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Method for preparing metacresol via alkaline hydrolysis of o-chlorotoluene

A technology of o-chlorotoluene and cresol, which is applied in the field of preparing m-cresol by alkaline hydrolysis of o-chlorotoluene, can solve the problems of low m-cresol content and multiple by-products, and achieve simple post-processing, low production cost, and environmental protection Effect

Inactive Publication Date: 2014-02-05
SHANDONG NORMAL UNIV
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

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Problems solved by technology

[0012] O-chlorotoluene can be hydrolyzed in aqueous solution of sodium hydroxide to prepare m-cresol. The optimized process is: the ratio of the amount of feed material n (sodium hydroxide): n (o-chlorotoluene) = 2.5: 1, and the concentration of alkali is 20 %, the temperature is 350°C, the reaction time is 1h, and the pressure is 1.6Mpa. This synthesis method has abundant sources of raw materials, but the content of m-cresol is not high, and there are many by-products

Method used

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Embodiment 1

[0028] In a 1L autoclave, 112g potassium hydroxide, 56g calcium oxide, 175mL (1.5mol) o-chlorotoluene, 300mL pyridine were added, the reaction temperature was 200°C, and the constant pressure 1.5MPa was reacted for 20h. Cool to room temperature, take out the reactant in the kettle and filter, collect the solid and filtrate separately, and recover the filtrate directly for the next batch reaction. The solid was dissolved in water, fully dissolved, filtered, washed with water, collected the aqueous solution, adjusted to pH 3 with 15% hydrochloric acid, extracted twice with 100 mL of toluene, dried and distilled to remove the solvent to obtain 62.0 g of crude product. Then 62.0g of the crude product was passed through 200 mesh silica gel, using petroleum ether 60-90 as the eluent, and subjected to silica gel column chromatography to obtain 37.8g of pure m-cresol product, with a yield of 35.0% (calculated as potassium hydroxide), a by-product 19.9g of o-cresol. See the proton nucl...

Embodiment 2

[0030] In a 1L autoclave, add 299.9 g of cesium hydroxide after dewatering, 56 g of calcium oxide, 175 mL (1.5 mol) of o-chlorotoluene, and 250 mL of pyridine. The reaction temperature is 120° C. and the constant pressure is 2.0 MPa for 24 hours. Cool to room temperature, take out the reactant in the kettle and filter, collect the solid and filtrate separately, and recover the filtrate directly for the next batch reaction. The solid was dissolved in water, fully dissolved, filtered, washed with water, and the aqueous solution was collected, adjusted to pH 5 with 5% hydrochloric acid, and extracted twice with 100 mL of toluene. After drying, the solvent was distilled off to obtain 46.3 g of crude product. Then 46.3g of the crude product was passed through 300 mesh silica gel, using petroleum ether 60-90 as the eluent, and subjected to silica gel column chromatography. After silica gel column chromatography, 28.8 g of pure m-cresol product was obtained, and the yield was 26.7% (wi...

Embodiment 3

[0032] In a 1 L autoclave, add 80 g of sodium hydroxide, 56 g of calcium oxide, 175 mL (1.5 mol) of o-chlorotoluene, and 250 mL of 4,4'-bipyridine. The reaction temperature is 220° C. and the constant pressure is 2.5 MPa for 18 hours. Cool to room temperature, take out the reactant in the kettle and filter, collect the solid and filtrate separately, and recover the filtrate directly for the next batch reaction. The solid was dissolved in water, fully dissolved, filtered, washed with water, collected the aqueous solution, adjusted to pH 4 with 10% hydrochloric acid, extracted twice with 100 mL of toluene, dried and distilled to remove the solvent to obtain 38.9 g of crude product. Then 38.9g crude product was passed through 150 mesh silica gel, using petroleum ether 60-90 as the eluent, and silica gel column chromatography was used to obtain 22.7g pure m-cresol product, with a yield of 21.0% (calculated as sodium hydroxide), a by-product 12.3 g of o-cresol.

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Abstract

The invention discloses a method for preparing metacresol via alkaline hydrolysis of o-chlorotoluene. The method comprises the following steps: adding o-chlorotoluene, an alkali metal hydroxide and calcium oxide which are taken as raw materials and an alkaline aprotic organic solvent which is taken as a solvent into a pressure kettle under the conditions that the molar ratio of the alkali metal hydroxide to o-chlorotoluene to calcium oxide to the alkaline aprotic organic solvent is 1:0.5:0.5:2-1:3:1:10, the reaction pressure is within 0 to 2.5MPa, the reaction temperature is within 100 DEG C to 220 DEG C and the reaction time is within 10 to 24 hours; then performing an acidification reaction so as to obtain a crude product; leading the crude product to pass through 200 to 300 meshes of silica gel and performing silica gel column chromatography separation by taking 60 to 90 parts of petroleum ether as a leaching liquid, thereby obtaining pure metacresol. The method has the beneficial effects that the synthesis process is simple; the cost of the raw materials is low; the solvent and o-chlorotoluene can be recycled after being simply filtered, so that the aftertreatment is simple and the production cost is low, thereby being favorable for environmental protection. The yield of metacresol reaches 20% to 35% under the process conditions while o-cresol is obtained as a byproduct; the ratio of metacresol to o-cresol is (1.8-2.1):1.

Description

Technical field [0001] The invention relates to the production field of chemical raw material intermediates, in particular to a method for preparing m-cresol by alkaline hydrolysis of o-chlorotoluene. Background technique [0002] Meta-cresol is an important fine chemical raw material intermediate, mainly used in the synthesis of pesticides, medicines, antioxidants, spices, etc., and is an important raw material for the synthesis of vitamin E. At present, the main production processes of m-cresol at home and abroad are: [0003] 1. Separation method [0004] It is obtained by fractional distillation from coal tar or petroleum products. This method has limited resources, complicated technological process and separation equipment, which is far from meeting the needs of the product and the final product is a mixture of multiple cresols, which requires special separation to obtain pure m-methyl phenol [0005] 2. Toluene chlorination hydrolysis method [0006] The toluene benzene ring is...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C39/07C07C37/02
CPCC07C37/02C07C39/07
Inventor 石志强郭伟伟王永霞位燕红张安东
Owner SHANDONG NORMAL UNIV