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CN106008555A - Cefdinir synthesizing technology - Google Patents

Cefdinir synthesizing technology Download PDF

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Publication number
CN106008555A
CN106008555A CN201610548324.8A CN201610548324A CN106008555A CN 106008555 A CN106008555 A CN 106008555A CN 201610548324 A CN201610548324 A CN 201610548324A CN 106008555 A CN106008555 A CN 106008555A
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CN
China
Prior art keywords
cefdinir
acid
synthesis technique
stirring
retort
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CN201610548324.8A
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Chinese (zh)
Inventor
张齐
王臣
何欢欢
谢春雷
张文伯
赵君彦
鲁红红
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TIANJIN PHARMACEUTICAL GROUP GENCOM PHARMACEUTICAL CO Ltd
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TIANJIN PHARMACEUTICAL GROUP GENCOM PHARMACEUTICAL CO Ltd
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Priority to CN201610548324.8A priority Critical patent/CN106008555A/en
Publication of CN106008555A publication Critical patent/CN106008555A/en
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D501/00Heterocyclic compounds containing 5-thia-1-azabicyclo [4.2.0] octane ring systems, i.e. compounds containing a ring system of the formula:, e.g. cephalosporins; Such ring systems being further condensed, e.g. 2,3-condensed with an oxygen-, nitrogen- or sulfur-containing hetero ring
    • C07D501/14Compounds having a nitrogen atom directly attached in position 7
    • C07D501/16Compounds having a nitrogen atom directly attached in position 7 with a double bond between positions 2 and 3
    • C07D501/207-Acylaminocephalosporanic or substituted 7-acylaminocephalosporanic acids in which the acyl radicals are derived from carboxylic acids
    • C07D501/227-Acylaminocephalosporanic or substituted 7-acylaminocephalosporanic acids in which the acyl radicals are derived from carboxylic acids with radicals containing only hydrogen and carbon atoms, attached in position 3
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D501/00Heterocyclic compounds containing 5-thia-1-azabicyclo [4.2.0] octane ring systems, i.e. compounds containing a ring system of the formula:, e.g. cephalosporins; Such ring systems being further condensed, e.g. 2,3-condensed with an oxygen-, nitrogen- or sulfur-containing hetero ring
    • C07D501/02Preparation
    • C07D501/04Preparation from compounds already containing the ring or condensed ring systems, e.g. by dehydrogenation of the ring, by introduction, elimination or modification of substituents
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D501/00Heterocyclic compounds containing 5-thia-1-azabicyclo [4.2.0] octane ring systems, i.e. compounds containing a ring system of the formula:, e.g. cephalosporins; Such ring systems being further condensed, e.g. 2,3-condensed with an oxygen-, nitrogen- or sulfur-containing hetero ring
    • C07D501/02Preparation
    • C07D501/12Separation; Purification

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Cephalosporin Compounds (AREA)

Abstract

The invention provides a cefdinir synthesizing technology. The technology comprises the steps that (Z)-2-(2-aminothiazole-4-yl)-2-acetoxyl imino thioacetic acid(S-2-benzothiazole)ester and 7-amino-3-vinyl-8-oxo-5-thia-1-azabicyalo[4.2.0]oct-2-alkene-2-carboxylic acid are subjected to condensation; acetyl protection is removed through hydrolysis, and a cefdinir finished product is finally obtained. The method for preparing the cefdinir has the advantages of being short in production cycle, high in yield, high in product quality and suitable for industrial production.

Description

Cefdinir synthesis technique
Technical field
The present invention relates to field of medicaments, particularly relate to the new production process of a kind of cefdinir, it is ensured that produce low one-tenth Originally, high-quality cefdinir crude drug.
Background technology
Cefdinir (Cefdinir) is that the third generation is administered orally cephalosporins, and chemistry is entitled: (6R, 7R)-7-[(Z)-2- (2-amino-4-thiazolyl)-2-hydroxyl imide base acetylamino]-8-oxo-3-vinyl-5-thia-1-azabicyclo [4.2.0] oct-2-ene-2-carboxylic acid.Its chemical constitution feature is to introduce hydroxyl Asia on 7 side chains of 7-amino-cephalosporanic acid skeleton Amido, 3 side chains introduce vinyl.Not only maintain the antibacterial efficacy of Gram-negative coccus, but also enhance existing During oral cephalosporins, the effect of gram-positive cocci, the particularly antibacterial efficacy to staphylococcus, can suppress The clinical isolates of 90%~100%.Clinic is primarily adapted for use in acute episode of chronic bronchitis, bacterial pneumonia, upper breathing The treatment of road infection, skin and soft tissue infection etc..Its chemical structural formula is as follows:
The production technology of traditional cefdinir is: with (Z)-2-(thiazolamine-4-base)-2-triphen methoxyimino Thiacetic acid. (S-2-benzothiazole) ester (i.e. cefdinir side-chain acid active ester) and 7-amino-3-vinyl-8-oxo-5-sulfur Miscellaneous-1-azabicyclo [4.2.0] oct-2-ene-2-carboxylic acid (i.e. 7-AVCA) is condensed, then sloughs protection group and obtain cefdinir Finished product.
Its synthesis route is as follows:
Condensation operation:
Deprotection operation (i.e. hydrolyzes, refines):
(i) condensation operation:
7-AVCA, cefdinir side-chain acid active ester are put in retort, is slowly added dropwise into triethylamine with stirring; After waiting to drip, stir and all dissolve to material, be incubated;In reactant liquor, add quantitative ethyl acetate, add activated carbon mistake Filter;Add p-methyl benzenesulfonic acid, rejection filter.
(ii) hydrolyzing process:
Dropping formic acid, insulation reaction;After insulation reaction terminates, temperature is down to 5~6 DEG C;And prepare in 5~6 DEG C of additions Sodium bicarbonate aqueous solution, finish, in 5~6 DEG C of insulation reaction 1 hour;Add activated carbon appropriate, filter to being layered tank, start Layering;After feed liquid remove impurity, cross to purifying area.
(iii) refining step:
Filter is finished, and adds dilute hydrochloric acid acid and makes its crystallize, obtains cefdinir finished product.
Using traditional synthesis technique, its production cycle is long, and yield is relatively low, though through purification step, but its finished product purity The defect such as the most relatively low.This application provides a kind of new cefdinir synthesis technique, it effectively prevent above-mentioned tradition preparation work The defect of skill, is more suitable for industrialized production.
Summary of the invention
The purpose of the present invention, is to provide a kind of new cefdinir synthesis technique, and its route map is as follows:
Specifically include following steps:
Condensation operation: with (Z)-2-(thiazolamine-4-base)-2-acetyl oxyimino group thiacetic acid. (S-2-benzo thiophene Azoles) ester (i.e. cefdinir side-chain acid active ester) and 7-amino-3-vinyl-8-oxo-5-thia-1-azabicyclo [4.2.0] oct-2-ene-2-carboxylic acid (i.e. 7-AVCA) is condensed;
Hydrolyzing process: through hydrolysis deacetylate protection, and generate potassium salt of cefdinir;
Refining step: potassium salt of cefdinir, through acid treatment, crystallize, obtains cefdinir finished product.
Wherein, described
Condensation operation: 7-AVCA, cefdinir side-chain acid active ester, organic solvent A are put in retort, in stirring Under be slowly added dropwise into alkali liquor;After waiting to drip, stirring to material is all dissolved;Residual≤0.5% of sampling detection 7-AVCA Time, in reactant liquor, adding quantitative organic solvent B, stirring layering, the organic layer separated discards, and water layer is waited to hydrolyze.
Hydrolyzing process: add wet chemical in water layer, adjust pH=7-9, with stirring clock reaction 30 minutes; Reaction puts into potassium acetate after terminating, rejection filter of lowering the temperature, and obtains potassium salt of cefdinir.
Refining step: dissolve in potassium salt of cefdinir is put into purified water, adds acid and makes its crystallize, obtain cefdinir Finished product.
Preferably, described
Condensation operation:
(1) in retort, 30-50Kg 7-AVCA, 70-100Kg active ester, 300-500Kg oxolane, 100-are put into 300Kg water, stirring is cooled to 0-50 DEG C
(2) dropping alkali liquor 18-36Kg
(3) drip finish, clock reaction
(4) complete molten time add 0.4KgEDTA, sampling detection, during 7-AVCA≤0.5 reaction terminate
(5) add dichloromethane 500-700Kg stirring 5min, the 100-300Kg that adds water and stir 5min, layering.Water layer is used 331.5Kg*2 dichloromethane is washed twice, and combined dichloromethane layer 130Kg washes, and combining water layer puts into retort, adds EDTA 0.4Kg, is cooled to 0-50 DEG C, and water layer is waited to hydrolyze.
Hydrolyzing process:
(6) dropping solution of potassium carbonate, adjusts pH=7-9
(7) clock reaction 30min
(8) add potassium acetate 50-100Kg, after being cooled to 0 DEG C, stir 10min
(9) filter, with 40Kg acetone drip washing, drain, obtain potassium salt of cefdinir.
Refining step:
(10) filter cake puts into retort, adds 2200Kg water, is warming up to 30-60 DEG C
(11) add charcoal 12Kg, EDTA 1Kg, stir 30min
(12) filtering, wash filter cake with 300Kg, filtrate puts into retort, intensification 30-60 DEG C
(13) dropping acid solution, adjusts pH to 1.5-2.5, stirs 1h, and repetition measurement pH is constant
(14) filter, wash filter cake with 200Kg, then use 60Kg ethanol rinse, drain
(15) placing, is dried, obtains cefdinir finished product.
It is furthermore preferred that it is described
In condensation operation, organic solvent A is oxolane or ethyl acetate;Alkali liquor is triethylamine, ammonia or sodium hydroxide Solution;Organic solvent B is dichloromethane or ethyl acetate;
In refining step, acid solution is sulphuric acid, hydrochloric acid, glacial acetic acid etc..
The application new technology, compared with traditional handicraft, has the advantage that
1, the application new technology relatively traditional handicraft simplifies operation, improves production capacity.Condensation is merged with hydrolysis, in Between without separating condensed product, be directly produced out potassium salt of cefdinir, the quality of monitoring potassium salt of cefdinir, for the number of this product Foundation is provided according to analysis.The potassium salt of cefdinir of output, it is not necessary to be dried and can carry out deprotection reaction, reduce production process In energy consumption.Producing traditional handicraft cefdinir product needed and pass through condensation, deprotection operation, its production cycle is 5 days.Utilize The production cycle of the cefdinir product that the application new technology produces shortens to 4 days.Production in the condensation of cefdinir new technology During, also have adjusted the feed way of triethylamine, " triethylamine is slowly added to a part, and detects anti-by traditional handicraft Answer terminal, without reaching reaction end, the most again add ", be adjusted to new technology " calculates condensation reaction triethylamine Consumption, puts into quantitative triethylamine, timing reaction, finally detects the terminal that feeds intake ".The mode being relatively interrupted input triethylamine is saved In the response time, it is simple to operation, it is more suitable for industrialized production.
2, reduce cost, decrease the use of raw material.Formic acid in the production of new technology cefdinir not in use by, carry High this product safety in process of production.The building-up process of new technology cefdinir is compared with the raw material inventory of traditional handicraft Decrease 20%.Use purified water as solvent in deprotection reaction, decrease cefdinir finished product right in Crystallization Process The parcel of solvent, it is to avoid the risk that this product dissolvent residual in finished product detection is too high.
3, improve the quality of finished product.The content of conventionally produced cefdinir product, about 98%, utilizes new The content of the cefdinir product that technique produces can reach more than 99%.In the subtractive process of cefdinir product, crystallization System is purified water, it is to avoid the appearance of the problem such as solvent residual in finished product crystallizes.By increasing the usage amount of EDTA, significantly Avoid the metal impact on material in course of reaction.
Detailed description of the invention
Below in conjunction with specific embodiment, the invention will be further described, but does not limit protection scope of the present invention.
The synthesis of embodiment 1 cefdinir
Condensation operation:
(1) in retort, 30Kg 7-AVCA is put into, 80Kg active ester, 300Kg oxolane, 200Kg water, stirring fall Temperature is to 0-50 DEG C
(2) dropping triethylamine 24Kg
(3) drip finish, clock reaction
(4) complete molten time add 0.4Kg EDTA, sampling detection, during 7-AVCA≤0.5 reaction terminate
(5) add dichloromethane 700Kg stirring 5min, the 200Kg that adds water and stir 5min, layering.Water layer 331.5Kg*2 bis- Chloromethanes is washed twice, and combined dichloromethane layer 130Kg washes, and combining water layer puts into retort, adds EDTA 0.4Kg, fall Temperature is to 0-50 DEG C, and water layer is waited to hydrolyze.
Hydrolyzing process:
(6) dropping solution of potassium carbonate, adjusts pH=8
(7) clock reaction 30min
(8) add potassium acetate 50Kg, after being cooled to 0 DEG C, stir 10min
(9) filter, with 40Kg acetone drip washing, drain, obtain potassium salt of cefdinir.
Refining step:
(10) filter cake puts into retort, adds 2200Kg water, is warming up to 30-60 DEG C
(11) add charcoal 12Kg, EDTA 1Kg, stir 30min
(12) filtering, wash filter cake with 300Kg, filtrate puts into retort, intensification 30-60 DEG C
(13) dripping 5% sulphuric acid, adjust pH to 1.5, stir 1h, repetition measurement pH is constant
(14) filter, wash filter cake with 200Kg, then use 60Kg ethanol rinse, drain
(15) placing, is dried, obtains cefdinir finished product, total recovery 75%.
The synthesis of embodiment 2 cefdinir
Condensation operation:
(1) in retort, 40Kg 7-AVCA is put into, 90Kg active ester, 400Kg oxolane, 100Kg water, stirring fall Temperature is to 0-50 DEG C
(2) dropping ammonia 36Kg
(3) drip finish, clock reaction
(4) complete molten time add 0.4Kg EDTA, sampling detection, during 7-AVCA≤0.5 reaction terminate
(5) add dichloromethane 600Kg stirring 5min, the 200Kg that adds water and stir 5min, layering.Water layer 331.5Kg*2 bis- Chloromethanes is washed twice, and combined dichloromethane layer 130Kg washes, and combining water layer puts into retort, adds EDTA 0.4Kg, fall Temperature is to 0-50 DEG C, and water layer is waited to hydrolyze.
Hydrolyzing process:
(6) dropping solution of potassium carbonate, adjusts pH=7
(7) clock reaction 30min
(8) add potassium acetate 70Kg, after being cooled to 0 DEG C, stir 10min
(9) filter, with 40Kg acetone drip washing, drain, obtain potassium salt of cefdinir.
Refining step:
(10) filter cake puts into 3L four-hole bottle, adds 2200Kg water, is warming up to 30-60 DEG C
(11) add charcoal 12Kg, EDTA 1Kg, stir 30min
(12) filtering, wash filter cake with 300Kg, filtrate puts into 3L four-hole bottle, intensification 30-60 DEG C
(13) dripping 5% sulphuric acid, adjust pH to 2, stir 1h, repetition measurement pH is constant
(14) filter, wash filter cake with 200Kg, then use 60Kg ethanol rinse, drain
(15) placing, is dried, obtains cefdinir finished product, total recovery 77%.
The synthesis of embodiment 3 cefdinir
Condensation operation:
(1) in retort, 50Kg 7-AVCA is put into, 70Kg active ester, 500Kg oxolane, 300Kg water, stirring fall Temperature is to 0-50 DEG C
(2) dropping sodium hydroxide solution 24Kg
(3) drip finish, clock reaction
(4) complete molten time add 0.4Kg EDTA, sampling detection, during 7-AVCA≤0.5 reaction terminate
(5) add dichloromethane 500Kg stirring 5min, the 200Kg that adds water and stir 5min, layering.Water layer 331.5Kg*2 bis- Chloromethanes is washed twice, and combined dichloromethane layer 130Kg washes, and combining water layer puts into retort, adds EDTA 0.4Kg, fall Temperature is to 0-50 DEG C, and water layer is waited to hydrolyze.
Hydrolyzing process:
(6) dropping solution of potassium carbonate, adjusts PH=9
(7) clock reaction 30min
(8) add potassium acetate 100Kg, after being cooled to 0 DEG C, stir 10min
(9) filter, with 40Kg acetone drip washing, drain, obtain potassium salt of cefdinir.
Refining step:
(10) filter cake puts into 3L four-hole bottle, adds 2200Kg water, is warming up to 30-60 DEG C
(11) add charcoal 12Kg, EDTA 1Kg, stir 30min
(12) filtering, wash filter cake with 300Kg, filtrate puts into 3L four-hole bottle, intensification 30-60 DEG C
(13) dripping 5% sulphuric acid, adjust pH to 2.5, stir 1h, repetition measurement pH is constant
(14) filter, wash filter cake with 200Kg, then use 60Kg ethanol rinse, drain
(15) placing, is dried, obtains cefdinir finished product, total recovery 78%.
The synthesis of embodiment 4 cefdinir
Condensation operation:
(1) in retort, 45Kg 7-AVCA is put into, 100Kg active ester, 450Kg oxolane, 300Kg water, stirring fall Temperature is to 0-50 DEG C
(2) dropping triethylamine solution 30Kg
(3) drip finish, clock reaction
(4) complete molten time add 0.4Kg EDTA, sampling detection, during 7-AVCA≤0.5 reaction terminate
(5) add dichloromethane 600Kg stirring 5min, the 300Kg that adds water and stir 5min, layering.Water layer 331.5Kg*2 second Acetoacetic ester is washed twice, and combined ethyl acetate layer 130Kg washes, and combining water layer puts into retort, adds EDTA 0.4Kg, fall Temperature is to 0-50 DEG C, and water layer is waited to hydrolyze.
Hydrolyzing process:
(6) dropping solution of potassium carbonate, adjusts PH=8.5
(7) clock reaction 30min
(8) add potassium acetate 90Kg, after being cooled to 0 DEG C, stir 10min
(9) filter, with 40Kg acetone drip washing, drain, obtain potassium salt of cefdinir.
Refining step:
(10) filter cake puts into 3L four-hole bottle, adds 2200Kg water, is warming up to 30-60 DEG C
(11) add charcoal 12Kg, EDTA 1Kg, stir 30min
(12) filtering, wash filter cake with 300Kg, filtrate puts into 3L four-hole bottle, intensification 30-60 DEG C
(13) dripping 5% sulphuric acid, adjust pH to 2.5, stir 1h, repetition measurement pH is constant
(14) filter, wash filter cake with 200Kg, then use 60Kg ethanol rinse, drain
(15) placing, is dried, obtains cefdinir finished product, total recovery 80%.
The synthesis of embodiment 5 cefdinir
Condensation operation:
(1) in retort, 35Kg 7-AVCA is put into, 75Kg active ester, 400Kg ethyl acetate, 300Kg water, stirring fall Temperature is to 0-50 DEG C
(2) dropping ammonia 18Kg
(3) drip finish, clock reaction
(4) complete molten time add 0.4Kg EDTA, sampling detection, during 7-AVCA≤0.5 reaction terminate
(5) add dichloromethane 600Kg stirring 5min, the 100Kg that adds water and stir 5min, layering.Water layer 331.5Kg*2 bis- Chloromethanes is washed twice, and combined dichloromethane layer 130Kg washes, and combining water layer puts into retort, adds EDTA 0.4Kg, fall Temperature is to 0-50 DEG C, and water layer is waited to hydrolyze.
Hydrolyzing process:
(6) dropping solution of potassium carbonate, adjusts PH=8
(7) clock reaction 30min
(8) add potassium acetate 90Kg, after being cooled to 0 DEG C, stir 10min
(9) filter, with 40Kg acetone drip washing, drain, obtain potassium salt of cefdinir.
Refining step:
(10) filter cake puts into 3L four-hole bottle, adds 2200Kg water, is warming up to 30-60 DEG C
(11) add charcoal 12Kg, EDTA 1Kg, stir 30min
(12) filtering, wash filter cake with 300Kg, filtrate puts into 3L four-hole bottle, intensification 30-60 DEG C
(13) dripping 5% sulphuric acid, adjust pH to 2.5, stir 1h, repetition measurement pH is constant
(14) filter, wash filter cake with 200Kg, then use 60Kg ethanol rinse, drain
(15) placing, is dried, obtains cefdinir finished product, total recovery 76%.
The above, be only presently preferred embodiments of the present invention, and technical scheme is not made any form On restriction.Any simple modification that above example is made by every technical spirit according to the present invention, equivalent variations with repair Decorations, all still fall within the range of technical scheme.

Claims (9)

1. a cefdinir synthesis technique, it is characterised in that comprise the steps:
Condensation operation: with (Z)-2-(thiazolamine-4-base)-2-acetyl oxyimino group thiacetic acid. (S-2-benzothiazole) Ester, i.e. cefdinir side-chain acid active ester, with 7-amino-3-vinyl-8-oxo-5-thia-1-azabicyclo [4.2.0] Oct-2-ene-2-carboxylic acid, i.e. 7-AVCA, it is condensed;
Hydrolyzing process: through hydrolysis deacetylate protection, and generate potassium salt of cefdinir;
Refining step: potassium salt of cefdinir, through acid treatment, crystallize, obtains cefdinir finished product.
2. synthesis technique as claimed in claim 1, it is characterised in that
Described condensation operation, is to put in retort by 7-AVCA, cefdinir side-chain acid active ester, organic solvent A, in stirring Mix down and be slowly added dropwise into alkali liquor;After waiting to drip, stirring to material is all dissolved;The residual of sampling detection 7-AVCA≤ When 0.5%, adding quantitative organic solvent B in reactant liquor, stirring layering, the organic layer separated discards, and water layer is waited to hydrolyze;
Described hydrolyzing process, is addition wet chemical in water layer, adjusts pH=7-9, with stirring clock reaction 30 points Clock;Reaction puts into potassium acetate after terminating, rejection filter of lowering the temperature, and obtains potassium salt of cefdinir;
Described refining step, is that potassium salt of cefdinir is put into dissolving in purified water, adds acid and make its crystallize, obtain cephalo ground Buddhist nun's finished product.
3. as claimed in claim 1 synthesis technique, it is characterised in that described condensation operation specifically includes following steps:
(1) in retort, 30-50Kg 7-AVCA, 70-100Kg active ester, 300-500Kg oxolane, 100-are put into 300Kg water, stirring is cooled to 0-50 DEG C;
(2) dropping alkali liquor 18-36Kg;
(3) drip finish, clock reaction;
(4) complete molten time add 0.4Kg EDTA, sampling detection, during 7-AVCA≤0.5 reaction terminate;
(5) adding dichloromethane 500-700Kg stirring 5min, the 100-300Kg that adds water and stir 5min, layering, water layer is used 331.5Kg*2 dichloromethane is washed twice, combined dichloromethane layer, washes with 130Kg, combining water layer, puts into retort, adds EDTA 0.4Kg, is cooled to 0-50 DEG C, and water layer is waited to hydrolyze.
4. as claimed in claim 1 synthesis technique, it is characterised in that described hydrolyzing process specifically includes following steps:
(6) condensation operation gained water layer, drips solution of potassium carbonate, adjusts pH=7-9
(7) clock reaction 30min;
(8) add potassium acetate 50-100Kg, after being cooled to 0 DEG C, stir 10min;
(9) filter, with 40Kg acetone drip washing, drain, obtain potassium salt of cefdinir.
5. as claimed in claim 1 synthesis technique, it is characterised in that described refining step specifically includes following steps:
(10) potassium salt of cefdinir filter cake puts into retort, adds 2200Kg water, is warming up to 30-60 DEG C;
(11) add charcoal 12Kg, EDTA 1Kg, stir 30min;
(12) filtering, wash filter cake with 300Kg, filtrate puts into retort, intensification 30-60 DEG C;
(13) dropping acid solution, adjusts pH to 1.5-2.5, stirs 1h, and repetition measurement pH is constant;
(14) filter, wash filter cake with 200Kg, then use 60Kg ethanol rinse, drain;
(15) placing, is dried, obtains cefdinir finished product.
6. as claimed in claim 2 synthesis technique, it is characterised in that in described condensation operation, organic solvent A be oxolane or Ethyl acetate.
7. synthesis technique as claimed in claim 2, it is characterised in that in described condensation operation, alkali liquor is triethylamine, ammonia or hydrogen Sodium hydroxide solution.
8. as claimed in claim 2 synthesis technique, it is characterised in that in described condensation operation, organic solvent B be dichloromethane or Ethyl acetate.
9. synthesis technique as claimed in claim 2, it is characterised in that in described refining step, acid solution is sulphuric acid, hydrochloric acid, ice vinegar Acid etc..
CN201610548324.8A 2016-06-30 2016-06-30 Cefdinir synthesizing technology Pending CN106008555A (en)

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Publication number Priority date Publication date Assignee Title
WO2005121154A1 (en) * 2004-06-08 2005-12-22 Teva Pharmaceutical Industries Ltd. Process for the preparation of cefdinir
US7105659B2 (en) * 2003-06-02 2006-09-12 Aurobind - Pharma Ltd. Process for preparing cefdinir
WO2007053723A2 (en) * 2005-10-31 2007-05-10 Teva Pharmaceutical Industries Ltd. Process for the preparation of cefdinir
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CN102516261A (en) * 2011-12-20 2012-06-27 浙江国邦药业有限公司 Preparation method of cefdinir
CN102659817A (en) * 2012-05-08 2012-09-12 浙江普洛得邦制药有限公司 Preparation method of cefdinir

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Publication number Priority date Publication date Assignee Title
US7105659B2 (en) * 2003-06-02 2006-09-12 Aurobind - Pharma Ltd. Process for preparing cefdinir
WO2005121154A1 (en) * 2004-06-08 2005-12-22 Teva Pharmaceutical Industries Ltd. Process for the preparation of cefdinir
WO2007053723A2 (en) * 2005-10-31 2007-05-10 Teva Pharmaceutical Industries Ltd. Process for the preparation of cefdinir
CN102153566A (en) * 2010-02-11 2011-08-17 深圳市立国药物研究有限公司 Method for preparing cefdinir
CN102516261A (en) * 2011-12-20 2012-06-27 浙江国邦药业有限公司 Preparation method of cefdinir
CN102659817A (en) * 2012-05-08 2012-09-12 浙江普洛得邦制药有限公司 Preparation method of cefdinir

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Application publication date: 20161012