CN108727411A - A kind of preparation method of cefotiam hydrochloride - Google Patents
A kind of preparation method of cefotiam hydrochloride Download PDFInfo
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- CN108727411A CN108727411A CN201810827308.1A CN201810827308A CN108727411A CN 108727411 A CN108727411 A CN 108727411A CN 201810827308 A CN201810827308 A CN 201810827308A CN 108727411 A CN108727411 A CN 108727411A
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Classifications
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D501/00—Heterocyclic 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
- C07D501/02—Preparation
- C07D501/04—Preparation from compounds already containing the ring or condensed ring systems, e.g. by dehydrogenation of the ring, by introduction, elimination or modification of substituents
- C07D501/06—Acylation of 7-aminocephalosporanic acid
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D501/00—Heterocyclic 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
- C07D501/14—Compounds having a nitrogen atom directly attached in position 7
- C07D501/16—Compounds having a nitrogen atom directly attached in position 7 with a double bond between positions 2 and 3
- C07D501/20—7-Acylaminocephalosporanic or substituted 7-acylaminocephalosporanic acids in which the acyl radicals are derived from carboxylic acids
- C07D501/24—7-Acylaminocephalosporanic or substituted 7-acylaminocephalosporanic acids in which the acyl radicals are derived from carboxylic acids with hydrocarbon radicals, substituted by hetero atoms or hetero rings, attached in position 3
- C07D501/36—Methylene radicals, substituted by sulfur atoms
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Cephalosporin Compounds (AREA)
Abstract
The present invention provides a kind of preparation methods of cefotiam hydrochloride, it is characterised in that：Under conditions of using dimethyl carbonate as solvent, after condensation reaction using boron trifluoride complex catalysis 7-amino-cephalosporanic acid and 1- (2- dimethyl aminoethyls) -1H-5- mercapto tetrazoles, without Crystallization Separation, it is condensed into Cefotiam by reaction dissolvent and aminothiazole acetyl chloride hydrochloride of pure water again, Cefotiam obtains cefotiam hydrochloride after hydrochloric acid acidizing crystal.Solvent used in this is bright can greatly reduce environmental protection pressure with recovery, and environmental pollution is small, improves the index of cefotiam hydrochloride while cost is reduced.
Description
Technical field
The present invention relates to organic synthesis fields, and in particular, to a kind of a kind of new preparation of antibacterials Cefotiam
Method.
Background technology
Cefotiam hydrochloride chemical name：7- [2- (thiazolamine -4- bases) acetylamino]-[3- [[[(N, N)-diformazans
Base-amino-ethyl-tetrazole -1- bases] sulphur] methyl] -8 bicyclic [4,2,0] oct-2-ene -2- carboxylics of oxo -5- thia -1- nitrogen oxygen
Acid] dihydrochloride be second generation injection antibacterial cephalosporin class antimicrobial.
The kind technology is mainly 7-amino-cephalosporanic acid and 1- (2- dimethyl aminoethyls) -1H-5- sulfydryls four at present
Nitrogen azoles (MTZ) catalyzes and synthesizes 7-ACMT in acetonitrile solvent, with boron trifluoride complex, and the solvents such as methanol are then added, and is added dropwise
Triethylamine adjusts pH crystallizations, is centrifugally separating to obtain 7-ACMT solids, the solid is in one or more in the mixed solvents and ATC.HCL
It is condensed to yield Cefotiam, then acidizing crystal is centrifugally separating to obtain cefotiam hydrochloride crude product.
Above-mentioned reaction process is complicated, needs multiple purification processes, and its extent of reaction is poor, low yield, and obtain product color
Grade is higher, and impurity is higher, is unfavorable for subsequent production, research and utilizes.
Invention content
Present invention aims to overcome that shortcoming present in above-mentioned technology, using green and environment-friendly solvent dimethyl carbonate
To synthesize Cefotiam intermediate 7-ACMT, and Cefotiam crude product is synthesized by solvent of pure water.Solvent used in invention
Environmental protection pressure can be greatly reduced with recovery, environmental pollution is small, improves cefotiam hydrochloride while cost is reduced
The quality of peace.
In order to achieve the above object, the preparation method of a kind of cefotiam hydrochloride provided by the invention, it is characterised in that：With
Under conditions of dimethyl carbonate is solvent, using boron trifluoride complex catalysis 7-amino-cephalosporanic acid and 1- (2- dimethylaminos
Base ethyl) -1H-5- mercapto tetrazoles condensation reaction after, without Crystallization Separation, then using pure water as reaction dissolvent and aminothiazole
Acetyl chloride hydrochloride is condensed into Cefotiam, and Cefotiam obtains cefotiam hydrochloride after hydrochloric acid acidizing crystal.
Further, the preparation method of a kind of cefotiam hydrochloride provided by the invention, also has the characteristics that such：I.e.,
Above-mentioned boron trifluoride complex is selected from boron trifluoride acetonitrile complex compound, boric carbonic acid dimethyl ester complex trifluoride, boron trifluoride ammonia
Base ethyl complex compound.
Further, the preparation method of a kind of cefotiam hydrochloride provided by the invention, also has the characteristics that such：I.e.,
Specific process step is as follows：
S1. in dimethyl carbonate, boron trifluoride complex, 7-amino-cephalosporanic acid and 1- (2- dimethylaminos is added
Ethyl) after -1H-5- mercapto tetrazoles, under the action of an acid, reacts 0.5-5 hours at a temperature of 20-50 DEG C, go out through water quenching
After reaction, extraction extraction water phase (i.e., 3- [[[(N, N)-dimethyl-amino-ethyl-tetrazole -1- bases] sulphur] methyl] -8- oxygen
Generation -5- thia -1H- azepines
The reaction solution of bicyclic [4,2,0] oct-2-ene -2- carboxylics)；Specific reaction equation is as follows：
S2. it keeps at 10 DEG C of temperature below of water phase, regulation system pH is alkalescent, adds aminothiazole chloroacetic chloride hydrochloric acid
After salt, controlling reaction temperature is to react 0.5-5 hours at 5 DEG C of temperature below, target product is obtained after acidified processing.
Specific reaction equation is as follows：
Further, the preparation method of a kind of cefotiam hydrochloride provided by the invention, also has the characteristics that such：I.e.,
The molar ratio of above-mentioned 7-amino-cephalosporanic acid and 1- (2- dimethyl aminoethyls) -1H-5- mercapto tetrazoles is 1:0.85-
1.25；Its mass percent concentration reacted is 10-35%.
The dosage of above-mentioned boron trifluoride complex is 7-amino-cephalosporanic acid and 1- (2- dimethyl aminoethyls) -1H-5-
The 0.01-15% of mercapto tetrazole total weight.
Further, the preparation method of a kind of cefotiam hydrochloride provided by the invention, also has the characteristics that such：I.e.,
Above-mentioned acid is selected from sulfonic derivative (such as：Methanesulfonic acid, benzene sulfonic acid etc. sulfonic classes of organic acids), alkyl acid (such as：Formic acid, acetic acid,
The alkyl acids such as propionic acid, butyric acid, octanoic acid), inorganic acid (such as：One or more of the inorganic acids such as hydrochloric acid, sulfuric acid)；
The dosage of above-mentioned acid is that 7-amino-cephalosporanic acid and 1- (2- dimethyl aminoethyls) -1H-5- mercapto tetrazoles are total
The 0.01-15% of weight.
Further, the preparation method of a kind of cefotiam hydrochloride provided by the invention, also has the characteristics that such：I.e.,
Extraction process in above-mentioned S1, used extractant be halogenated alkane (such as：Carbon tetrachloride, chloroform, dichloromethane,
Dichloroethanes, tetrachloroethanes etc.), esters solvent (such as：Ethyl acetate, methyl acetate, Ethyl formate, methyl formate) in one kind
Or it is a variety of.
Further, the preparation method of a kind of cefotiam hydrochloride provided by the invention, also has the characteristics that such：I.e.,
The molar ratio of above-mentioned aminothiazole acetyl chloride hydrochloride and 7-amino-cephalosporanic acid additive amount is 1：0.8-1.2.
Further, the preparation method of a kind of cefotiam hydrochloride provided by the invention, also has the characteristics that such：I.e.,
In step s 2, the process of above-mentioned acidified processing is as follows：
S2-1. after reaction, hydrochloric acid reaction is added；The dosage of the pure hydrochloric acid is 0.3-2.5 times of solvent dosage,
Its mole dosage is 1-5 times of 7-amino-cephalosporanic acid.
S2-2. after filtering, target pure products are obtained by crystallisation；The method of the crystallization is using ketone, ethers, alcohols
Reagent and its lower culture for carrying out crystal of mixing, are separated by solid-liquid separation by modes such as centrifugations later.
Or
S2-1. after reaction, hydrochloric acid reaction is added；
S2-2. activated carbon decolorizing 5-30min；
S2-2. after filtering, target pure products are obtained by crystallisation.
Further, the preparation method of a kind of cefotiam hydrochloride provided by the invention, also has the characteristics that such：I.e.,
The preparation method of above-mentioned aminothiazole acetyl chloride hydrochloride is：Aminothiazole acid hydrochloride, in acylated preparation under the action of system
Obtain target product.
The acylating reagent can be any acyl halide reagent, such as：Thionyl chloride, phosphorus oxychloride, phosphorus pentachloride, oxalyl
Chlorine, phosgene, surpalite, triphosgene etc..The molar ratio of itself and aminothiazole acid hydrochloride is 1：0.8-1.5.
Further, the preparation method of a kind of cefotiam hydrochloride provided by the invention, also has the characteristics that such：I.e.,
Above-mentioned reaction can also add solvent and be reacted；
Above-mentioned solvent be selected from dimethyl carbonate, dichloromethane, carbon tetrachloride, chloroform, acetonitrile, acetone, triethylamine,
Water, DMF, ethyl acetate.A concentration of 10-45% of solute.
The function and effect of the present invention：
Cefotiam content in crude product produced by the invention is high, and color is fabulous, and impurity residual is considerably less.
In addition, during three intermediate 7-ACMT of Cefotiam in the present invention are synthesized, using in green and environment-friendly solvent carbon
It is condensed in dimethyl phthalate, Cefotiam is directly condensed into water phase and ATC.HCl using technique of cooking all things in one pot without isolation
Crude product reduces cost, has saved energy consumption, reduces the pollution to environment.
In addition, the solvent used in this is bright can greatly reduce environmental protection pressure with recovery, environmental pollution is small,
The index of cefotiam hydrochloride is improved while cost is reduced.
Specific implementation mode
The preparation of embodiment 1-1, aminothiazole acetyl chloride hydrochloride (ATC.HCL).
10 degree of acetonitrile 120ml temperature controls are added in reactor hereinafter, DMF is added.Phosphorus oxychloride 50g is added dropwise, drips and finishes addition ammonia
Then base thiazolyl acetic acid hydrochloride 60g, clock reaction 10-20hr cool down, acetonitrile 120ml is added.Growing the grain 1.0-2.0hr.Centrifugation
The aminothiazole acetyl chloride hydrochloride (ATC.HCL) of separation, high pressure liquid phase purity 98%
Embodiment 1-2,
10 degree of acetonitrile 100ml temperature controls are added in reactor hereinafter, DMF is added.Thionyl chloride 60g is added dropwise, drips and finishes addition ammonia
Then base thiazolyl acetic acid hydrochloride 60g, clock reaction 4-6hr cool down, acetonitrile 100ml is added.Growing the grain 1.0-2.0hr.Centrifugation point
From aminothiazole acetyl chloride hydrochloride (ATC.HCL), high pressure liquid phase purity 97.5%
Embodiment 2,
Dimethyl carbonate 100ml, 7-amino-cephalosporanic acid 40g, MTZ15g are added at room temperature.Boron trifluoride-is added in equality of temperature
Then carbonic acid dimethyl ester complex 15g, methanesulfonic acid 5g, 35-40 DEG C of clock reaction 1-2.0hr of temperature control are cooled to 20 DEG C or less and add
Enter pure water 320ml hydrolysis, adds 300ml carbon tetrachloride extraction 10min, be layered.Then activated carbon decolorizing 20min mistakes are added
Filter.By 5 DEG C of filtrate temperature control hereinafter, be added dropwise triethylamine tune pH7.0-8.0, then be added ATC.HCL (embodiment 1-1), 5 DEG C with
Lower clock reaction 1-2.0hr is added concentrated hydrochloric acid 60ml, adds activated carbon decolorizing 20min after complete reaction, filters, filtrate
Acetone 1400-1500ml is added dropwise, is added crystal seed growing the grain, it is to be crystallized completely after, then acetone 500-600ml is added dropwise, drips Bi Yangjing
1.0hr.It centrifuges, obtains cefotiam hydrochloride crude product.High pressure liquid phase purity 98.2%, yield 85%, color grade are less than yellowish green
Colour standard color solution 2.
Embodiment 3,
Dimethyl carbonate 150ml, 7-amino-cephalosporanic acid 40g, MTZ25g are added at room temperature.Boron trifluoride-is added in equality of temperature
Then carbonic acid dimethyl ester complex 25g, glacial acetic acid 10g, 45-50 DEG C of clock reaction 1-2.0hr of temperature control are cooled to 20 DEG C or less and add
Enter pure water 300ml hydrolysis, adds 310ml dichloromethane extraction 10min, layering.Then activated carbon decolorizing 20min mistakes are added
Filter.By 5 DEG C of filtrate temperature control hereinafter, be added dropwise triethylamine tune PH7.0-8.0, then be added ATC.HCL (embodiment 1-1), 5 DEG C with
Lower clock reaction 1-2.0hr is added concentrated hydrochloric acid 60ml, adds activated carbon decolorizing 20min after complete reaction, filters, filtrate
Acetone 1400-1500ml is added dropwise, is added crystal seed growing the grain, it is to be crystallized completely after, then acetone 500-600ml is added dropwise, drips Bi Yangjing
1.0hr.It centrifuges, obtains cefotiam hydrochloride crude product.High pressure liquid phase purity 98.5%, yield 89%, color grade are less than yellowish green
Colour standard color solution 3.
Embodiment 4,
Dimethyl carbonate 120ml, 7-amino-cephalosporanic acid 40g, MTZ20g are added at room temperature.Boron trifluoride-is added in equality of temperature
Then carbonic acid dimethyl ester complex 10g, glacial acetic acid 10g, 45-50 DEG C of clock reaction 1-2.0hr of temperature control are cooled to 20 DEG C or less and add
Enter pure water 300ml hydrolysis, adds 310ml chloroform extraction 10min, be layered.Then activated carbon decolorizing 20min mistakes are added
Filter.By 5 DEG C of filtrate temperature control hereinafter, be added dropwise triethylamine tune PH7.0-8.0, then be added ATC.HCL (embodiment 1-2), 5 DEG C with
Lower clock reaction 1-2.0hr is added concentrated hydrochloric acid 60ml, adds activated carbon decolorizing 20min after complete reaction, filters, filtrate
Acetone 1400-1500ml is added dropwise, is added crystal seed growing the grain, it is to be crystallized completely after, then acetone 500-600ml is added dropwise, drips Bi Yangjing
1.0hr.It centrifuges, obtains cefotiam hydrochloride crude product.High pressure liquid phase purity 98.0%, yield 91%, color grade are less than yellowish green
Colour standard color solution 3.
Embodiment 5,
Dimethyl carbonate 120ml, 7-amino-cephalosporanic acid 40g, MTZ30g are added at room temperature.Boron trifluoride-is added in equality of temperature
Then carbonic acid dimethyl ester complex 30g, concentrated sulfuric acid 2g, 45-50 DEG C of clock reaction 1-2.0hr of temperature control are cooled to 20 DEG C or less and add
Enter pure water 300ml hydrolysis, adds 240ml ethyl acetate extraction 10min, layering.Then activated carbon decolorizing 20min mistakes are added
Filter.By 5 DEG C of filtrate temperature control hereinafter, be added dropwise triethylamine tune PH7.0-8.0, then be added ATC.HCL (embodiment 1-2), 5 DEG C with
Lower clock reaction 1-2.0hr is added concentrated hydrochloric acid 60ml, adds activated carbon decolorizing 20min after complete reaction, filters, filtrate
Acetone 1400-1500ml is added dropwise, is added crystal seed growing the grain, it is to be crystallized completely after, then acetone 500-600ml is added dropwise, drips Bi Yangjing
1.0hr.It centrifuges, obtains cefotiam hydrochloride crude product.High pressure liquid phase purity 98.6%, yield 85%, color grade are less than yellowish green
Colour standard color solution 3.
Claims (10)
1. a kind of preparation method of cefotiam hydrochloride, it is characterised in that：Under conditions of using dimethyl carbonate as solvent, using three
Boron fluoride complex catalysis 7-amino-cephalosporanic acid and the condensation of 1- (2- dimethyl aminoethyls) -1H-5- mercapto tetrazoles are anti-
Ying Hou is condensed into Cefotiam, cephalo without Crystallization Separation, then by reaction dissolvent and aminothiazole acetyl chloride hydrochloride of pure water
For peace cefotiam hydrochloride is obtained after hydrochloric acid acidizing crystal.
2. a kind of preparation method of cefotiam hydrochloride as described in claim 1, it is characterised in that：
The boron trifluoride complex is selected from boron trifluoride acetonitrile complex compound, boric carbonic acid dimethyl ester complex trifluoride, borontrifluoride
Boron amino-ethyl complex compound.
3. a kind of preparation method of cefotiam hydrochloride as described in claim 1, which is characterized in that specific process step is as follows
It is shown：
S1. in dimethyl carbonate, boron trifluoride complex, 7-amino-cephalosporanic acid and 1- (2- dimethylaminoethyls is added
Base) after -1H-5- mercapto tetrazoles, under the action of an acid, reacts 0.5-5 hours at a temperature of 20-50 DEG C, go out instead through water quenching
Ying Hou, extraction extraction water phase；
S2. it keeps at 10 DEG C of temperature below of water phase, regulation system pH is alkalescent, adds aminothiazole acetyl chloride hydrochloride
Afterwards, controlling reaction temperature is to react 0.5-5 hours at 5 DEG C of temperature below, target product is obtained after acidified processing.
4. a kind of preparation method of cefotiam hydrochloride as claimed in claim 3, it is characterised in that：
The molar ratio of the 7-amino-cephalosporanic acid and 1- (2- dimethyl aminoethyls) -1H-5- mercapto tetrazoles is 1:0.85-
1.25；
The dosage of the boron trifluoride complex is 7-amino-cephalosporanic acid and 1- (2- dimethyl aminoethyls) -1H-5- sulfydryls
The 0.01-15% of tetrazole total weight.
5. a kind of preparation method of cefotiam hydrochloride as claimed in claim 3, it is characterised in that：
The acid is selected from one or more of sulfonic derivative, alkyl acid, inorganic acid；
The dosage of the acid is 7-amino-cephalosporanic acid and 1- (2- dimethyl aminoethyls) -1H-5- mercapto tetrazole total weights
0.01-15%.
6. a kind of preparation method of cefotiam hydrochloride as claimed in claim 3, it is characterised in that：
Extraction process in the S1, used extractant are one or more in halogenated alkane, esters solvent.
7. a kind of preparation method of cefotiam hydrochloride as claimed in claim 3, it is characterised in that：
The molar ratio of the aminothiazole acetyl chloride hydrochloride and 7-amino-cephalosporanic acid additive amount is 1：0.8-1.2.
8. a kind of preparation method of cefotiam hydrochloride as claimed in claim 3, it is characterised in that：
In step s 2, the process of the acidified processing is as follows：
S2-1. after reaction, hydrochloric acid reaction is added；
S2-2. after filtering, target pure products are obtained by crystallisation；
Or
S2-1. after reaction, hydrochloric acid reaction is added；
S2-2. activated carbon decolorizing 5-30min；
S2-2. after filtering, target pure products are obtained by crystallisation.
9. a kind of preparation method of cefotiam hydrochloride as described in claim 1, it is characterised in that：
The preparation method of the aminothiazole acetyl chloride hydrochloride is：
Target product is made under the action of acylated preparation in aminothiazole acid hydrochloride.
10. a kind of preparation method of cefotiam hydrochloride as claimed in claim 9, it is characterised in that：
Solvent can be also added to be reacted；
The solvent be selected from dimethyl carbonate, dichloromethane, carbon tetrachloride, chloroform, acetonitrile, acetone, triethylamine, water,
DMF, ethyl acetate.
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| CN201810827308.1A CN108727411A (en) | 2018-07-25 | 2018-07-25 | A kind of preparation method of cefotiam hydrochloride |
| CN201910355682.0A CN110003238A (en) | 2018-07-25 | 2019-04-29 | A kind of preparation method of cefotiam |
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| CN201810827308.1A CN108727411A (en) | 2018-07-25 | 2018-07-25 | A kind of preparation method of cefotiam hydrochloride |
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| CN201810827308.1A Withdrawn CN108727411A (en) | 2018-07-25 | 2018-07-25 | A kind of preparation method of cefotiam hydrochloride |
| CN201910355682.0A Pending CN110003238A (en) | 2018-07-25 | 2019-04-29 | A kind of preparation method of cefotiam |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109336906A (en) * | 2018-11-21 | 2019-02-15 | 山东罗欣药业集团股份有限公司 | A kind of cefotiam chloride drying process |
| CN110563749A (en) * | 2019-09-11 | 2019-12-13 | 山东罗欣药业集团恒欣药业有限公司 | Preparation method of cefotiam hydrochloride compound |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB9115287D0 (en) * | 1991-07-15 | 1991-08-28 | Antibioticos Spa | Process for the preparation of cephalosporins intermediates |
| CN101648961B (en) * | 2009-08-25 | 2011-06-29 | 哈药集团制药总厂 | Method and equipment for preparing cefotiam hydrochloride |
| CN102372729B (en) * | 2011-12-14 | 2014-09-24 | 哈药集团制药总厂 | Novel method for synthesizing cefoperazone sodium compound |
| CN104356146B (en) * | 2014-11-14 | 2016-09-14 | 浙江浙邦制药有限公司 | A kind of preparation method of cefotiam chloride |
| CN106565750B (en) * | 2016-11-09 | 2018-09-11 | 哈药集团制药总厂 | A kind of synthetic method of dextrorotation Mandokef acid |
-
2018
- 2018-07-25 CN CN201810827308.1A patent/CN108727411A/en not_active Withdrawn
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- 2019-04-29 CN CN201910355682.0A patent/CN110003238A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109336906A (en) * | 2018-11-21 | 2019-02-15 | 山东罗欣药业集团股份有限公司 | A kind of cefotiam chloride drying process |
| CN110563749A (en) * | 2019-09-11 | 2019-12-13 | 山东罗欣药业集团恒欣药业有限公司 | Preparation method of cefotiam hydrochloride compound |
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Application publication date: 20181102 |