CN106350233A - Preparation method of high-quality ethyl linolenate - Google Patents

Preparation method of high-quality ethyl linolenate Download PDF

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Publication number
CN106350233A
CN106350233A CN201610710733.3A CN201610710733A CN106350233A CN 106350233 A CN106350233 A CN 106350233A CN 201610710733 A CN201610710733 A CN 201610710733A CN 106350233 A CN106350233 A CN 106350233A
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China
Prior art keywords
ethyl
ester
fatty acid
acid ethyl
preparation
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Pending
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CN201610710733.3A
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Chinese (zh)
Inventor
张全智
杨军龙
张博坤
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HARBIN PURUN GREASE Co Ltd
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HARBIN PURUN GREASE Co Ltd
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Priority to CN201610710733.3A priority Critical patent/CN106350233A/en
Publication of CN106350233A publication Critical patent/CN106350233A/en
Pending legal-status Critical Current

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    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11CFATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
    • C11C3/00Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom
    • C11C3/04Fats, oils, or fatty acids by chemical modification of fats, oils, or fatty acids obtained therefrom by esterification of fats or fatty oils
    • C11C3/10Ester interchange
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11CFATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
    • C11C1/00Preparation of fatty acids from fats, fatty oils, or waxes; Refining the fatty acids
    • C11C1/08Refining
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11CFATTY ACIDS FROM FATS, OILS OR WAXES; CANDLES; FATS, OILS OR FATTY ACIDS BY CHEMICAL MODIFICATION OF FATS, OILS, OR FATTY ACIDS OBTAINED THEREFROM
    • C11C1/00Preparation of fatty acids from fats, fatty oils, or waxes; Refining the fatty acids
    • C11C1/08Refining
    • C11C1/10Refining by distillation

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Microbiology (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Fats And Perfumes (AREA)

Abstract

The invention relates to a preparation method of high-quality ethyl linolenate. The preparation method comprises the following preparation steps: filtering and drying original oil, uniformly mixing with an ethanol solution under the action of a KOH catalyst, stirring, heating, and refluxing to perform an ester exchange reaction, thus obtaining mixed fatty acid ethyl ester; separating saturated fatty acid ethyl ester from unsaturated fatty acid ethyl ester by virtue of a crystallization method, thus obtaining an unsaturated fatty acid ethyl ester semi-finished product; and evaporating the unsaturated fatty acid ethyl ester semi-finished product by using a film evaporator, separating excessive ethanol and light components in the material, enabling heavy phase to enter primary molecular distillation, separating the heavy phase in the material by virtue of heating separation, enabling a light phase to enter secondary molecular distillation, separating high-carbon ester in the material, and obtaining a product consisting of ethyl oleate, ethyl linoleate and ethyl linolenate at a light phase material outlet. The method is stable, reliable and simple in operation, and has the advantages of high purity, low cost and suitability for mass production.

Description

A kind of high-quality ethyl linolenate preparation method
Technical field
The present invention relates to the technology of preparing of unsaturated fatty acid ethyl ester, it is specifically related to a kind of high-quality ethyl linolenate system Preparation Method.
Background technology
Linoleic acid plus linolenic acid, is unsaturated fatty acid needed by human, and human body itself can not synthesize, and can only take the photograph from the external world Take.Linoleic acid plus linolenic acid can be effectively reduced hyperlipidemia and hypertension, the formation of suppression thromboxane, mitigates arteriosclerosis, Prevention and cure of cardiovascular disease etc.;Liver synthetic fatty acid and lipoprotein can also be suppressed, change blood viscosity, expansion of blood vessels, suppress blood Platelet aggregation;And also there are anticancer, defying age, nootropics, cardioprotection etc. acts on.In view of the weight of linoleic acid plus linolenic acid The property wanted and the situation of the universal Deficiency of Intake of the mankind, World Health Organization (WHO) and FAO's suggestion be special supplement linoleic acid and Linolenic acid.
Content of the invention
The technical problem to be solved is to provide a kind of high-quality ethyl linolenate preparation method, from crude oil fat The product containing ethyl oleate, Ethyl linoleate and ethyl linolenate extracting high-quality supplies human body to supplement.
For solving above-mentioned technical problem, the present invention provides a kind of technical scheme below: high-quality ethyl linolenate preparation side Method, including following preparation process:
(1) by the crude oil fat containing ethyl linolenate through filtration, dried;
(2) the crude oil fat obtaining in step (1) is mixed homogeneously with ethanol solution under koh catalyst action, stirring, plus Hot reflux carries out ester exchange reaction;After cooling, add water the dilute regulation ph of solution to acid, isolate oils and fatss, extractant extracts, then Washing, dry, filtration, obtain the mixing-in fat acetoacetic ester containing saturated fat acetoacetic ester and unsaturated fatty acid ethyl ester;Wherein, Saturated fat acetoacetic ester is made up of ethyl palmitate, ethyl stearte, and unsaturated fatty acid ethyl ester is by ethyl oleate, linoleic acid second Ester and ethyl linolenate composition;
(3) utilize saturated fat acetoacetic ester different with the freezing point of unsaturated fatty acid ethyl ester, will be satisfied by crystallization method Separate with fatty-acid ethyl ester and unsaturated fatty acid ethyl ester, obtain unsaturated fatty acid ethyl ester semi-finished product;
(4) the unsaturated fatty acid ethyl ester semi-finished product that step (3) obtains are evaporated, by material using membrane evaporator In excess ethyl alcohol and light component separate, heavy phase enter next procedure pending;
(5) the heavy phase material that step (4) obtains is carried out first order molecular distillation in first order molecular distillator, heated point From after the heavy phase in material is separated, light phase entrance next procedure pending;
(6) the light phase material that step (5) obtains is carried out secondary molecules distillation in secondary molecules distillator, by material High carbon chain ethyl ester separate, light phase material outlet i.e. can get by ethyl oleate, Ethyl linoleate and ethyl linolenate The product of composition.
On the basis of such scheme, the vacuum level requirements of the molecular distillation in described step (5) and step (6) are less than 1.0pa.
On the basis of such scheme, the crude oil fat in described step (1) is Semen Lini oil or perilla oil.
On the basis of such scheme, in described step (2), the amount of koh catalyst accounts for the 1~1.8% of former oil quality, former Oils and fatss and ethanol solution mass volume ratio are 1: 2.5~4.
On the basis of such scheme, in described step (2), crude oil fat is heated to reflux carrying out adding of ester exchange reaction Hot temperature is 50-60 DEG C, and reflux time is 2-5 hour.
On the basis of such scheme, described reflux time is 3 hours.
The present invention compared with prior art has the beneficial effect that the inventive method is reliable and stable, easy and simple to handle, has Purity height, low cost, the advantage being suitable for large-scale production.
Specific embodiment
In order that the objects, technical solutions and advantages of the present invention become more apparent, with reference to embodiments, to the present invention It is further elaborated.It should be appreciated that specific embodiment described herein, only in order to explain the present invention, is not used to Limit the present invention.
A kind of high-quality ethyl linolenate preparation method, including following preparation process:
(1) by the crude oil fat containing ethyl linolenate through filtration, dried;Crude oil fat at this can be Semen Lini Oil or perilla oil.
(2) the crude oil fat obtaining in step (1) is mixed homogeneously with ethanol solution under koh catalyst action, stirring, It is heated to reflux at 50 DEG C 3 hours carrying out ester exchange reaction;After cooling, add water the dilute regulation ph of solution to acid, isolate oils and fatss, extraction Agent is taken to extract, then washing, dry, filtration, obtain the mixing fat containing saturated fat acetoacetic ester and unsaturated fatty acid ethyl ester Fat acetoacetic ester;Wherein, saturated fat acetoacetic ester is made up of ethyl palmitate, ethyl stearte, and unsaturated fatty acid ethyl ester is by oil Acetoacetic ester, Ethyl linoleate and ethyl linolenate composition;Wherein, the amount of koh catalyst accounts for the 1.4% of former oil quality, crude oil Fat and ethanol solution mass volume ratio are 1: 2.5.
(3) utilize saturated fat acetoacetic ester different with the freezing point of unsaturated fatty acid ethyl ester, will be satisfied by crystallization method Separate with fatty-acid ethyl ester and unsaturated fatty acid ethyl ester, obtain unsaturated fatty acid ethyl ester semi-finished product.
(4) the unsaturated fatty acid ethyl ester semi-finished product that step (3) obtains are evaporated, by material using membrane evaporator In excess ethyl alcohol and light component separate, heavy phase enter next procedure pending.
(5) the heavy phase material that step (4) obtains is carried out first order molecular distillation, molecular distillation in first order molecular distillator Vacuum 0.8pa, after heated separation, the heavy phase in material is separated, light phase entrance next procedure pending.
(6) the light phase material that step (5) obtains is carried out secondary molecules distillation, molecular distillation in secondary molecules distillator Vacuum 0.8pa, the high carbon chain ethyl ester in material is separated, light phase material outlet i.e. can get by ethyl oleate, Ethyl linoleate and the product of ethyl linolenate composition.

Claims (6)

1. a kind of high-quality ethyl linolenate preparation method is it is characterised in that include following preparation process:
(1) by the crude oil fat containing ethyl linolenate through filtration, dried;
(2) the crude oil fat obtaining in step (1) is mixed homogeneously with ethanol solution under koh catalyst action, stirring, heat back Stream carries out ester exchange reaction;After cooling, add water the dilute regulation ph of solution to acid, isolate oils and fatss, extractant extracts, Ran Houshui Wash, be dried, filter, obtain the mixing-in fat acetoacetic ester containing saturated fat acetoacetic ester and unsaturated fatty acid ethyl ester;Wherein, satisfy It is made up of ethyl palmitate, ethyl stearte with fatty-acid ethyl ester, unsaturated fatty acid ethyl ester is by ethyl oleate, Ethyl linoleate With ethyl linolenate composition;
(3) utilize saturated fat acetoacetic ester different with the freezing point of unsaturated fatty acid ethyl ester, by crystallization method by saturated fat Fat acetoacetic ester and unsaturated fatty acid ethyl ester separately, obtain unsaturated fatty acid ethyl ester semi-finished product;
(4) the unsaturated fatty acid ethyl ester semi-finished product that step (3) obtains are evaporated, by material using membrane evaporator Excess ethyl alcohol and light component separate, and it is pending that heavy phase enters next procedure;
(5) the heavy phase material that step (4) obtains is carried out first order molecular distillation in first order molecular distillator, after heated separation Heavy phase in material is separated, light phase entrance next procedure is pending;
(6) the light phase material that step (5) obtains is carried out secondary molecules distillation in secondary molecules distillator, by the height in material Carbochain ethyl ester is separated, and can get in light phase material outlet and is made up of ethyl oleate, Ethyl linoleate and ethyl linolenate Product.
2. high-quality ethyl linolenate preparation method according to claim 1 it is characterised in that described step (5) and step Suddenly the vacuum level requirements of the molecular distillation in (6) are less than 1.0pa.
3. high-quality ethyl linolenate preparation method according to claim 1 is it is characterised in that in described step (1) Crude oil fat is Semen Lini oil or perilla oil.
4. high-quality ethyl linolenate preparation method according to claim 1 is it is characterised in that koh in described step (2) The amount of catalyst accounts for the 1~1.8% of former oil quality, and crude oil fat and ethanol solution mass volume ratio are 1: 2.5~4.
5. high-quality ethyl linolenate preparation method according to claim 1 is it is characterised in that incite somebody to action in described step (2) The heating-up temperature that crude oil fat is heated to reflux carrying out ester exchange reaction is 50-60 DEG C, and reflux time is 2-5 hour.
6. high-quality ethyl linolenate preparation method according to claim 5 is it is characterised in that described reflux time For 3 hours.
CN201610710733.3A 2016-08-24 2016-08-24 Preparation method of high-quality ethyl linolenate Pending CN106350233A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109337939A (en) * 2018-09-30 2019-02-15 河北康睿达脂质有限公司 A kind of preparation method of polyunsaturated fatty acid structured lipid
CN109369389A (en) * 2018-12-20 2019-02-22 燕园泽龙(涿鹿)生物科技有限公司 The preparation process of high-purity alpha-linolenic acid ethyl ester
CN110857270A (en) * 2018-08-22 2020-03-03 大连医诺生物股份有限公司 High-content conjugated linoleic acid triglyceride and preparation method thereof
CN111302940A (en) * 2020-04-08 2020-06-19 燕园泽龙(涿鹿)生物科技有限公司 Production method of high-purity α -ethyl linolenate

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1394944A (en) * 2001-07-11 2003-02-05 北京万博力科技发展有限公司 Method for preparing alpha-ethyl linolenate from linseed oil by means of ester exchange
CN101139289A (en) * 2007-08-22 2008-03-12 安阳化学工业集团有限责任公司 Technique for producing alpha-linolenic acid ethyl with 90 percent more purity
CN102993011A (en) * 2011-09-13 2013-03-27 丰宁京北第一草原原生态食品科技开发有限公司 Method for preparing alpha-ethyl linolenate through using Fructus Perillae oil

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1394944A (en) * 2001-07-11 2003-02-05 北京万博力科技发展有限公司 Method for preparing alpha-ethyl linolenate from linseed oil by means of ester exchange
CN101139289A (en) * 2007-08-22 2008-03-12 安阳化学工业集团有限责任公司 Technique for producing alpha-linolenic acid ethyl with 90 percent more purity
CN102993011A (en) * 2011-09-13 2013-03-27 丰宁京北第一草原原生态食品科技开发有限公司 Method for preparing alpha-ethyl linolenate through using Fructus Perillae oil

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Title
丁保淼等: "《食用油脂贮藏加工技术100问》", 31 August 2015, 中国农业出版社 *

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110857270A (en) * 2018-08-22 2020-03-03 大连医诺生物股份有限公司 High-content conjugated linoleic acid triglyceride and preparation method thereof
CN110857270B (en) * 2018-08-22 2022-11-29 大连医诺生物股份有限公司 High-content conjugated linoleic acid triglyceride and preparation method thereof
CN109337939A (en) * 2018-09-30 2019-02-15 河北康睿达脂质有限公司 A kind of preparation method of polyunsaturated fatty acid structured lipid
CN109369389A (en) * 2018-12-20 2019-02-22 燕园泽龙(涿鹿)生物科技有限公司 The preparation process of high-purity alpha-linolenic acid ethyl ester
CN111302940A (en) * 2020-04-08 2020-06-19 燕园泽龙(涿鹿)生物科技有限公司 Production method of high-purity α -ethyl linolenate

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Application publication date: 20170125