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CN103772465A - Preparation method of high-purity hyodeoxycholic acid - Google Patents

Preparation method of high-purity hyodeoxycholic acid Download PDF

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Publication number
CN103772465A
CN103772465A CN201410019946.2A CN201410019946A CN103772465A CN 103772465 A CN103772465 A CN 103772465A CN 201410019946 A CN201410019946 A CN 201410019946A CN 103772465 A CN103772465 A CN 103772465A
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hyodeoxycholic acid
preparation
acid
water
high purity
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CN201410019946.2A
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CN103772465B (en
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沈惠宾
祝国祥
刘骅
李晓鹤
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Zhongshan Bailing Biotechnology Co ltd
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Zhongshan Belling Biotechnology Co ltd
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Abstract

The invention discloses a preparation method of high-purity hyodeoxycholic acid, which comprises the following steps: taking raw materials, adding strong base and water, saponifying at 95-100 ℃ for 16-24h, cooling to room temperature, standing, siphoning out supernatant fluid, discarding, adding water into lower-layer paste, stirring and dissolving, enhancing acid acidification until Congo red test paper turns blue, adding ethyl acetate, stirring and extracting for 20-50min, standing and layering, discarding water phase, adding ethyl acetate, washing until pH =6-7 of water phase, adding anhydrous sodium sulfate into ethyl acetate phase for dehydration, decolorizing with activated carbon, filtering, concentrating until precipitate is separated out, cooling, filtering or squeezing, and vacuum drying; adding alcohol solvent, stirring for dissolving, slowly adding alkaline organic solvent, stirring, cooling, precipitating, filtering, and drying; adding water and sodium hydroxide, stirring for dissolving, dropwise adding hydrochloric acid with the volume ratio of 1:1, stirring, filtering, and drying to obtain hyodeoxycholic acid. The invention aims to provide a preparation method of hyodeoxycholic acid, which is simple in process, high in product yield and high in purity.

Description

A kind of preparation method of high purity Hyodeoxycholic Acid
Technical field
The present invention relates to a kind of preparation method of high purity Hyodeoxycholic Acid.
Background technology
Hyodeoxycholic Acid (Hyodesoxycholic Acid, HDCA) is a kind of biochemical substances being extensively present in animal bile, and content is 0.1%~0.2%, and chemical name is 3 α, 6 alpha-dihydroxy--5 β-ursodeoxycholic acids, molecular formula C 24h 40o 4, molecular weight is 392.58, easily molten in ethanol, slightly soluble in acetone, and soluble,very slightly in ethyl acetate, chloroform or ether, almost insoluble in water.The effect that HDCA has reducing blood-fat, antispastic and eliminates the phlegm, is used for the treatment of hyperlipidemia, atherosclerosis, trachitis, child virus upper respiratory tract infection clinically, and the maldigestion being caused by liver and gall diseases; Bacillus pertussis, diphtheria corynebacterium, streptococcus aureus etc. are had to certain restraining effect; As the effective constituent in QINGKAILING ZHUSHEJI, through clinical observation, the treatment of acute leukemia is had to good action, experiment in vitro proves that HDCA has cell death inducing, suppresses the effect that cell proliferation is divided.
At present, the content of the Hyodeoxycholic Acid that " Chinese Pharmacopoeia " is written into is greater than 90%, is to adopt determination of acid-basetitration.The content that commercially available Hyodeoxycholic Acid indicates is 98%, fusing point 197-199 ℃, but, show by thin-layer chromatographic analysis, wherein contain the impurity of more amount, further analyze by high performance liquid chromatography, find except Hyodeoxycholic Acid, foreign matter content accounts for 9-15% left and right.
Produce at present Hyodeoxycholic Acid technology and mainly contain following three kinds:
1, ethyl acetate or acetone recrystallization method, though this technology main drawback is to produce the product of fusing point more than 195, product liquid phase purity is low, between Hyodeoxycholic Acid liquid phase purity 88-95%.
2, esterification acetylate derivatization method, although this technology can be produced highly purified Hyodeoxycholic Acid, Hyodeoxycholic Acid purity more than 98%, is used the strong carcinogens such as benzene in technological process, technique is more loaded down with trivial details, is not suitable for suitability for industrialized production.
3, chromatography column method, this technology first goes pig cholic acid crude product to carry out esterification, then goes up silicagel column and separates, and the main drawback of this method is that the production cycle is long, and production efficiency is low.
So, in order to improve Hyodeoxycholic Acid product purity, overcome that existing HDCA purification process technique is loaded down with trivial details, not easy to operate, the production cycle is long, high in cost of production defect, is badly in need of a kind of technological method with advantages such as the large production of the technology of being easy to, cost are low, with short production cycle of exploitation.
Summary of the invention
The object of the invention is, in order to overcome weak point of the prior art, provides a kind of technique simple, and product yield is high, the preparation method of the Hyodeoxycholic Acid that purity is high.
In order to achieve the above object, the present invention adopts following scheme:
A preparation method for high purity Hyodeoxycholic Acid, is characterized in that comprising the following steps:
The preparation of A, Hyodeoxycholic Acid crude product
Get raw material, add highly basic, water, saponification 16-24h at 95-100 ℃, be chilled to room temperature, leave standstill, siphon goes out supernatant liquor and discards, lower floor's paste adds water stirring and dissolving, add strong acid and be acidified to congo-red test paper change indigo plant, add ethyl acetate to stir extraction 20-50min, stratification, water discards, ethyl acetate is added and is washed to water pH=6-7, and ethyl acetate is added to anhydrous sodium sulfate dehydration, activated carbon decolorizing, filter, be concentrated into Precipitation, be cooled to 0-5 ℃, filtered or squeezing, vacuum-drying, obtains Hyodeoxycholic Acid crude product; Wherein said raw material is fresh pig bile or bilirubin tankage;
The preparation of B, Hyodeoxycholic Acid amine salt
Hyodeoxycholic Acid crude product in steps A adds alcoholic solvent, and stirring and dissolving slowly adds alkali organic solvent to stir, and is cooled to 0-5 ℃, has a large amount of Precipitations, and filtration drying obtains Hyodeoxycholic Acid amine salt;
The preparation of C, high purity Hyodeoxycholic Acid
Hyodeoxycholic Acid amine salt in step B adds water, sodium hydroxide, and stirring and dissolving, drips volume ratio 1:1 hydrochloric acid, stirs, and filters, and is dried to obtain Hyodeoxycholic Acid.
The preparation method of a kind of high purity Hyodeoxycholic Acid as above, is characterized in that the tankage of bilirubin described in steps A, highly basic, and the mass ratio of water is bilirubin tankage: highly basic: water=1:0.1-0.5:0.1-0.3.
The preparation method of a kind of high purity Hyodeoxycholic Acid as above, is characterized in that the highly basic described in steps A is potassium hydroxide or potassium hydroxide.
The preparation method of a kind of high purity Hyodeoxycholic Acid as above, is characterized in that strong acid described in steps A is concentrated hydrochloric acid or 50% sulfuric acid.
The preparation method of a kind of high purity Hyodeoxycholic Acid as above, it is characterized in that ethyl acetate described in steps A with the volume mass of, gac than being ethyl acetate (ml): anhydrous sodium sulphate (g): gac (g)=60-100ml:1-3g:1g.
The preparation method of a kind of high purity Hyodeoxycholic Acid as above, it is characterized in that Hyodeoxycholic Acid crude product and alcoholic solvent in step B, the weightmeasurement ratio of alkali organic solvent is Hyodeoxycholic Acid crude product (g): alcoholic solvent (ml): alkali organic solvent (g)=1g:4-8ml:0.2-0.5g.
The preparation method of a kind of high purity Hyodeoxycholic Acid as above, it is characterized in that Hyodeoxycholic Acid amine salt and water in step C, sodium hydroxide, the mass volume ratio of hydrochloric acid is Hyodeoxycholic Acid amine salt (g): water (ml): sodium hydroxide (g): hydrochloric acid (ml)=1:8-12:0.05-0.15:0.4-0.8.
The preparation method of a kind of high purity Hyodeoxycholic Acid as above, is characterized in that described hydrochloric acid is the hydrochloric acid of 1:1 volumetric concentration.
The preparation method of a kind of high purity Hyodeoxycholic Acid as above, is characterized in that alcoholic solvent described in step B is one or more the mixture in ethanol, methyl alcohol, Virahol, the trimethyl carbinol, sec-butyl alcohol.
The preparation method of a kind of high purity Hyodeoxycholic Acid as above, is characterized in that the alkali organic solvent described in step B is one or more the mixture in triethylamine, methylamine, diethylamine, propylamine, TERTIARY BUTYL AMINE, aniline.
In sum, beneficial effect of the present invention:
1, technological operation of the present invention is simple, is easy to industrialized production.
2, solvent environment close friend in the present invention.
3, product yield is high, and product purity is high.
Embodiment
Below in conjunction with embodiment, the present invention is described further:
Embodiment 1
1, the preparation of Hyodeoxycholic Acid crude product
Get bilirubin tankage 100g, add sodium hydroxide or potassium hydroxide 30g, water 200ml, 98 ℃ of saponification 20h, be chilled to room temperature, leave standstill, siphon goes out supernatant liquor and discards, lower floor's paste adds water 200ml, stirring and dissolving, adds concentrated hydrochloric acid and is acidified to congo-red test paper change indigo plant, adds ethyl acetate 800ml to stir extraction 30min, stratification, water discards.Ethyl acetate is added to 800ml and is washed to water pH=6, and ethyl acetate is added to anhydrous sodium sulphate 20g dehydration, 10g activated carbon decolorizing 30min, filter, be concentrated into 160ml left and right, have Precipitation, be cooled to 3 ℃, filter or squeezing vacuum drying Hyodeoxycholic Acid crude product 35g.
2, Hyodeoxycholic Acid amine salt preparation
Hyodeoxycholic Acid crude product 35g, adds dehydrated alcohol 200ml, stirring and dissolving, and slowly stream adds triethylamine 10.5g, stirs 2h, is cooled to 2 degree, has a large amount of Precipitations.Filtration drying obtains Hyodeoxycholic Acid amine salt 20g.
3, the preparation of high purity hdca
Hyodeoxycholic Acid amine salt 20g, adds water 200ml, sodium hydroxide 2g, and stirring and dissolving, to drip volumetric concentration be 1:1 hydrochloric acid 12ml, stirs 1h, filters, the dry Hyodeoxycholic Acid 15g that to obtain, liquid content is more than 99%, fusing point 200-201 ℃.
Embodiment 2
1, the preparation of Hyodeoxycholic Acid crude product
Get bilirubin tankage 100g, add sodium hydroxide or potassium hydroxide 10g, water 10g, 95 ℃ of saponification 16h, be chilled to room temperature, leave standstill, siphon goes out supernatant liquor and discards, lower floor's paste adds water 200ml, stirring and dissolving, adds 50% sulfuric acid acidation to congo-red test paper and becomes blue, adds ethyl acetate 600ml to stir extraction 30min, stratification, water discards.Ethyl acetate is added to 800ml and is washed to water pH=6, and ethyl acetate is added to anhydrous sodium sulphate 10g dehydration, 10g activated carbon decolorizing 30min, filter, be concentrated into 160ml left and right, have Precipitation, be cooled to 0 ℃, filter or squeezing vacuum drying Hyodeoxycholic Acid crude product 34.8g.
2, Hyodeoxycholic Acid amine salt preparation
Hyodeoxycholic Acid crude product 34.8g, adds dehydrated alcohol 200ml, stirring and dissolving, and slowly stream adds triethylamine 10.5g, stirs 2h, is cooled to 0 ℃, has a large amount of Precipitations.Filtration drying obtains Hyodeoxycholic Acid amine salt 19g.
3, the preparation of high purity hdca
Hyodeoxycholic Acid amine salt 19g, adds water 160ml, sodium hydroxide 1g, and stirring and dissolving, to drip volumetric concentration be 1:1 hydrochloric acid 8ml, stirs 1h, filters, the dry Hyodeoxycholic Acid 14.5g that to obtain, liquid content is more than 99%, fusing point 200-201 ℃.
Embodiment 3
1, the preparation of Hyodeoxycholic Acid crude product
Get fresh pig bile 1000ml, add sodium hydroxide or potassium hydroxide 50g, water 300ml, 100 ℃ of saponification 24h, be chilled to room temperature, leave standstill, siphon goes out supernatant liquor and discards, lower floor's paste adds water 200ml, stirring and dissolving, adds concentrated hydrochloric acid and is acidified to congo-red test paper change indigo plant, adds ethyl acetate 1000ml to stir extraction 30min, stratification, water discards.Ethyl acetate is added to 1000ml and is washed to water pH=7, and ethyl acetate is added to anhydrous sodium sulphate 19.5g dehydration, 10g activated carbon decolorizing 30min, filter, be concentrated into 160ml left and right, have Precipitation, be cooled to 5 ℃, filter or squeezing vacuum drying Hyodeoxycholic Acid crude product 34.2g.
2, Hyodeoxycholic Acid amine salt preparation
Hyodeoxycholic Acid crude product 34.2g, adds dehydrated alcohol 250ml, stirring and dissolving, and slowly stream adds triethylamine 15g, stirs 2h, is cooled to 5 degree, has a large amount of Precipitations.Filtration drying obtains Hyodeoxycholic Acid amine salt 19.3g.
3, the preparation of high purity hdca
Hyodeoxycholic Acid amine salt 19.3g, adds water 230ml, sodium hydroxide 2.5g, and stirring and dissolving, to drip volumetric concentration be 1:1 hydrochloric acid 15ml, stirs 1h, filters, the dry Hyodeoxycholic Acid 14.8g that to obtain, liquid content is more than 99%, fusing point 200-201 ℃.
More than show and described ultimate principle of the present invention and principal character and advantage of the present invention.The technician of the industry should understand; the present invention is not restricted to the described embodiments; that in above-described embodiment and specification sheets, describes just illustrates principle of the present invention; without departing from the spirit and scope of the present invention; the present invention also has various changes and modifications, and these changes and improvements all fall in the claimed scope of the invention.The claimed scope of the present invention is defined by appending claims and equivalent thereof.

Claims (10)

1. a preparation method for high purity Hyodeoxycholic Acid, is characterized in that comprising the following steps:
The preparation of A, Hyodeoxycholic Acid crude product
Get raw material, add highly basic, water, saponification 16-24h at 95-100 ℃, be chilled to room temperature, leave standstill, siphon goes out supernatant liquor and discards, lower floor's paste adds water stirring and dissolving, add strong acid and be acidified to congo-red test paper change indigo plant, add ethyl acetate to stir extraction 20-50min, stratification, water discards, ethyl acetate is added and is washed to water pH=6-7, and ethyl acetate is added to anhydrous sodium sulfate dehydration, activated carbon decolorizing, filter, be concentrated into Precipitation, be cooled to 0-5 ℃, filtered or squeezing, vacuum-drying, obtains Hyodeoxycholic Acid crude product; Wherein said raw material is fresh pig bile or bilirubin tankage;
The preparation of B, Hyodeoxycholic Acid amine salt
Hyodeoxycholic Acid crude product in steps A adds alcoholic solvent, and stirring and dissolving slowly adds alkali organic solvent to stir, and is cooled to 0-5 ℃, has a large amount of Precipitations, and filtration drying obtains Hyodeoxycholic Acid amine salt;
The preparation of C, high purity Hyodeoxycholic Acid
Hyodeoxycholic Acid amine salt in step B adds water, sodium hydroxide, and stirring and dissolving, drips volume ratio 1:1 hydrochloric acid, stirs, and filters, and is dried to obtain Hyodeoxycholic Acid.
2. the preparation method of a kind of high purity Hyodeoxycholic Acid according to claim 1, is characterized in that the tankage of bilirubin described in steps A, highly basic, and the mass ratio of water is bilirubin tankage: highly basic: water=1:0.1-0.5:0.1-0.3.
3. the preparation method of a kind of high purity Hyodeoxycholic Acid according to claim 1, is characterized in that the highly basic described in steps A is potassium hydroxide or potassium hydroxide.
4. the preparation method of a kind of high purity Hyodeoxycholic Acid according to claim 1, is characterized in that strong acid described in steps A is concentrated hydrochloric acid or 50% sulfuric acid.
5. the preparation method of a kind of high purity Hyodeoxycholic Acid according to claim 1, it is characterized in that ethyl acetate described in steps A with the volume mass of, gac than being ethyl acetate (ml): anhydrous sodium sulphate (g): gac (g)=60-100ml:1-3g:1g.
6. the preparation method of a kind of high purity Hyodeoxycholic Acid according to claim 1, it is characterized in that Hyodeoxycholic Acid crude product and alcoholic solvent in step B, the weightmeasurement ratio of alkali organic solvent is Hyodeoxycholic Acid crude product (g): alcoholic solvent (ml): alkali organic solvent (g)=1g:4-8ml:0.2-0.5g.
7. the preparation method of a kind of high purity Hyodeoxycholic Acid according to claim 1, it is characterized in that Hyodeoxycholic Acid amine salt and water in step C, sodium hydroxide, the mass volume ratio of hydrochloric acid is Hyodeoxycholic Acid amine salt (g): water (ml): sodium hydroxide (g): hydrochloric acid (ml)=1:8-12:0.05-0.15:0.4-0.8.
8. according to the preparation method of a kind of high purity Hyodeoxycholic Acid described in claim 1 or 7, it is characterized in that described hydrochloric acid is the hydrochloric acid of 1:1 volumetric concentration.
9. according to the preparation method of a kind of high purity Hyodeoxycholic Acid described in claim 1 or 6, it is characterized in that alcoholic solvent described in step B is one or more the mixture in ethanol, methyl alcohol, Virahol, the trimethyl carbinol, sec-butyl alcohol.
10. according to the preparation method of a kind of high purity Hyodeoxycholic Acid described in claim 1 or 6, it is characterized in that the alkali organic solvent described in step B is one or more the mixture in triethylamine, methylamine, diethylamine, propylamine, TERTIARY BUTYL AMINE, aniline.
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CN104152387A (en) * 2014-08-21 2014-11-19 曹国华 Bile salt, preparation method thereof, and application of the bile salt in production of dry powder bacterium culture medium
CN105140490A (en) * 2015-09-28 2015-12-09 中南大学 Preparation method of lithium-sulfur battery flexible positive electrode
CN105175472A (en) * 2015-08-19 2015-12-23 安徽科宝生物工程有限公司 Refining method for high-content hyodeoxycholic acid
CN105541953A (en) * 2016-03-15 2016-05-04 成都市新功生物科技有限公司 Recrystallization purification method for high-purity obeticholic acid
CN106279008A (en) * 2015-05-19 2017-01-04 浙江九洲药业股份有限公司 A kind of purifying process of sulfasalazine
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CN107549123A (en) * 2017-10-18 2018-01-09 湖北聚注通用技术研究有限公司 A kind of scorpion breeding method
CN110256517A (en) * 2019-07-19 2019-09-20 中山百灵生物技术有限公司 A method of producing high-purity chenodeoxy cholic acid from pig's bile or leftover bits and pieces
CN111961105A (en) * 2020-09-23 2020-11-20 安徽科宝生物工程有限公司 Method for separating hyodeoxycholic acid from pig bile paste by extraction method
CN112094883A (en) * 2020-09-28 2020-12-18 常德云港生物科技有限公司 Method for preparing beta-hyodeoxycholic acid by microbial transformation

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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104152387A (en) * 2014-08-21 2014-11-19 曹国华 Bile salt, preparation method thereof, and application of the bile salt in production of dry powder bacterium culture medium
CN106279008A (en) * 2015-05-19 2017-01-04 浙江九洲药业股份有限公司 A kind of purifying process of sulfasalazine
CN105175472A (en) * 2015-08-19 2015-12-23 安徽科宝生物工程有限公司 Refining method for high-content hyodeoxycholic acid
CN105140490A (en) * 2015-09-28 2015-12-09 中南大学 Preparation method of lithium-sulfur battery flexible positive electrode
WO2017137931A1 (en) 2016-02-10 2017-08-17 Dr. Reddy’S Laboratories Limited Amine salt of obeticholic acid
EP3414256B1 (en) 2016-02-10 2022-01-19 Dr. Reddy's Laboratories Limited Purification process involving amine salt of obeticholic acid
CN105541953A (en) * 2016-03-15 2016-05-04 成都市新功生物科技有限公司 Recrystallization purification method for high-purity obeticholic acid
CN107549123A (en) * 2017-10-18 2018-01-09 湖北聚注通用技术研究有限公司 A kind of scorpion breeding method
CN110256517A (en) * 2019-07-19 2019-09-20 中山百灵生物技术有限公司 A method of producing high-purity chenodeoxy cholic acid from pig's bile or leftover bits and pieces
CN110256517B (en) * 2019-07-19 2021-03-09 中山百灵生物技术股份有限公司 A method for producing high-purity chenodeoxycholic acid from pig bile or leftovers
CN111961105A (en) * 2020-09-23 2020-11-20 安徽科宝生物工程有限公司 Method for separating hyodeoxycholic acid from pig bile paste by extraction method
CN112094883A (en) * 2020-09-28 2020-12-18 常德云港生物科技有限公司 Method for preparing beta-hyodeoxycholic acid by microbial transformation

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