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Method for preparing linezolid crystal form I

A technology of linezolid and crystal form, which is applied in the field of producing linezolid crystal form I with high crystal purity and chemical purity, and can solve the problems of low crystal form purity and unstable process of linezolid crystal form I

Inactive Publication Date: 2014-07-02
SHANGHAI ACEBRIGHT PHARMA GRP +1
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Among them, linezolid crystal form I was prepared by suspending crystals in water at high temperature. Since the solubility of linezolid in water varies greatly with temperature, the solubility is larger at high temperature and lower at low temperature, and it will be more stable during the cooling process. The crystal form II is precipitated, resulting in the rapid conversion of the crystal form I to the crystal form II at a lower temperature. The process for preparing the linezolid crystal form I is unstable, and the purity of the crystal form is not high.

Method used

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  • Method for preparing linezolid crystal form I
  • Method for preparing linezolid crystal form I
  • Method for preparing linezolid crystal form I

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preparation example Construction

[0050]The present invention provides a method for preparing linezolid crystal form I, wherein the crude product of linezolid used in the present invention may be a crude product containing linezolid crystal form II, said linezolid containing crystal form II The crude product can be prepared by any known method in the art (for example WO02085849A2), and the crude product with the content of linezolid crystal form II ≥ 75% (preferably 75-98%) can also be used.

[0051] Preferably, the preparation method of the linezolid crystal form I comprises the steps of:

[0052] (1) Mix the crude product of linezolid with the first solvent, filter, and collect the filtrate;

[0053] Preferably, the step (1) is: after mixing the crude product of linezolid with the first solvent, stirring at 85-105° C. until the crude product is dissolved, then filtering while hot, and collecting the filtrate.

[0054] Wherein, the weight-to-volume ratio of the crude linezolid to the first solvent is 1:15-1:...

Embodiment 1

[0072] Weigh 20g of linezolid crystal form II (crude product, the crystal form II content is about 82%) and 700ml of DMF-toluene (w / w=10:90) mixed solvent, add it to a 2000ml three-necked flask, the temperature of the solution in the flask A DF-101S collector type constant temperature magnetic stirrer is used for program temperature control (internal temperature is controlled at 95-100°C), and mechanical stirring is used for thorough mixing until the solute is dissolved;

[0073] The solution was filtered while hot and the resulting clear filtrate was transferred to a flask. Adjust the mechanical stirrer so that its stirring rate is 300rpm / min;

[0074] Start the feeding device, dropwise add 560ml of heptane at a rate of 0.6ml / min, after the dropwise addition of heptane is completed, grow the crystal for 10min, slowly cool down to 3-5°C, and continue stirring for 1h in this temperature range;

[0075] The crystal slurry was filtered, and the filter cake was washed with 3×5 mL...

Embodiment 2

[0080] Weigh 18g of linezolid crystal form II (crude product, the content of crystal form II is about 80%) and 540ml of DMF-toluene (w / w=15:85) mixed solvent, add it to a 2000ml three-necked flask, the temperature of the solution in the flask A DF-101S collector type constant temperature magnetic stirrer is used for program temperature control (internal temperature is controlled at 98-102°C), and mechanical stirring is used for thorough mixing until the solute is completely dissolved;

[0081] The solution was filtered while hot and the resulting clear filtrate was transferred to a flask. Adjust the mechanical stirrer so that the stirring rate is 300 rpm / min, and add 0.95 g of seed crystals whose particle size range is 63-75 μm;

[0082] Start the feeding device, add the second solvent heptane 540ml heptane dropwise at a rate of 0.8ml / min, grow the crystal for 10min, slowly cool down to 3-5°C, and continue stirring for 1h in this temperature range;

[0083] The crystal slurry...

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Abstract

The invention discloses a method for preparing a linezolid crystal form I. Particularly, the preparation method comprises the following steps: (1) mixing a linezolid coarse product and a first solvent, filtering and collecting filtrate; (2) adding a second solvent into the filtrate in the step (1) to separate crystal; and (3) separating the separated crystal to obtain the linezolid crystal form I. The method is simple in process, and is advantageous to large-scale production; and the prepared linezolid crystal form I has the advantages of high purity, good stability, good fluidity, small static electricity, good dissolubility and the like.

Description

technical field [0001] The invention belongs to the technical field of separation and purification. Specifically, the present invention relates to a method for producing linezolid crystal form I with high crystalline purity and chemical purity by subjecting a crude linezolid product to a dissolution crystallization method. Background technique [0002] Linezolid, molecular formula: C 16 h 20 FN 3 o 4 , molecular weight: 337.35, CAS number: 165800-03-3, chemical name (S)-5-(acetamidomethyl)-3-[(3-fluoro-4-morpholinyl)phenyl]-1, 3-oxazolidin-2-one, its molecular structure formula is as follows: [0003] [0004] Linezolid was developed by the Upjohn Company of the United States. It was approved by the FDA for marketing in April 2000, and then produced and marketed by Pfizer. It is used to treat infections caused by Gram-positive cocci, including those caused by methicillin-resistant ( Suspected or confirmed hospital-acquired pneumonia (HAP), community-acquired pneumon...

Claims

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Application Information

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IPC IPC(8): C07D263/20
CPCC07D263/20
Inventor 安晓霞李祯张袁伟祖远远
Owner SHANGHAI ACEBRIGHT PHARMA GRP