EP1916294B1 - Essential oil and aromatic water extraction process from vegetable matrices - Google Patents
Essential oil and aromatic water extraction process from vegetable matrices Download PDFInfo
- Publication number
- EP1916294B1 EP1916294B1 EP07020630A EP07020630A EP1916294B1 EP 1916294 B1 EP1916294 B1 EP 1916294B1 EP 07020630 A EP07020630 A EP 07020630A EP 07020630 A EP07020630 A EP 07020630A EP 1916294 B1 EP1916294 B1 EP 1916294B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- water
- vegetable
- essential oil
- matrix
- extraction process
- 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.)
- Not-in-force
Links
- 235000013311 vegetables Nutrition 0.000 title claims abstract description 28
- 125000003118 aryl group Chemical group 0.000 title claims abstract description 18
- 239000000341 volatile oil Substances 0.000 title claims abstract description 18
- 238000000034 method Methods 0.000 title description 17
- 238000003809 water extraction Methods 0.000 title 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 35
- 239000011159 matrix material Substances 0.000 claims abstract description 26
- 238000010438 heat treatment Methods 0.000 claims abstract description 17
- 238000000605 extraction Methods 0.000 claims abstract description 10
- 150000003839 salts Chemical class 0.000 claims abstract description 10
- 239000002904 solvent Substances 0.000 claims abstract description 7
- 238000009835 boiling Methods 0.000 claims abstract description 6
- 238000009833 condensation Methods 0.000 claims abstract description 3
- 230000005494 condensation Effects 0.000 claims abstract description 3
- 238000001704 evaporation Methods 0.000 claims abstract 2
- 230000008020 evaporation Effects 0.000 claims abstract 2
- 229910017053 inorganic salt Inorganic materials 0.000 claims description 5
- 239000000463 material Substances 0.000 description 7
- 210000004027 cell Anatomy 0.000 description 6
- 239000012530 fluid Substances 0.000 description 4
- 239000003921 oil Substances 0.000 description 4
- 238000000265 homogenisation Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 239000005418 vegetable material Substances 0.000 description 2
- 239000003643 water by type Substances 0.000 description 2
- 239000008346 aqueous phase Substances 0.000 description 1
- 235000019568 aromas Nutrition 0.000 description 1
- 238000000222 aromatherapy Methods 0.000 description 1
- 150000001491 aromatic compounds Chemical class 0.000 description 1
- 210000000170 cell membrane Anatomy 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229930014626 natural product Natural products 0.000 description 1
- 230000003204 osmotic effect Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, e.g. BY PRESSING RAW MATERIALS OR BY EXTRACTION FROM WASTE MATERIALS, REFINING OR PRESERVING FATS, FATTY SUBSTANCES, e.g. LANOLIN, FATTY OILS OR WAXES; ESSENTIAL OILS; PERFUMES
- C11B9/00—Essential oils; Perfumes
- C11B9/02—Recovery or refining of essential oils from raw materials
- C11B9/027—Recovery of volatiles by distillation or stripping
Definitions
- the invention regards an extraction process of natural products from plant material, in the absence of solvent.
- the obtained products are essential oils and aromatic water
- the oils are volatile aromatic compounds that are obtained by distillation of the vapor that is created as a result of the heating of the vegetable matrix, after that the cell structures are demolished and the water in them contained is released.
- FR-A-2787347 describes a process that provides for the extraction of oils and aromatic water from plant matrices in the absence of solvent, only taking advantage of the water contained in the vegetable structures and proceeding to the heating under vacuum and the separation of the aqueous phase from the oil. So it is a hydrodistillation process without homogenization of the vegetable matrix, in which by microwave irradiation of plant material the vegetable structures are broken. Moreover in this process heating uniformity is not guaranteed as heating treatment and vacuum conditions are contextual.
- WO-A-9426853 defines a demolition technique of cell structures of a plant material by irradiation with microwave, aimed at extracting essential oils by hydrodistillation. Also in this case the extraction is performed in the absence of solvent and the obtained water originates from the matrix. Again in this process heating uniformity is not guaranteed as heating treatment and vacuum conditions are contextual.
- the salt is an organic salt.
- the salt is an inorganic salt.
- Another characteristic is given by the fact that the vegetable matrix is heated with a hot bath to a temperature 30 degrees higher than the boiling point.
- the vegetable matrix is homogenized with an inorganic salt, added to 20%, in order to create on the cell membrane a proper osmotic pressure to the leakage of the water and the consequent demolition of the cell structures and placed in a container 1.
- the container 1 with the homogenized plant material is placed under vacuum, created by vacuum pump 6 (wide range, centred at 20 mmHg) and the container 1 is dipped in a fluid heating bath 2 previously heated.
- the temperature of the bath 2 must be at least 30 degrees higher than the water boiling point under the used pressure conditions.
- the fast heating and vacuum conditions involve the generation of a water vapor current in which the volatile organic components resulting from the demolition of cell structures codistill.
- the vapors pass through the tube 3 and condense in the collector 4 maintained at low temperature by the cold bath 5.
- the essential oil is recovered by separation from the aromatic water.
- the obtained aromatic water is ideal for the preparation of cosmetic products and constitutes (according to the type and the state of the matrix) the 20-80 % in weight of the matrix subjected to the treatment.
- the aromatic water and the essential oil so obtained can find application in the field of aromatherapy and food productions and aromas.
- the duration of the separation process is short, only 15-30 minutes per 500 g of material.
- the process can be applied to flowers, leaves, peels and every kind of vegetable material.
- This invention has numerous advantages and will permit to overcome problems which could not be achieved by heating systems on the market today.
Landscapes
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Fats And Perfumes (AREA)
- Extraction Or Liquid Replacement (AREA)
Abstract
Description
- The invention regards an extraction process of natural products from plant material, in the absence of solvent. In particular at the end of this process the obtained products are essential oils and aromatic water, the oils are volatile aromatic compounds that are obtained by distillation of the vapor that is created as a result of the heating of the vegetable matrix, after that the cell structures are demolished and the water in them contained is released.
- For the extraction of oils and aromatic waters from vegetable matrices in the absence of solvent were used different processes.
describes a process that provides for the extraction of oils and aromatic water from plant matrices in the absence of solvent, only taking advantage of the water contained in the vegetable structures and proceeding to the heating under vacuum and the separation of the aqueous phase from the oil. So it is a hydrodistillation process without homogenization of the vegetable matrix, in which by microwave irradiation of plant material the vegetable structures are broken. Moreover in this process heating uniformity is not guaranteed as heating treatment and vacuum conditions are contextual.FR-A-2787347 -
defines a demolition technique of cell structures of a plant material by irradiation with microwave, aimed at extracting essential oils by hydrodistillation. Also in this case the extraction is performed in the absence of solvent and the obtained water originates from the matrix. Again in this process heating uniformity is not guaranteed as heating treatment and vacuum conditions are contextual.WO-A-9426853 - The limits of these processes are as follows:
- Lack of homogenization of the vegetable matrix;
- Lack of uniformity of heating temperature because the heating treatment occurs concurrently with the pression reduction.
- The limitations and disadvantages existing in the state of the art are overcome by the present extraction process of aromatic water and essential oils from plant material, in the absence of solvent, in which the vegetable matrix is placed under vacuum and heated to a temperature higher than the water boiling point, in which the evaporated water comes exclusively from vegetable matrix as a result of the breaking of the cell structures, in which vapors condense by lowering of the temperature, in which after condensation in a collector water and essential oil are recovered, characterized by the fact that the vegetable matrix is homogenized with the addition of a salt soluble in water, that the heating is performed under vacuum with a hot bath.
- Another characteristic is given by the fact that the salt is an organic salt.
- Another characteristic is given by the fact that the salt is an inorganic salt.
- Another characteristic is given by the fact that the vegetable matrix is heated with a hot bath to a temperature 30 degrees higher than the boiling point.
- Other characteristics and advantages of the invention will appear clear from the following description of some methods of creating the invention, given as non-limiting examples in
figure 1 . -
-
Fig. 1 : The figure schematically represents a way to realize a system in order to carry out the process object of the invention. - For the realization of the process object of the present invention, the vegetable matrix is homogenized with an inorganic salt, added to 20%, in order to create on the cell membrane a proper osmotic pressure to the leakage of the water and the consequent demolition of the cell structures and placed in a container 1.
- The container 1 with the homogenized plant material is placed under vacuum, created by vacuum pump 6 (wide range, centred at 20 mmHg) and the container 1 is dipped in a fluid heating bath 2 previously heated. The temperature of the bath 2 must be at least 30 degrees higher than the water boiling point under the used pressure conditions. The fast heating and vacuum conditions involve the generation of a water vapor current in which the volatile organic components resulting from the demolition of cell structures codistill.
- The vapors pass through the
tube 3 and condense in the collector 4 maintained at low temperature by the cold bath 5. - From the collector 4 are recovered:
- 1. aromatic water, that is the water contained exclusively in the vegetable matrix, that is made aromatic by the volatile components that codistill with water and that in it are soluble;
- 2. essential oil constituted by the volatile components present in the vegetable matrix. This is immiscible in the water.
- The essential oil is recovered by separation from the aromatic water. The obtained aromatic water is ideal for the preparation of cosmetic products and constitutes (according to the type and the state of the matrix) the 20-80 % in weight of the matrix subjected to the treatment. The aromatic water and the essential oil so obtained can find application in the field of aromatherapy and food productions and aromas.
- The duration of the separation process is short, only 15-30 minutes per 500 g of material.
- The process can be applied to flowers, leaves, peels and every kind of vegetable material.
- The process is performed implementing the following steps:
- 1. the organic matrix is homogenized with an organic or inorganic salt, placed under vacuum and heated. The developed vapors are condensed by lowering the temperature.
- 1.1 Any organic or inorganic salt, water-soluble, can be used in the process of homogenization. It contributes to demolish the cell structures of the vegetable material and indirectly promotes the heat conduction in the heating step.
- 1.2 In experiments carried out without the addition of salt the yields in recovered product are reduced until 50% for aromatic waters and 65% for essential oils.
- 1.3 The heating is performed by a fluid bath. The vegetable matrix can be heated also by coils in which a hot fluid flows in and placed in the same matrix.
- 1.4 The temperature of the heating fluid can be changed in a single process and/or depending on the material to treat.
- 1.5 The products of the process are: 1) essential oil and aromatic water; 2) aromatic water only; 3) essential oil only. The variability of the products depends on the type of matrix, the state of the matrix (fresh or dried) and the period of its collection.
- 1.6 The vegetable matrix can be constituted by flowers, leaves, parts of stalk, parts of roots, peels etc.
- This invention is not limited to the representation given by the figures but can be perfected and modified by men expert in the art without altering the aim of the patent.
- This invention has numerous advantages and will permit to overcome problems which could not be achieved by heating systems on the market today.
Claims (4)
- Aromatic water and essential oil extraction process from vegetable matrices, in the absence of solvent, in which the vegetable matrix is placed under vacuum and heated to a temperature higher than the water boiling point, in which the water that is obtained from the evaporation comes exclusively from the vegetable matrix as a result of the breaking of the cell structures, in which vapors condense by lowering the temperature, in which after condensation in a collector water and essential oil are recovered, characterized by the fact that the vegetable matrix is homogenized with an homogenizer and with the addition of a salt soluble in water and that the heating is performed under vacuum with a hot bath.
- Aromatic water and essential oil extraction process from vegetable matrices according to claim 1, characterized by the facet that the salt is an organic salt.
- Aromatic water and essential oil extraction process from vegetable matrices according to claim 1, characterized by the fact that the salt is an inorganic salt.
- Aromatic water and essential oil extraction process from vegetable matrices according to claim 1 or 2, characterized by the fact that the vegetable matrix is heated with a hot bath to a temperature 30 degrees higher than the boiling point of water measured at the respective vacuum.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| IT000028A ITCZ20060028A1 (en) | 2006-10-23 | 2006-10-23 | PROCESS OF EXTRACTION OF ESSENTIAL OILS AND AROMATIC WATERS FROM VEGETABLE MATRICES |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP1916294A1 EP1916294A1 (en) | 2008-04-30 |
| EP1916294B1 true EP1916294B1 (en) | 2011-06-15 |
Family
ID=38896663
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP07020630A Not-in-force EP1916294B1 (en) | 2006-10-23 | 2007-10-22 | Essential oil and aromatic water extraction process from vegetable matrices |
Country Status (3)
| Country | Link |
|---|---|
| EP (1) | EP1916294B1 (en) |
| AT (1) | ATE513029T1 (en) |
| IT (1) | ITCZ20060028A1 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9549567B2 (en) | 2012-12-28 | 2017-01-24 | Clariant International Ltd. | Method for obtaining aromatics |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR3013563B1 (en) * | 2013-11-28 | 2017-06-30 | Finat Conseil & Distrib | PROCESS FOR MANUFACTURING NATURAL AND STABLE AROMATIZING PREPARATIONS AND AROMATIZING PREPARATIONS OBTAINED BY SAID METHOD |
| CN112760172A (en) * | 2021-02-05 | 2021-05-07 | 贵阳新奇微波工业有限责任公司 | Device and method for collecting flower aromatic water through low-temperature microwave heating and condensation |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE511794C (en) * | 1927-03-17 | 1930-11-12 | Chem Fab Vormals Sandoz | Process for the extraction of the cardiac glycoside from the sea onion |
| FR675658A (en) * | 1929-05-24 | 1930-02-13 | Process for the extraction of odorous and volatile substances from plants and plant parts | |
| FR2787347B1 (en) * | 1998-12-17 | 2001-01-19 | Gattefosse Ets Sa | METHOD FOR MANUFACTURING AN EMULSION BASED ON AROMATIC PLANT MATERIAL, EMULSION LIKELY TO BE OBTAINED BY SAID METHOD AND USE OF SAID EMULSION |
| BR0215660A (en) * | 2002-03-25 | 2005-01-25 | Council Scient Ind Res | Essential oil with citronellol and dracocephalum heterophyllum agrostis rose oxides and a process for obtaining it |
-
2006
- 2006-10-23 IT IT000028A patent/ITCZ20060028A1/en unknown
-
2007
- 2007-10-22 AT AT07020630T patent/ATE513029T1/en not_active IP Right Cessation
- 2007-10-22 EP EP07020630A patent/EP1916294B1/en not_active Not-in-force
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9549567B2 (en) | 2012-12-28 | 2017-01-24 | Clariant International Ltd. | Method for obtaining aromatics |
Also Published As
| Publication number | Publication date |
|---|---|
| ITCZ20060028A1 (en) | 2008-04-24 |
| ATE513029T1 (en) | 2011-07-15 |
| EP1916294A1 (en) | 2008-04-30 |
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