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152 results about "Methyl acetoacetate" patented technology

Method for preparing butyrate clevidipine

The invention discloses a method for preparing butyrate clevidipine. The method comprises that 2, 3-dichlorobenzaldehyde, acetoacetate propionitrile ester and 3-amino-2-methyl crotonate are mixed and one-pot Hantzsch reaction is conducted, base catalyst is added to remove 2-cyanoethyl to obtain key intermediate, the key intermediate reacts with n-butyric acid chloromethyl ester to obtain butyrate clevidipine crude product, and the crude product is recrystallized to obtain high-purity butyrate clevidipine. Raw material 3-amino-2-methyl crotonate can be prepared by using low-price methyl acetoacetate. Raw material acetoacetate propionitrile ester can be prepared by using diketene. The synthesis of all raw materials requires no chromatographic separation for purification. The intermediate is synthesized through one-pot Hantzsch reaction, the reaction speed is fast, the condition is mild, the technological reliability is high and the purity of the intermediate is high. The conditions for the reaction of the key intermediate and the n-butyric acid chloromethyl ester can be easily controlled, the operation is simple and convenient, the cost is low, the post treatment requires no chromatographic separation for purification, the purity of the obtained butyrate clevidipine is above 99.5 percent and the mass production can be realized.
Owner:SUN YAT SEN UNIV +1

4-methoxy methyl acetoacetate preparation method

The invention discloses a 4-methoxy methyl acetoacetate preparation method. The 4-methoxy methyl acetoacetate preparation method comprises the following steps of adding a solvent tetrahydrofuran into a reaction kettle and leading inert gas into the reaction kettle, setting the internal temperature of the reaction kettle to be 15 DEG C to 25 DEG C, adding industrial sodium hydride and a metal alkaline compound in a stirring state, then adding the solvent tetrahydrofuran, dropwise adding mixed liquid of methyl alcohol and methyl-4-chloroacetoacetate at the temperature of lower than 20 DEG C to perform reaction for 4-6 hours, rising the temperature to be 20 DEG C to 25 DEG C to continue to react for 4-15 hours, reducing the system temperature to be 6 DEG C to 10 DEG C after TLC detection reaction is completed, adding a hydrochloric acid solution with molar concentration of 2 mol / L to regulate the pH of a system to be 5 to 7, performing standing and laying, concentrating and spin-drying upper-layer liquid to remove the solvent tetrahydrofuran after liquid separation and then obtaining a colorless product 4-methoxy methyl acetoacetate through wiped-film molecular distillation. The 4-methoxy methyl acetoacetate can react at room temperature, a product can be produced at low temperature through distillation, and dangerousness in the production process and product impurity content can be directly and effectively reduced.
Owner:ZHONGSHAN NIKEMEI PHARMA

Preparation method of felodipine synthetic intermediate methyl 2-(2,3-dichlorobenzylidine)acetoacetate

The invention discloses a preparation method of methyl 2-(2,3-dichlorobenzylidine)acetoacetate which is a synthetic intermediate of antihypertensive drug felodipine. The method is characterized by allowing a condensation reaction between 2, 3-dichlorobenzaldehyde and methyl acetoacetate in alcohol solution under the catalytic action of a novel combined catalyst consisting of secondary amine and quinoline carboxylic acid. Reaction liquid is cooled at room temperature for crystallization, filtered, washed and dried after the condensation reaction to obtain primary eluent of the intermediate methyl 2-(2,3-dichlorobenzylidine)acetoacetate with purity not less than 98%. Mother liquor is subject to vacuum condensation, cooling crystallization, filtering and recrystallization to obtain secondary eluent product of the intermediate methyl 2-(2,3-dichlorobenzylidine)acetoacetate with purity not less than 98%. Compared with the prior art, the new method helps enhance synthetic yield of the felodipine intermediate, and provide ideal intermediate purity. The method is also applicable to preparing other 4-sustituted-1,4-dihydropyridine antihypertensive drug intermediates with chemical structure and pharmaceutical and clinical actions similar to those of felodipine.
Owner:HEFEI LIFEON PHARMA

Production method of phenolic foam without formaldehyde release

The invention relates to a production method of phenolic foam without formaldehyde release, which adopts the following raw materials and the steps of: (1) preparing for phenol, industrial paraformaldehyde, sodium hydroxide, hydrogen peroxide, methyl acetoacetate and water; (2) adding the phenol, the sodium hydroxide and the water into a reaction kettle, heating up and adding the industrial paraformaldehyde; (3) performing vacuum dehydration; (4) adding the hydrogen peroxide and the methyl acetoacetate, and stirring; (5) taking thermosetting phenolic resin obtained in the step (4), H-330 organic silicon and petroleum ether and stirring; and (6) adding p-toluenesulfonic acid, phosphoric acid and the water, stirring and foaming to obtain the phenolic foam. According to the production method disclosed by the invention, acid is not required to be added for regulating PH value, so that operation process is simplified and economic benefits are significant. Furthermore, compared with the traditional phenolic foam, the phenolic foam has the advantages of obviously reducing the content of free formaldehyde, and avoiding the formaldehyde release during the use, and can be widely applied to the fields including air pipes of central air conditioners, heat insulation of interior walls, heat insulation of clean rooms and other places with high requirements on environmental protection.
Owner:湖南中野高科技特种材料有限公司

Process of continuously producing methyl acetoacetate

The invention discloses a process of continuously producing methyl acetoacetate and relates to the technical field of production of chemical raw materials. The production process comprises the following steps of firstly, welding a separation board at the middle of an esterification reactor for separating the esterification reactor into a cooling bin and an insulating bin; secondly, adding a methyl acetoacetate finished product into the esterification reactor to serve as a bottom material in the reactor, and meanwhile, simultaneously dropping DK and methanol into the cooling bin; thirdly, realizing water cooling and air cooling in the cooling bin; after the cooling bin is cooled, realizing pressurization; after pressurization, enabling a product to overflow to the inside of the insulating bin through an overflow pipe; during overflowing, adding diketene on the overflow pipe; fourthly, when the product in the insulation bin reaches a certain amount, transferring the methyl acetoacetate to the inside of a rectifying tower through a transfer pump; fifthly, vacuumizing the inside of the rectifying tower for exhausting air, and meanwhile, inputting nitrogen, and rectifying the methyl acetoacetate in a reflux state to obtain a final product at the moment. According to the process disclosed by the invention, quick production can be realized, the finished product output is improved, the accuracy in control is realized, and the time and the cost are saved.
Owner:JIANGSU TIANCHENG BIOCHEM PROD

Method for preparing methyl acetoacetate

The invention discloses a method for preparing methyl acetoacetate. The method comprises the following steps: adding a catalyst once, continuously adding ketene dimer and a methanol solution through a raw material feeding hole, continuously adding an extraction agent through an extraction agent feeding hole, simultaneously adding two materials into a reaction-extraction rectifying tower, and starting heating; carrying out total reflux so as to obtain the methanol solution through the tower top of the reaction-extraction rectifying tower and obtain a mixed liquid of the methyl acetoacetate, the catalyst and the extraction agent through the tower bottom of the reaction-extraction rectifying tower, and enabling the mixed liquid to flow into a decompression extraction tower from a tower-bottom discharging hole, so as to obtain a target product, namely the methyl acetoacetate from the tower top of the decompression extraction tower. Due to the arrangement of the reaction-extraction rectifying tower and the decompression extraction tower, the methyl acetoacetate is prepared by virtue of a reaction-rectification and extraction-separation integrated reaction, the materials are fed once, and the catalyst and the extraction agent can be recycled, so that the operation is simple, the cost is lowered, the purity and rate of the prepared methyl acetoacetate are high, and the energy consumption is reduced.
Owner:NANJING NORMAL UNIVERSITY
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