CN1594340A - Process for extraction refining amygdalin - Google Patents

Process for extraction refining amygdalin Download PDF

Info

Publication number
CN1594340A
CN1594340A CN 200410012381 CN200410012381A CN1594340A CN 1594340 A CN1594340 A CN 1594340A CN 200410012381 CN200410012381 CN 200410012381 CN 200410012381 A CN200410012381 A CN 200410012381A CN 1594340 A CN1594340 A CN 1594340A
Authority
CN
China
Prior art keywords
amygdaloside
drying
raw material
ground
ethanol
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
CN 200410012381
Other languages
Chinese (zh)
Other versions
CN1288162C (en
Inventor
侯相林
杜俊民
齐永琴
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.)
Shanxi Institute of Coal Chemistry of CAS
Original Assignee
Shanxi Institute of Coal Chemistry of CAS
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 Shanxi Institute of Coal Chemistry of CAS filed Critical Shanxi Institute of Coal Chemistry of CAS
Priority to CN 200410012381 priority Critical patent/CN1288162C/en
Publication of CN1594340A publication Critical patent/CN1594340A/en
Application granted granted Critical
Publication of CN1288162C publication Critical patent/CN1288162C/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Landscapes

  • Medicines Containing Plant Substances (AREA)
  • Coloring Foods And Improving Nutritive Qualities (AREA)

Abstract

The invention provides a process for extraction refining amygdalin which consists of, disintegrating the plant raw material containing rich bitter apricot seed into powder, removing the grease from the raw material powder by using CO2 as extracting agent, carrying out decompression segregation to the carbon dioxide containing vegetable fat, charging alcohol into ground-slag containing bitter apricot seed glycosides by the solid-to-liquid ratio of 1 : 3-10, agitating, filtering by suction to obtain the filter liquor, distilling and drying the filter liquor to obtain crude product of bitter apricot seed glycoside, dissolving the bitter apricot seed glycoside into ethanol, low temperature crystallizing, filtering and drying to obtain the high purity bitter apricot seed glycosides.

Description

A kind of method of extracting refining amygdaloside
Technical field
The present invention relates to a kind of from plant material the method for extracting effective components amygdaloside, be meant the separation and refining method that from Gynocardia odorata R. Br, Europe Lee's seed, almond, peach kernel, extracts amygdaloside especially.
Technical background
Amygdaloside is with a kind of aromatic series cyanogen glycosides, is present in the seed of Flacourtiaceae Gynocardia odorata R. Br, Rosaceae Europe Lee, apricot and peach etc.Discover that amygdaloside is the effective constituent of treatment respiratory system disease, it benumbs inhibition respiratory centre system by slowly discharging prussic acid in vivo, thereby plays the effect of relievining asthma, and is widely used in Chinese traditional treatment, coughs in order to treatment etc.But a large amount of oral Semen Armeniacae Amarums, amygdaloside easily cause serious poisoning, and amygdaloside generates prunasin and almond cyanogen under the synaptase hydrolysis, and almond cyanogen instability is met heat and easily decomposed generation phenyl aldehyde and prussic acid.The intravital cytopigment enzyme of prussic acid and cell pellets ferric iron reacts, and inhibitory enzyme activity causes the histocyte respiration inhibition, even causes death.
Amygdaloside also is a kind of effective constituent for the treatment of cancer, and in the resident of the Pei Ji of island country, the incidence of cancer is very low, this and this state plants a large amount of apricots, often edible its fruit of resident is relevant with seed, and modern medicine study proves that amygdaloside has very strong lethality to cancer cells.The many cancer patientss that comprise western countries often select for use the preparation that contains amygdaloside as medicine.And these preparations have also brought many peculiar curative effects to the patient.Produce the amygdaloside extract and undoubtedly great market is being arranged aspect medicine and the healthcare products.
Nature contains the maximum Flacourtiaceae Gynocardia odorata R. Br of amygdaloside, and its content reaches 6~8%, and amygdaloside content is about 6% in Lee's seed of Europe, and amygdaloside content is about 3.0% in Semen Armeniacae Amarum and the peach kernel.Therefore extract the high purity amygdaloside with these raw materials and have application promise in clinical practice.
At present, the research of relevant amygdaloside extract is less, and CN02100460.9 begins to extract amygdaloside from Semen Armeniacae Amarum squeeze cake, and this method oil removing rate is not high, and the product purity that causes next step alcohol extraction process to obtain is not high; The high temperature extruding makes and produces Semen Armeniacae Amarum enzyme-to-substrate amygdaloside Long contact time and decompose in the while expressing process; CN02146618.1 has reported the method for extracting Europe Lee's oil from Europe Lee's seed raw material, use organic solvent extraction Europe Lee's oil such as hexane, hexane costs an arm and a leg, inflammable and explosive, industrialization safety in production difficulty, and product has higher dissolvent residual, relates to low-carbon alcohol subsequently and extracts amygdaloside, but do not provide concrete technology.
Summary of the invention
The purpose of this invention is to provide a kind of method for preparing amygdaloside by supercritical carbon dioxide extraction in conjunction with solvent extraction, crystallization.
Purpose of the present invention realizes by following scheme:
(1). the plant material that will be rich in amygdaloside is ground into 10-40 purpose meal, is prepared into raw material powder;
(2). with the raw material powder extractor of packing into, with food-class CO 2For carrying out grease to raw material powder, extraction agent removes, control extracting pressure 15~35MPa, and temperature is at 31.1~60 ℃; The carbonic acid gas that contains Vegetable oil lipoprotein flows out from the extractor top, enters the separator decompression separation and removes separating pressure 4~10MPa, 10~80 ℃ of separation temperatures;
(3). the ground-slag that contains amygdaloside is emitted from the separator bottom, adds edible ethanol by solid-to-liquid ratio 1: 3~10 in ground-slag, stirs, and suction filtration gets suction filtration liquid;
(4). suction filtration liquid gets the amygdaloside crude product through distillation, drying;
(5). in ethanol, low temperature crystallization gets the high purity amygdaloside behind the filtration drying with the amygdaloside dissolving crude product.
The aforesaid plant material that contains amygdaloside is Gynocardia odorata R. Br, Europe Lee's seed, almond or peach kernel etc.
In aforesaid (3) step solvent seasoning is common drying, vacuum-drying, spraying drying etc.
Also can use the ultrasonic wave means in aforesaid (4) step dissolution process, promote dissolving fast.
Can also directly adopt ultrasonic dissolution in aforesaid (5) step crystallization filtration drying, normal temperature leaves standstill filtration drying.
The present invention has following advantage:
(1) amygdaloside is a polar material, is not dissolved in the supercritical carbon dioxide fluid.Supercritical carbon dioxide fluid can more fully remove the fat-soluble component in the raw material.And the milling process degreasing is unclean, and residual fat-soluble composition can enter solution along with the extraction using alcohol process, and product purity is descended.Compare supercritical CO with traditional solvent 2Be green solvent, operational condition gentleness, no fire hazard free from environmental pollution, on-the-spot.
(2) contain synaptase in the plant seed simultaneously, the extruding that squeezing produces in the skimming processes and localized hyperthermia can promote contacting and reaction of synaptase and amygdaloside, cause the reduction of amygdaloside yield, and supercritical CO 2Fluid medium has gentle operational condition and higher extraction efficiency, and service temperature is low, and the extraction time is short, and the material form is constant before and after the extraction, and synaptase is in lower active condition all the time, and the amygdaloside composition in the raw material does not decompose substantially.
Embodiment
Example 1:
Get Europe Lee's seed, be ground into the 10-40 order, take by weighing raw material 200 grams, put and pass through supercritical CO in the extractor 2Carry out de-oiling behind the fluid extraction, extracting pressure 30MPa, 40 ℃ of extraction temperature, separating pressure 8MPa, 50 ℃ of separation temperatures are after 4 hours, ground-slag is drawn off by the extractor bottom, add 1200 milliliters of ethanol, divide three extractions, each 400 milliliters, merging filtrate, decompression recycling ethanol be to an amount of, 65 ℃ of vacuum-drying 3 hours, get pale brown look extract 11 grams, measuring content through the HPLC method is 55%.
Get extract 3 grams of being carried, add the small amount of ethanol dissolution filter, placed 4 ℃ of refrigerators then static 10 hours, separate out white crystals, filter, wash after drying with small amount of ethanol, get 1.3 grams, detect through HPLC, content reaches 98.0%.
Example 2:
Get Europe Lee's seed, put shearing pulverizer and be ground into the 20-40 order, take by weighing raw material 200 grams, put and pass through supercritical CO in the extractor 2Carry out de-oiling behind the fluid extraction, extracting pressure 20MPa, 60 ℃ of extraction temperature, separating pressure 9MPa, 70 ℃ of separation temperatures are after 6 hours, ground-slag is drawn off by the extractor bottom, add 1200 milliliters of ethanol, divide three extractions, each 400 milliliters, merging filtrate, decompression recycling ethanol be to an amount of, dry 3 hours of 65 ℃ of vacuum-drying, get pale brown look extract 12 grams, measuring content through the HPLC method is 50%.
The extract carried 4 grams add the small amount of ethanol ultrasonic dissolution, under the normal temperature static 1 hour then, filter white crystals, drying, 1.6 grams, detect through HPLC, content reaches 92.3%.
Example 3:
Get the Semen Armeniacae Amarum seed, put shearing pulverizer and be ground into the 20-40 order, take by weighing raw material 200 grams, put and pass through supercritical CO in the extractor 2Carry out de-oiling behind the fluid extraction, extracting pressure 32MPa, 50 ℃ of extraction temperature, separating pressure 5Mpa, 30 ℃ of separation temperatures are after 4 hours, ground-slag is drawn off by the extractor bottom, add 1500 milliliters of ethanol, divide three extractions, each 500 milliliters, merging filtrate, decompression recycling ethanol be to an amount of, 65 ℃ of vacuum-drying 3 hours, get pale brown look extract 5.5 grams, measuring content through the HPLC method is 60%.
Get extract 4 grams of being carried, add the small amount of ethanol dissolution filter, place 4 ℃ to leave standstill then 10 hours, separate out white crystals, filter, wash after drying with small amount of ethanol, get 1.8 grams, detect through HPLC, content reaches 95.4%
Embodiment 4:
Get peach kernel and put shearing pulverizer and be ground into the 10-40 order, take by weighing raw material 300 grams, put and pass through supercritical CO in the extractor 2Carry out de-oiling behind the fluid extraction, extracting pressure 25MPa, 35 ℃ of extraction temperature, separating pressure 5MPa, 20 ℃ of separation temperatures are after 4 hours, ground-slag is drawn off by the extractor bottom, add 900 milliliters of ethanol, divide three extractions, each 300 milliliters, merging filtrate, decompression recycling ethanol be to an amount of, pours into behind the white disk 65 ℃ of dryings of vacuum drier 3 hours, get pale brown look extract 5.8 grams, measuring content through the HPLC method is 58%.
Get extract 4 grams of being carried, add the small amount of ethanol dissolution filter, place 4 ℃ to leave standstill then 10 hours, separate out white crystals, filter, wash after drying with small amount of ethanol, get 2.1 grams, detect through HPLC, content reaches 93.0%.

Claims (5)

1, a kind of method of extracting refining amygdaloside is characterized in that comprising the steps:
(1). the plant material that will be rich in amygdaloside is ground into 10-40 purpose meal, is prepared into raw material powder;
(2). with the raw material powder extractor of packing into, with food-class CO 2For carrying out grease to raw material powder, extraction agent removes, control extracting pressure 15~35MPa, and temperature is at 31.1~60 ℃; The carbonic acid gas that contains Vegetable oil lipoprotein flows out from the extractor top, enters the separator decompression separation and removes separating pressure 4~10MPa, 10~80 ℃ of separation temperatures;
(3). the ground-slag that contains amygdaloside is emitted from the separator bottom, adds edible ethanol by solid-to-liquid ratio 1: 3~10 in ground-slag, stirs, and suction filtration gets suction filtration liquid;
(4). suction filtration liquid gets the amygdaloside crude product through distillation, drying;
(5). in ethanol, low temperature crystallization gets the high purity amygdaloside behind the filtration drying with the amygdaloside dissolving crude product.
2, the method for claim 1 is characterized in that the described plant material that contains amygdaloside is Gynocardia odorata R. Br, Europe Lee's seed, almond or peach kernel.
3, the method for claim 1 is characterized in that in described (3) step solvent seasoning be common drying, vacuum-drying or spraying drying.
4, the method for claim 1 is characterized in that also can using the ultrasonic wave means in described (4) step dissolution process, promotes dissolving fast.
5, the method for claim 1 is characterized in that can also directly adopting ultrasonic dissolution in described (5) step crystallization filtration drying, and normal temperature leaves standstill filtration drying.
CN 200410012381 2004-07-02 2004-07-02 Process for extraction refining amygdalin Expired - Fee Related CN1288162C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200410012381 CN1288162C (en) 2004-07-02 2004-07-02 Process for extraction refining amygdalin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200410012381 CN1288162C (en) 2004-07-02 2004-07-02 Process for extraction refining amygdalin

Publications (2)

Publication Number Publication Date
CN1594340A true CN1594340A (en) 2005-03-16
CN1288162C CN1288162C (en) 2006-12-06

Family

ID=34662755

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 200410012381 Expired - Fee Related CN1288162C (en) 2004-07-02 2004-07-02 Process for extraction refining amygdalin

Country Status (1)

Country Link
CN (1) CN1288162C (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1879724B (en) * 2006-05-10 2010-05-12 西北师范大学 A method for preparing blood fat-reducing natural product
CN101967426A (en) * 2010-10-15 2011-02-09 王朝臣 Preparation process and system for ultrasonic reinforced supercritical CO2 extraction of tussah pupa oil
CN101362782B (en) * 2008-08-26 2011-09-14 山西百利士生物科技有限公司 Extraction method of amygdalin
CN102234298A (en) * 2010-04-23 2011-11-09 华东理工大学 Method for extracting and purifying amygdalin from peach seeds
CN102399622A (en) * 2010-09-09 2012-04-04 北京市农林科学院 Method for preparing bitter almond extract product
CN102399623A (en) * 2010-09-09 2012-04-04 北京市农林科学院 Method for preparing Cerasus humilis kernel extract
CN102850371A (en) * 2012-09-25 2013-01-02 南京泽朗农业发展有限公司 Method for preparing ryanodine
CN101768194B (en) * 2009-12-31 2013-07-24 西北大学 Method for extracting amygdalin and albumen powder from Amygdalus pedunculata pall. oil residues
CN103214529A (en) * 2013-05-10 2013-07-24 浙江省农业科学院 Method for extracting amygdalin from kernel of red bayberry fruit
CN107927696A (en) * 2017-11-20 2018-04-20 广东聿津食品有限公司 A kind of preparation method of black pepper essential oil

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1879724B (en) * 2006-05-10 2010-05-12 西北师范大学 A method for preparing blood fat-reducing natural product
CN101362782B (en) * 2008-08-26 2011-09-14 山西百利士生物科技有限公司 Extraction method of amygdalin
CN101768194B (en) * 2009-12-31 2013-07-24 西北大学 Method for extracting amygdalin and albumen powder from Amygdalus pedunculata pall. oil residues
CN102234298A (en) * 2010-04-23 2011-11-09 华东理工大学 Method for extracting and purifying amygdalin from peach seeds
CN102399622A (en) * 2010-09-09 2012-04-04 北京市农林科学院 Method for preparing bitter almond extract product
CN102399623A (en) * 2010-09-09 2012-04-04 北京市农林科学院 Method for preparing Cerasus humilis kernel extract
CN102399623B (en) * 2010-09-09 2013-05-08 北京市农林科学院 Method for preparing Cerasus humilis kernel extract
CN101967426A (en) * 2010-10-15 2011-02-09 王朝臣 Preparation process and system for ultrasonic reinforced supercritical CO2 extraction of tussah pupa oil
CN102850371A (en) * 2012-09-25 2013-01-02 南京泽朗农业发展有限公司 Method for preparing ryanodine
CN103214529A (en) * 2013-05-10 2013-07-24 浙江省农业科学院 Method for extracting amygdalin from kernel of red bayberry fruit
CN107927696A (en) * 2017-11-20 2018-04-20 广东聿津食品有限公司 A kind of preparation method of black pepper essential oil

Also Published As

Publication number Publication date
CN1288162C (en) 2006-12-06

Similar Documents

Publication Publication Date Title
Stéphane et al. Extraction of bioactive compounds from medicinal plants and herbs
CN110304994B (en) Method for extracting high-purity cannabidiol from industrial cannabis sativa
CN106860492B (en) Preparation method of cannabinol compound
US8871217B2 (en) Method for producing fucoxanthin
CN104673497B (en) A kind of extraction process of plants essential oil, polysaccharide and flavones
CN102432582A (en) Preparation method of proanthocyanidin
CN1288162C (en) Process for extraction refining amygdalin
CN102405988A (en) Method for extracting krill oil with high phospholipid content from krill
CN102492538A (en) Method for extracting Antarctic krill oil with high phosphatide content from Antarctic krill
CN102533433A (en) Method for supercritical extraction of sea buckthorn oil
CN102060728A (en) Method for extracting capsorubin and capsaicin from chillies
CN103254092A (en) Production process of capsaicin
CN104059163A (en) Novel method for preparing Qinghai Qaidam lycium barbarum polysaccharide in extraction and separation manner
CN101812087A (en) Method for extracting high-purity phospholipid from sleeve-fish-processing waste
CN111072618B (en) Method for conveniently and rapidly purifying dihydromyricetin from self-display ampelopsis grossedentata leaves
CN1315953C (en) Preparation method of lycopene
CN101385746A (en) Extraction method of effective ingredient from pine pollen using supercritical carbon dioxide extraction
WO2024169351A1 (en) Method for extracting polyphenol substances from lettuce
CN113913029A (en) Method for preparing effective components of gardenia jasminoides
CN101269093A (en) Wall-breaking abstraction melissa powder oil and fat method with supercritical carbonic anhydride
CN102228473B (en) Extraction method for active substances in cornua cervi pantotrichum
CN1560072A (en) Process of preparing ganoderma tricterpinyl acid and ganoderma polyose from ganoderma
CN102038044A (en) Supercritical CO2 extraction process of onion oil
CN104606164B (en) A kind of preparation method of safflower " Jinghuasu " essence capsule
CN111961111B (en) American cockroach polypeptide extraction method

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: 20061206

Termination date: 20160702