CN109232609A - A method of preparing high-purity Cefpodoxime Proxetil - Google Patents

A method of preparing high-purity Cefpodoxime Proxetil Download PDF

Info

Publication number
CN109232609A
CN109232609A CN201811135618.3A CN201811135618A CN109232609A CN 109232609 A CN109232609 A CN 109232609A CN 201811135618 A CN201811135618 A CN 201811135618A CN 109232609 A CN109232609 A CN 109232609A
Authority
CN
China
Prior art keywords
cefpodoxime
carbonate
ionic liquid
ester
alcohol
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201811135618.3A
Other languages
Chinese (zh)
Other versions
CN109232609B (en
Inventor
祝占根
厉昆
李如宏
厉梦琳
陈亮
杨彩霞
金龙
胡京晗
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
APELOA PHARMACEUTICAL Co.,Ltd.
ZHEJIANG APELOA TOSPO PHARMACEUTICAL Co.,Ltd.
Original Assignee
ZHEJIANG PULUO DEBANG PHARMACEUTICAL CO Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by ZHEJIANG PULUO DEBANG PHARMACEUTICAL CO Ltd filed Critical ZHEJIANG PULUO DEBANG PHARMACEUTICAL CO Ltd
Priority to CN201811135618.3A priority Critical patent/CN109232609B/en
Publication of CN109232609A publication Critical patent/CN109232609A/en
Application granted granted Critical
Publication of CN109232609B publication Critical patent/CN109232609B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • 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
    • C07D501/247-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
    • C07D501/26Methylene radicals, substituted by oxygen atoms; Lactones thereof with the 2-carboxyl group
    • C07D501/34Methylene radicals, substituted by oxygen atoms; Lactones thereof with the 2-carboxyl group with the 7-amino radical acylated by carboxylic acids containing hetero rings
    • 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

Abstract

The invention discloses a kind of methods for preparing high-purity Cefpodoxime Proxetil, comprising: under the action of carbonate and alkali ionic liquid, cefpodoxime acid reacts in organic solvent with iodo-ester, obtains the Cefpodoxime Proxetil after post treatment after reaction.Method of the invention obtains Cefpodoxime ester products total impurities less than 3%, Δ3(EP7.0 provides that total impurities provide total impurities less than 6%) less than 4%, USP35 to 1.5% or less isomers, and product stability is good, molar yield 78.3%~83.7%, high income, suitable industrialized production easy to operate.

Description

A method of preparing high-purity Cefpodoxime Proxetil
Technical field
The invention belongs to technical field of medicine synthesis, and in particular to a kind of to prepare height by raw material one-step method of cefpodoxime acid The method of pure cefditoren pool oxime ester.
Background technique
Cefpodoxime Proxetil Cefpodoxime Proxetil, CPDX-PR, (6R, 7R) -7- [2- (thiazolamine -4- Base) -2- (z)-(methoxyimino)-acetamido] -3- methoxyl methyl -8- oxo -5- sulphur -1- azabicyclo-[4.2.0] octyl- 2- alkene -2- formic acid isopropyl oxygen carbonyl oxygen ethyl ester is a kind of cephalosporin ester prodrugs shown in structure such as formula (I), is given when oral When, by the esterase being present in intestinal wall, fast hydrolyzing and be converted into Cefpodoxime, Cefpodoxime is a kind of antibacterial agent. Cefpodoxime shows resisting gram-positive and negative bacterium, for example, staphylococcus aureus, golden yellow streptococcus, Escherichia coli, The wide antibacterial activity range of bacillus canalis capsulatus and proteus vulgaris, while also having highly stable to beta-lactamase Property.Cefpodoxime Proxetil belongs to third generation oral cephalosporin drug.
Document (J.of Antibiotics, Vol40,370 (1987)) report, by making cefpodoxime acid (structure such as formula Shown in II) it is reacted in the presence of strong organic base such as dicyclohexyl amine with iodo-ester (structure is as shown in formula III) and prepares Cefpodoxime Ester.The product that this method obtains, by-product especially isomers Δ3It is relatively high, generally 3% or more.Due to structure Similitude is difficult to separate this undesirable by-product with product.It once attempted isomers Δ3It is opposite to be converted into body Δ2It is different Structure body, but this method needs a series of reaction, therefore is not economically feasible.
Chinese patent (CN1305876C) discloses a kind of method of one-step method preparation high-purity Cefpodoxime Proxetil, with cephalo Mooring oxime (acid) is raw material, is the organic weak bases such as sodium acetate, sodium propionate, sodium iso-octoate, potassium acetate, potassium propionate or isooctyl acid potassium After reactant salt, iodo-ester is added, Cefpodoxime Proxetil is made, product yield 70%~75% is repeating Chinese patent (CN1305876C) it finds to obtain Cefpodoxime Proxetil product cis-trans-isomer R/ (R+S) < 0.5 when and does not meet States Pharmacopoeia specifications.(medicine Allusion quotation provides: in the test solution chromatogram recorded under content determination item, Cefpodoxime Proxetil B isomer peak area and cephalo are moored Oxime ester A, B isomer peak area and the ratio between should be 0.50~0.60).
The patent application of Publication No. WO01/34611, which is disclosed, makees catalyst using crown ether, prepares head from cefpoxime proxetil Spore moors oxime ester.Firstly, it is necessary to prepare Cefpodoxime Proxetil using crown ether, not only higher cost, and also the toxicity of crown ether is for last It is unfavorable for preparing finished product, meanwhile, if not having to crown ether, the isomers of formation is up to 6-8% (weight) range, therefore is preparing On it is still defective.
United States Patent (USP) 5,498,787 is disclosed with quaternary ammonium salt phase transfer catalyst, such as 4-butyl ammonium hydrogen sulfate, is moored from cephalo The method that oximate prepares Cefpodoxime Proxetil, is based on Cefpodoxime, and the amount of quaternary ammonium salt phase transfer catalyst (is rubbed for 35 to 120% You).This method can effectively inhibit isomers Δ3Formation, but the problem for having the yield of desired product low, yield exist In the range of 50%-60%, and need using expensive quaternary ammonium salt.
In addition, according to South Korea No.99-54751 is disclosed disclosed in method, by make the cephem compounds of Cefpodoxime with Alkyl carbonate reaction obtains ester, then acylated with the active ester form of aminothiazole guanidine-acetic acid in the presence of a large amount of quaternary ammonium salts Ester obtained and prepare Cefpodoxime Proxetil.This method is also needed using expensive quaternary ammonium salt, and due to needing about 3 days Long reaction process and cause low yield.
Summary of the invention
Technical problems to be solved needed for the present invention are to overcome above-mentioned shortcoming, and it is high-purity to provide a kind of preparing for simplicity The method of Cefpodoxime Proxetil is spent, and product stability is good.
A method of preparing high-purity Cefpodoxime Proxetil, comprising:
Under the action of carbonate and alkali ionic liquid, cefpodoxime acid and iodo-ester occur instead in organic solvent It answers, obtains the Cefpodoxime Proxetil after post treatment after reaction;
The cation of the carbonate is selected from alkali metal ion or alkaline-earth metal ions;
The alkali ionic liquid is hydroxide 1- butyl -3- methylimidazole salt ([bmlm] OH).
Synthetic route is as follows:
The purity is high of the Cefpodoxime Proxetil made from the method for the present invention, the HPLC method detection through European Pharmacopoeia EP7.0 is wherein Δ3Isomers 1.5% hereinafter, total impurities less than 3%, and European Pharmacopoeia EP7.0 provide total impurities less than 4%, United States Pharmacopeia USP35 provides total impurities less than 6%, illustrates product made from the method for the present invention better than European standard and Unite States Standard.
In the present invention, the weight ratio of alkali ionic liquid and carbonate is 0.001~1.0:1, preferably 0.2:1.
In the present invention, used alkali ionic liquid dosage is 0.001~0.2 times of the weight of cefpodoxime acid.Instead Answering temperature is -20 DEG C~-5 DEG C, and relatively good temperature range is -20 DEG C~-10 DEG C.Reaction time is 0.5 to 2.5 hour, excellent It selects 0.5 to 1.5 hour.
In the present invention, used organic solvent is selected from acetonitrile, tetrahydrofuran, n,N-Dimethylformamide, N, N- dimethyl Sulfoxide, DMAC N,N' dimethyl acetamide and their mixture;Preferably DMAC N,N' dimethyl acetamide.
Preferably, the carbonate is potassium carbonate or sodium carbonate.
In the present invention, the amount based on cefpodoxime acid, the amount of used iodo-ester is 1 to 3 molar equivalent, preferably 1 To 1.2 equivalents.When the amount of iodo-ester increases, the rising of impurity or the increase of cost will cause.
Preferably, the post-processing includes: by the active carbon decoloring of reaction solution, filtering, alcohol and water is added in filtrate It is crystallized in mixed solution, the high-purity Cefpodoxime Proxetil is obtained after the completion of crystallization.As a further preference, described Mixed solution in, the weight ratio of alcohol and water is 0.01-0.1:1;
The alcohol is methanol or ethyl alcohol.
Compared with the existing technology, the beneficial effects of the present invention are embodied in:
Method of the invention obtains Cefpodoxime ester products total impurities less than 3%, Δ31.5% or less (EP7.0 of isomers Providing that total impurities provide total impurities less than 6%) less than 4%, USP35, product stability is good, molar yield 78.3%~ 83.7%, high income, suitable industrialized production easy to operate.
Specific embodiment
Further illustrate that the present invention, following embodiment are for illustration purposes only combined with specific embodiments below, without trying Figure limits the scope of the invention.
Embodiment 1
By 10g (0.0234moL) cefpodoxime acid B under the reaction flask of 250ml, nitrogen protection, 50ml DMAc is put into In (n,N-dimethylacetamide), stirring cools to -20 DEG C of dissolutions, and [bmlm] OH0.05g, potassium carbonate 3.5g, stirring 20 is added Minute.It being added dropwise alpha-iodine ethyl oxygen propylene carbonate 6.5g (0.0253mol), temperature control is at -18 DEG C~-19 DEG C, after reaction 30 minutes, HPLC controls raw material cefpodoxime acid B≤0.5%, and esterification terminates, and the decoloration of 1g medical active carbon is added, and decoloration finishes slowly Reactant of esterification be pressed into pre-cool to 5 DEG C containing in 1% methanol/purification of aqueous solutions 400ml, filters pressing finishes continues to stir It mixes 30 minutes, rejection filter, purified water 50mL cleaning product, is dried in vacuo, obtains white powder solid 10.5g (molar yield 80.6%).
Product (R+S) HPLC=99.2%, R/ (R+S)=0.51, Δ3=0.35%.
Embodiment 2
By 10g (0.0234moL) cefpodoxime acid B under the reaction flask of 250ml, nitrogen protection, 50ml DMAc is put into In, stirring cools to -20 DEG C of dissolutions, and [bmlm] OH0.1g is added, and sodium carbonate 3.1g is stirred 20 minutes.Alpha-iodine ethyl oxygen carbon is added dropwise Isopropyl propionate 6.5g0.0253mol), temperature control is at -18 DEG C~-19 DEG C, after reaction 30 minutes,
HPLC controls raw material cefpodoxime acid B≤0.5%, and esterification terminates, and the decoloration of 1g medical active carbon, decoloration is added It finishes slowly to be pressed into reactant of esterification and pre-cool to 5 DEG C containing in 1% methanol/purification of aqueous solutions 400ml, filters pressing is complete Bi Jixu stir 30 minutes, rejection filter, purified water 50mL cleaning product, vacuum drying, obtain white powder solid 10.2g (mole Yield=78.3%).
Product (R+S) HPLC=99.1%, R/ (R+S)=0.53, Δ 3=0.36%.
Embodiment 3
By 20g (0.0468moL) cefpodoxime acid B under the four-hole bottle of 250ml, nitrogen protection, 100mlDMF is put into In, stirring cools to -15 DEG C~-18 DEG C dissolutions, and [bmlm] OH0.2g, potassium carbonate 6.3g is added, and stirs 20 minutes.Alpha-iodine is added dropwise Ethyl oxygen propylene carbonate 13g (0.0505mol), after insulation reaction 30 minutes, HPLC control raw material cefpodoxime acid B≤ 0.5%, esterification terminates, and the decoloration of 2g medical active carbon is added, and decoloration, which finishes, is slowly pressed into reactant of esterification in advance Be cooled to 5 DEG C containing in 2% ethyl alcohol/purification of aqueous solutions 800ml, filters pressing finishes precipitation solid, continues stirring 30 minutes.Rejection filter, Purified water 50mL washing, vacuum drying obtain white powder solid 18.9g (weight yield=94.5%).
Product (R+S) HPLC=99.2%, R/ (R+S)=0.51, Δ3=0.37%.
Embodiment 4
By 10g (0.0234moL) cefpodoxime acid B under the reaction flask of 250ml, nitrogen protection, 50ml DMAc is put into In, stirring cools to -19 DEG C~-20 DEG C dissolutions, and [bmlm] OH 1.5g, sodium carbonate 3.0g is added, and stirs 20 minutes.α-is added dropwise Iodine ethyl oxygen propylene carbonate 6.5g (0.0253mol), temperature control is at -17 DEG C~-19 DEG C, and after reaction 30 minutes, HPLC control is former Expect cefpodoxime acid B≤0.5%, esterification terminates, and addition 1g medical active carbon decolourizes, and decoloration, which finishes, will slowly be esterified instead Object is answered to be pressed into pre-cool to 5 DEG C and continues stirring 30 minutes containing in 1% ethyl alcohol/purification of aqueous solutions 400ml, filters pressing is finished, Rejection filter, purified water 50mg cleaning product, vacuum drying obtain white powder solid 10.9g (molar yield=83.7%).
Product (R+S) HPLC=99.1%, R/ (R+S)=0.53, Δ3=0.36%.
Embodiment 5
By 20g (0.0468moL) cefpodoxime acid B under the four-hole bottle of 250ml, nitrogen protection, 100mlDMF is put into In, stirring cools to -18 DEG C~-15 DEG C dissolutions, and [bmlm] OH 1.1g is added, and potassium carbonate 5.5g is stirred 20 minutes.Alpha-iodine is added dropwise Ethyl oxygen propylene carbonate 13.3g (0.0517mol), after insulation reaction 30 minutes, HPLC control raw material cefpodoxime acid B≤ 0.5%, esterification terminates, and the decoloration of 2g medical active carbon is added, and decoloration, which finishes, is slowly pressed into reactant of esterification in advance Be cooled to 5 DEG C containing in 2% ethyl alcohol/purification of aqueous solutions 800ml, filters pressing finishes precipitation solid, continues stirring 30 minutes.Rejection filter, Purified water 50mL washing, vacuum drying obtain white powder solid 21.4g (molar yield 82.2%).
Product (R+S) HPLC=99.2%, R/ (R+S)=0.52, Δ3=0.38%.
Embodiment 6
By 10g (0.0234moL) cefpodoxime acid B under the reaction flask of 250ml, nitrogen protection, 50ml DMAc is put into In, stirring cools to -20 DEG C of dissolutions, and [bmlm] OH0.9g is added, and sodium carbonate 2.5g is stirred 20 minutes.Alpha-iodine ethyl oxygen carbon is added dropwise Isopropyl propionate 6.5g (0.0253mol), temperature control is at -18 DEG C~-17 DEG C, and after reaction 30 minutes, HPLC controls raw material Cefpodoxime Sour B≤0.5%, esterification terminate, and the decoloration of 1g medical active carbon is added, and decoloration, which finishes, is slowly pressed into reactant of esterification In advanceIt is cooled to5 DEG C are continued stirring 30 minutes, rejection filter, purified water containing in 1% ethyl alcohol/purification of aqueous solutions 400ml, filters pressing is finished 50mL cleaning product, vacuum drying obtain white powder solid 10.4g (, molar yield 80.0%).
Product (R+S) HPLC=99.2%, R/ (R+S)=0.54, Δ3=0.38%.
Comparative example 7 (refers to CN1305876C document)
20g (0.0468moL) cefpodoxime acid B is put into 120ml DMAc in the reaction flask of 250ml, stirring drop Dissolution is added anhydrous sodium acetate 4.6g and 1g water, is stirred at room temperature 30 minutes.It is cooled to 5 DEG C, alpha-iodine ethyl oxygen propylene carbonate is added 15g (0.0584mol), 5 DEG C~10 DEG C are reacted 1.5 hours.Esterification terminates, and pours into 200ml ethyl acetate and 100 5% In NaHCO3 mixed liquor, stirring separates organic phase, and water phase is extracted with 100ml ethyl acetate, merges organic phase, uses saturated common salt Water washing is twice, organic to be added to 10g anhydrous magnesium sulfate and 10g activity carbon decoloring 30min, and filtering is concentrated under reduced pressure into 80g, fastly 500ml isopropyl ether is added in speed, filters after high degree of agitation, is dried in vacuo, obtain it is white to off-white powder 18.8g (weight yield= 94.0%.Molar yield 72.2%).With European Pharmacopoeia EP7.0HPLC testing result: product (R+S) HPLC=96.23%, R/ (R+S)=0.497 < 0.5 (not meeting pharmacopoeial requirements 0.5~0.6), Δ 3=0.54%.
The product of embodiment 1,3 and 7 is subjected to stability test, the results are shown in Table 1:
The stability test result of the different embodiment products of table 1

Claims (9)

1. a kind of method for preparing high-purity Cefpodoxime Proxetil characterized by comprising
Under the action of carbonate and alkali ionic liquid, cefpodoxime acid reacts in organic solvent with iodo-ester, instead The Cefpodoxime Proxetil is obtained after answering after post treatment;
The cation of the carbonate is selected from alkali metal ion or alkaline-earth metal ions;
The alkali ionic liquid is hydroxide 1- butyl -3- methylimidazole salt.
2. the method according to claim 1, wherein the carbonate is potassium carbonate or sodium carbonate.
3. the method according to claim 1, wherein the weight ratio of the alkali ionic liquid and carbonate is 0.001~1.0:1.
4. the method according to claim 1, wherein the weight of the alkali ionic liquid and cefpodoxime acid Than 0.01~0.2:1.
5. the method according to claim 1, wherein reaction temperature is -20 DEG C~-5 DEG C.
6. according to the method described in claim 5, it is characterized in that, reaction temperature is -20 DEG C~-10 DEG C.
7. the method according to claim 1, wherein the organic solvent is selected from acetonitrile, tetrahydrofuran, N, N- Dimethylformamide, N, N- dimethyl sulfoxide, DMAC N,N' dimethyl acetamide and their mixture.
8. the method according to claim 1, wherein the post-processing includes: to take off reaction solution with active carbon Color, filtering, filtrate are added in the mixed solution of alcohol and water and are crystallized, and the high-purity Cefpodoxime is obtained after the completion of crystallization Ester.
9. according to the method described in claim 8, it is characterized in that, in the mixed solution, the weight ratio of alcohol and water is 0.01~0.1:1;
The alcohol is methanol or ethyl alcohol.
CN201811135618.3A 2018-09-27 2018-09-27 Method for preparing high-purity cefpodoxime proxetil Active CN109232609B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811135618.3A CN109232609B (en) 2018-09-27 2018-09-27 Method for preparing high-purity cefpodoxime proxetil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811135618.3A CN109232609B (en) 2018-09-27 2018-09-27 Method for preparing high-purity cefpodoxime proxetil

Publications (2)

Publication Number Publication Date
CN109232609A true CN109232609A (en) 2019-01-18
CN109232609B CN109232609B (en) 2021-07-02

Family

ID=65057348

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811135618.3A Active CN109232609B (en) 2018-09-27 2018-09-27 Method for preparing high-purity cefpodoxime proxetil

Country Status (1)

Country Link
CN (1) CN109232609B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113999252A (en) * 2021-12-03 2022-02-01 浙江东邦药业有限公司 Cefpodoxime proxetil impurity cefpodoxime dippivoxil and preparation method thereof

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5498787A (en) * 1994-04-20 1996-03-12 Standard Chemical & Pharmaceutical Co., Ltd. Method for preparing cephalosporin derivatives
CN1288466A (en) * 1998-01-09 2001-03-21 生物化学有限公司 Process for prepn. of sefpodoxime proxetil diastereoisomers
CN1160361C (en) * 1999-11-08 2004-08-04 韩美药品工业株式会社 Method for prepairng highly purity cefpodoxime proxetil
US20080255200A1 (en) * 2007-04-11 2008-10-16 Auspex Pharmaceuticals, Inc. Substituted benzimidazoles
WO2010097675A1 (en) * 2009-02-27 2010-09-02 Dhanuka Laboratories Ltd. An improved preparation process for cefpodoxime proxetil
CN101843599A (en) * 2009-03-23 2010-09-29 杭州锐思医药科技有限公司 Oral cephalosporin ester capsule

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5498787A (en) * 1994-04-20 1996-03-12 Standard Chemical & Pharmaceutical Co., Ltd. Method for preparing cephalosporin derivatives
CN1288466A (en) * 1998-01-09 2001-03-21 生物化学有限公司 Process for prepn. of sefpodoxime proxetil diastereoisomers
CN1160361C (en) * 1999-11-08 2004-08-04 韩美药品工业株式会社 Method for prepairng highly purity cefpodoxime proxetil
US20080255200A1 (en) * 2007-04-11 2008-10-16 Auspex Pharmaceuticals, Inc. Substituted benzimidazoles
WO2010097675A1 (en) * 2009-02-27 2010-09-02 Dhanuka Laboratories Ltd. An improved preparation process for cefpodoxime proxetil
CN101843599A (en) * 2009-03-23 2010-09-29 杭州锐思医药科技有限公司 Oral cephalosporin ester capsule

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
HONG WOO LEE等,: ""Preparation Of Ceph-3-Em Esters Unaccompanied By δ3 To δ2 Isomerization Of The Cephalosporin Derivatives"", 《SYNTHETIC COMMUNICATIONS》 *
杨涛,: ""功能化离子液体的制备及其在头孢托仑酯合成中的应用"", 《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113999252A (en) * 2021-12-03 2022-02-01 浙江东邦药业有限公司 Cefpodoxime proxetil impurity cefpodoxime dippivoxil and preparation method thereof

Also Published As

Publication number Publication date
CN109232609B (en) 2021-07-02

Similar Documents

Publication Publication Date Title
ES2281685T3 (en) SALTS OF CEFDINIR CRYSTALS.
BR102012032754A2 (en) CONTINUOUS PROCESS FOR THE ALKYLATION OF CYCLIC TERTIARY AMINES
CN109232609A (en) A method of preparing high-purity Cefpodoxime Proxetil
KR101577488B1 (en) Cefdinir acid double salt and its preparation
CN109651402B (en) Preparation process of cefazedone sodium
CN103232475B (en) A kind of preparation method of Aspoxicillin trihydrate
CN108033972B (en) Synthesis method of cefprozil
CN109553630B (en) Synthesis method of cefazedone sodium
US11124526B2 (en) Crystalline beta-lactamase inhibitor
US7482486B2 (en) Methods for the preparation and formulation of magnesium valproate hydrate
EP2520578A1 (en) Process for purification of cephalosporins
CN102898443B (en) The process for purification of high yield super-clean high-purity Cefodizime Sodium
CN111004255A (en) Preparation method of cefcapene lactone compound or hydrochloride thereof
US4634556A (en) Crystalline sodium (5R, 6S, 8R)-6-(1-hydroxyethyl)-2-(2-carbamoyloxyethylthio)-penem-3-carboxylate and process for making same
CN111100144B (en) Synthesis process of cefathiamidine
KR100378731B1 (en) Method for producing crystalline cefuroxime axetil ester
CN108299468B (en) Refining method of cefprozil
CN113185538B (en) Preparation method of cefpodoxime acid
CN1295234C (en) Cefuroxime axetil diastereoisomer separating method
KR100327708B1 (en) Method for producing crystalline cefuroxime axetil
EP1073625B1 (en) Tilidine mesylate, processes for its preparation and pharmaceutical composition thereof
KR101670857B1 (en) Method for preparing cefroxadine
CN113461709A (en) Synthesis method of penethamate hydroiodide
CN117069739A (en) Preparation method of high-purity sodium cefuroxime axetil
KR100202279B1 (en) Process for preparing cefuroxime ester derivatives

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
TA01 Transfer of patent application right
TA01 Transfer of patent application right

Effective date of registration: 20200629

Address after: 322118, 519, Zhenjiang South Road, Dongyang, Zhejiang, Jinhua, Hengdian

Applicant after: ZHEJIANG APELOA TOSPO PHARMACEUTICAL Co.,Ltd.

Applicant after: APELOA PHARMACEUTICAL Co.,Ltd.

Address before: 322118, 519, Zhenjiang South Road, Dongyang, Zhejiang, Jinhua, Hengdian

Applicant before: ZHEJIANG APELOA TOSPO PHARMACEUTICAL Co.,Ltd.

GR01 Patent grant
GR01 Patent grant