CN103319495A - Preparation method of high-purity carnosol - Google Patents

Preparation method of high-purity carnosol Download PDF

Info

Publication number
CN103319495A
CN103319495A CN2013103050811A CN201310305081A CN103319495A CN 103319495 A CN103319495 A CN 103319495A CN 2013103050811 A CN2013103050811 A CN 2013103050811A CN 201310305081 A CN201310305081 A CN 201310305081A CN 103319495 A CN103319495 A CN 103319495A
Authority
CN
China
Prior art keywords
carnosol
organic solvent
preparation
high purity
elutriant
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
CN2013103050811A
Other languages
Chinese (zh)
Other versions
CN103319495B (en
Inventor
刘海龙
高政
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.)
Gao Zheng
Liu Hailong
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN201310305081.1A priority Critical patent/CN103319495B/en
Publication of CN103319495A publication Critical patent/CN103319495A/en
Application granted granted Critical
Publication of CN103319495B publication Critical patent/CN103319495B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Medicines Containing Plant Substances (AREA)
  • Saccharide Compounds (AREA)

Abstract

The invention relates to a preparation method of a natural active compound. The preparation method provided by the invention comprises the following steps: 1, extracting a dry carnosol-containing raw material per kilogram by the use of 3-10 liters of a lipophilic organic solvent for 2-5 times, merging extracts, and condensing to obtain a carnosol-containing extract or solid; 2, dissolving by the use of a 10-90% hydrophilic organic solvent, filtering and precipitating, and carrying out macroreticular resin refining processing on a filtrate to obtain a carnosol-containing precipitate; 3, dissolving the precipitate by the use of a mixed lipophilic organic solvent, standing, precipitating a precipitate; and filtering the precipitate to obtain a carnosol crude product; and 4, crystallizing by the use of a hydrophilic organic solvent so as to obtain high-purity carnosol crystals with the HPLC detection content being more than 95%. The preparation method provided by the invention has advantages of simple operation process and controllable cost, and is suitable for large-scale preparation and production of high-purity carnosol.

Description

The preparation method of high purity carnosol
Technical field
The present invention relates to a kind of preparation method of natural radioactivity compound.
Background technology
Rosmarinus officinalis ( Rosmarinus officinalisL.) etc. the phenol diterpene-kind compounds such as carnosol that contain in the plant are the natural antioxidantss of generally acknowledging in recent years, are widely used in fields such as foodstuffs industry, day chemical industry and medicines and health protection; And studies show that carnosol can have antineoplastic action by suppressing the NF-kB passage, so it is a new drug research person natural radioactivity compound looking at of parent relatively in recent years.
About the preparation of carnosol, among the Chinese patent CN101040901A, by Rosmarinus officinalis is put forward methods such as taking, putting cryoprecipitate, activated carbon decolorizing with solvent, make the rosemary extract that contains carnosol 5-12%; Among the Chinese patent CN101402864A, by to Rosmarinus officinalis earlier with the vapor extraction essential oil, organic solvent extracts processes such as residue, macroporous adsorbent resin and silica gel column chromatography again, obtains containing carnosol and the rosemary antioxidant of Salvin sum more than 50%; Among the Chinese patent CN102031116A, by to Rosmarinus officinalis earlier with the vapor extraction essential oil, again organic solvent extract residue obtain extract, with CO 2This extract of supercritical extraction obtains containing the main rosemary antioxidant of oxidation-resistant active ingredient more than 80% such as carnosol, Salvin, rosmarinic acid.The product that these methods obtain all is the mixture that contains a certain amount of carnosol, and for research and the application of a monomer reactivity material, these mixtures do not meet standard and requirement.Among the Chinese patent CN102115442A; by Rosmarinus officinalis is extracted, carries out means such as phosphoric acid-silica gel column chromatography under nitrogen protection with solvent; obtain content and reach 92% carnosol; though this method can obtain the carnosol of higher degree, used condition is too harsh, and silica gel is wanted phosphorylation; make phosphoric acid-silica gel; the nitrogen protection of chromatography process need is difficult to carry out a large amount of preparation carnosols, also is difficult to promote and this special methods of practical application.Restrain sharp David Stauffer Wei Ruili at patent CN101835782A, CN101835783A, and among the CN101835783A, means such as the oxidation by Salvin being carried out hydrogen peroxide or peroxy acid, acetic acid crystallization obtain the carnosol more than 90%.This method gained carnosol content height, flow process is fairly simple, and is better than above-mentioned other several method.But needing highly purified Salvin is raw material; Salvin also is the active compound that extraction separation obtains from Rosmarinus officinalis etc. plant; obtain highly purified carnosol if carry out peroxidation with highly purified Salvin; then its source will be limited greatly; and manufacturing cost is very high; if make carnosol with the Salvin that purity is not high; the carnosol yield that then prepares is low; be difficult to obtain a large amount of target substances; therefore, obtain the method for highly purified carnosol with the Salvin peroxidation, aspect mass-producing and cost control; very big difficulty is arranged, be difficult to practical application.
Summary of the invention
The objective of the invention is at preparation high purity carnosol in the prior art exist not enough and difficult, propose that a kind of flow process is simple, cost is controlled, be fit to the preparation method of the high purity carnosol of large-scale production.
The preparation method of high purity carnosol of the present invention is made up of following steps:
One, with the raw material that contains carnosol of drying, each kilogram rises the lipotropy organic solvent with 3-10 and extracts 2-5 time, and united extraction liquid concentrates the medicinal extract or the solid that obtain containing carnosol;
Two, the described medicinal extract of each kilogram or solid, rise the wetting ability organic solvent dissolving of 10-90% again with 5-10, filtering-depositing, filtrate is carried out the macroporous adsorbent resin refinement treatment, the elutriant Fractional Collections, merge carnosol content greater than the total elutriant of elutriant conduct of 4g/L, concentrate total elutriant to solvent-free flavor; Add the concentrated solution volume again than 1-3 water doubly, stir, precipitation, filter the throw out of carnosol;
Three, the described throw out of each kilogram rises the lipotropy organic solvent dissolving that mixes with 5-10 again, places, and separates out precipitation; Filtering-depositing gets the carnosol crude product;
Four, the described carnosol crude product of each kilogram with the wetting ability organic solvent crystallization of 8-12 liter, obtains with the HPLC detection level at the high purity carnosol crystal more than 95% again.
The described raw material that contains carnosol of step 1, refer to Rosmarinus officinalis ( Rosmarinus officinalisL.), Salvia japonica Thunb., the red sage root etc. contain the plant of carnosol, wherein contain carnosol and are not less than 0.1% to detect HPLC, or the extract of these plants, wherein contain carnosol and be not less than 1% to detect HPLC.
The described lipotropy organic solvent of step 1, refer to boiling point be lower than 100 degrees centigrade, with the organic solvent that layering can take place after water mixes, as sherwood oil, benzene, ether, methylene dichloride, chloroform, ethyl acetate etc.
The described wetting ability organic solvent of step 2 refers to that boiling point is lower than 100 degrees centigrade, organic solvent that can be miscible with water, as acetone, ethanol, methyl alcohol, Virahol etc.Described 10-90% is the volume percent aqueous solution.More superior is the 40-70% volume percent aqueous solution.
The described macroporous adsorbent resin of step 2 refers to wherein any one of D101, AB-8, HZ818.
The present invention adopts the lipotropy organic solvent that the raw material that contains carnosol is extracted, and fat-soluble component is dissolved in the organic solvent, has fully effectively reduced the interference of big polar material such as polysaccharide, protein in the plant; And then will extract concentrated solution wetting ability organic solvent dissolving, filtering-depositing is removed with carnosol polarity and is differed bigger little polar material, has been further purified macroporous resin upper prop liquid, attached with parsing by the macroporous resin selective adsorption, Fractional Collections contains the carnosol lower column liquid; Use lipotropy organic solvent and the fractional precipitation of wetting ability organic solvent and crystallization treatment again, both got the high purity carnosol crystal more than 95%.
The method of the invention can be from the lower raw material of carnosol content, and the disposable carnosol content that obtains is higher than 95% high purity carnosol crystal, is that this field can not be accomplished at present.Present method operating process is simple, cost is controlled, preparation and the production high purity carnosol of suitable mass-producing.
Embodiment
Embodiment 1:
Get dry Rosmarinus officinalis branches and leaves 2000g, add sherwood oil 14L, refluxing extraction 3 times, each 3 hours, merge No. 3 times extracting solution, concentrate and reclaim sherwood oil, get medicinal extract; With medicinal extract with 40% dissolve with ethanol, remove by filter insolubles, get the 1000ml mother liquor as adsorption liquid, adsorb with 500ml D101 macroporous adsorbent resin, after finishing, absorption leads to wash-out with the 1000ml purified water, use 1500ml 90% ethanolic soln wash-out again, elutriant is divided into 6 sections, merges middle 4 parts; The elutriant that merges is evaporated to 100ml, adds water 200ml, stirs and separates out precipitation, places 3 hours; Centrifugal the precipitation that contains carnosol; Precipitation 200ml acetic acid ethyl dissolution to wherein adding the 200ml sherwood oil, stirs, and separates out precipitation; Filter the carnosol crude product, this crude product obtains the carnosol crystallization with the crystallization of 800ml dehydrated alcohol; Filtration, drying obtain crystallization 13.6 g, and it is 96.1% that HPLC detects carnosol content.
Embodiment 2:
Get dry Rosmarinus officinalis branches and leaves 2000g, add methylene dichloride 10L, refluxing extraction 3 times, each 3 hours, merge No. 3 times extracting solution, concentrate and reclaim methylene dichloride, get medicinal extract; With medicinal extract with 60% dissolve with ethanol, remove by filter insolubles, get the 1000ml mother liquor as adsorption liquid, adsorb with 500ml AB-8 macroporous adsorbent resin, after finishing, absorption leads to wash-out with the 1000ml purified water, use 2000ml 80% ethanolic soln wash-out again, elutriant is divided into 6 sections, merges middle 4 parts; The elutriant that merges is evaporated to 150ml, adds water 200ml, stirs and separates out precipitation, places 5 hours; Centrifugal the precipitation that contains carnosol; Precipitation, stirs to wherein adding the 200ml sherwood oil with the dissolving of 150ml methylene dichloride, separates out precipitation; Filter the carnosol crude product, this crude product obtains the carnosol crystallization with the 700ml methanol crystallization; Filtration, drying obtain crystallization 14.7 g, and it is 95.3% that HPLC detects carnosol content.
Embodiment 3:
Taking by weighing rosemary extract 500g(HPLC mensuration carnosol content is 5.7%), dissolve with ethanol with 2500ml 60%, remove by filter insolubles, mother liquor is as adsorption liquid, adsorb with 800ml HZ818 macroporous adsorbent resin, with the logical wash-out of 2000ml purified water, use 2000ml 90% ethanolic soln wash-out again after absorption is finished, elutriant is divided into 6 sections, merges middle 4 parts; The elutriant that merges is evaporated to 300ml, adds water 350ml, stirs and separates out precipitation, places 3 hours; Centrifugal the precipitation that contains carnosol; Precipitation 300ml acetic acid ethyl dissolution to wherein adding the 200ml sherwood oil, stirs, and separates out precipitation; Filter the carnosol crude product, this crude product obtains the carnosol crystallization with the 1000ml methanol crystallization; Filtration, drying obtain crystallization 23.9 g, and it is 96.3% that HPLC detects carnosol content.
Embodiment 4:
Taking by weighing Radix Salviae Miltiorrhizae extract 500g(HPLC mensuration carnosol content is 3.1%), dissolve with ethanol with 3000ml 50%, remove by filter insolubles, mother liquor adsorbs with 1000ml D101 macroporous adsorbent resin, after finishing, absorption leads to wash-out with the 2000ml purified water, use 2000ml 90% ethanolic soln wash-out again, elutriant is divided into 6 sections, merges middle 4 parts; The elutriant that merges is evaporated to 500ml, adds water 500ml, stirs and separates out precipitation, places 3 hours; Centrifugal the precipitation that contains carnosol; Precipitation 200ml acetic acid ethyl dissolution to wherein adding the 150ml sherwood oil, stirs, and separates out precipitation; Filter the carnosol crude product, this crude product obtains the carnosol crystallization with the crystallization of 600ml dehydrated alcohol; Filtration, drying obtain crystallization 12.2 g, and it is 95.8% that HPLC detects carnosol content.
Embodiment 5:
Taking by weighing rosemary extract 500g(HPLC mensuration carnosol content is 17.0%), dissolve with ethanol with 4000ml 60%, remove by filter insolubles, mother liquor adsorbs with 1500ml D101 macroporous adsorbent resin, after finishing, absorption leads to wash-out with the 4000ml purified water, use 4000ml 90% ethanolic soln wash-out again, elutriant is divided into 6 sections, merges middle 4 parts; The elutriant that merges is evaporated to 800ml, adds water 1000ml, stirs and separates out precipitation, places 4 hours; Centrifugal the precipitation that contains carnosol; Precipitation 1000ml acetic acid ethyl dissolution to wherein adding the 800ml sherwood oil, stirs, and separates out precipitation; Filter the carnosol crude product, this crude product obtains the carnosol crystallization with the 4500ml methanol crystallization; Filtration, drying obtain crystallization 73.3 g, and it is 96.8% that HPLC detects carnosol content.
The HPLC detection method:
Test set: Tianjin, island-LC-10AT vp plus
Chromatographic column: Wondasil TMC18 5nm 4.6*250mm
Chromatographic condition:
Mobile phase A: 0.1% phosphate aqueous solution (crossing the 0.45nm filtering membrane)
Mobile phase B: acetonitrile (chromatographic grade)
A:B=40:60
Flow velocity: 0.8ml/mine
Detect wavelength: 285nm
Appearance time: about 14mine
Trial-product and reference substance obtain solution: hplc grade methanol dissolving.

Claims (7)

1. the preparation method of a high purity carnosol is characterized in that being made up of following steps:
One, with the raw material that contains carnosol of drying, each kilogram rises the lipotropy organic solvent with 3-10 and extracts 2-5 time, and united extraction liquid concentrates the medicinal extract or the solid that obtain containing carnosol;
Two, the described medicinal extract of each kilogram or solid, rise the wetting ability organic solvent dissolving of 10-90% again with 5-10, filtering-depositing, filtrate is carried out the macroporous adsorbent resin refinement treatment, the elutriant Fractional Collections, merge carnosol content greater than the total elutriant of elutriant conduct of 4g/L, concentrate total elutriant to solvent-free flavor; Add the concentrated solution volume again than 1-3 water doubly, stir, precipitation, filter the throw out of carnosol;
Three, the described throw out of each kilogram rises the lipotropy organic solvent dissolving that mixes with 5-10 again, places, and separates out precipitation; Filtering-depositing gets the carnosol crude product;
Four, the described carnosol crude product of each kilogram with the wetting ability organic solvent crystallization of 8-12 liter, obtains with the HPLC detection level at the high purity carnosol crystal more than 95% again.
2. the preparation method of high purity carnosol as claimed in claim 1, it is characterized in that the described raw material that contains carnosol of step (), refer to contain the plant of carnosol, wherein contain carnosol and be not less than 0.1% to detect HPLC, or the extract of these plants, wherein contain carnosol and be not less than 1% to detect HPLC.
3. the preparation method of high purity carnosol as claimed in claim 1 is characterized in that the described lipotropy organic solvent of step (), refer to boiling point be lower than 100 degrees centigrade, with the organic solvent that layering can take place after water mixes.
4. the preparation method of high purity carnosol as claimed in claim 1 is characterized in that the described wetting ability organic solvent of step (two), refers to that boiling point is lower than 100 degrees centigrade, organic solvent that can be miscible with water.
5. the preparation method of high purity carnosol as claimed in claim 1 is characterized in that the described macroporous adsorbent resin of step (two), refers to wherein any one of D101, AB-8, HZ818.
6. the preparation method of high purity carnosol as claimed in claim 2 is characterized in that the described plant that contains carnosol is Rosmarinus officinalis.
7. the preparation method of high purity carnosol as claimed in claim 2 is characterized in that the described plant that contains carnosol is Salvia japonica Thunb..
CN201310305081.1A 2013-07-20 2013-07-20 The preparation method of high-purity carnosol Expired - Fee Related CN103319495B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201310305081.1A CN103319495B (en) 2013-07-20 2013-07-20 The preparation method of high-purity carnosol

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201310305081.1A CN103319495B (en) 2013-07-20 2013-07-20 The preparation method of high-purity carnosol

Publications (2)

Publication Number Publication Date
CN103319495A true CN103319495A (en) 2013-09-25
CN103319495B CN103319495B (en) 2016-03-02

Family

ID=49188583

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201310305081.1A Expired - Fee Related CN103319495B (en) 2013-07-20 2013-07-20 The preparation method of high-purity carnosol

Country Status (1)

Country Link
CN (1) CN103319495B (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104530074A (en) * 2015-01-07 2015-04-22 浙江泰康生物科技有限公司 Method for extracting carnosol from complete salvia
CN105696194A (en) * 2016-04-05 2016-06-22 东华大学 Preparation method of carnosol and chitosan self-assembly core sheath composite nanometer fiber mat
CN105696195A (en) * 2016-04-05 2016-06-22 东华大学 Preparation method of carnosol and chitosan composite nanometer fiber mat
CN111440184A (en) * 2018-01-30 2020-07-24 北京联合大学 Method for preparing high-purity carnosol
CN114988983A (en) * 2022-06-09 2022-09-02 新疆师范大学 Method for separating sclareol from sclareol extract

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TR201912820A2 (en) * 2019-08-26 2021-03-22 Tuerkiye Bilimsel Ve Teknolojik Arastirma Kurumu Tuebitak CARNOSIC ACID, CARNOSOL AND ROSMARINIC ACID ISOLATION METHOD

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101402864A (en) * 2008-11-21 2009-04-08 中国农业大学 Method for producing oxidation resistant product from rosemary
WO2009053026A2 (en) * 2007-10-22 2009-04-30 Dsm Ip Assets B.V. Process for producing carnosol from carnosic acid using hydrogen peroxide or peracids
CN102115442A (en) * 2011-01-05 2011-07-06 广州和博生物科技有限公司 Method for separating carnosic acid from rosemary leaf extract

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009053026A2 (en) * 2007-10-22 2009-04-30 Dsm Ip Assets B.V. Process for producing carnosol from carnosic acid using hydrogen peroxide or peracids
CN101402864A (en) * 2008-11-21 2009-04-08 中国农业大学 Method for producing oxidation resistant product from rosemary
CN102115442A (en) * 2011-01-05 2011-07-06 广州和博生物科技有限公司 Method for separating carnosic acid from rosemary leaf extract

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
李玉山: "迷迭香的综合提取工艺研究", 《化学与黏合》 *

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104530074A (en) * 2015-01-07 2015-04-22 浙江泰康生物科技有限公司 Method for extracting carnosol from complete salvia
CN105696194A (en) * 2016-04-05 2016-06-22 东华大学 Preparation method of carnosol and chitosan self-assembly core sheath composite nanometer fiber mat
CN105696195A (en) * 2016-04-05 2016-06-22 东华大学 Preparation method of carnosol and chitosan composite nanometer fiber mat
CN111440184A (en) * 2018-01-30 2020-07-24 北京联合大学 Method for preparing high-purity carnosol
CN111440184B (en) * 2018-01-30 2021-08-27 北京联合大学 Method for preparing high-purity carnosol
CN114988983A (en) * 2022-06-09 2022-09-02 新疆师范大学 Method for separating sclareol from sclareol extract

Also Published As

Publication number Publication date
CN103319495B (en) 2016-03-02

Similar Documents

Publication Publication Date Title
CN103319495B (en) The preparation method of high-purity carnosol
CN101559088B (en) Production technique of andrographolide and neoandrographolide, dehydroanddrographolide, oxyandrographolide
CN103393671B (en) The extracting and purifying method of bilobalide
CN107129505B (en) The industrial production process of lactone element monomers in a kind of ginkgo leaf purification
CN104435226B (en) Fevervine extract and application thereof
CN101274953B (en) Method for extracting corosolic acid from plant
CN105132172B (en) A method of preparing tobacco orrisroot Flavonoid substances from orrisroot
CN105294623B (en) A kind of Sesquiterpene lactones compound, its preparation method and application
CN111960930A (en) Method for separating and purifying cannabidiol from industrial cannabis sativa leaves
CN103254225B (en) A kind of method adopting ion liquid abstraction separating and purifying phosphatidyl choline
CN103058978B (en) Method for synchronized preparation of pinocembrin and 2', 4'-dihydroxy chalcone from oxytropis falcate bunge
CN102875450A (en) Technological method for extracting 1-deoxynojirimycin from mulberry leaf
CN103665079A (en) Separation and purification method of pachymic acid monomer
CN102078341B (en) High-purity ginkgo flavone and composition thereof
CN102533431B (en) Method for continuously extracting and separating sea buckthorn oil and isorhamnetin from sea buckthorn pulps
CN103288870B (en) A kind of preparation method of injection stage lecithin in high purity
CN104398619B (en) Fevervine extract and application thereof
CN106117191B (en) A method of efficiently separating puerarin purification
CN102145043A (en) Medicinal composition for treating cardiovascular diseases, and preparation and preparation method thereof
CN104474068B (en) Fevervine extract and application thereof
CN1253456C (en) Improved process for preparing podophyllotoxin from Chinese podophyllum root
WO2019113861A1 (en) Ginkgo biloba extract medicinal raw material and preparation method therefor
CN104961667B (en) A kind of purification process of sulforaphen
CN107375356A (en) Method that is a kind of while preparing high-purity total flavonoids and ginkgolides
CN103265572B (en) A kind of method adopted containing carboxyl/polyhydroxyl solvents extraction separation purification phosphatidylcholine

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C41 Transfer of patent application or patent right or utility model
CB03 Change of inventor or designer information

Inventor after: Liu Hailong

Inventor after: Gao Zheng

Inventor after: Xiao Li

Inventor before: Liu Hailong

Inventor before: Gao Zheng

COR Change of bibliographic data
TA01 Transfer of patent application right

Effective date of registration: 20160114

Address after: 650033, room 5, floor 690, comprehensive business building, Jinding Science and Technology Park, No. 502, Xuefu Road, Kunming, Yunnan

Applicant after: Gao Zheng

Applicant after: Xiao Li

Address before: 650033, room 5, floor 690, comprehensive business building, Jinding Science and Technology Park, No. 502, Xuefu Road, Kunming, Yunnan

Applicant before: Gao Zheng

C14 Grant of patent or utility model
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20200615

Address after: 650033, room 5, floor 690, comprehensive business building, Jinding Science and Technology Park, No. 502, Xuefu Road, Kunming, Yunnan

Co-patentee after: Liu Hailong

Patentee after: Gao Zheng

Address before: 650033, room 5, floor 690, comprehensive business building, Jinding Science and Technology Park, No. 502, Xuefu Road, Kunming, Yunnan

Co-patentee before: Xiao Li

Patentee before: Gao Zheng

CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20160302