5:1.
本发明的技术方案中具体制备步骤如下:The specific preparation steps in the technical solution of the present invention are as follows:
在反应釜中,分别加入二氢香芹酮和Cu/Cr催化剂,搅拌均匀,升温至160~200℃,反应4~5h,冷却至室温,过滤除去催化剂Cu/Cr回收利用,有机相减压精馏,得到香芹酚。In the reaction vessel, dihydrocarvone and Cu/Cr catalyst were added separately, stirred uniformly, heated to 160-200 ° C, reacted for 4-5 h, cooled to room temperature, filtered to remove catalyst Cu/Cr for recycling, organic phase decompression Rectification to obtain carvacrol.
优选地,二氢香芹酮与活性Cu的质量比为500~1000:2~50。Preferably, the mass ratio of dihydrocarvone to active Cu is from 500 to 1000:2 to 50.
本发明采用Cu/Cr催化二氢香芹酮脱氢异构化合成香芹酚,催化剂颗粒相对于铜碳催化剂稍大,反应原料与催化剂的附着度高,且反应结束后,催化剂颗粒与产物易分离,可多次循环使用且催化效率基本不变,反应转化率高,无工业三废产生;另外,本发明中的催化剂便宜易得,工艺简单,绿色无污染,更适用于工业规模化生产香芹酚。The invention adopts Cu/Cr to catalyze the dehydroisomerization of dihydrocarvone to synthesize carvacrol, the catalyst particles are slightly larger than the copper carbon catalyst, the adhesion of the reaction raw materials to the catalyst is high, and after the reaction, the catalyst particles and products are obtained. Easy to separate, can be recycled many times and the catalytic efficiency is basically unchanged, the reaction conversion rate is high, no industrial waste is produced; in addition, the catalyst in the invention is cheap and easy to obtain, the process is simple, the green is pollution-free, and is more suitable for industrial scale production. Carvacrol.
具体实施方式Detailed ways
下面通过实施案例对本发明作出进一步的详细说明。The present invention will be further described in detail below by way of embodiments.
实施例1Example 1
在1000mL反应釜中加入500g二氢香芹酮和2.5gCu/Cr催化剂(Cu/Cr摩尔比为5:1),搅拌均匀后升温至160℃反应4h,GC显示反应结束后,冷却至室温,过滤回收Cu/Cr催化剂,滤液经过减压精馏得到纯度99.2%的香芹酚345g,有效产率为69%,同时得到含量99%的四氢香芹酮150g,产率为30%。500 g of dihydro carvone and 2.5 g of Cu/Cr catalyst (5:1 Cu/Cr molar ratio) were added to a 1000 mL reactor. After stirring, the temperature was raised to 160 ° C for 4 h. After GC showed that the reaction was completed, it was cooled to room temperature. The Cu/Cr catalyst was recovered by filtration, and the filtrate was subjected to vacuum distillation to obtain 345 g of carotenol having a purity of 99.2%, an effective yield of 69%, and 150 g of tetrahydrocarvone having a content of 99% was obtained in a yield of 30%.
催化剂再利用:将过滤回收的Cu/Cr催化剂用500g二氢香芹酮冲洗至反应釜,升温至160℃反应约4h,GC显示反应结束后,过滤继续回收Cu/Cr催化剂,滤液经过减压精馏得到含量99.2%的香芹酚342g,有效产率为68.4%,同时得到含量99%的四氢香芹酮156g,产率为31.2%。如此重复套用6次,催化剂效率没有明显降低。Catalyst reuse: The Cu/Cr catalyst recovered by filtration was flushed to the reaction vessel with 500 g of dihydrocarvone, and the temperature was raised to 160 ° C for about 4 hours. After the GC showed that the reaction was completed, the Cu/Cr catalyst was continuously recovered by filtration, and the filtrate was decompressed. Rectification yielded 342 g of carvacrol with a content of 99.2%, an effective yield of 68.4%, and a yield of 99% of tetrahydrocarvone 156 g, a yield of 31.2%. By repeating this application 6 times, the catalyst efficiency was not significantly lowered.
实施例2Example 2
在1000mL反应釜中加入500g二氢香芹酮和3gCu/Cr催化剂(Cu/Cr摩尔比为5:1),搅拌均匀后升温至180℃反应4.5h,GC显示反应结束后,冷却至室温,过滤回收Cu/Cr催化剂,滤液经过减压精馏得到 纯度99.1%的香芹酚360g,有效产率为72%,同时得到含量99%的四氢香芹酮137g,产率为27.4%。500 g of dihydro carvone and 3 g of Cu/Cr catalyst (5:1 Cu/Cr molar ratio) were added to a 1000 mL reactor. After stirring, the temperature was raised to 180 ° C for 4.5 h. After GC showed that the reaction was completed, it was cooled to room temperature. The Cu/Cr catalyst was recovered by filtration, and the filtrate was subjected to vacuum distillation to obtain 360 g of carotenol having a purity of 99.1%, an effective yield of 72%, and a 137 g of tetrahydrocarvone having a content of 99% was obtained in a yield of 27.4%.
催化剂再利用:将过滤回收的Cu/Cr催化剂用500g二氢香芹酮冲洗至反应釜,升温至180℃反应约4.5h,GC显示反应结束后,过滤继续回收Cu/Cr催化剂,滤液经过减压精馏得到含量99.1%的香芹酚355g,有效产率为71.2%,同时得到含量99%的四氢香芹酮143g,产率为28%。如此重复套用7次,催化剂效率没有明显降低。Catalyst reuse: The Cu/Cr catalyst recovered by filtration was flushed to the reaction vessel with 500 g of dihydrocarvone, and heated to 180 ° C for about 4.5 h. After GC showed that the reaction was over, the Cu/Cr catalyst was recovered by filtration, and the filtrate was reduced. Press distillation was carried out to obtain 355 g of carvacrol having a content of 99.1%, an effective yield of 71.2%, and at the same time, 143 g of tetrahydrocarvone having a content of 99% was obtained in a yield of 28%. When the application was repeated 7 times, the catalyst efficiency was not significantly lowered.
实施例3Example 3
在1000mL反应釜中加入500g二氢香芹酮和5gCu/Cr催化剂(Cu/Cr摩尔比为5:1),搅拌均匀后升温至200℃反应5h,GC显示反应结束后,冷却至室温,过滤回收Cu/Cr催化剂,滤液经过减压精馏得到纯度99.3%的香芹酚375g,有效产率为75%,同时得到含量99.1%的四氢香芹酮123g,产率为24.6%。500 g of dihydro carvone and 5 g of Cu/Cr catalyst (5:1 Cu/Cr molar ratio) were added to a 1000 mL reactor. After stirring, the temperature was raised to 200 ° C for 5 h. After GC showed that the reaction was completed, it was cooled to room temperature and filtered. The Cu/Cr catalyst was recovered, and the filtrate was subjected to vacuum distillation to obtain 375 g of carotenol having a purity of 99.3%, an effective yield of 75%, and a yield of 99.1% of tetrahydrocarvone 123g, a yield of 24.6%.
催化剂再利用:将过滤回收的Cu/Cr催化剂用500g二氢香芹酮冲洗至反应釜,升温至200℃反应约5h,GC显示反应结束后,过滤继续回收Cu/Cr催化剂,滤液经过减压精馏得到含量99.3%的香芹酚372g,有效产率为74.9%,同时得到含量99.1%的四氢香芹酮125g,产率为24.7%。如此重复套用8次,催化剂效率没有明显降低。Recycling of the catalyst: The Cu/Cr catalyst recovered by filtration was flushed to the reaction vessel with 500 g of dihydrocarvone, and the temperature was raised to 200 ° C for about 5 hours. After the GC showed that the reaction was completed, the Cu/Cr catalyst was continuously recovered by filtration, and the filtrate was decompressed. Rectification yielded 372 g of carvacrol with a content of 99.3%, an effective yield of 74.9%, and a yield of 99.1% of tetrahydrocarvone 125 g, a yield of 24.7%. By repeating this application 8 times, the catalyst efficiency was not significantly lowered.

Claims (4)

  1. 一种催化二氢香芹酮异构化合成香芹酚的方法,其特征在于:二氢香芹酮在催化剂Cu/Cr的作用下发生脱氢异构化反应,反应结束后,过滤除去Cu/Cr重复利用,有机相减压精馏,得到香芹酚。A method for catalyzing the isomerization of dihydrocarvone to carvacrol, characterized in that: dihydrocarvone undergoes a dehydroisomerization reaction under the action of a catalyst Cu/Cr, and after the reaction is finished, the Cu is removed by filtration. /Cr is reused, and the organic phase is subjected to vacuum distillation to obtain carvacrol.
  2. 根据权利要求书1所述的一种催化二氢香芹酮异构化合成香芹酚的方法,其特征在于:催化剂Cu/Cr为活性铜负载在铬材料上形成的催化剂,Cu/Cr摩尔比为5:1。A method for synthesizing carvacrol by isomerization of dihydrocarvone according to claim 1, wherein the catalyst Cu/Cr is a catalyst formed by supporting active copper on a chromium material, Cu/Cr mole The ratio is 5:1.
  3. 根据权利要求书1或2所述的一种催化二氢香芹酮异构化合成香芹酚的方法,其特征在于具体制备步骤如下:A method for catalyzing the isomerization of dihydrocarvone to carvacrol according to claim 1 or 2, wherein the specific preparation steps are as follows:
    在反应釜中,分别加入二氢香芹酮和Cu/Cr催化剂,搅拌均匀,升温至160~200℃,反应4~5h,冷却至室温,过滤除去催化剂Cu/Cr回收利用,有机相减压精馏,得到香芹酚。In the reaction vessel, dihydrocarvone and Cu/Cr catalyst were added separately, stirred uniformly, heated to 160-200 ° C, reacted for 4-5 h, cooled to room temperature, filtered to remove catalyst Cu/Cr for recycling, organic phase decompression Rectification to obtain carvacrol.
  4. 根据权利要求3所述的一种催化二氢香芹酮异构化合成香芹酚的方法,其特征在于:二氢香芹酮与活性Cu的质量比为500~1000:2~50。A method for catalyzing the isomerization of dihydrocarvone to carvacrol according to claim 3, wherein the mass ratio of dihydrocarvone to active Cu is from 500 to 1000:2 to 50.
PCT/CN2018/089942 2017-07-28 2018-06-05 Method for synthesizing carvacrol by catalyzing dihydrocarvone isomerization WO2019019808A1 (en)

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