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Chemical synthesis process of antibacterial agent spice carvacrol

A technology of carvacrol and antibacterial agent, applied in the field of chemical synthesis technology of antibacterial agent spice carvacrol, can solve the problems of high transportation storage and price, low final yield, low boiling point and the like

Active Publication Date: 2019-06-07
亿如科技(北京)有限公司 +1
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  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

Chinese invention patent CN 1488615A also introduces a method for producing carvacrol by condensation reaction with 2-chloropropane using o-cresol as raw material and anhydrous aluminum trichloride as a catalyst. However, there are alkylation materials 2 in the above method - Chloropropane is highly toxic, has low boiling point, is difficult to transport and store, and has high prices.
[0004] It has been reported to use Zr-Al-SiO 2 The composite catalyst catalyzes the reaction of isopropanol and o-cresol to synthesize carvacrol (Journal of Chemical Technology and Biotechnology, 2009, 84, 1499-1508), but the reaction temperature of this method needs to be 180°C, and the final yield is low, only 73%

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  • Chemical synthesis process of antibacterial agent spice carvacrol

Examples

Experimental program
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Effect test

Embodiment 1

[0021] Measure 500L of dichloromethane and add it to a 1000L reaction kettle with a stirring and cooling device, add 300kg of catalyst anhydrous aluminum trichloride, stir and cool down to -5°C, slowly add 100kg of o-cresol, and wait until the temperature of the reaction system reaches -5°C Finally, 72 kg of isopropanol was added dropwise, and the reaction was completed at -5 °C for 4 h. At room temperature, slowly add the reaction product into a reaction kettle with a stirrer equipped with 1200kg of crushed ice and stir until the ice melts

[0022] The ice was completely melted, left to stand, and the oil layer was separated, and the water layer was washed twice with 150L dichloromethane each time, and the separated oil layer was combined, concentrated at 55°C under normal pressure until no dichloromethane solvent was evaporated, and the fragrant 122.2 kilograms of crude product of cervacrol, carvacrol content 65.6% (HPLC assay). Vacuum distillation of 100 Pa, the fraction a...

Embodiment 2

[0024] Measure 500L of n-hexane and add it to a 1000L reaction kettle with a stirring and cooling device, add 300kg of catalyst anhydrous aluminum trichloride, stir and cool down to -5°C, slowly add 100kg of o-cresol, and wait until the temperature of the reaction system reaches -5°C , add 72kg of isopropanol dropwise, and react at -5 ℃ for 4h to end the reaction. At room temperature, slowly add the reaction product into a reaction kettle with a stirrer equipped with 1200kg of crushed ice and stir until the ice is completely melted, leave it to stand, separate the oil layer, and wash the water layer with 150L of dichloromethane each time for a total of two The second time, the separated oil layers were combined and concentrated under normal pressure at 70°C until no n-hexane (petroleum ether) solvent was evaporated to obtain 121.6 kg of crude carvacrol with a carvacrol content of 65.4% (as determined by HPLC). Vacuum rectification at 100 Pa vacuum degree collected the distilla...

Embodiment 3

[0026] Measure 500L of dichloromethane and add it to a 1000L reaction kettle with a stirring and cooling device, add 300.0kg of catalyst anhydrous ferric chloride, stir and cool down to -5°C, slowly add 100kg of o-cresol, and wait until the temperature of the reaction system reaches - After 5°C, 72kg of isopropanol was added dropwise, and reacted at -5°C for 4 hours to end the reaction. At room temperature, slowly add the reaction product into a reaction kettle with a stirrer equipped with 1200kg of crushed ice and stir until the ice is completely melted, let it stand, separate the oil layer, and wash the water layer with 150L of dichloromethane each time, a total of two The second time, the separated oil layers were combined and concentrated under normal pressure at 55°C until no dichloromethane solvent was evaporated to obtain 121.4 kg of carvacrol crude product with a carvacrol content of 65.4% (as determined by HPLC). Vacuum rectification at 100Pa vacuum degree collected t...

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Abstract

The invention relates to a chemical synthesis process of antibacterial agent carvacrol. According to the synthesis process, o-methylphenol and isopropanol are selected as raw materials and compounds such as dichloromethane and n-hexane (petroleum ether) are reaction solvents, and the carvacrol is prepared through the steps of alkylation reaction, liquid-liquid extraction, normal-pressure concentration, reduced-pressure concentration, reduced-pressure distillation and the like. The synthesis process has the characteristics of simple process, low production cost, high yield, excellent product quality and the like, and is easy for industrialized production.

Description

technical field [0001] The invention relates to a chemical synthesis process of antibacterial agent carvacrol. Background technique [0002] Carvacrol is a phenolic compound with bactericidal effect, which mainly exists in the essential oil of thyme plants in nature. One of the main antibacterial ingredients in products such as natural oregano oil and capsicum oil is carvacrol. Because of its broad-spectrum antibacterial properties, safety, and extremely low residues in animals, it is used in the treatment of dysentery and anti-coccidiosis in chickens, piglets and other animals. [0003] US Patent 2286953 introduces a method for preparing carvacrol by condensation reaction with 2-chloropropane using o-cresol as raw material and anhydrous aluminum trichloride as catalyst. Chinese invention patent CN 1488615A also introduces a method for producing carvacrol by condensation reaction with 2-chloropropane using o-cresol as raw material and anhydrous aluminum trichloride as a ca...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C37/16C07C37/68C07C37/70C07C37/72C07C37/74C07C39/06
Inventor 张聚成汪志强张宁
Owner 亿如科技(北京)有限公司