CN101935278A - Method for extracting, separating and purifying chlorogenic acid through folium cortex eucommiae - Google Patents

Method for extracting, separating and purifying chlorogenic acid through folium cortex eucommiae Download PDF

Info

Publication number
CN101935278A
CN101935278A CN2009101479281A CN200910147928A CN101935278A CN 101935278 A CN101935278 A CN 101935278A CN 2009101479281 A CN2009101479281 A CN 2009101479281A CN 200910147928 A CN200910147928 A CN 200910147928A CN 101935278 A CN101935278 A CN 101935278A
Authority
CN
China
Prior art keywords
chlorogenic acid
purifying
solution
separation
extraction
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
CN2009101479281A
Other languages
Chinese (zh)
Inventor
周大捷
吴美娟
丁松法
周宗明
乔玉环
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.)
Fengning Jingbei No.1 Grasslands Original Ecological Food Technology Development Co., Ltd.
Original Assignee
周大捷
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 周大捷 filed Critical 周大捷
Priority to CN2009101479281A priority Critical patent/CN101935278A/en
Publication of CN101935278A publication Critical patent/CN101935278A/en
Pending legal-status Critical Current

Links

Abstract

The invention relates to a method for extracting, separating and purifying chlorogenic acid through folium cortex eucommiae, which comprises the following steps of: A. preparing a chlorogenic acid extracting solution; B. separating the chlorogenic acid extracting solution; C. purifying the chlorogenic acid; and D. preparing a chlorogenic acid fine product. The invention effectively overcomes the defects of complicated working procedures, complex operation, more consumed solvents, difficult material regeneration, more generated sewage, high energy consumption and relatively higher extraction cost during the extraction process of the chlorogenic acid by combining an ultrafiltration membrane and a nanofiltration membrane technology with a macroporous absorbent resin purification technology; and the invention provides a new method for extracting, separating and purifying the chlorogenic acid through the folium cortex eucommiae, and the method has the advantages of simple process, low cost, low energy consumption and used material regeneration and recycling, can not generate pollution and is beneficial to industrialized production.

Description

Method by Folium Eucommiae extraction, separation, purifying chlorogenic acid
The present invention relates to a kind of method of manufacturing chlorogenic acid, particularly by the method for Folium Eucommiae extraction, separation, purifying chlorogenic acid.
Chlorogenic acid (chlorogenic acid is called for short CA) is a kind of depside, belongs to phenolic compound.Have effects such as antibiotic, antiviral, leukocyte increasing, hepatic cholagogic, antitumor, hypotensive, reducing blood-fat, removing free radical.Thereby in the application of dietotherapy and pharmacy industry, be subjected to people and pay much attention to.
Existingly adopt organic solvent under acidic conditions, to extract by Folium Eucommiae chlorogenic acid extracting product extraction process, have following shortcoming: the sewage that product purity is low, complex procedures, complex operation, consumption solvent are many, material is difficult for regeneration, produce is more, energy consumption height, extraction cost compare higher, and the purity of end product can only arrive 60%.
The purpose of this invention is to provide a kind of is raw material with the Folium Eucommiae, prepares the method for chlorogenic acid through extraction, separation, purifying.It is more that it can solve the sewage that the consumption solvent is many in the prior art, material is difficult for regeneration, produce, the shortcoming that energy consumption is high.The present invention has been owing to used ultrafiltration, resin isolation and nanofiltration, and its separation, purification process technology are easy, and cost is low, and material therefor can regeneration, does not produce pollution, is beneficial to suitability for industrialized production.The technical process of chlorogenic acid is in the extraction separation Folium Eucommiae:
Folium Eucommiae → drying and crushing → ethanolic soln refluxing extraction → remove under reduced pressure ethanol → flocculation impurity elimination → decolouring → XDA-5 resin absorption → pure water wash-out sugar and Geniposidic acid → 20% ethanol elution obtain chlorogenic acid crude product → decompression recycling ethanol → mistake 150Da nanofiltration membrane, and concentrated → ethyl alcohol recrystallization → cryodrying gets the chlorogenic acid elaboration.It comprises the steps:
A. prepare the chlorogenic acid extracting solution
The Folium Eucommiae of drying and crushing is crossed 60 mesh sieves, be added in the aqueous ethanolic solution, transfer PH=4, heated and stirred is extracted, and filters, and filtrate decompression is steamed ethanol, gets the chlorogenic acid aqueous extract.
B. the separation of chlorogenic acid extracting solution
Filtrate adds decolorizing with activated carbon, crosses ultra-filtration membrane deproteinize, polysaccharide, gets chlorogenic acid crude product aqueous extract.
C. purifying chlorogenic acid:
Chlorogenic acid crude product solution absorption with macroporous adsorbent resin with acidiferous ethanolic soln desorption, gets the pure product solution of chlorogenic acid.
D. prepare the chlorogenic acid elaboration
The chlorogenic acid refined solution is through nanofiltration, and ethyl alcohol recrystallization gets the pure product of chlorogenic acid.
Be used in the steps A crossing the 40-80 mesh sieve after the chlorogenic acid extracting Folium Eucommiae is pulverized;
Heating temperature described in the steps A is 65 degree, and stirring extraction time is 2 hours, and extraction time is 2 times;
Solution described in the steps A is 60% ethanol, and the solid-liquid ratio is 1: 12, the PH=4 of solution.
Discoloring agent described in the step B is an activated carbon, and adding proportion is that 5% stirring bleaching time is 20 minutes,
Ultra-filtration membrane described in the step B is the hollow-fibre membrane of 5000Da, ultrafiltration pressure 0.4PM, and temperature is 30 degree.
The resin that is used to adsorb among the step C is XAD-5, and the ratio of resin and adsorption liquid is 1: 5, adsorption time 4 hours;
The solution that is used for desorption among the step C is 20% aqueous ethanolic solution, the PH=3 of solution; The solution of desorption and the ratio of resin are 4: 1, and the desorption time is 3 hours.
Used nanofiltration membrane is that molecular weight cut-off is the ceramic membrane of 150Da among the step D, and operating pressure is 0.4Mpa, and temperature is a normal temperature;
Used recrystallization solution is dehydrated alcohol and normal hexane among the step D, and two kinds of liquor capacity ratios are 1: 1, and recrystallization temperature is 0 degree.
Adopt among the present invention that extraction using alcohol, ultrafiltration, resin absorption, nanofiltration separation purifying concentrate, the method for ethyl alcohol recrystallization, it has substituted the technology that existing organic solvent extracts, extracts under the acid-basicity condition.Present method is at first used 60% ethanolic soln materials such as chlorogenic acid extracting, albumen, polysaccharide and flavones from Folium Eucommiae, removes protein, polysaccharide, pigment through decolouring, ultrafiltration, separate the chlorogenic acid crude product; Through macroporous resin, nanofiltration purifying, ethyl alcohol recrystallization, the pure product of chlorogenic acid have been prepared.
Advantage of the present invention be pollution-free, energy consumption is low, the renewable recycling of material therefor, but the low continuous production of extraction cost.Do not use noxious solvent in leaching process, product safety easily realizes batch production production.
With embodiment the present invention is specified below.
Embodiment: the method by Folium Eucommiae extraction, separation, purifying chlorogenic acid may further comprise the steps:
A. preparation contains the water extract of chlorogenic acid:
The dried Folium Eucommiae 0.5KG (chlorogenic acid content is 4.96%) that pulverized 60 mesh sieves is put into the there-necked flask of 10L, uses the 6L60% ethanolic soln, add HCL and transfer PH=4, be stirred and heated to 65 degree, under this temperature, extracted 2 hours, filter, filtrate (1); Filter residue adds the 4L60% ethanolic soln and transfers PH=4, is stirred and heated to 65 degree, extracts 2 hours under this temperature, filters, and gets filtrate (2).Merging filtrate (1) and (2), decompression recycling ethanol gets extracting solution 3L.
B. preparation contains the crude product solution of chlorogenic acid
The aqueous extract that will contain chlorogenic acid is heated to 50 degree, adds activated carbon 150g with 5% ratio, stirred 30 minutes,
Left standstill centrifuging 30 minutes; Is ultrafiltration under 0.4MP, temperature 30 degree with filtrate at pressure, and the liquid that dams adds the deionized water ultrafiltration 3 times.Add water 2L at every turn, get the about 8L of chlorogenic acid crude product solution.
C. purifying chlorogenic acid:
Get the XAD-5 resin through manipulation of regeneration, the ratio of chlorogenic acid crude product solution and amount of resin is 5: 1, is 1.6KG in the present embodiment, and solution is transferred PH=4, and whip attachment is 4 hours in the 20L stirred pot,
Centrifuging, resin is washed 3 times with deionized water and stirring, and is haze-free until washing out water; Each water 10L, the collection eluting water can be crossed and reclaim use again after nanofiltration membrane is taken off polysaccharide; Resin after the washing is washed 1 time with 10% ethanol 3L, and filtering solution must be adsorbed with the resin of chlorogenic acid.Get 6.5L PH=3 20% ethanolic soln (with the resin ratio be 4: 1) and resin put into stirred pot together, stirred wash-out 3 hours, filter, wash once with deionized water, collect the about 9L of filtrate.
D. prepare the chlorogenic acid elaboration
The solution of chlorogenic acid of purifying is crossed nanofiltration membrane at normal temperatures, and film is that molecular weight cut-off is the ceramic membrane of 150Da, and operating pressure is 0.4MP; Concentrated ratio is 10 times, gets concentrated solution 900ml, and concentrating under reduced pressure gets solid substance; With dehydrated alcohol under 60 degree, dissolve 150ml solution, add equal-volume normal hexane recrystallization 16 hours under 0 degree, purity is 92% chlorogenic acid elaboration 17.86 grams.

Claims (10)

1. method by Folium Eucommiae extraction, separation and purifying chlorogenic acid
A prepares the chlorogenic acid extracting solution
The Folium Eucommiae of drying and crushing is crossed 60 mesh sieves, be added in the aqueous ethanolic solution, transfer PH=4, heated and stirred is extracted, and filters, and filtrate decompression is steamed ethanol, gets the chlorogenic acid aqueous extract
B. the separation of chlorogenic acid extracting solution
Filtrate adds decolorizing with activated carbon, crosses ultra-filtration membrane deproteinize, polysaccharide, gets chlorogenic acid crude product aqueous extract
C. purifying chlorogenic acid:
Chlorogenic acid crude product solution absorption with macroporous adsorbent resin with acidiferous ethanolic soln desorption, gets the pure product solution of chlorogenic acid.
D. prepare the chlorogenic acid elaboration
The chlorogenic acid crude product solution is crossed nanofiltration membrane, and ethyl alcohol recrystallization gets the pure product of chlorogenic acid.
2. according to the described method by Folium Eucommiae extraction, separation and purifying chlorogenic acid of claim 1, it is characterized in that: the extraction temperature described in the steps A is 65 degree, and stirring extraction time is 2 hours.
3. according to the described method by Folium Eucommiae extraction, separation and purifying chlorogenic acid of claim 1, it is characterized in that: the solution that is used for chlorogenic acid extracting in the steps A is 60% ethanolic soln, and its PH is 4.
4. according to the described method by Folium Eucommiae extraction, separation and purifying chlorogenic acid of claim 1, it is characterized in that: the solid-to-liquid ratio that is used for chlorogenic acid extracting in the steps A is 1: 12.
5. according to the described method by Folium Eucommiae extraction, separation and purifying chlorogenic acid of claim 1, it is characterized in that: the molecular weight cut-off that is used for the film of ultrafiltration among the step B is the hollow-fibre membrane of 5000Da, and operating pressure is 0.4MPa during ultrafiltration, and working temperature is 30 degree.
6. according to the described method by Folium Eucommiae extraction, separation and purifying chlorogenic acid of claim 1, it is characterized in that: used discoloring agent is an activated carbon among the step B, and adding proportion is 5% of a solution; Stirring bleaching temperature is 40 degree, and stirring bleaching time is 30 minutes.
7. according to the described method by Folium Eucommiae extraction, separation and purifying chlorogenic acid of claim 1, it is characterized in that: used purifying resin is XAD-5 among the step C, and resin demand is 1: 5 with being purified solution proportion; Adsorption time is 4 hours, solution PH=4.
8. according to the described method by Folium Eucommiae extraction, separation and purifying chlorogenic acid of claim 1, it is characterized in that: the solution that is used for wash-out absorption among the step C is 20% ethanolic soln, solution PH=3, and elution time is 3 hours.
9. according to the described method of claim 1 by Folium Eucommiae extraction, separation and purifying chlorogenic acid, it is characterized in that: being used for the spissated film of purifying among the step D is that molecular weight cut-off is the ceramic membrane of 150Da, operating pressure is 0.4MPa, and working temperature is a normal temperature, and it is 10 times that the solution behind the purifying is concentrated multiple.
10. according to the described method by Folium Eucommiae extraction, separation and purifying chlorogenic acid of claim 1, the solvent that it is characterized in that being used among the step D recrystallization is ethanol and normal hexane, and the temperature of recrystallization is 0 degree.
CN2009101479281A 2009-06-11 2009-06-11 Method for extracting, separating and purifying chlorogenic acid through folium cortex eucommiae Pending CN101935278A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2009101479281A CN101935278A (en) 2009-06-11 2009-06-11 Method for extracting, separating and purifying chlorogenic acid through folium cortex eucommiae

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2009101479281A CN101935278A (en) 2009-06-11 2009-06-11 Method for extracting, separating and purifying chlorogenic acid through folium cortex eucommiae

Publications (1)

Publication Number Publication Date
CN101935278A true CN101935278A (en) 2011-01-05

Family

ID=43388881

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2009101479281A Pending CN101935278A (en) 2009-06-11 2009-06-11 Method for extracting, separating and purifying chlorogenic acid through folium cortex eucommiae

Country Status (1)

Country Link
CN (1) CN101935278A (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102579564A (en) * 2012-03-15 2012-07-18 中国科学院西北高原生物研究所 Preparing method of Tibetan capillaris effective part extractives
CN102731309A (en) * 2012-06-25 2012-10-17 浙江农林大学 Method for extracting and separating chlorogenic acid from chrysanthemum indicum
CN102786417A (en) * 2011-05-18 2012-11-21 中国医学科学院药物研究所 Chlorogenic acid crystal III characterization and preparation methods, and applications of chlorogenic acid crystal III in medicines and healthcare products
CN103497106A (en) * 2013-09-04 2014-01-08 草本创想生物科技(成都)有限公司 Method for extracting chlorogenic acid from green coffee beans
CN103641718A (en) * 2013-12-23 2014-03-19 聊城大学 Method for separating and purifying chlorogenic acid and 3,5-dicaffeoylquinic acid from honeysuckle flower
CN104224891A (en) * 2014-09-26 2014-12-24 西北农林科技大学 Eucommia ulmoides fine powder and preparation method thereof
CN105254500A (en) * 2015-11-11 2016-01-20 中国科学院烟台海岸带研究所 Method for preparing high-purity chlorogenic acid from eucommia ulmoides leaf crude extract
CN108147964A (en) * 2017-12-23 2018-06-12 安徽名创新材料科技有限公司 A kind of method with Integrated Membrane Technology separating chlorogenic acid
EP3251683A4 (en) * 2015-01-30 2018-09-26 Sichuan Jiuzhang Biological Science And Technology Co., Ltd Eucommia leaf extract, and preparation method and use thereof
CN110193034A (en) * 2019-05-06 2019-09-03 普正药业集团股份有限公司 A kind of eucommia leaf extract and its application in alleviation physical fatigue product
CN112807263A (en) * 2021-03-01 2021-05-18 科丝美诗(中国)化妆品有限公司 Anti-aging composition and preparation method and application thereof
CN114409542A (en) * 2021-09-09 2022-04-29 南京工业大学 Method for extracting chlorogenic acid and flavone by membrane separation of eucommia ulmoides

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1400199A (en) * 2001-08-06 2003-03-05 西北农林科技大学 Method for continuously extracting active component from eucommia leaf
CN1616402A (en) * 2003-12-12 2005-05-18 贵州家诚药业有限责任公司 Method for extracting and separating chlorogenic acid
CN1974527A (en) * 2006-12-01 2007-06-06 广州汉方现代中药研究开发有限公司 Process of preparing high purity chlorogenic acid and flavonid with eucommia leaf

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1400199A (en) * 2001-08-06 2003-03-05 西北农林科技大学 Method for continuously extracting active component from eucommia leaf
CN1616402A (en) * 2003-12-12 2005-05-18 贵州家诚药业有限责任公司 Method for extracting and separating chlorogenic acid
CN1974527A (en) * 2006-12-01 2007-06-06 广州汉方现代中药研究开发有限公司 Process of preparing high purity chlorogenic acid and flavonid with eucommia leaf

Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102786417B (en) * 2011-05-18 2016-04-27 中国医学科学院药物研究所 The brilliant type III of chlorogenic acid characterizes and preparation method and applying in medicine and healthcare products
CN102786417A (en) * 2011-05-18 2012-11-21 中国医学科学院药物研究所 Chlorogenic acid crystal III characterization and preparation methods, and applications of chlorogenic acid crystal III in medicines and healthcare products
CN102579564B (en) * 2012-03-15 2013-07-31 中国科学院西北高原生物研究所 Preparing method of Tibetan capillaris effective part extractives
CN102579564A (en) * 2012-03-15 2012-07-18 中国科学院西北高原生物研究所 Preparing method of Tibetan capillaris effective part extractives
CN102731309A (en) * 2012-06-25 2012-10-17 浙江农林大学 Method for extracting and separating chlorogenic acid from chrysanthemum indicum
CN102731309B (en) * 2012-06-25 2016-12-21 浙江农林大学 A kind of method extracting separating chlorogenic acid from Herba Dendranthematis indici
CN103497106A (en) * 2013-09-04 2014-01-08 草本创想生物科技(成都)有限公司 Method for extracting chlorogenic acid from green coffee beans
CN103641718A (en) * 2013-12-23 2014-03-19 聊城大学 Method for separating and purifying chlorogenic acid and 3,5-dicaffeoylquinic acid from honeysuckle flower
CN104224891A (en) * 2014-09-26 2014-12-24 西北农林科技大学 Eucommia ulmoides fine powder and preparation method thereof
CN104224891B (en) * 2014-09-26 2018-05-15 西北农林科技大学 A kind of bark of eucommia fine powder and preparation method thereof
EP3251683A4 (en) * 2015-01-30 2018-09-26 Sichuan Jiuzhang Biological Science And Technology Co., Ltd Eucommia leaf extract, and preparation method and use thereof
CN105254500A (en) * 2015-11-11 2016-01-20 中国科学院烟台海岸带研究所 Method for preparing high-purity chlorogenic acid from eucommia ulmoides leaf crude extract
CN105254500B (en) * 2015-11-11 2017-06-16 中国科学院烟台海岸带研究所 A kind of method that high-purity chlorogenic acid is prepared in the Leave extract from the bark of eucommia
CN108147964A (en) * 2017-12-23 2018-06-12 安徽名创新材料科技有限公司 A kind of method with Integrated Membrane Technology separating chlorogenic acid
CN110193034A (en) * 2019-05-06 2019-09-03 普正药业集团股份有限公司 A kind of eucommia leaf extract and its application in alleviation physical fatigue product
CN112807263A (en) * 2021-03-01 2021-05-18 科丝美诗(中国)化妆品有限公司 Anti-aging composition and preparation method and application thereof
CN114409542A (en) * 2021-09-09 2022-04-29 南京工业大学 Method for extracting chlorogenic acid and flavone by membrane separation of eucommia ulmoides

Similar Documents

Publication Publication Date Title
CN101935278A (en) Method for extracting, separating and purifying chlorogenic acid through folium cortex eucommiae
CN102040519B (en) Method for preparing chlorogenic acid in Eucommia ulmoides leaves
CN103333067B (en) A kind of extracting method of high-purity chlorogenic acid
CN104356106B (en) The extracting and purifying method of a kind of purple potato anthocyanidin
CN101336949B (en) Method for extracting polysaccharide and flavone from Gynura divaricata
CN101948501B (en) Preparation method of hydroxyl asiaticoside
CN101862385B (en) Sanguisorba saponins and preparation method of sanguisorbin I
CN103319441B (en) A kind of method of separating-purifying 10-deacetylate Bakating III from Ramulus et folium taxi cuspidatae
CN102516325A (en) Method for producing crocin with higher than 95% purity from gardenia
CN102351926B (en) A kind of preparation method of arctinin
CN103012544B (en) A kind of method extracting saponin and polysaccharide from tea seed grouts
CN103788152A (en) Method for preparing geniposide in eucommia leaf
CN101503357A (en) Method for extracting chlorogenic acid in honeysuckle
CN103058871A (en) Separation and purification method of tobacco chlorogenic acid
WO2022057603A1 (en) Method for extracting coenzyme q10 from fermentation broth of coenzyme q10
CN101558803A (en) Extracting and purifying method of extract of bitter leaves
CN112225774A (en) Novel method for extracting tea saponin with high purity and high extraction rate
CN102558254A (en) Extract of willow barks or willow branches and method for preparing salicin
CN110437290A (en) A kind of steviol glycoside extracting and developing and purification process
CN101973977B (en) Method for preparing osthole
CN103772457B (en) Method for preparing geniposidic acid in eucommia leaf
CN106831930B (en) A kind of extractant and extracting method for ursolic acid extraction
CN110917240B (en) Continuous method for separating multiple effective components from cyclocarya paliurus
CN103860626B (en) Method for preparing total flavonoids in eucommia ulmoides leaves
CN1250502C (en) Method of extracting purified solanesol from tobacco leaf

Legal Events

Date Code Title Description
DD01 Delivery of document by public notice

Addressee: Wu Meijuan

Document name: Notification of Passing Preliminary Examination of the Application for Invention

C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
ASS Succession or assignment of patent right

Owner name: FENGNING JINGBEI NO.1 GRASSLAND ECOLOGICAL FOOD TE

Free format text: FORMER OWNER: ZHOU DAJIE

Effective date: 20120903

C41 Transfer of patent application or patent right or utility model
COR Change of bibliographic data

Free format text: CORRECT: ADDRESS; FROM: 100193 HAIDIAN, BEIJING TO: 068350 CHENGDE, HEBEI PROVINCE

TA01 Transfer of patent application right

Effective date of registration: 20120903

Address after: 068350, Fengning Hebei Manchu Autonomous County in the town of grain court hospital

Applicant after: Fengning Jingbei No.1 Grasslands Original Ecological Food Technology Development Co., Ltd.

Address before: 100193 Beijing Old Summer Palace West Road, Haidian District, No. 2

Applicant before: Zhou Dajie

C02 Deemed withdrawal of patent application after publication (patent law 2001)
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20110105