CN102041163A - Multi-body multi-stage supercritical CO2 extraction method of ganoderma lucidum spore oil - Google Patents

Multi-body multi-stage supercritical CO2 extraction method of ganoderma lucidum spore oil Download PDF

Info

Publication number
CN102041163A
CN102041163A CN2011100010993A CN201110001099A CN102041163A CN 102041163 A CN102041163 A CN 102041163A CN 2011100010993 A CN2011100010993 A CN 2011100010993A CN 201110001099 A CN201110001099 A CN 201110001099A CN 102041163 A CN102041163 A CN 102041163A
Authority
CN
China
Prior art keywords
ganoderma lucidum
extraction
supercritical
lucidum spore
ganoderma
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
CN2011100010993A
Other languages
Chinese (zh)
Other versions
CN102041163B (en
Inventor
邓泽元
章晋武
李广焱
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.)
NANCHANG TONGXIN ZICHAO BIOENGINEERING CO Ltd
Original Assignee
NANCHANG TONGXIN ZICHAO BIOENGINEERING 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 NANCHANG TONGXIN ZICHAO BIOENGINEERING CO Ltd filed Critical NANCHANG TONGXIN ZICHAO BIOENGINEERING CO Ltd
Priority to CN 201110001099 priority Critical patent/CN102041163B/en
Publication of CN102041163A publication Critical patent/CN102041163A/en
Application granted granted Critical
Publication of CN102041163B publication Critical patent/CN102041163B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The invention relates to a multi-body multi-stage supercritical CO2 extraction method of ganoderma lucidum spore oil, which is characterized by comprising the following steps: (1) carrying out ultra-fine pulverization for breaking walls to obtain ganoderma lucidum spore powder; (2) granulating the wall-broken ganoderma lucidum spore powder by a dry press method in a one-step granulator; (3) placing the ganoderma lucidum spore powder granules in three-stage separation supercritical CO2 extraction kettles; and (4) respectively obtaining ganoderma lucidum spore oil components of different solubilities from a separation kettle I and a separation kettle II, and discharging an entrainer mainly from a separation kettle III. The invention has the following technical advantages: 1. more functional components in ganoderma lucidum spores can be extracted more efficiently, thereby achieving high oil yield and increasing the triterpenoid constituent content in the ganoderma lucidum spore oil; 2. the multi-body multi-stage extraction can separate the ganoderma lucidum spore oil from carrying agents such as ethanol, water and other components more effectively, thereby ensuring better quality of the extract; and 3. the extraction is carried out in the absence of oxygen gas, thereby lowering the damage possibility of active components of the ganoderma lucidum spores.

Description

The multistage supercritical CO of a kind of many bodies 2The method of Ganoderma Lucidum Spores Oil Extracted
Technical field
The present invention relates to a kind of method of Ganoderma Lucidum Spores Oil Extracted, relate in particular to the multistage supercritical CO of a kind of many bodies 2The method of Ganoderma Lucidum Spores Oil Extracted.
Background technology
Glossy ganoderma is the polyporaceae fungi, have the reputation of " celestial grass ", states clearly in the Pharmacopoeia of the People's Republic of China, glossy ganoderma has the function of " invigorating QI and tranquilization, relieving cough and asthma ", and " be used for dizzy egersis; shortness of breath and palpitation, consumptive disease is coughed and breathed heavily " is listed in first-selection in having the moving plant and biology of medicine food of antitumous effect.Ganoderma spore is the glossy ganoderma growth and maturity phase to produce the seed that discharges, sexual cell for glossy ganoderma, whole hereditary active substance with glossy ganoderma, it is the elite of glossy ganoderma, and comprised the triterpenes in the Ganoderma spore, fatty acid, sterols, polyose, alkaloids, and composition such as ucleosides in the Ganoderma spore oil, be the aggregate of Ganoderma spore effective constituent, have multiple physiologically active.Wherein the Ganoderma triterpenoids constituents is the main effective constituent of glossy ganoderma, because of the diversity of its chemical structure, make ganoderma lucidum triterpene compounds have antitumor, anti-oxidant, suppress that cholesterol is synthetic, anticoagulant, protect the liver, pharmacologically active more widely such as analgesia.At present glossy ganoderma medicine on the domestic market, healthcare products are of a great variety, and a lot of ganoderma lucidum prods are with total triterpene property functional component as a token of.Ganoderma lucidum triterpene compounds is not only the focus of current glossy ganoderma chemistry and pharmacological research, and has better industrial application prospects.In recent years, the Ganoderma spore oil production has become the treasure in the high-grade healthcare products, has crucial utility value and economic worth.
The traditional extracting method of Ganoderma spore oil generally adopts methyl alcohol or the lixiviate of ethanol equal solvent, and extraction efficiency is low, extraction time is many, energy consumption is high, solvent load is big, many shortcomings such as dissolvent residual are arranged but this method exists.Supercritical CO 2Abstraction technique is the technology of emerging extraction, separation and a purifying of foodstuffs industry, compare with traditional solvent extration, have no solvent residue, pollution-free, avoid at high temperature thermo-cracking of extract, help the extraction of lipid-soluble substance and heat-sensitive substance, and technology is simple, energy consumption is low, advantages such as extraction agent is nontoxic, easy recovery have been widely used in the extraction of medicinal herb components and spices.
The patent application and the report of existing employing supercritical CO 2 Ganoderma Lucidum Spores Oil Extracted are more.It is that Ganoderma spore with broken wall is a raw material that patent CN1239100C discloses its method for preparing Ganoderma spore oil, with volume percent is after 5%~95% the aqueous ethanolic solution granulation drying, to use supercritical carbon dioxide extraction, but adopt ethanolic soln to granulate, hot-air seasoning, ethanol is inflammable, and is dangerous.Among the patent CN1194079C, Ganoderma spore powder, granulation expanded through bulking machine, changed the raw material bulk density, can improve mass transfer effect, increase oil yield, but adopt puffing technique temperature higher (80~140 ℃), can quicken the oxidation and the process of becoming sour of lipid in the spore powder, can bring disadvantageous effect the quality of oil.Patent CN1255519C discloses the method for its Ganoderma Lucidum Spores Oil Extracted, under the CO 2 supercritical state, Ganoderma spore powder with cellular wall broken is substep step-down and change temperature in nonionogenic tenside Tween80, obtain the component of different solubilities at last by one-level resolver and secondary resolver, but tensio-active agent can be blended in the spore oil, and the ability of auxiliary extraction is also limited.
Adopt supercritical CO 2The method of Ganoderma Lucidum Spores Oil Extracted is a lot, but perfect not enough, needs further to explore the processing condition of best suitable suitability for industrialized production.
Summary of the invention
The object of the present invention is to provide the multistage supercritical CO of a kind of many bodies 2The method of Ganoderma Lucidum Spores Oil Extracted, this method is simple and easy, efficient, the production time short, be fit to suitability for industrialized production.
The present invention is achieved like this, and method steps is:
(1) Ganoderma spore is put into the supper micron mill broken wall, obtained Ganoderma spore powder;
(2) Ganoderma spore powder with cellular wall broken is granulated with the one-step-granulating method dry pressing, makes 10-40 purpose particle;
(3) the Ganoderma spore powder particles is put into had three grades of isolating supercritical COs 2In the extraction kettle, with the aqueous ethanolic solution of massfraction 25%~95% as carrying agent, 25%~95% of every kilogram of dress material adding 20~250ml aqueous ethanolic solution in the extraction kettle, carry out supercritical extraction then, extracting pressure is 25~40MPa, extraction temperature is 35~60 ℃, and the extraction time is 2~4 hours;
(4) obtain the Ganoderma spore oil ingredient of different solubilities respectively from separating still I and separating still II, entrainment agent is then mainly emitted from the separating still III.
At supercritical CO 2Install rectifier unit and many gradient temperatures pressure in the separating still device in the extraction plant additional and regulated separation system, the separating pressure of separating still I is 10~20MPa, temperature is 35~50 ℃, the separating pressure of separating still II is 7.5~10MPa, temperature is 30~45 ℃, the separating pressure of separating still III is 4~7MPa, and temperature is 30~40 ℃.
Know-why of the present invention:
1. common supercritical CO 2In the extraction process because CO 2Polarity a little less than, it only can extract nonpolar attitude composition and the less composition of polarity, but the extracts active ingredients poor effect relatively large to polarity.Triterpene substance in the Ganoderma spore is that chemical structure is various, and a class material of polarity a wider range needs higher extraction conditions just can extract, and it is dissolved in ethanol, further increasing of solubleness under condition of high voltage.So agent and CO are carried in the second alcohol and water conduct by certain proportioning 2Form many bodies CO of polarity a wider range 2Medium, many bodies CO 2Medium can effectively extract the opposed polarity composition in the Ganoderma spore, thereby reaches triterpenes, fatty acid, sterols isoreactivity composition in the high efficiency extraction Ganoderma spore.
2. at supercritical CO 2Install a rectifier unit and many gradient temperatures pressure regulating system in the separating still device of extraction plant additional, make it to become multistage separation temperature, pressure gradient, thereby reach stage trapping by optimization temperature, pressure parameter, under the trickleer temperature difference, pressure reduction change, make effective constituent, ethanol, water and the CO of Ganoderma spore 2Between separate, improved quality product, changed and can not realize carrying agent and the complete isolating situation of effective constituent under the single separation temperature pressure gradient condition.
Technique effect of the present invention is: 1. owing to adopted the multistage CO of many bodies 2The extraction mode can more effectively more extract the multiple functional component in the Ganoderma spore, so the oil yield height, and triterpenes content also increases in the Ganoderma spore oil; 2. because the multistage extraction of many bodies is more can be effectively separating of oil with carrying composition such as agent second alcohol and water and Ganoderma spore, so the quality of extract is better; 3. extract under oxygen free condition, the destroyed probability of the active ingredient of Ganoderma spore reduces.
Embodiment
Embodiment 1:
After Ganoderma spore powder with cellular wall broken 6Kg granulation, place supercritical CO 2In the extraction kettle, extracting pressure is 25MPa, and extraction temperature is 40 ℃, carrying agent is 90% aqueous ethanolic solution, 800 ml, extracted 2 hours, the separating pressure of separating still I is 13MPa, and temperature is 45 ℃, the separating pressure of separating still II is 8.5MPa, temperature is 40 ℃, and the separating pressure of separating still III is 6MPa, and temperature is 35 ℃, from the separating still I, emit the more weak Ganoderma spore oil ingredient 1.52Kg of polarity at last, oil yield 25.3%; From the separating still II, emit the stronger Ganoderma spore oil ingredient 0.33Kg of polarity, oil yield 5.5%.
Embodiment 2:
After Ganoderma spore powder with cellular wall broken 6Kg granulation, place supercritical CO 2In the extraction kettle, extracting pressure is 30MPa, and extraction temperature is 50 ℃, carrying agent is 85% aqueous ethanolic solution, 1000 ml, extracted 4 hours, the separating pressure of separating still I is 15MPa, and temperature is 45 ℃, the separating pressure of separating still II is 8MPa, temperature is 45 ℃, and the separating pressure of separating still III is 5MPa, and temperature is 40 ℃, from the separating still I, emit the more weak Ganoderma spore oil ingredient 1.65Kg of polarity at last, oil yield 27.5%; From the separating still II, emit the stronger Ganoderma spore oil ingredient 0.47Kg of polarity, oil yield 7.8%.

Claims (2)

1. the multistage supercritical CO of body more than a kind 2The method of Ganoderma Lucidum Spores Oil Extracted is characterized in that method steps is:
(1) Ganoderma spore is put into the supper micron mill broken wall, obtained Ganoderma spore powder;
(2) Ganoderma spore powder with cellular wall broken is granulated with the one-step-granulating method dry pressing, makes 10-40 purpose particle;
(3) the Ganoderma spore powder particles is put into had three grades of isolating supercritical COs 2In the extraction kettle, with the aqueous ethanolic solution of massfraction 25%~95% as carrying agent, 25%~95% of every kilogram of dress material adding 20~250ml aqueous ethanolic solution in the extraction kettle, carry out supercritical extraction then, extracting pressure is 25~40MPa, extraction temperature is 35~60 ℃, and the extraction time is 2~4 hours;
(4) obtain the Ganoderma spore oil ingredient of different solubilities respectively from separating still I and separating still II, entrainment agent is then mainly emitted from the separating still III.
2. the multistage supercritical CO of a kind of many bodies according to claim 1 2The method of Ganoderma Lucidum Spores Oil Extracted is characterized in that at supercritical CO 2Install rectifier unit and many gradient temperatures pressure in the separating still device in the extraction plant additional and regulated separation system, the separating pressure of separating still I is 10~20MPa, temperature is 35~50 ℃, the separating pressure of separating still II is 7.5~10MPa, temperature is 30~45 ℃, the separating pressure of separating still III is 4~7MPa, and temperature is 30~40 ℃.
CN 201110001099 2011-01-05 2011-01-05 Multi-body multi-stage supercritical CO2 method for extraction of ganoderma lucidum spore oil Active CN102041163B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201110001099 CN102041163B (en) 2011-01-05 2011-01-05 Multi-body multi-stage supercritical CO2 method for extraction of ganoderma lucidum spore oil

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201110001099 CN102041163B (en) 2011-01-05 2011-01-05 Multi-body multi-stage supercritical CO2 method for extraction of ganoderma lucidum spore oil

Publications (2)

Publication Number Publication Date
CN102041163A true CN102041163A (en) 2011-05-04
CN102041163B CN102041163B (en) 2013-04-17

Family

ID=43907712

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201110001099 Active CN102041163B (en) 2011-01-05 2011-01-05 Multi-body multi-stage supercritical CO2 method for extraction of ganoderma lucidum spore oil

Country Status (1)

Country Link
CN (1) CN102041163B (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103351941A (en) * 2013-06-17 2013-10-16 浙江龙泉佳宝生物科技有限公司 Supercritical CO2 variable-temperature variable-pressure extraction method of lucid ganoderma spore oil
CN104073344A (en) * 2014-07-16 2014-10-01 江苏斯威森生物医药工程研究中心有限公司 Extracting method for ganoderma lucidum spore oil
CN104946383A (en) * 2015-04-30 2015-09-30 江苏江大源生态生物科技有限公司 Method for preparing ganoderma lucidum spores oil through supercritical CO2 composite microwave-assisted extraction
CN106318612A (en) * 2016-09-19 2017-01-11 中山大学 Method for supercritical extraction of ganoderma lucidum spore oil
CN106398861A (en) * 2016-10-31 2017-02-15 中山大学 Entrainer-containing supercritical CO2 extraction method of ganderma lucidum spore oil
CN106867657A (en) * 2017-03-17 2017-06-20 广州康琪莱生物科技有限公司 A kind of efficient, multi-stage supercritical CO2The method of Ganoderma Lucidum Spores Oil Extracted
CN110577463A (en) * 2019-09-16 2019-12-17 广州绿和缘生物科技有限公司 System and method for supercritical carbon dioxide extraction of cannabidiol
CN115125059A (en) * 2022-06-15 2022-09-30 中科健康产业集团股份有限公司 Method for removing fat-soluble harmful ingredients in ganoderma lucidum spore oil
CN115177974A (en) * 2022-07-07 2022-10-14 广州海文森特实业有限公司 Method and equipment for extracting and concentrating high-purity ganoderma lucidum triterpenoids
CN116462780A (en) * 2023-05-17 2023-07-21 深圳杉海创新技术有限公司 Method for extracting active ingredients of ganoderma lucidum spore powder
WO2023237058A1 (en) * 2022-06-10 2023-12-14 南京中科药业有限公司 Method for removing free fatty acids from ganoderma spore powder

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101288694A (en) * 2007-04-16 2008-10-22 中国科学院地球化学研究所 Preparation method of magnolia bark extracts with no residual solvent, low oiliness and high content
CN101831351A (en) * 2010-06-03 2010-09-15 吉林大学 Method for extracting ganoderma oil with supercritical carbon dioxide fluid

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101288694A (en) * 2007-04-16 2008-10-22 中国科学院地球化学研究所 Preparation method of magnolia bark extracts with no residual solvent, low oiliness and high content
CN101831351A (en) * 2010-06-03 2010-09-15 吉林大学 Method for extracting ganoderma oil with supercritical carbon dioxide fluid

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
朱坚; 李晔; 邓优锦; 吴小平; 张理平; 李观荣; 谢宝贵; 江玉姬: "超临界CO_2萃取灵芝孢子油的工艺研究", 《中国食用菌》, 30 June 2009 (2009-06-30) *
李琴韵; 梁静; 何威之; 钱燕娟: "超临界CO_2萃取灵芝孢子油的工艺条件研究", 《中成药》, 31 March 2008 (2008-03-31) *

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103351941B (en) * 2013-06-17 2015-06-17 浙江龙泉佳宝生物科技有限公司 Supercritical CO2 variable-temperature variable-pressure extraction method of lucid ganoderma spore oil
CN103351941A (en) * 2013-06-17 2013-10-16 浙江龙泉佳宝生物科技有限公司 Supercritical CO2 variable-temperature variable-pressure extraction method of lucid ganoderma spore oil
CN104073344B (en) * 2014-07-16 2016-08-24 江苏斯威森生物医药工程研究中心有限公司 A kind of extracting method of Ganoderma spore oil
CN104073344A (en) * 2014-07-16 2014-10-01 江苏斯威森生物医药工程研究中心有限公司 Extracting method for ganoderma lucidum spore oil
CN104946383B (en) * 2015-04-30 2018-07-03 江苏江大源生态生物科技有限公司 A kind of supercritical CO2The method that composite microwave auxiliary extraction prepares ganoderma lucidum spore oil
CN104946383A (en) * 2015-04-30 2015-09-30 江苏江大源生态生物科技有限公司 Method for preparing ganoderma lucidum spores oil through supercritical CO2 composite microwave-assisted extraction
CN106318612A (en) * 2016-09-19 2017-01-11 中山大学 Method for supercritical extraction of ganoderma lucidum spore oil
CN106398861A (en) * 2016-10-31 2017-02-15 中山大学 Entrainer-containing supercritical CO2 extraction method of ganderma lucidum spore oil
CN106867657A (en) * 2017-03-17 2017-06-20 广州康琪莱生物科技有限公司 A kind of efficient, multi-stage supercritical CO2The method of Ganoderma Lucidum Spores Oil Extracted
CN110577463A (en) * 2019-09-16 2019-12-17 广州绿和缘生物科技有限公司 System and method for supercritical carbon dioxide extraction of cannabidiol
WO2023237058A1 (en) * 2022-06-10 2023-12-14 南京中科药业有限公司 Method for removing free fatty acids from ganoderma spore powder
CN115125059A (en) * 2022-06-15 2022-09-30 中科健康产业集团股份有限公司 Method for removing fat-soluble harmful ingredients in ganoderma lucidum spore oil
WO2023241456A1 (en) * 2022-06-15 2023-12-21 南京中科药业有限公司 Method for removing fat-soluble harmful ingredients in ganoderma lucidum spore oil
CN115125059B (en) * 2022-06-15 2024-03-26 南京中科药业有限公司 Method for removing fat-soluble harmful components in ganoderma lucidum spore oil
CN115177974A (en) * 2022-07-07 2022-10-14 广州海文森特实业有限公司 Method and equipment for extracting and concentrating high-purity ganoderma lucidum triterpenoids
CN116462780A (en) * 2023-05-17 2023-07-21 深圳杉海创新技术有限公司 Method for extracting active ingredients of ganoderma lucidum spore powder

Also Published As

Publication number Publication date
CN102041163B (en) 2013-04-17

Similar Documents

Publication Publication Date Title
CN102041163B (en) Multi-body multi-stage supercritical CO2 method for extraction of ganoderma lucidum spore oil
CN104073344B (en) A kind of extracting method of Ganoderma spore oil
CN103351941B (en) Supercritical CO2 variable-temperature variable-pressure extraction method of lucid ganoderma spore oil
CN110304994B (en) Method for extracting high-purity cannabidiol from industrial cannabis sativa
CN101987809A (en) Production technology for extracting purified lycopene from tomato waste residue
CN104194917A (en) Method for extracting folium artemisiae argyi essential oil
CN109232346A (en) A kind of industrialized process for preparing of lutein and marigold flavones
CN102876456A (en) Method for extracting volatile oil and alkaloid from pepper by using subcritical fluid
CN102965198A (en) Method for extracting and processing lavender essential oil
CN106417783A (en) Preparation methods of Fu tea instant tea powder and double-layer compound Fu tea instant tea tablets
CN102250198A (en) Method for extracting phytosterol from stems of dragon fruits
CN100425247C (en) Refining ganoderam lucidum spore oil and method for preparing same
CN100998613B (en) Method for producing effective component of glossy ganoderma by using supercritical technology
CN100998626B (en) Method for preparing extract of korea thistle leaf
CN103146473A (en) Method for simultaneously extracting Australian tea tree essential oil and flavonoid glycosides
CN103755583B (en) Method for extracting and separating ceramide in konjac flying powder
CN101683362A (en) Method for extracting ganoderma oil by using supercritical carbon dioxide
CN101390975A (en) Extraction method of citrus active ingredient
CN101628857A (en) Production technique for extracting resveratrol from giant knotweed
CN104083556B (en) A kind of method that konjak ceramide is extracted from konjaku
CN103897800A (en) Process for extracting wheat germ oil by adopting supercritical extraction method
CN105362300A (en) Method for using seaweed to prepare concentrated solution rich in seaweed polyphenols
CN106187978A (en) A kind of method extracting pitaya peel procyanidins
CN102206241B (en) Technological process for extracting ergosterol with high purity and feed protein from penicillin waste residue
CN102267855A (en) Extraction method of lycopene

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