CN108640900A - A kind of purification process of Erdosteine - Google Patents

A kind of purification process of Erdosteine Download PDF

Info

Publication number
CN108640900A
CN108640900A CN201810577239.3A CN201810577239A CN108640900A CN 108640900 A CN108640900 A CN 108640900A CN 201810577239 A CN201810577239 A CN 201810577239A CN 108640900 A CN108640900 A CN 108640900A
Authority
CN
China
Prior art keywords
erdosteine
purification process
aqueous solution
crude product
acid
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.)
Pending
Application number
CN201810577239.3A
Other languages
Chinese (zh)
Inventor
史登健
马振千
金荣章
李生勤
鹿贵花
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.)
Jiangsu Haici Biological Pharmaceutical Co Ltd Of Yangtze River Pharmaceutical Group
Yangtze River Pharmaceutical Group Co Ltd
Original Assignee
Jiangsu Haici Biological Pharmaceutical Co Ltd Of Yangtze River Pharmaceutical Group
Yangtze River Pharmaceutical Group 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 Jiangsu Haici Biological Pharmaceutical Co Ltd Of Yangtze River Pharmaceutical Group, Yangtze River Pharmaceutical Group Co Ltd filed Critical Jiangsu Haici Biological Pharmaceutical Co Ltd Of Yangtze River Pharmaceutical Group
Priority to CN201810577239.3A priority Critical patent/CN108640900A/en
Publication of CN108640900A publication Critical patent/CN108640900A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D333/00Heterocyclic compounds containing five-membered rings having one sulfur atom as the only ring hetero atom
    • C07D333/02Heterocyclic compounds containing five-membered rings having one sulfur atom as the only ring hetero atom not condensed with other rings
    • C07D333/04Heterocyclic compounds containing five-membered rings having one sulfur atom as the only ring hetero atom not condensed with other rings not substituted on the ring sulphur atom
    • C07D333/26Heterocyclic compounds containing five-membered rings having one sulfur atom as the only ring hetero atom not condensed with other rings not substituted on the ring sulphur atom with hetero atoms or with carbon atoms having three bonds to hetero atoms with at the most one bond to halogen, e.g. ester or nitrile radicals, directly attached to ring carbon atoms
    • C07D333/30Hetero atoms other than halogen
    • C07D333/36Nitrogen atoms

Abstract

The present invention provides a kind of purification process of Erdosteine, include the following steps:1)Prepare Erdosteine crude product aqueous solution:Erdosteine crude product is dissolved in weakly acidic pH to the aqueous solution of alkalinity, addition can be extracted with the organic solvent of water stratification, obtain Erdosteine crude product aqueous solution, and the volume ratio of organic solvent and alkaline aqueous solution is 0.05~20:1;2)Prepare Erdosteine fine work:The Erdosteine crude product aqueous solution that step 1) obtains is adjusted with acid to acidity, solid, filtering is precipitated, drying obtains Erdosteine fine work.The present invention is based on the particularity for containing " carboxyl " group in Erdosteine structure, the column chromatography method for being not suitable for industrialized production greatly without operation difficulty is purified, only purified by " alkali soluble acid is heavy ", purification process is easy to operate, the impurity in Erdosteine crude product can be effectively removed, last Erdosteine fine work purity can reach 99.4% or more, and list is miscellaneous to be less than 0.1%, and high income, it is suitable for industrialized production.

Description

A kind of purification process of Erdosteine
Technical field
The present invention relates to a kind of purification process of Erdosteine, belong to pharmaceutical chemistry technical field.
Background technology
Erdosteine(Erdosteine), chemical entitled:(±)- N- [2-(carboxymethyl sulfydryl)-acetyl group]-high half Guang Propylhomoserin thiolactone, molecular formula are:C8H11NO4S2, molecular weight:249.3 No. CAS:84611-23-4, structural formula are as follows:
Erdosteine is Italian Edmond Pharma and the mucolytic drugs that Refarmed companies of Switzerland develop, main use Treatment when thick sputum is not easy expectoration when acute and chronic bronchitis, the diseases such as obstructive lung disease.
There is no the report of special Erdosteine purification process in existing literature, and common purification process is recrystallization, Recrystallization solvent is generally ethyl alcohol, acetone etc..The Erdosteine of the prior art readily available 95%, but to be further purified When obtaining 99% or higher Erdosteine, general purification process is often extremely difficult to desired effect.
The method that the prior art commonly obtains the compound of high-purity for example has column chromatography method.The separation of column chromatography is former Reason is that adsorption capacity on filler is different and detached according to substance, entire chromatography process be total material Adsorption and desorption, It adsorbs again, desorption process again.Column chromatography method is used to need to consider column effect to reach different material Adsorption and desorption, adsorb again, again Desorption ability is different, and separation process needs a large amount of eluting solvent, is easily introduced new impurity;And every time purifying bulk it is small, Operating time is very long, cumbersome right
Operating personnel are more demanding, and hardly possible is suitable for industrialized production.
Therefore, it is badly in need of proposing that new technical solution optimizes the purification process of Erdosteine.
Invention content
The purpose of the present invention is overcoming the deficiencies of the prior art and provide, one kind is efficient, easy to operate to be suitable for industrialization rule The purification process of the Erdosteine of mould production.
It is an unexpected discovery of the invention that containing the particularity of " carboxyl " group in Erdosteine structure, pass through " alkali soluble acid is heavy " Purification process, end product quality can be controlled in highest list miscellaneous 0.1% hereinafter, 99% or more content, and equipment investment is few, Production cost is low, and process stabilizing is simultaneously suitble to industrialized production.
Technical scheme is as follows:
A kind of purification process of Erdosteine, includes the following steps:
1)Prepare Erdosteine crude product aqueous solution:Erdosteine crude product is dissolved in weakly acidic pH to the aqueous solution of alkalinity
In, addition can be extracted with the organic solvent of water stratification, obtain Erdosteine crude product aqueous solution, the Erdosteine The purity of crude product is 90%~98%, and the volume ratio of organic solvent and alkaline aqueous solution is 0.05~20:1;
2)Prepare Erdosteine fine work:The Erdosteine crude product aqueous solution that step 1) obtains is adjusted with acid to acidity, is precipitated solid Body, filtering, drying obtain Erdosteine fine work.
Preferably,
The step 1)Process is as follows:Erdosteine crude product is added to the water, adjusts pH to 5~14 with inorganic base, stirring is molten Solution, addition and the immiscible organic solvent of water, are extracted, obtain Erdosteine crude product aqueous solution.
The step 1)In, inorganic base includes sodium hydroxide, potassium hydroxide, lithium hydroxide, magnesium hydroxide, hydroxide One or more of ammonium, sodium carbonate, sodium bicarbonate, potassium carbonate and saleratus.
The step 1)In, the organic solvent with water stratification includes in esters, ethers, alkanes and arene It is one or more of.
The step 1)In, organic solvent esters include ethyl acetate, Ethyl formate, methyl acetate and isopropyl acetate One or more of.
The step 1)In, organic solvent ethers includes ether, methyl phenyl ethers anisole, isopropyl ether, methyl tertiary butyl ether(MTBE) and tetrahydrochysene One or more of furans.
The step 1)In, organic solvent alkanes include n-hexane, dichloromethane, hexahydrotoluene, hexamethylene, penta One or more of alkane, heptane and octane.
The step 1)In, organic solvent arene includes one or both of toluene, dimethylbenzene.
The step 2)Process is as follows:The Erdosteine crude product aqueous solution that step 1) obtains is adjusted to pH with inorganic acid To 1~6, solid, filtering is precipitated in stirring, and drying obtains Erdosteine fine work.
The step 2)In, inorganic acid includes one kind or several in hydrochloric acid, nitric acid, boric acid, sulfuric acid, carbonic acid and phosphoric acid Kind.
The step 2)In, the temperature that solid is precipitated in stirring is 0 DEG C~40 DEG C.It is preferred that 25 ± 5 DEG C.
The present invention has the following technical effect that:
The present invention is based on the particularity for containing " carboxyl " group in Erdosteine structure, are not suitable for work greatly without operation difficulty The column chromatography method of industry metaplasia production is purified, and is only purified by " alkali soluble acid is heavy ", purification process is easy to operate, Neng Gouyou Impurity in effect removal Erdosteine crude product, last Erdosteine fine work purity can reach 99.4% or more, and list is miscellaneous to be less than 0.1%, And high income, it is suitable for industrialized production.
Specific implementation mode
It is described further below with reference to specific embodiment, to fully understand the purposes, features and effects of the present invention.
Embodiment 1
In the present embodiment, the purification process of Erdosteine includes the following steps:
1)10Kg Erdosteine crude products are added in 200L reaction kettles, 100L purified waters are added, with 1% NaOH aqueous solution tune PH to 8.5 is saved, then 20L ethyl acetate is added in the stirring and dissolving at 25 ± 5 DEG C, stir 10min, static layering 20min, point Liquid repeats above-mentioned extracting and washing twice, and liquid separation obtains Erdosteine crude product aqueous solution.
2)By Erdosteine crude product aqueous solution salt acid for adjusting pH to 2.5 obtained above, the stirring and crystallizing at 25 ± 5 DEG C 5h, filtering, drying obtain Erdosteine fine work 9.2Kg, and yield 92%, HPLC purity 99.7%, miscellaneous highest list is 0.07%.
Embodiment 2
In the present embodiment, the purification process of Erdosteine includes the following steps:
1)10Kg Erdosteine crude products are added in 200L reaction kettles, 100L purified waters are added, with sodium bicarbonate aqueous solution tune Save pH to 5.0, the stirring and dissolving at 25 ± 5 DEG C, then be added 5L isopropyl ethers, stir 10min, static layering 20min, liquid separation, Repeat above-mentioned extracting and washing twice, liquid separation obtains Erdosteine crude product aqueous solution.
2)By Erdosteine crude product aqueous solution phosphorus acid for adjusting pH to 1.0 obtained above, the stirring and crystallizing at 25 ± 5 DEG C 5h, filtering, drying obtain Erdosteine fine work 8.9Kg, and yield 89%, HPLC purity 99.5%, miscellaneous highest list is 0.05%.
Embodiment 3
In the present embodiment, the purification process of Erdosteine includes the following steps:
1)10Kg Erdosteine crude products are added in 200L reaction kettles, add 100L purified waters, it is water-soluble with 1% potassium hydroxide Liquid adjusts pH to 14, and then 2000L dichloromethane is added in the stirring and dissolving at 25 ± 5 DEG C, stir 10min, static layering 20min, liquid separation repeat above-mentioned extracting and washing twice, and liquid separation obtains Erdosteine crude product aqueous solution.
2)By Erdosteine crude product aqueous solution sulphur acid for adjusting pH to 6.0 obtained above, the stirring and crystallizing at 25 ± 5 DEG C 5h, filtering, drying obtain Erdosteine fine work 9.0Kg, and yield 90%, HPLC purity 99.4%, miscellaneous highest list is 0.08%.
Embodiment 4
In the present embodiment, the purification process of Erdosteine includes the following steps:
1)10Kg Erdosteine crude products are added in 200L reaction kettles, 100L purified waters are added, with ammonium hydroxide aqueous solution tune Save pH to 9.5, the stirring and dissolving at 25 ± 5 DEG C, then be added 100L toluene, stir 10min, static layering 20min, liquid separation, Repeat above-mentioned extracting and washing twice, liquid separation obtains Erdosteine crude product aqueous solution.
2)By Erdosteine crude product aqueous solution salt acid for adjusting pH to 3.5 obtained above, the stirring and crystallizing at 25 ± 5 DEG C 5h, filtering, drying obtain Erdosteine fine work 9.5Kg, and yield 95%, HPLC purity 99.9%, miscellaneous highest list is 0.03%.

Claims (11)

1. a kind of purification process of Erdosteine, which is characterized in that include the following steps:
1)Prepare Erdosteine crude product aqueous solution:Erdosteine crude product is dissolved in weakly acidic pH to the aqueous solution of alkalinity
In, addition can be extracted with the organic solvent of water stratification, obtain Erdosteine crude product aqueous solution, organic solvent and alkali Property aqueous solution volume ratio be 0.05~20:1;
2)Prepare Erdosteine fine work:The Erdosteine crude product aqueous solution that step 1) obtains is adjusted with acid to acidity, is precipitated solid Body, filtering, drying obtain Erdosteine fine work.
2. the purification process of Erdosteine according to claim 1, which is characterized in that the step 1)Process is as follows: Erdosteine crude product is added to the water, adjusts pH to 5~14 with inorganic base, stirring and dissolving is added immiscible organic molten with water Agent is extracted, and Erdosteine crude product aqueous solution is obtained.
3. the purification process of Erdosteine according to claim 2, which is characterized in that the step 1)In, inorganic base Including sodium hydroxide, potassium hydroxide, lithium hydroxide, magnesium hydroxide, ammonium hydroxide, sodium carbonate, sodium bicarbonate, potassium carbonate and carbonic acid One or more of hydrogen potassium.
4. the purification process of Erdosteine according to claim 1, which is characterized in that the step 1)In, with moisture The organic solvent of layer includes one or more of esters, ethers, alkanes and arene.
5. the purification process of Erdosteine according to claim 4, which is characterized in that the step 1)In, You Jirong Agent esters include one or more of ethyl acetate, Ethyl formate, methyl acetate and isopropyl acetate.
6. the purification process of Erdosteine according to claim 4, which is characterized in that the step 1)In, You Jirong Agent ethers includes one or more of ether, methyl phenyl ethers anisole, isopropyl ether, methyl tertiary butyl ether(MTBE) and tetrahydrofuran.
7. the purification process of Erdosteine according to claim 4, which is characterized in that the step 1)In, You Jirong Agent alkanes include one or more of n-hexane, dichloromethane, hexahydrotoluene, hexamethylene, pentane, heptane and octane.
8. the purification process of Erdosteine according to claim 4, which is characterized in that the step 1)In, You Jirong Agent arene includes one or both of toluene, dimethylbenzene.
9. the purification process of Erdosteine according to claim 1, which is characterized in that the step 2)Process is as follows: The Erdosteine crude product aqueous solution that step 1) obtains is adjusted to pH to 1~6 with inorganic acid, solid is precipitated in stirring, filters, drying Obtain Erdosteine fine work.
10. the purification process of Erdosteine according to claim 9, which is characterized in that the step 2)In, inorganic acid Including one or more of hydrochloric acid, nitric acid, boric acid, sulfuric acid, carbonic acid and phosphoric acid.
11. the purification process of Erdosteine according to claim 9, which is characterized in that the step 2)In, stirring analysis The temperature for going out solid is 0 DEG C~40 DEG C.
CN201810577239.3A 2018-06-07 2018-06-07 A kind of purification process of Erdosteine Pending CN108640900A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810577239.3A CN108640900A (en) 2018-06-07 2018-06-07 A kind of purification process of Erdosteine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810577239.3A CN108640900A (en) 2018-06-07 2018-06-07 A kind of purification process of Erdosteine

Publications (1)

Publication Number Publication Date
CN108640900A true CN108640900A (en) 2018-10-12

Family

ID=63752002

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810577239.3A Pending CN108640900A (en) 2018-06-07 2018-06-07 A kind of purification process of Erdosteine

Country Status (1)

Country Link
CN (1) CN108640900A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4411909A (en) * 1981-03-19 1983-10-25 Refarmed, Recherches Pharmaceutiques Et Medicales, S.A. [(2-Oxo-3-tetrahydrothienylcarbamoyl)-alkylthio] acetic acids, their salts and esters, a process for preparation thereof and the pharmaceutical compositions containing same
KR100554108B1 (en) * 2003-10-02 2006-02-22 주식회사 한서켐 A process for preparing erdosteine
CN101941963A (en) * 2010-04-22 2011-01-12 浙江康乐药业股份有限公司 Synthesis method of erdosteine

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4411909A (en) * 1981-03-19 1983-10-25 Refarmed, Recherches Pharmaceutiques Et Medicales, S.A. [(2-Oxo-3-tetrahydrothienylcarbamoyl)-alkylthio] acetic acids, their salts and esters, a process for preparation thereof and the pharmaceutical compositions containing same
KR100554108B1 (en) * 2003-10-02 2006-02-22 주식회사 한서켐 A process for preparing erdosteine
CN101941963A (en) * 2010-04-22 2011-01-12 浙江康乐药业股份有限公司 Synthesis method of erdosteine

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
张须学: "《天然药物化学》", 30 September 2012 *
李飞等: "厄多司坦的合成", 《中国医药工业杂志》 *
马丽等: "厄多司坦原料药中有关物质的测定方法", 《药学学报》 *

Similar Documents

Publication Publication Date Title
EP2069290B1 (en) Method for producing 3-(2,2,2-trimethylhydrazinium)propionate dihydrate
CN112533908B (en) Synthetic method of calicheazine
JP5390617B2 (en) Purification method of adefovir dipivoxil
CN110372609A (en) A kind of purification process for disliking La Geli sodium salt
CN107573248A (en) The recovery method of resolving agent R phenyl ethylamines in prepared by R-DHLA
CN102093444A (en) Method for preparing isepamicin and salts thereof
CN105254721A (en) Purification salt conversion method of micafungin
CN108640900A (en) A kind of purification process of Erdosteine
CN107501296B (en) From the method for Cefprozil crystalline mother solution recycling Cefprozil
CN107200758A (en) A kind of preparation method of high-purity clindamycin and clindamycin salt
CN110845349B (en) Purification method of Sacubitril valsartan sodium intermediate
CN109111468A (en) A kind of removal methods of latamoxef carboxyl and hydroxyl protection base
CN111072500B (en) Preparation method of ambroxol hydrochloride
CA3039053C (en) Method for purifying p1,p4-di(uridine 5'-)tetraphosphate
EP2938572B1 (en) Method for purifying borazane
CN105418477A (en) Method for reducing content of diastereoisomer impurity in Ledipasvir intermediate
CN101492400A (en) Method for preparing high-purity acamprosate calcium
CN110818581A (en) Post-treatment method of Sacubitril valsartan sodium intermediate
CN105859546B (en) The method of S-MA is recycled from tomoxetine hydrochloride production waste liquid
TW387886B (en) Process for producing ascorbic acid derivative
JP5438974B2 (en) Process for treating aqueous mixtures containing dipolar aprotic compounds
CN104649948B (en) Cilastatin calcium crystal, preparation method and application thereof
CN103772275B (en) Singulair di-n-propylamine salt crystal formation and preparation method and application
CN107311990A (en) A kind of preparation method of olmesartan medoxomil
JP4659111B2 (en) Method for producing 3-alkenylcephem compound

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
RJ01 Rejection of invention patent application after publication

Application publication date: 20181012

RJ01 Rejection of invention patent application after publication