CN110437187A - A kind of purification process of potassium dehydroandrographolide succinate - Google Patents

A kind of purification process of potassium dehydroandrographolide succinate Download PDF

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Publication number
CN110437187A
CN110437187A CN201910798271.9A CN201910798271A CN110437187A CN 110437187 A CN110437187 A CN 110437187A CN 201910798271 A CN201910798271 A CN 201910798271A CN 110437187 A CN110437187 A CN 110437187A
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CN
China
Prior art keywords
purification process
process according
dehydroandrographolide succinate
potassium dehydroandrographolide
concentration
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Pending
Application number
CN201910798271.9A
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Chinese (zh)
Inventor
李晓琳
范伟川
毛宇龙
张庆坤
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CHENGDU TONGDE PHARMACEUTICAL Co Ltd
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CHENGDU TONGDE PHARMACEUTICAL Co Ltd
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Priority to CN201910798271.9A priority Critical patent/CN110437187A/en
Publication of CN110437187A publication Critical patent/CN110437187A/en
Pending legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07DHETEROCYCLIC COMPOUNDS
    • C07D307/00Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom
    • C07D307/02Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings
    • C07D307/34Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members
    • C07D307/56Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members 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
    • C07D307/60Two oxygen atoms, e.g. succinic anhydride

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The present invention provides a kind of purification process of potassium dehydroandrographolide succinate, by the concentration and additional amount that accurately control ethyl alcohol, reduce impurity generation, and this method is more conducive to industrialization amplification compared with the existing technology, it is lower to equipment requirement, it can be achieved that the closed production of overall process, reduces microbial contamination risk, the quality for guaranteeing product, has practical extending application value.

Description

A kind of purification process of potassium dehydroandrographolide succinate
Technical field
The present invention relates to a kind of purification process of potassium dehydroandrographolide succinate.
Background technique
Potassium dehydroandrographolide succinate is the andrographolide and the resulting Herba Andrographitis of Potassium Suceinate anhydride reactant extracted from Chinese medicine Folium Andrographis Lactone disuccinic acid half ester sylvite, for white to faint yellow solid.With antiviral, antipyretic, antiinflammation.Potassium dehydroandrographolide succinate is because having The features such as significant in efficacy low with toxicity, has been cited as one of first batch of institute of traditional Chinese medicine's first aid indispensability Chinese patent drug in China.As the medicine is facing Bed is widely used, and Reporting of harms increases year by year, main reason is that purity is not high enough.
To improve potassium dehydroandrographolide succinate purity, potassium dehydroandrographolide succinate adverse reaction is reduced, product quality, patent CN1357546A report warp are improved It crosses product quality made of the potassium dehydroandrographolide succinate raw material of ultrafiltration to significantly improve, still, this method purification process is complicated for operation, ultra-filtration process Temperature requirement guarantee that potassium dehydroandrographolide succinate be in solution state, and ultrafiltration temperature control it is more difficult;Secondly, the ultrafiltration membrane mistake of this method It needs to regenerate after filter, needs to retain substance in a large amount of solvent elution film, just can guarantee that film can reuse, but with using Number increases, and the retention efficiency decline of film, equipment loss is big, high production cost, and industrialization is difficult.
Summary of the invention
In order to solve the above technical problems, the present invention provides a kind of purification process of potassium dehydroandrographolide succinate, it includes the following steps:
Potassium dehydroandrographolide succinate crude product is taken, the ethyl alcohol that concentration is 20-60% is added to dissolve, filtering, filtrate adds concentration to be the second of 90-100% Alcoholic solution mixes, and stands crystallization, and filtering, filter residue is dried under reduced pressure, crush to get.
Further, the potassium dehydroandrographolide succinate crude product adds the ethanol solution that concentration is 40% to dissolve.
Further, the mass volume ratio when crude product adds ethanol solution to dissolve is 1g:4-15ml.
Further, described to be dissolved as dissolving by heating, heating temperature is preferably 60 DEG C to 40-80 DEG C.
Further, the filtrate adds concentration to be 95% ethanol solution.
Further, the volume mass ratio for the ethanol solution and crude product that the concentration is 90-100% is 50-100ml:1g, It is preferred that 100ml:1g.
Further, the standing crystallization time 10h or more, preferably 10-24h;The temperature for standing crystallization is normal Temperature.
Further, the drying temperature is 50-70 DEG C, and the time is greater than 6h.
The purification process of potassium dehydroandrographolide succinate of the present invention reduces impurity generation by accurately controlling the concentration and additional amount of ethyl alcohol, This method simultaneously is more conducive to industrialization amplification compared with the existing technology, while equipment requirement is lower, it can be achieved that the closed life of overall process It produces, reduces microbial contamination risk, have practical extending application value.
Obviously, above content according to the present invention is not being departed from according to the ordinary technical knowledge and customary means of this field Under the premise of the above-mentioned basic fundamental thought of the present invention, the modification, replacement or change of other diversified forms can also be made.
The specific embodiment of form by the following examples remakes further specifically above content of the invention It is bright.But the range that this should not be interpreted as to the above-mentioned theme of the present invention is only limitted to example below.It is all to be based on above content of the present invention The technology realized all belongs to the scope of the present invention.
Specific embodiment
The purification process of the potassium dehydroandrographolide succinate of the present invention of embodiment 1
Potassium dehydroandrographolide succinate crude product 10g is taken, 40% ethanol solution 40ml is added, is gradually heated to 60 DEG C, stirs to being completely dissolved, takes advantage of 95% ethyl alcohol of 1000ml is added in heat filtration, filtrate slowly, and stirring to room temperature stands crystallization 10 hours, filtration, and 50 DEG C of filter residue dry Dry 6 hours, it is finely ground after to obtain the final product.
The purification process of the potassium dehydroandrographolide succinate of the present invention of embodiment 2
Potassium dehydroandrographolide succinate crude product 10g is taken, 60% ethanol solution 50ml is added, is gradually heated to 60 DEG C, stirs to being completely dissolved, takes advantage of 90% ethyl alcohol of 900ml is added in heat filtration, filtrate slowly, and stirring to room temperature stands 24 hours, filtration, and 60 DEG C of dryings 8 of filter residue are small When, it is finely ground after to obtain the final product.
The purification process of the potassium dehydroandrographolide succinate of the present invention of embodiment 3
Potassium dehydroandrographolide succinate crude product 10g is taken, 20% ethanol solution 70ml is added, is gradually heated to 80 DEG C, stirs to being completely dissolved, takes advantage of 1000ml100% ethyl alcohol is added in heat filtration, filtrate slowly, and stirring to room temperature stands 10 hours, filtration, 70 DEG C of dryings 10 of filter residue Hour, it is finely ground after to obtain the final product.
Beneficial effects of the present invention are further illustrated below by way of test example.
The potassium dehydroandrographolide succinate that the purification process of the present invention of test example 1 obtains compares
7 batches of potassium dehydroandrographolide succinate crude products are taken respectively, are purified with 6 batches according to 1 method of embodiment, using 1 batch as reference, the production that will be obtained Product sampling, detects related substance, related substance data such as the following table 1.
Obtain from table 1: after the method for the present invention refines, amount of impurities and total amount are substantially reduced in fine work, total miscellaneous It is reduced to by 2.92% 1.0% hereinafter, impurity number is reduced to 6 or so by 14.
To sum up, the purification process of potassium dehydroandrographolide succinate of the present invention reduces impurity by accurately controlling the concentration and additional amount of ethyl alcohol It generates, while equipment requirement is low, it can be achieved that the closed production of overall process, reduces microbial contamination risk, has practical popularization and answer With value.

Claims (8)

1. a kind of purification process of potassium dehydroandrographolide succinate, it is characterised in that: it includes the following steps:
Potassium dehydroandrographolide succinate crude product is taken, the ethanol solution that concentration is 20-60% is added to dissolve, filtering, filtrate adds concentration to be the second of 90-100% Alcoholic solution mixes, and stands crystallization, and filtering, filter residue is dried under reduced pressure, crush to get.
2. purification process according to claim 1, it is characterised in that: the potassium dehydroandrographolide succinate crude product adds concentration to be 40% ethyl alcohol Solution dissolution.
3. purification process according to claim 1 or 2, it is characterised in that: the matter when crude product adds ethanol solution to dissolve Amount volume ratio is 1g:4-15ml.
4. purification process according to claim 1, which is characterized in that described to be dissolved as dissolving by heating, heating temperature is extremely 40-80 DEG C, preferably 60 DEG C.
5. purification process according to claim 1, which is characterized in that the filtrate adds concentration to be 95% ethanol solution.
6. purification process according to claim 1, which is characterized in that ethanol solution that the concentration is 90-100% and thick The volume mass ratio of product is 50-100ml:1g, preferably 100ml:1g.
7. purification process according to claim 1, which is characterized in that the standing crystallization time 10h or more;Preferably 10-24h;The temperature for standing crystallization is room temperature.
8. purification process according to claim 1, which is characterized in that the drying temperature is 50-70 DEG C, and the time is greater than 6h。
CN201910798271.9A 2019-08-27 2019-08-27 A kind of purification process of potassium dehydroandrographolide succinate Pending CN110437187A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910798271.9A CN110437187A (en) 2019-08-27 2019-08-27 A kind of purification process of potassium dehydroandrographolide succinate

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CN110437187A true CN110437187A (en) 2019-11-12

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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102617527A (en) * 2012-03-01 2012-08-01 湖北荷普药业股份有限公司 Method for preparing potassium dehydroandrographolide succinate or potassium sodium dehydroandroan drographolide succinate
CN103087017A (en) * 2013-02-28 2013-05-08 成都倍特药业有限公司 Refinement method of crude potassium sodium dehydroandroan drographolide succinate product
CN103113330A (en) * 2013-02-28 2013-05-22 成都倍特药业有限公司 Andrographolide salifying process
CN103159710A (en) * 2013-04-16 2013-06-19 成都天台山制药有限公司 Antiviral decalin derivate
CN103159709A (en) * 2013-04-16 2013-06-19 成都天台山制药有限公司 Potassium dehydroandrograpolide succinate crystal and preparation method thereof
CN107857747A (en) * 2017-10-16 2018-03-30 广州普星药业有限公司 A kind of preparation method of potassium dehydroandrographolide succinate

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102617527A (en) * 2012-03-01 2012-08-01 湖北荷普药业股份有限公司 Method for preparing potassium dehydroandrographolide succinate or potassium sodium dehydroandroan drographolide succinate
CN103087017A (en) * 2013-02-28 2013-05-08 成都倍特药业有限公司 Refinement method of crude potassium sodium dehydroandroan drographolide succinate product
CN103113330A (en) * 2013-02-28 2013-05-22 成都倍特药业有限公司 Andrographolide salifying process
CN103159710A (en) * 2013-04-16 2013-06-19 成都天台山制药有限公司 Antiviral decalin derivate
CN103159709A (en) * 2013-04-16 2013-06-19 成都天台山制药有限公司 Potassium dehydroandrograpolide succinate crystal and preparation method thereof
CN107857747A (en) * 2017-10-16 2018-03-30 广州普星药业有限公司 A kind of preparation method of potassium dehydroandrographolide succinate

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Application publication date: 20191112