CN1586696A - Desorb-heat extracting two-step extracting method for plant active component - Google Patents
Desorb-heat extracting two-step extracting method for plant active component Download PDFInfo
- Publication number
- CN1586696A CN1586696A CN 200410051011 CN200410051011A CN1586696A CN 1586696 A CN1586696 A CN 1586696A CN 200410051011 CN200410051011 CN 200410051011 CN 200410051011 A CN200410051011 A CN 200410051011A CN 1586696 A CN1586696 A CN 1586696A
- Authority
- CN
- China
- Prior art keywords
- extraction
- plant
- extracting
- desorb
- solvent
- 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
Links
Landscapes
- Medicines Containing Plant Substances (AREA)
Abstract
The two-step desorbing and heat extracting extraction process of effective plant component includes first desorbing the effective component from embedding or adsorbing plant tissue with small amount of water solution of alcohol and then extraction with hot solvent. Compared with available technology, the present invention has the advantages of short extraction time, low power consumption, 5-10 % raised yield, 5-30 % raised effective component content in the extracted matter and over 10 times lower solvent consumption compared with alcohol extraction process.
Description
Technical field
The present invention relates to the extracting method of effective ingredients in plant in the separation engineering, particularly effective ingredients in plant adopts desorb-Re to put forward the method for two steps extraction.
Background technology
Active ingredient in the plant is usually by plant tissue embedding and absorption, be provided with certain obstacle to extraction, conventional extracting method adopts a single solvent such as a step such as water, alcohol and benzinum to extract, this method only needs a kind of extraction solvent, simple to operation, extraction rate is slow, yield is low, CE impurity reaches shortcomings such as energy consumption is big more but exist.To some water-soluble extracts active ingredients preferably, often, also adopt alcohol extract, thereby increased the consumption of ethanol in order to improve the impurity content of yield and reduction CE.Some modern extracting methods are extracted as microwave and ultrasonic wave, and extraction rate reaches the yield height soon, but will realize industrialization, and production cost is still than higher.
Summary of the invention
The purpose of this invention is to provide a kind of extraction time short, yield is high, the product impurity content is low and the effective plant component extracting process of easy realization, it is characterized in that earlier extracting with hot solvent then with the small amount of ethanol aqueous solution active ingredient is desorbed from the plant tissue embedding and adsorbing.
Basic principle of the present invention is that the process that active ingredient is suggested the solvent from plant tissue inside is in two steps, the first step is active ingredient desorb from plant tissue embedding and absorption, the solvent that this step needs is called strippant, strippant has strong infiltration and destroy the ability of organization structure of the plant and the ability that active ingredient is cemented out from adsorbed state, for example certain density ethanol water, its infiltration and destruction organization structure of the plant and desorption ability are stronger, are a kind of strippants of nontoxic cheapness.Second step was that active ingredient is transferred to the outside from plant tissue inside, the solvent that this step needs is called the extraction solvent, the ratio of solvent strippant requires low, as long as can dissolve active ingredient, the higher solvent of temperature be dissolved with the strippant of active ingredient under the effect of temperature and concentration difference, the mutual rapid diffusion of portion within plant tissue, extraction rate is accelerated greatly.The temperature of desorption process is generally normal temperature, and the strippant consumption is also less, thereby the impurity level that desorption process produces seldom, and the speed of follow-up extraction is fast, and impurity proposition amount is few, and whole process extract impurity content lacks than one-step method.
Performing step of the present invention and condition are as follows:
(1) dried or half-dried plant are ground into granularity>20 orders;
(2) add the ethanol water that concentration is 50%~85%, quantity is weight of material 60%~200% and make material evenly moistening, normal temperature was placed 5~60 minutes down;
(3) solvent extraction of adding more than 50 ℃ is one to three time, each 5~30 minutes.
The present invention compares with existing extractive technique, and its outstanding substantive distinguishing features and obvious improvement is:
(1) extraction time shortens 2~6 times, realizes easily.
(2) directly add hot solvent after the desorb, extractor can save heater, and the operation cycle is short, and energy consumption is low.
(3) yield improves 5%~10%, and the active constituent content of extract improves 5%~30%, and later separation and purification are more easy.
(4) to the leaching process of available water as solvent, the ethanol consumption reduces more than 10 times than alcohol extracting.
The specific embodiment
Embodiment one
The extraction of chlorogenic acid in the honeysuckle: dried honeysuckle powder is broken into 20~50 orders, adding weight of material 60%~140%, concentration are 60%~80% ethanol water, desorb is 5~20 minutes under the normal temperature, use twice of 85~100 ℃ of hot water extracting at last, each 10~15 minutes, to carry and comparing with an existing step water, extraction time reduces 3 times, the yield of chlorogenic acid increases by 8%, and chlorogenic acid contents improves 30% in the CE.
Embodiment two
The extraction of flavones in the ginkgo leaf: dry Folium Ginkgo is ground into 50~100 orders, it is fully wetting to add weight of material 80%~180%, concentration and be 50%~80% alcohol, desorb is 10~40 minutes under the normal temperature, use 70~80 ℃ at last, 30%~60% alcohol extract twice, each 10~20 minutes, compare with an existing step alcohol extracting, extraction time reduces 4 times, and the yield of flavones increases by 6%, and the content of flavones improves 15% in the CE.
Claims (2)
1, a kind of desorb-Re of effective ingredients in plant puies forward two step extracting methods, it is characterized in that earlier extracting with hot solvent then with the small amount of ethanol aqueous solution active ingredient is desorbed from the plant tissue embedding and adsorbing.
2,, it is characterized in that the extraction step of two-step method and condition are as follows according to the method shown in the claim 1:
(1) dried or half-dried plant are ground into granularity>20 orders;
(2) add the ethanol water that concentration is 50%~85%, quantity is weight of material 60%~200% and make material evenly moistening, normal temperature was placed 5~60 minutes down;
(3) solvent extraction of adding more than 50 ℃ is one to three time, each 5~30 minutes.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200410051011 CN1586696A (en) | 2004-08-06 | 2004-08-06 | Desorb-heat extracting two-step extracting method for plant active component |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200410051011 CN1586696A (en) | 2004-08-06 | 2004-08-06 | Desorb-heat extracting two-step extracting method for plant active component |
Publications (1)
Publication Number | Publication Date |
---|---|
CN1586696A true CN1586696A (en) | 2005-03-02 |
Family
ID=34602338
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 200410051011 Pending CN1586696A (en) | 2004-08-06 | 2004-08-06 | Desorb-heat extracting two-step extracting method for plant active component |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN1586696A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101920127B (en) * | 2009-06-15 | 2013-03-06 | 福建中烟工业有限责任公司 | Device for extracting natural plant scent components at low temperature and extracting process thereof |
-
2004
- 2004-08-06 CN CN 200410051011 patent/CN1586696A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101920127B (en) * | 2009-06-15 | 2013-03-06 | 福建中烟工业有限责任公司 | Device for extracting natural plant scent components at low temperature and extracting process thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101797447B (en) | Method for separating and purifying effective ingredients in natural product | |
CN102911055B (en) | Method for extracting chlorogenic acid | |
CN103694364A (en) | Method for synchronously extracting, separating and purifying polysaccharides and flavones of cyclocarya paliurus | |
CN103725420B (en) | A kind of extract the method for Nigella damascena L. platymiscium Volatile Oil from Seed, device and application | |
CN102349951B (en) | Preparation method of hawthorn leaf extract | |
CN101851297A (en) | High-efficiency extraction process of polygahatous plysaccharides | |
CN104277915A (en) | Method for extracting peony essential oil from peony | |
CN104523767A (en) | Method for extracting flavones substances in cacumen biotae | |
CN104311676A (en) | Method for extracting edible starch from oak seeds and obtaining byproduct tannin | |
CN103446195B (en) | The preparation method of Folium Ginkgo extract | |
CN104610417B (en) | A kind of method of extracting ursolic acid and oleanolic acid from hawthorn | |
CN101168537A (en) | Method for simultaneously preparing andrographolide and dehydrated andrographolide | |
CN108503674A (en) | A method of extracting aurantiin from the honey shaddock of well ridge | |
CN107519232A (en) | One kind extraction Gueldenstaedtia verna extractive of general flavone and preparation method thereof | |
CN102002072A (en) | Process for extracting flavone from date pit | |
CN1586696A (en) | Desorb-heat extracting two-step extracting method for plant active component | |
CN102558248A (en) | Method for extracting polyphenol from chestnut shells | |
CN1272331C (en) | Method of extracting effective components in kudzu vine root | |
CN105175426A (en) | Method of extracting and purifying bergenin from cissus pteroclada hayata | |
CN101863957B (en) | Method for synchronously extracting tanshinone IIA and salvianolic acid B from danshen root efficiently | |
CN112480053B (en) | Method for extracting and separating baicalin and baicalein | |
AU2020101090A4 (en) | A Method for Preparing Flavonoids in Functional Passion Fruit Shells | |
CN114133987A (en) | Method for extracting essential oil from cinnamomum camphora leaves | |
CN106986904A (en) | A kind of Gastrodin extracted in the anesthesia stem from day and preparation method thereof | |
CN111419892A (en) | Extraction method of abrus herb total flavone |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
WD01 | Invention patent application deemed withdrawn after publication |