CN1710043A - Method for extracting passiflora seed oil from passiflora seeds - Google Patents
Method for extracting passiflora seed oil from passiflora seeds Download PDFInfo
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- CN1710043A CN1710043A CN 200510031720 CN200510031720A CN1710043A CN 1710043 A CN1710043 A CN 1710043A CN 200510031720 CN200510031720 CN 200510031720 CN 200510031720 A CN200510031720 A CN 200510031720A CN 1710043 A CN1710043 A CN 1710043A
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Abstract
This invention has disclosed a method for extracting seed oil from passionflower seed, it includes the following step: (1)Crush passionflower seed to dry, crush to 20-50 mesh, put it in the material tube of the extraction jar; (2) set up cold case temperature for extraction at - - 3 Deg. C, injet the liquified CO2 into the extraction cauldron passing through the purify machine and the preheater by using a high-pressure pump, the pressure up to l5MPa- 30MPa, the temp is 35 60 Deg. C and the extraction time for 4-5 hours; (3)Separate the CO2 fluid dissolved with oil which enters the separating cauldron from the extraction jar , the pressure of separating cauldron I is 8MPa- 12MPa, temperature is 35 - 60 Deg. C, the pressure of separating cauldron II keeps being balanced with the way of escape, temperature keeps 35 - 55 Deg. C. Advantages: high efficiency in extracting, energy consumption is low, the products are of high quality, there is no solvent to remain, pollution-free to the environment.
Description
Technical field
The present invention relates to a kind of method of from the Herba Passiflorae Caeruleae seed, extracting passionflower seed oil, especially relate to a kind of employing supercritical CO
2Abstraction technique extracts the method for passionflower seed oil from the Herba Passiflorae Caeruleae seed.
Background technology
Herba Passiflorae Caeruleae seed oleaginousness reaches 21.7%～29.2%, and seed benevolence oleaginousness is up to more than 60%, and it is formed based on unsaturated fatty acids--and linolic acid, oleic acid, particularly essential fatty acid--linoleic acid content is up to more than 72%.Linolic acid has the effect of anti-hemostasis suppository generation, vasodilation and nourishing brain cell, and vessel softening, reducing cholesterol are had extraordinary effect.In addition, also have physiological actions such as the function of keeping epithelium and neurocyte normal configuration and anti-oxidant, anti-ageing, vision protection, promotion upgrowth and development of children.Therefore, passionflower seed oil is a kind of fine natural product.
At present, extract seed oil and mostly be the organic solvent extraction method from the Herba Passiflorae Caeruleae seed, this method is not only extracted long flow path, energy consumption height, low, the serious environment pollution of yield; And the quality product of extraction is relatively poor, purity is low, and peculiar smell and dissolvent residual are arranged, and has had a strong impact on the promotion and application of passionflower seed oil.
Summary of the invention
The object of the present invention is to provide a kind of extraction efficiency height, product is pure, the method for extracting passionflower seed oil from the Herba Passiflorae Caeruleae seed of no solvent residue and environmentally safe.
The objective of the invention is to be achieved through the following technical solutions.
It comprises the steps: that (1) pulverizing with the Herba Passiflorae Caeruleae seed oven dry of cleaning, is crushed to 20～50 orders (preferred version is 30～40 orders), places the barrel of extraction cylinder, installs sealing-ring, screws plug; (2) extraction ice chest temperature is set to-3 ℃～3 ℃ (preferred version is 0 ℃), opens CO
2Steel cylinder, CO
2Come out from steel cylinder, enter in the ice chest through gas purifier I and liquefy, squeeze into the extraction cylinder by high-pressure pump through cleaner II, preheater I then, boost to 15MPa～30MPa, make it to become supercutical fluid and in the extraction cylinder, extract; Control extraction cylinder temperature is 35 ℃～60 ℃; 4～5 hours extraction time; (3) separation is dissolved with greasy CO
2Fluid from the extraction cylinder after decompression enters separation system, separate in separating still, the pressure of separation reactor I is 8MPa～12MPa (preferred version is 10MPa), and temperature is 35 ℃～60 ℃, the pressure of separation reactor I I keeps and way of escape balance, and temperature keeps 35 ℃～55 ℃.With this understanding, grease and CO
2Realize good separation, and emit CO from the separating still bottom
2Draw from the separating still top, enter ice chest liquefaction, recycle through cleaner I.
Advantage of the present invention is: technical process is simple, the extraction efficiency height, and product is pure, no solvent residue, environmentally safe.
Description of drawings
Accompanying drawing is the present invention's technological process apparatus synoptic diagram.
Embodiment
Below in conjunction with accompanying drawing and preferred embodiment the present invention is further described, but does not mean that and limit the scope of the invention.
Embodiment 1
(1) 2 kilograms of Herba Passiflorae Caeruleae seeds is cleaned oven dry, be crushed to the barrel of putting into 5L extraction cylinder 8 behind 30 orders; (2) open refrigeration, cold circulation, the temperature of ice chest 5 is set to 0 ℃; The temperature of extraction cylinder 8 is made as 45 ℃, the temperature of separation reactor I 10 is made as 40 ℃, the temperature of separation reactor I I12 and is made as 55 ℃, open CO
2Steel cylinder 2, CO
2Come out from steel cylinder 2, enter liquefaction in the ice chest 5, start high-pressure pump 6 then, CO through gas purifier I3
2Squeeze into extraction cylinder 8 through cleaner II4, preheater I7, boost to 30MPa, make it to become supercutical fluid and in the extraction cylinder, extract; (3) be dissolved with greasy CO
2Fluid enters separation system again after decompression enters preheater II9 preheating from extraction cylinder 8, in order to realize separating fully of unsaturated fatty acids and non-lipid material, reduce subsequent disposal work, adopt the secondary separating still that it is separated, the pressure of regulating separation reactor I 10 is 10MPa, and the pressure of separation reactor I I12 keeps and way of escape balance.Unsaturated fatty acids and CO
2I10 separates in separating still, and emits from separation reactor I 10 bottoms; Non-lipid material enters separation reactor I I12 after preheater III11 preheating, with CO
2In separation reactor I I12, separate CO
2Draw from the top, enter ice chest 5 liquefaction through cleaner I3, recycle by under meter 1.Extract after 4 hours, collect grease 540 grams, percentage extraction is 27%.
Embodiment 2
2 kilograms of Herba Passiflorae Caeruleae seeds are cleaned oven dry, be crushed to 40 orders; The pressure of control extraction cylinder is 15Mpa, and temperature is set to 35 ℃, and the pressure of separation reactor I is adjusted to 8Mpa, and temperature is set to 55 ℃, and the temperature of separation reactor I I is set to 40 ℃, and other extracted 5 hours with embodiment 1, collects grease 516 grams, and percentage extraction is 25.8%.
Embodiment 3
The pressure of control extraction cylinder is 20Mpa, and temperature is set to 55 ℃, and the pressure of separation reactor I is adjusted to 10Mpa, temperature is set to 35 ℃, and the temperature of separation reactor I I is set to 35 ℃, and all the other conditions remain unchanged, extracted 4.5 hours, and collected grease 500 grams, percentage extraction is 25%.
Claims (5)
1, a kind of method of extracting Passion Flower seed oil from the Passion Flower seed is characterized in that, comprises the steps: that (1) pulverizing with the Passion Flower seed oven dry of cleaning, is crushed to 20～50 orders, places the barrel of extraction cylinder, installs sealing-ring, screws plug; (2) extraction ice chest temperature is set to-3 ℃～3 ℃, opens CO
2Steel cylinder, CO
2Come out from steel cylinder, enter in the ice chest through gas purifier I and liquefy, squeeze into the extraction cylinder by high-pressure pump through cleaner II, preheater I then, boost to 15MPa～30MPa, make it to become supercutical fluid and in the extraction cylinder, extract; Control extraction cylinder temperature is 35 ℃～60 ℃; 4～5 hours extraction time; (3) separation is dissolved with greasy CO
2Fluid after decompression enters separation system, separates in separating still from the extraction cylinder, and the pressure of separation reactor I is 8MPa～12MPa, and temperature is 35 ℃～60 ℃ branches, and the pressure of separation reactor I I keeps and way of escape balance, and temperature keeps 35 ℃～55 ℃, grease and CO
2After the separation, emit CO from the separating still bottom
2Draw from the separating still top, enter ice chest liquefaction through cleaner I.
2, the method for extracting Passion Flower seed oil from the Passion Flower seed according to claim 1 is characterized in that, described Passion Flower seed is crushed to 30～40 orders.
3, the method for extracting Passion Flower seed oil from the Passion Flower seed according to claim 1 and 2 is characterized in that the ice chest temperature is set to 0 ℃.
4, the method for extracting Passion Flower seed oil from the Passion Flower seed according to claim 1 and 2 is characterized in that the pressure of separation reactor I is 10MPa.
5, the method for extracting Passion Flower seed oil from the Passion Flower seed according to claim 3 is characterized in that the pressure of separation reactor I is 10MPa.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100317205A CN1294242C (en) | 2005-06-17 | 2005-06-17 | Method for extracting passiflora seed oil from passiflora seeds |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100317205A CN1294242C (en) | 2005-06-17 | 2005-06-17 | Method for extracting passiflora seed oil from passiflora seeds |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1710043A true CN1710043A (en) | 2005-12-21 |
| CN1294242C CN1294242C (en) | 2007-01-10 |
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| Application Number | Title | Priority Date | Filing Date |
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| CNB2005100317205A Expired - Fee Related CN1294242C (en) | 2005-06-17 | 2005-06-17 | Method for extracting passiflora seed oil from passiflora seeds |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101851553A (en) * | 2010-07-15 | 2010-10-06 | 刘东波 | Method for extracting tea seed oil from tea tree seeds |
| EP2415743A1 (en) * | 2009-04-03 | 2012-02-08 | Morinaga & Co., Ltd. | Piceatannol-containing composition and method of producing piceatannol-containing composition |
| CN101874528B (en) * | 2009-04-29 | 2013-03-13 | 江城绿色版纳生态食品有限公司 | Method for extracting passionflower seed oil by cold pressing process |
| CN103952233A (en) * | 2014-04-30 | 2014-07-30 | 桂林军供生化技术开发有限公司 | Method for extracting passionflower seed oil |
| CN103992876A (en) * | 2014-05-30 | 2014-08-20 | 桂林科技企业发展中心 | Extraction method of passionflower seed oil |
| WO2017219101A1 (en) * | 2016-06-24 | 2017-12-28 | Universidade Estadual De Campinas - Unicamp | Process for sequentially extracting bioactive compounds from passion fruit bagasse and use of said bioactive compounds |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102199481B (en) * | 2011-04-13 | 2012-05-23 | 北海田野食品有限公司 | Method for extracting passion flower seed oil by utilizing aqueous enzymatic method |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1088745C (en) * | 1999-05-13 | 2002-08-07 | 潘泰安 | Fruit seed oil obtained by supercritical CO2 extraction and its product |
| CN1414078A (en) * | 2002-09-30 | 2003-04-30 | 内蒙古宇航人高技术产业有限责任公司 | Super critical corbon dioxide extraction vegetable seed oil and its product |
-
2005
- 2005-06-17 CN CNB2005100317205A patent/CN1294242C/en not_active Expired - Fee Related
Cited By (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102307837B (en) * | 2009-04-03 | 2014-08-20 | 森永制果株式会社 | Piceatannol-containing composition and method of producing piceatannol-containing composition |
| EP2415743A1 (en) * | 2009-04-03 | 2012-02-08 | Morinaga & Co., Ltd. | Piceatannol-containing composition and method of producing piceatannol-containing composition |
| EP2415743A4 (en) * | 2009-04-03 | 2012-08-08 | Morinaga & Co | Piceatannol-containing composition and method of producing piceatannol-containing composition |
| JP5347018B2 (en) * | 2009-04-03 | 2013-11-20 | 森永製菓株式会社 | Piceatannol-containing composition and method for producing piceatannol-containing composition |
| US8617620B2 (en) | 2009-04-03 | 2013-12-31 | Morinaga & Co., Ltd. | Piceatannol-containing composition and method of producing piceatannol-containing composition |
| US9393191B2 (en) | 2009-04-03 | 2016-07-19 | Morinaga & Co., Ltd. | Piceatannol-containing composition and method of producing piceatannol-containing composition |
| CN101874528B (en) * | 2009-04-29 | 2013-03-13 | 江城绿色版纳生态食品有限公司 | Method for extracting passionflower seed oil by cold pressing process |
| CN101851553B (en) * | 2010-07-15 | 2012-11-14 | 湖南万源生物科技有限责任公司 | Method for extracting tea seed oil from tea tree seeds |
| CN101851553A (en) * | 2010-07-15 | 2010-10-06 | 刘东波 | Method for extracting tea seed oil from tea tree seeds |
| CN103952233A (en) * | 2014-04-30 | 2014-07-30 | 桂林军供生化技术开发有限公司 | Method for extracting passionflower seed oil |
| CN103952233B (en) * | 2014-04-30 | 2016-02-10 | 桂林融通科技有限公司 | A kind of extracting method of passionflower seed oil |
| CN103992876A (en) * | 2014-05-30 | 2014-08-20 | 桂林科技企业发展中心 | Extraction method of passionflower seed oil |
| WO2017219101A1 (en) * | 2016-06-24 | 2017-12-28 | Universidade Estadual De Campinas - Unicamp | Process for sequentially extracting bioactive compounds from passion fruit bagasse and use of said bioactive compounds |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1294242C (en) | 2007-01-10 |
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