CN104311614A - Method for extracting mangiferin from mango leaves - Google Patents

Method for extracting mangiferin from mango leaves Download PDF

Info

Publication number
CN104311614A
CN104311614A CN201410619517.9A CN201410619517A CN104311614A CN 104311614 A CN104311614 A CN 104311614A CN 201410619517 A CN201410619517 A CN 201410619517A CN 104311614 A CN104311614 A CN 104311614A
Authority
CN
China
Prior art keywords
extraction
mengiferin
phase
folium mangiferae
aqueous
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
CN201410619517.9A
Other languages
Chinese (zh)
Other versions
CN104311614B (en
Inventor
卢桦香
卢照凯
谢冬养
钟德品
周晓青
赵明东
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.)
GUILIN YIYUANSU BIOLOGICAL SCIENCE & TECHNOLOGY Co Ltd
Original Assignee
GUILIN YIYUANSU BIOLOGICAL SCIENCE & TECHNOLOGY 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 GUILIN YIYUANSU BIOLOGICAL SCIENCE & TECHNOLOGY Co Ltd filed Critical GUILIN YIYUANSU BIOLOGICAL SCIENCE & TECHNOLOGY Co Ltd
Priority to CN201410619517.9A priority Critical patent/CN104311614B/en
Publication of CN104311614A publication Critical patent/CN104311614A/en
Application granted granted Critical
Publication of CN104311614B publication Critical patent/CN104311614B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07HSUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
    • C07H17/00Compounds containing heterocyclic radicals directly attached to hetero atoms of saccharide radicals
    • C07H17/04Heterocyclic radicals containing only oxygen as ring hetero atoms
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07HSUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
    • C07H1/00Processes for the preparation of sugar derivatives
    • C07H1/06Separation; Purification
    • C07H1/08Separation; Purification from natural products

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Biochemistry (AREA)
  • Biotechnology (AREA)
  • General Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Molecular Biology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Medicines Containing Plant Substances (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Compounds Of Unknown Constitution (AREA)

Abstract

The invention discloses a method for extracting mangiferin from mango leaves. The method includes the following steps: raw material processing, high-pressure extraction, aqueous two-phase extraction, desalination, and recrystallization to obtain the mangiferin. The method provided by the invention has the advantages of high mangiferin content, high extraction rate, simple process, suitability for production, low production cost and the like.

Description

A kind of method extracting Mengiferin from Folium mangiferae
Technical field
The present invention relates to the extracting method of biological technical field, is a kind of method extracting Mengiferin from Folium mangiferae specifically.
Background technology
Mango is aiphyllium, originates in India, and existing tropical various places are all planted, and cultivate in South China, and by Guangxi, Guangdong, village, various places, Hainan or room residence, wetting a little soil is scattered about like the stars plant as seen.Folium mangiferae is the leaf of Anacardiaceae plant mango Mangifera indica L, for Guangxi Local commonly uses Chinese medicine, record in " Guangxi Chinese medicinal materials standard " nineteen ninety version, contained Mengiferin (Mangiferin) is Folium mangiferae cough-relieving, reduce phlegm, the main active ingredient of anti-inflammatory, Mengiferin has anti-inflammatory, antiviral, nervus centralis suppresses and immunosuppressive action, also has anti peroxidation of lipid, antitumor action, conventional to treat hepatitis, Mengiferin treatment chronic bronchitis has good therapeutic effect, Mengiferin has obvious toxic action to hepatoma cell strain, energy liver cancer apoptosis reducing, Mengiferin has anti-oxidant vigor and delaying senility function.
Disclosed Mengiferin extracting and purifying method mostly is water extract-alcohol precipitation, alcohol extracting macroporous resin purification method at present, as Chinese patent CN100475830C " high purity Mengiferin preparation method ", patent CN101759689A " a kind of preparation method of Mengiferin " and patent CN101429222A " extract a kind of method of Mengiferin ", all adopt macroporous resin purification as main separating step, but adopt macroporous resin purification method, resin is with front needing process, purifying need through absorption and elution process, and the production cycle is long.When carrying out purifying wash-out with macroporous resin, due to physical adsorption, also easily causing a part of sample extremely to adsorb, and causing the rate of transform to reduce.Adopt macroporous resin purification effluent volume comparatively large in addition, the solvent recuperation time is long, adds production cost, and solvent recuperation produces more waste liquid, causes certain burden to environmental protection.In addition due to the use of macroporous resin, add the risk introducing the organic residual solvents such as benzene,toluene,xylene, vinylbenzene, alkanes, diethylbenzene class, the security of product is exerted a certain influence.
In sum, study a kind of simple possible, the extracting method of Mengiferin that environmental pollution is little has good realistic meaning.
Summary of the invention
The object of this invention is to provide a kind of method extracting Mengiferin from Folium mangiferae, there is technique simple, be applicable to producing, the advantages such as the time is short.
The present invention is achieved through the following technical solutions, and specifically comprises the steps:
1) Feedstock treating: Folium mangiferae is pulverized or smashes;
2) high pressure extract: by the raw material after process, put into pressure pan, add the pure water of identical weight, be forced into 4kgf/cm 2, make its pressure uniform, and keep 10-15min, recover normal pressure, filter, obtain extracting solution;
3) be separated: aqueous two-phase extraction is carried out to Folium mangiferae, obtain the upper lower phase with extraction mutually of extraction, the double-aqueous phase system that aqueous two-phase extraction uses is made up of polyoxyethylene glycol, sodium hydroxide and water, the mass percent of described polyoxyethylene glycol in described double-aqueous phase system is 10-20%, the mass percent of described sodium hydroxide in described double-aqueous phase system is 10-20%, surplus is water, and the weight-average molecular weight of described polyoxyethylene glycol is 1000-8000;
4) subsequent disposal: by step 3) phase in the extraction that obtains, desalination, recrystallization, by step 3) phase under the extraction that obtains, add and be equivalent to extract lower phase mass percent 5-10% sodium hydroxide, desalination, recrystallization;
5) the acquisition thing after merging recrystallization obtains Mengiferin.
Folium mangiferae of the present invention is fresh and/or dried Folium mangiferae.
Described desalination preferably adopts ultrafiltration process or dialysis method, and ultrafiltration process employing molecular weight cut-off is the ultra-filtration membrane desalination of 1000-100000, and dialysis method employing molecular weight cut-off is the dialysis tubing desalination of 1000-100000.
The Mengiferin that the present invention obtains, detect through HPLC, content is more than 98.5%.
Compared with prior art, advantage of the present invention:
1, prior art is when carrying out the extraction of Mengiferin, pre-treatment is all generally for solvent with water or ethanol etc., by heating extraction by effective constituent stripping, and the present invention adopts high pressure extract, compare heating to extract, through High Pressure, make the composition such as organic acid, polyphenol, the Mengiferin energy fully stripping contained in Folium mangiferae, be beneficial to the process of subsequent technique, be beneficial to the yield improving activeconstituents.
2, Mengiferin poorly water-soluble, is soluble in rare alcohol, hot methyl alcohol and ethanol, is soluble in sig water; Usually the Mengiferin 7-O-glycoside (Mangiferin-7-0-R-D-glucopy-ranoside) with its amount 5% coexists in leaf.Because the hydroxyl acidity of 3 in structure is comparatively strong, therefore two compounds are all soluble in alkaline water liquid, and Mengiferin 7-0-glycoside also can be hydrolyzed into Mengiferin in alkaline water liquid, thus can improve yield and the purity of Mengiferin.The present invention adds basic solution when extracting, and fully can be separated Mengiferin and Mengiferin 7-O-glycoside, then by subsequent technique, makes Mengiferin 7-O-glycoside to be converted into Mengiferin, improve yield.
3, the Mengiferin content that prior art obtains generally is no more than 98%, the present invention adopts the combination of high pressure extract and aqueous two phase extraction technique, can enhance productivity greatly, prior art column chromatography resin used, for being generally non-polar resin, can only obtain the extract of Mengiferin content 40-50% through primary sorption; If employing polar resin, also can only obtain Mengiferin content about 50% through primary sorption, the Mengiferin wanting to obtain more high-content by 2 times or more Adsorptions, thus must add process time and cost.Aqueous two phase extraction technique is as a kind of novel isolation technique, have mild condition, easy and simple to handle, be easy to series of advantages such as amplifying, separating power is strong, and adopt combine with technique of the present invention, there is the raising of matter, content and the extraction efficiency of Mengiferin can be increased, compare column chromatography after water extraction or alcohol extracting, the time of the present invention is short, and Mengiferin content is high.
4, present invention, avoiding the use of a large amount of organic solvent such as dehydrated alcohol, methyl alcohol, environmental protection more.
Embodiment
With embodiment, the invention will be further described below, but the present invention is not limited to these embodiments.
Embodiment 1:
From Folium mangiferae, extract a method for Mengiferin, specifically comprise the steps:
1) Feedstock treating: fresh mango leaf is smashed;
2) high pressure extract: by the raw material after process, put into pressure pan, add the pure water of identical weight, be forced into 4kgf/cm 2, make its pressure uniform, and keep 10min, recover normal pressure, filter, obtain extracting solution;
3) be separated: aqueous two-phase extraction is carried out to Folium mangiferae, obtain the upper lower phase with extraction mutually of extraction, the double-aqueous phase system that aqueous two-phase extraction uses is made up of polyoxyethylene glycol, sodium hydroxide and water, the mass percent of polyoxyethylene glycol in described double-aqueous phase system is 20%, the mass percent of sodium hydroxide in described double-aqueous phase system is 10%, surplus is water, and the weight-average molecular weight of polyoxyethylene glycol is 1000-8000;
4) subsequent disposal: by step 3) phase in the extraction that obtains, ultrafiltration process employing molecular weight cut-off is ultra-filtration membrane desalination, the recrystallization of 1000-100000, by step 3) phase under the extraction that obtains, add and be equivalent to extract lower phase mass percent 10% sodium hydroxide, ultrafiltration process employing molecular weight cut-off is ultra-filtration membrane desalination, the recrystallization of 1000-100000;
5) merge dried acquisition thing and obtain Mengiferin.
Embodiment 2:
From Folium mangiferae, extract a method for Mengiferin, specifically comprise the steps:
1) Feedstock treating: dry Folium mangiferae is pulverized;
2) high pressure extract: by the raw material after process, put into pressure pan, add the pure water of identical weight, be forced into 4kgf/cm 2, make its pressure uniform, and keep 15min, recover normal pressure, filter, obtain extracting solution;
3) be separated: aqueous two-phase extraction is carried out to Folium mangiferae, obtain the upper lower phase with extraction mutually of extraction, the double-aqueous phase system that aqueous two-phase extraction uses is made up of polyoxyethylene glycol, sodium hydroxide and water, the mass percent of polyoxyethylene glycol in described double-aqueous phase system is 10%, the mass percent of sodium hydroxide in described double-aqueous phase system is 20%, surplus is water, and the weight-average molecular weight of polyoxyethylene glycol is 1000-8000;
4) subsequent disposal: by step 3) phase in the extraction that obtains, dialysis method employing molecular weight cut-off is dialysis tubing desalination, the recrystallization of 1000-100000, by step 3) phase under the extraction that obtains, add and be equivalent to extract lower phase mass percent 5% sodium hydroxide, dialysis method employing molecular weight cut-off is dialysis tubing desalination, the recrystallization of 1000-100000;
5) merge dried acquisition thing and obtain Mengiferin.
Embodiment 3:
From Folium mangiferae, extract a method for Mengiferin, specifically comprise the steps:
1) Feedstock treating: dry Folium mangiferae is pulverized;
2) high pressure extract: by the raw material after process, put into pressure pan, add the pure water of identical weight, be forced into 4kgf/cm 2, make its pressure uniform, and keep 12min, recover normal pressure, filter, obtain extracting solution;
3) be separated: aqueous two-phase extraction is carried out to Folium mangiferae, obtain the upper lower phase with extraction mutually of extraction, the double-aqueous phase system that aqueous two-phase extraction uses is made up of polyoxyethylene glycol, sodium hydroxide and water, the mass percent of polyoxyethylene glycol in described double-aqueous phase system is 15%, the mass percent of sodium hydroxide in described double-aqueous phase system is 15%, surplus is water, and the weight-average molecular weight of polyoxyethylene glycol is 1000-8000;
4) subsequent disposal: by step 3) phase in the extraction that obtains, ultrafiltration process employing molecular weight cut-off is ultra-filtration membrane desalination, the recrystallization of 1000-100000, by step 3) phase under the extraction that obtains, add and be equivalent to extract lower phase mass percent 10% sodium hydroxide, ultrafiltration process employing molecular weight cut-off is ultra-filtration membrane desalination, the recrystallization of 1000-100000;
5) merge dried acquisition thing and obtain Mengiferin.
Result:

Claims (2)

1. from Folium mangiferae, extract a method for Mengiferin, it is characterized in that:
Comprise the steps:
1) Feedstock treating: Folium mangiferae is pulverized or smashes;
2) high pressure extract: by the raw material after process, put into pressure pan, add the pure water of identical weight, be forced into 4kgf/cm 2, make its pressure uniform, and keep 10-15min, recover normal pressure, filter, obtain extracting solution;
3) be separated: aqueous two-phase extraction is carried out to Folium mangiferae, obtain the upper lower phase with extraction mutually of extraction, the double-aqueous phase system that aqueous two-phase extraction uses is made up of polyoxyethylene glycol, sodium hydroxide and water, the mass percent of described polyoxyethylene glycol in described double-aqueous phase system is 10-20%, the mass percent of described sodium hydroxide in described double-aqueous phase system is 10-20%, surplus is water, and the weight-average molecular weight of described polyoxyethylene glycol is 1000-8000;
4) subsequent disposal: by step 3) phase in the extraction that obtains, desalination, recrystallization, by step 3) phase under the extraction that obtains, add and be equivalent to extract lower phase mass percent 5-10% sodium hydroxide, desalination, recrystallization;
5) the acquisition thing after merging recrystallization obtains Mengiferin.
2. a kind of method extracting Mengiferin from Folium mangiferae according to claim 1, is characterized in that: described Folium mangiferae is fresh and/or dried Folium mangiferae.
CN201410619517.9A 2014-11-05 2014-11-05 A kind of method extracting Mengiferin from Folium mangiferae Expired - Fee Related CN104311614B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410619517.9A CN104311614B (en) 2014-11-05 2014-11-05 A kind of method extracting Mengiferin from Folium mangiferae

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410619517.9A CN104311614B (en) 2014-11-05 2014-11-05 A kind of method extracting Mengiferin from Folium mangiferae

Publications (2)

Publication Number Publication Date
CN104311614A true CN104311614A (en) 2015-01-28
CN104311614B CN104311614B (en) 2016-07-20

Family

ID=52366950

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410619517.9A Expired - Fee Related CN104311614B (en) 2014-11-05 2014-11-05 A kind of method extracting Mengiferin from Folium mangiferae

Country Status (1)

Country Link
CN (1) CN104311614B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109438429A (en) * 2018-12-29 2019-03-08 桂林医学院 A method of extracting mangiferin from mango leaf

Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2108383A (en) * 1981-10-22 1983-05-18 Vnii Lekarstvennykh Rasteny Compound and composition for use against herpes virus
US4518592A (en) * 1980-07-16 1985-05-21 Rusakova Svetlana V Process for preparing mangiferin
WO1996016632A1 (en) * 1994-11-25 1996-06-06 Laboratoires De Biologie Vegetale Yves Rocher Cosmetic or pharmaceutical compositions containing mangiferin or derivatives thereof
CN1733785A (en) * 2005-09-01 2006-02-15 桂林莱茵生物科技股份有限公司 Method for extracting chimonin
CN1844133A (en) * 2006-04-18 2006-10-11 广西中医学院 Process for preparing high purity mangiferin
CN101429222A (en) * 2007-11-05 2009-05-13 南宁市百济生物工程有限公司 Method for extracting mangiferin
CN101693730A (en) * 2009-10-16 2010-04-14 天津中医药大学 Mangiferin and preparation method and application thereof
CN102232977A (en) * 2011-05-06 2011-11-09 南京泽朗医药科技有限公司 Method for extracting total saponins from pokeberry root
CN102617669A (en) * 2012-03-03 2012-08-01 浙江大学 Method for separating and purifying mangiferin from mango pericarp
CN102697839A (en) * 2012-06-01 2012-10-03 武汉工程大学 Aqueous two-phase extraction and separation method for flavonoids, saponins and polysaccharides of astragalus
CN103113442A (en) * 2013-02-28 2013-05-22 华南理工大学 Method for extracting cordyceps polysaccharide and adenosine from cordyceps sinensis mycelium
CN103772460A (en) * 2014-02-14 2014-05-07 江苏省中国科学院植物研究所 Extraction process of cordycepin (active substance) from silkworm pupa cordyceps militaris

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4518592A (en) * 1980-07-16 1985-05-21 Rusakova Svetlana V Process for preparing mangiferin
GB2108383A (en) * 1981-10-22 1983-05-18 Vnii Lekarstvennykh Rasteny Compound and composition for use against herpes virus
WO1996016632A1 (en) * 1994-11-25 1996-06-06 Laboratoires De Biologie Vegetale Yves Rocher Cosmetic or pharmaceutical compositions containing mangiferin or derivatives thereof
CN1733785A (en) * 2005-09-01 2006-02-15 桂林莱茵生物科技股份有限公司 Method for extracting chimonin
CN1844133A (en) * 2006-04-18 2006-10-11 广西中医学院 Process for preparing high purity mangiferin
CN101429222A (en) * 2007-11-05 2009-05-13 南宁市百济生物工程有限公司 Method for extracting mangiferin
CN101693730A (en) * 2009-10-16 2010-04-14 天津中医药大学 Mangiferin and preparation method and application thereof
CN102232977A (en) * 2011-05-06 2011-11-09 南京泽朗医药科技有限公司 Method for extracting total saponins from pokeberry root
CN102617669A (en) * 2012-03-03 2012-08-01 浙江大学 Method for separating and purifying mangiferin from mango pericarp
CN102697839A (en) * 2012-06-01 2012-10-03 武汉工程大学 Aqueous two-phase extraction and separation method for flavonoids, saponins and polysaccharides of astragalus
CN103113442A (en) * 2013-02-28 2013-05-22 华南理工大学 Method for extracting cordyceps polysaccharide and adenosine from cordyceps sinensis mycelium
CN103772460A (en) * 2014-02-14 2014-05-07 江苏省中国科学院植物研究所 Extraction process of cordycepin (active substance) from silkworm pupa cordyceps militaris

Non-Patent Citations (4)

* Cited by examiner, † Cited by third party
Title
李好文,等: "芒果苷国外研究进展", 《广西中医学院学报》 *
江咏,等: "双水相萃取技术的研究进展及应用", 《食品工业科技》 *
王瑞兰,等: "芒果皮活性成分的萃取及其生理活性研究", 《怀化学院学报》 *
赵爱丽,等: "应用双水相萃取法分离黄芩苷的研究", 《中成药》 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109438429A (en) * 2018-12-29 2019-03-08 桂林医学院 A method of extracting mangiferin from mango leaf

Also Published As

Publication number Publication date
CN104311614B (en) 2016-07-20

Similar Documents

Publication Publication Date Title
CN101323648B (en) Extraction method and and purification method of Sanghuang mushroom polysaccharide
CN102633895B (en) Extraction and preparation method by comprehensively utilizing liquorice
CN102924416B (en) Method for separating and purifying monomeric compounds from ash bark
CN102408415A (en) Preparation method of mangiferin
CN105963328A (en) Method for continuously extracting torreya grandis flavone and essential oil from torreya grandis aril
CN102617468A (en) Method for ultrasound-assisted extraction of lappaconitine
CN103920305A (en) Tank group type countercurrent cordyceps extracting method
CN102060905B (en) Technology method for preparing sea cucumber saponin Holotoxin A1 comparison product by utilizing fresh sea cucumber processing waste liquid
CN102807595A (en) Technique for preparing high-content (98 percent) icariin from Epimedium plant
CN103772339A (en) Method for extracting high-content epigallocatechin gallate from tea leftovers
CN102731592A (en) Method for extracting cleupin and amentoflavone from olive leaf
CN104119229A (en) Technology for producing pure chlorogenic acid
CN103408610A (en) Method for extracting arbutin from pear leaves
CN104069191B (en) A kind of extraction process of water polygonum flaccidum general flavone
CN104311614B (en) A kind of method extracting Mengiferin from Folium mangiferae
CN104788515B (en) Method for preparing high-purity water-soluble oleuropein by reduced pressure ultrasonic-assisted extraction
CN102617696A (en) Preparation method of asiaticoside
CN102250183B (en) Method for preparing high-purity ginsenoside Re by using ginseng flower buds as raw materials
CN102600215A (en) Method for extracting peganum harmala alkaloid
CN101993459A (en) Process for extraction separation of bamboo leaf flavonoids by two aqueous phases
CN104231011A (en) Preparation method of verbascoside
CN104435015A (en) High-quality ginkgetin extraction process
CN105348338A (en) Method for extracting and separating paederosidic acid from Saprosma merrillii Lo
CN104447780B (en) A kind of method extracting sesamin from sesame
CN104072570A (en) Preparation method of momordin Ic

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
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: 20160720

Termination date: 20181105