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CN101838406B - Method for simultaneously extracting and separating flaxseed gum and SDG (Secoisolariciresinol Diglucoside) from flaxseeds - Google Patents

Method for simultaneously extracting and separating flaxseed gum and SDG (Secoisolariciresinol Diglucoside) from flaxseeds Download PDF

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Publication number
CN101838406B
CN101838406B CN2010101799988A CN201010179998A CN101838406B CN 101838406 B CN101838406 B CN 101838406B CN 2010101799988 A CN2010101799988 A CN 2010101799988A CN 201010179998 A CN201010179998 A CN 201010179998A CN 101838406 B CN101838406 B CN 101838406B
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China
Prior art keywords
filtrate
linseed oil
temperature
cream
under
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CN2010101799988A
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CN101838406A (en
Inventor
董万有
张继义
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Aram Pharmaceutical Co., Ltd., Gansu
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GANSU YALAN SPECIAL MEDICINE HERBS PRODUCTION CO Ltd
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Abstract

The invention relates to a method for simultaneously extracting and separating flaxseed gum and SDG from flaxseeds, comprising the following steps of: (1) adding water to the flaxseeds and then extracting for several times under stirring, filtering decoction and merging filtrates; (2) carrying out reduced pressure concentration on the obtained filtrate in the step (1) to obtain cream the relative density of which is 1.12-1.18; (3) adding alcohol to the cream so as to make the alcohol content of the cream reach 30-95 percent, evenly stirring, standing for 24-48h at the room temperature and filtering to obtain precipitates; (4) washing, filtering, drying and crushing the precipitates to obtain the flaxseed gum and meanwhile a cleaning solution and the filtrate; and (5) merging the obtained cleaning solution and the filtrate in the step (4), then recovering the alcohol in manner of the reduced pressure and concentrating into cream the relative density of which is 1.08-1.23; and drying and crushing the cream to obtain the SDG. The invention has simple process, can simultaneously extract the flaxseed gum and the SDG from the flaxseeds and is especially suitable for scale production.

Description

The method of while extraction separation flaxseed gum and secoisolariciresinol diglycoside from linseed oil
Technical field
The present invention relates to the method for extracting effective components from linseed oil, relate in particular to from linseed oil the method for extraction separation flaxseed gum and secoisolariciresinol diglycoside simultaneously.
Background technology
Flax (Linum usitatissim um L.) is one of important oil crops of China.Linseed oil also contains higher food fiber, mineral substance, nutritive ingredient such as support one's family rope A, B, D, E and phenolic acids, flavonoid, phytic acid class, Yelkin TTS except that containing abundant grease and protein.Because linseed oil is rich in indispensable fatty acid (EFA ' S)---alpha-linolenic acid (LNA) and linolic acid, and these two kinds of lipid acid naturally than relatively being fit to the mankind again, so linseed oil is considered to the best that the mankind obtain indispensable fatty acid always and originates.
But discovering in recent years also contained a kind of composition---lignan of having very much a potentiality to be exploited in the linseed oil.Lignan is a kind of physiologically active substance that is present in the linseed oil kind skin, and its structure and human body oestrogenic hormon are quite similar, are considered to a kind of phytoestrogen; It is the styryl carbinol that is obtained by phenylalanine, the natural components that bimolecular is polymerized.Lignan causes the very big interest of people as a kind of phytoestrogen, mainly is because it is proved to be and has antitumor nucleus formation, oestrogenic hormon and estrogen antagonist effect, suppresses aromatase activity, suppresses DNA and RNA is synthetic, antiviral, the characteristic of fungi etc.Studies show that, all contain lignan in many cereal, but content is the highest in the linseed oil.Secoisolariciresinol diglycoside secoisolarciresinol diglucoside (SDG), the content in linseed oil are about 1~4% (W/W), and its content exceeds 75~800 times than other 66 kinds of food.
In addition, the flax glue that extracts from linseed oil is a kind of new type natural edible gum, and it is to be the natural polymer composite gum of main component with polysaccharose substance and protein, natural thickener.
At present, prior art mostly is aqueous alcoholic extraction secoisolariciresinol diglycoside from flax seed degreased dreg, or extracts flaxseed gum more separately extract secoisolariciresinol diglycoside from linseed oil after, but these production technique are all more loaded down with trivial details, energy dissipation is also bigger.
China is the big producing country of flax, therefore, how to bring into play the function of linseed oil largely, and the comprehensive utilization linseed oil improves added value of product, realizes that large-scale industrial production is significant.
Summary of the invention
Technical problem to be solved by this invention provides a kind of technology while extraction separation flaxseed gum from linseed oil simple, with low cost and the method for secoisolariciresinol diglycoside.
For addressing the above problem, of the present invention a kind of from linseed oil the method for extraction separation flaxseed gum and secoisolariciresinol diglycoside simultaneously, may further comprise the steps:
(1) linseed oil is added stir under 10~70 ℃ of temperature behind the water and extract for several times, decoction liquor filters, merging filtrate; Wherein each amount of water is 8~12 times of linseed oil quality;
(2) under 40~70 ℃ of temperature, be 1.12~1.18 clear cream with the filtrate of described step (1) gained through being evaporated to relative density;
(3) adding ethanol in described clear cream makes it contain the alcohol amount to reach 30%~95%, stir, and at room temperature leave standstill 24~48h, obtain throw out after filtering;
(4) described throw out promptly gets flax glue after washing, filtration, drying, pulverizing; Obtain washing lotion and filtrate simultaneously;
(5) washing lotion of described step (4) gained, filtrate are merged, decompression recycling ethanol under 40~70 ℃ of temperature, and to be concentrated into relative density be 1.08~1.23 clear cream; Promptly get secoisolariciresinol diglycoside after this clear cream drying, the pulverizing.
The present invention compared with prior art has the following advantages:
1, because the present invention can extract secoisolariciresinol diglycoside and flaxseed gum simultaneously from linseed oil, therefore, reduced production cost effectively, special suitability for scale production.
2, owing to solvent for use among the present invention is water and ethanol, and extract under relatively low temperature, therefore, not only technology is simple, and safe without toxic side effect.
Embodiment
1 one kinds of the embodiment method of extraction separation flaxseed gum and secoisolariciresinol diglycoside simultaneously from linseed oil may further comprise the steps:
(1) the 300kg linseed oil is added puts into the Wuxi behind the water and avenge the 2000L reactor that unrestrained chemical industry equipment factory produces, under 10~30 ℃ of temperature, stir 1~2h, open the 10m that filter plant company limited produces greatly with Shanghai then 2Flame filter press filters, and filter residue filters merging filtrate after extracting for several times with method to decoction liquor; Wherein each amount of water is 8 times of linseed oil quality.
(2) to be evaporated to relative density be 1.12~1.18 clear cream to the 20L Rotary Evaporators that the filtrate of step (1) gained is adopted Jiangsu Xing Hai Instrument and Equipment Company produce under 40~50 ℃ of temperature.
(3) adding ethanol in clear cream makes it contain the alcohol amount to reach 30%~95%, stir, and at room temperature leave standstill 24~48h, obtain the 30kg throw out after filtering;
(4) throw out adopts 10L ethanol (volumetric concentration is 95%) washing after-filtration, the vacuum drying oven that adopts Changzhou Dare pine pressurized vessel company limited to produce again, pressure 0.04~-pulverize behind dry 2~6h under the condition of 40~70 ℃ of 0.08Mpa, temperature, promptly get the 15kg flax glue; Obtain 9kg washing lotion and 600kg filtrate simultaneously;
(5) washing lotion of step (4) gained, filtrate are merged, under 40~50 ℃ of temperature, adopt 20L Rotary Evaporators decompression recycling ethanol, and to be concentrated into relative density be 1.08~1.23 clear cream; Promptly get the 10kg secoisolariciresinol diglycoside after the spray-dried or microwave vacuum drying of this clear cream, the pulverizing.
2 one kinds of the embodiment method of extraction separation flaxseed gum and secoisolariciresinol diglycoside simultaneously from linseed oil may further comprise the steps:
(1) the 300kg linseed oil is added put into the Wuxi behind the water and avenge the 2000L reactor that unrestrained chemical industry equipment factory produces, stir 1~2h under 30~50 ℃ of temperature, use flame filter press then, filter, filter residue filters merging filtrate after extracting for several times with method to decoction liquor; Wherein each amount of water is 12 times of linseed oil quality.
(2) filtrate of step (1) gained being adopted the 20L Rotary Evaporators be evaporated to relative density under 50~60 ℃ of temperature is 1.12~1.18 clear cream.
(3) adding ethanol in clear cream makes it contain the alcohol amount to reach 30%~95%, stir, and at room temperature leave standstill 24~48h, obtain the 35kg throw out after filtering;
(4) throw out adopts 12L ethanol (volumetric concentration is 95%) washing after-filtration, adopts vacuum drying oven again, pressure 0.04~-pulverize behind dry 2~6h under the condition of 40~70 ℃ of 0.08Mpa, temperature, promptly get the 17kg flax glue; Obtain 11kg washing lotion and 600kg filtrate simultaneously;
(5) washing lotion of step (4) gained, filtrate are merged, under 50~60 ℃ of temperature, adopt 20L Rotary Evaporators decompression recycling ethanol, and to be concentrated into relative density be 1.08~1.23 clear cream; Promptly get the 11kg secoisolariciresinol diglycoside after the spray-dried or microwave vacuum drying of this clear cream, the pulverizing.
3 one kinds of the embodiment method of extraction separation flaxseed gum and secoisolariciresinol diglycoside simultaneously from linseed oil may further comprise the steps:
(1) the 300kg linseed oil is added put into the Wuxi behind the water and avenge the 2000L reactor that unrestrained chemical industry equipment factory produces, stir 1~2h under 50~70 ℃ of temperature, use flame filter press then, filter, filter residue filters merging filtrate after extracting for several times with method to decoction liquor; Wherein each amount of water is 10 times of linseed oil quality.
(2) filtrate of step (1) gained being adopted the 20L Rotary Evaporators be evaporated to relative density under 60~70 ℃ of temperature is 1.12~1.18 clear cream.
(3) adding ethanol in clear cream makes it contain the alcohol amount to reach 30%~95%, stir, and at room temperature leave standstill 24~48h, obtain the 40kg throw out after filtering;
(4) throw out adopts 15L ethanol (volumetric concentration is 95%) washing after-filtration, adopts vacuum drying oven again, pressure 0.04~-pulverize behind dry 2~6h under the condition of 40~70 ℃ of 0.08Mpa, temperature, promptly get the 20kg flax glue; Obtain 14kg washing lotion and 600kg filtrate simultaneously;
(5) washing lotion of step (4) gained, filtrate are merged, under 60~70 ℃ of temperature, adopt 20L Rotary Evaporators decompression recycling ethanol, and to be concentrated into relative density be 1.08~1.23 clear cream; Promptly get the 12kg secoisolariciresinol diglycoside after the spray-dried or microwave vacuum drying of this clear cream, the pulverizing.

Claims (1)

1. method of extraction separation flaxseed gum and secoisolariciresinol diglycoside simultaneously from linseed oil may further comprise the steps:
(1) puts into the 2000L reactor after the 300kg linseed oil is added water, under 10~30 ℃ of temperature, stir 1~2h, use 10m then 2Flame filter press filters, and filter residue filters merging filtrate after extracting for several times with method to decoction liquor; Wherein each amount of water is 8 times of linseed oil quality;
(2) filtrate of step (1) gained being adopted the 20L Rotary Evaporators be evaporated to relative density under 40~50 ℃ of temperature is 1.12~1.18 clear cream;
(3) adding ethanol in clear cream makes it contain the alcohol amount to reach 30%~95%, stir, and at room temperature leave standstill 24~48h, obtain the 30kg throw out after filtering;
(4) to adopt 10L, volumetric concentration be 95% washing with alcohol after-filtration to throw out, adopts vacuum drying oven again, pressure 0.04~-pulverize behind dry 2~6h under the condition of 40~70 ℃ of 0.08Mpa, temperature, promptly get the 15kg flax glue; Obtain 9kg washing lotion and 600kg filtrate simultaneously;
(5) washing lotion of step (4) gained, filtrate are merged, under 40~50 ℃ of temperature, adopt 20L Rotary Evaporators decompression recycling ethanol, and to be concentrated into relative density be 1.08~1.23 clear cream; Promptly get the 10kg secoisolariciresinol diglycoside after the spray-dried or microwave vacuum drying of this clear cream, the pulverizing.
CN2010101799988A 2010-05-21 2010-05-21 Method for simultaneously extracting and separating flaxseed gum and SDG (Secoisolariciresinol Diglucoside) from flaxseeds Expired - Fee Related CN101838406B (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102532334B (en) * 2011-10-24 2013-10-02 巴勇舸 Method for producing flaxseed mucilage
CN102813063A (en) * 2012-09-13 2012-12-12 上海红马饲料有限公司 Application of secoisolariciresinol diglucoside in livestock feed additive
CN108902441A (en) * 2018-07-20 2018-11-30 广州利众生物科技有限公司 A kind of flaxseed meal deep working method
CN109077319A (en) * 2018-08-30 2018-12-25 祁景泉 The method that lipid containing plant extract prepares ice cream, milk tea and pulvis
CN109535276A (en) * 2018-12-28 2019-03-29 呼和浩特市蒙谷香生物科技有限公司 The extracting method of flax glue and lignan in a kind of linseed meal

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1319634A (en) * 2000-02-01 2001-10-31 新疆昌吉市绿旗生物制品有限责任公司 Technology for producing flaxseed gum
CN1436826A (en) * 2003-03-07 2003-08-20 清华大学 Extraction process of linseed glue from linseed coat
CN1821332A (en) * 2006-01-19 2006-08-23 中国科学院山西煤炭化学研究所 A kind of production method of flax glue
CN101139373A (en) * 2007-07-31 2008-03-12 中国科学院过程工程研究所 A method for rapid large-scale extraction and purification of flax lignans

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009518311A (en) * 2005-12-02 2009-05-07 アーチャー・ダニエルズ・ミッドランド カンパニー Process for obtaining lignan extract and composition containing lignan extract

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1319634A (en) * 2000-02-01 2001-10-31 新疆昌吉市绿旗生物制品有限责任公司 Technology for producing flaxseed gum
CN1436826A (en) * 2003-03-07 2003-08-20 清华大学 Extraction process of linseed glue from linseed coat
CN1821332A (en) * 2006-01-19 2006-08-23 中国科学院山西煤炭化学研究所 A kind of production method of flax glue
CN101139373A (en) * 2007-07-31 2008-03-12 中国科学院过程工程研究所 A method for rapid large-scale extraction and purification of flax lignans

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Owner name: ARAM PHARMACEUTICAL CO., LTD., GANSU

Free format text: FORMER NAME: GANSU YALAN SPECIAL MEDICINE HERBS PRODUCTION CO., LTD.

CP01 Change in the name or title of a patent holder

Address after: 730101, No. 148, industry and Trade Street, Heping Town, Yuzhong County, Lanzhou, Gansu

Patentee after: Aram Pharmaceutical Co., Ltd., Gansu

Address before: 730101, No. 148, industry and Trade Street, Heping Town, Yuzhong County, Lanzhou, Gansu

Patentee before: Gansu Yalan Special Medicine Herbs Production Co., Ltd.

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Granted publication date: 20111207

Termination date: 20190521

CF01 Termination of patent right due to non-payment of annual fee