CN112662476A - Extraction method of rose essential oil with high oil yield - Google Patents
Extraction method of rose essential oil with high oil yield Download PDFInfo
- Publication number
- CN112662476A CN112662476A CN202011615692.2A CN202011615692A CN112662476A CN 112662476 A CN112662476 A CN 112662476A CN 202011615692 A CN202011615692 A CN 202011615692A CN 112662476 A CN112662476 A CN 112662476A
- Authority
- CN
- China
- Prior art keywords
- rose
- oil
- distillation
- extraction method
- water
- 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.)
- Pending
Links
- 241000220317 Rosa Species 0.000 title claims abstract description 121
- 239000000341 volatile oil Substances 0.000 title claims abstract description 43
- 239000003921 oil Substances 0.000 title claims abstract description 26
- 238000000605 extraction Methods 0.000 title claims description 16
- 238000004821 distillation Methods 0.000 claims abstract description 97
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 39
- 239000000203 mixture Substances 0.000 claims abstract description 25
- 235000019198 oils Nutrition 0.000 claims abstract description 25
- 238000010438 heat treatment Methods 0.000 claims abstract description 20
- 239000010666 rose oil Substances 0.000 claims abstract description 20
- 235000019719 rose oil Nutrition 0.000 claims abstract description 20
- 238000000926 separation method Methods 0.000 claims abstract description 12
- 238000009833 condensation Methods 0.000 claims abstract description 10
- 230000005494 condensation Effects 0.000 claims abstract description 10
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 15
- 229910052802 copper Inorganic materials 0.000 claims description 15
- 239000010949 copper Substances 0.000 claims description 15
- 239000007788 liquid Substances 0.000 claims description 13
- 239000011521 glass Substances 0.000 claims description 12
- 238000009835 boiling Methods 0.000 claims description 10
- 238000000034 method Methods 0.000 abstract description 20
- 230000009286 beneficial effect Effects 0.000 abstract description 4
- 238000004321 preservation Methods 0.000 abstract description 3
- 239000000446 fuel Substances 0.000 abstract 1
- 239000008132 rose water Substances 0.000 abstract 1
- 235000004789 Rosa xanthina Nutrition 0.000 description 22
- 241000109329 Rosa xanthina Species 0.000 description 21
- 230000008569 process Effects 0.000 description 11
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 6
- 238000009423 ventilation Methods 0.000 description 6
- 244000105624 Arachis hypogaea Species 0.000 description 5
- 239000003205 fragrance Substances 0.000 description 5
- 235000020232 peanut Nutrition 0.000 description 5
- 230000035943 smell Effects 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 230000001737 promoting effect Effects 0.000 description 4
- 230000000630 rising effect Effects 0.000 description 4
- 235000013399 edible fruits Nutrition 0.000 description 3
- 239000000796 flavoring agent Substances 0.000 description 3
- 235000019634 flavors Nutrition 0.000 description 3
- 229910052742 iron Inorganic materials 0.000 description 3
- 239000002893 slag Substances 0.000 description 3
- CIWBSHSKHKDKBQ-JLAZNSOCSA-N Ascorbic acid Chemical compound OC[C@H](O)[C@H]1OC(=O)C(O)=C1O CIWBSHSKHKDKBQ-JLAZNSOCSA-N 0.000 description 2
- 208000035473 Communicable disease Diseases 0.000 description 2
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 2
- 206010061218 Inflammation Diseases 0.000 description 2
- 235000011449 Rosa Nutrition 0.000 description 2
- 240000008254 Rosa chinensis Species 0.000 description 2
- 235000000664 Rosa chinensis Nutrition 0.000 description 2
- 150000001299 aldehydes Chemical class 0.000 description 2
- 125000003118 aryl group Chemical group 0.000 description 2
- 230000003796 beauty Effects 0.000 description 2
- 230000017531 blood circulation Effects 0.000 description 2
- 239000006260 foam Substances 0.000 description 2
- 230000004054 inflammatory process Effects 0.000 description 2
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 2
- 210000004185 liver Anatomy 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 206010000087 Abdominal pain upper Diseases 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- WVDDGKGOMKODPV-UHFFFAOYSA-N Benzyl alcohol Chemical compound OCC1=CC=CC=C1 WVDDGKGOMKODPV-UHFFFAOYSA-N 0.000 description 1
- 206010006298 Breast pain Diseases 0.000 description 1
- 206010006312 Breast swelling Diseases 0.000 description 1
- ZZZCUOFIHGPKAK-UHFFFAOYSA-N D-erythro-ascorbic acid Natural products OCC1OC(=O)C(O)=C1O ZZZCUOFIHGPKAK-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- 208000006662 Mastodynia Diseases 0.000 description 1
- 208000037093 Menstruation Disturbances Diseases 0.000 description 1
- 206010027339 Menstruation irregular Diseases 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 240000006066 Rosa rugosa Species 0.000 description 1
- 235000000659 Rosa rugosa Nutrition 0.000 description 1
- 241000220222 Rosaceae Species 0.000 description 1
- 208000005392 Spasm Diseases 0.000 description 1
- 229930003268 Vitamin C Natural products 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 230000001154 acute effect Effects 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 239000008280 blood Substances 0.000 description 1
- 210000004369 blood Anatomy 0.000 description 1
- 230000000711 cancerogenic effect Effects 0.000 description 1
- 231100000357 carcinogen Toxicity 0.000 description 1
- 239000003183 carcinogenic agent Substances 0.000 description 1
- 230000019522 cellular metabolic process Effects 0.000 description 1
- 230000001684 chronic effect Effects 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 208000029078 coronary artery disease Diseases 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 230000003467 diminishing effect Effects 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 230000036541 health Effects 0.000 description 1
- 239000005556 hormone Substances 0.000 description 1
- 229940088597 hormone Drugs 0.000 description 1
- 208000014674 injury Diseases 0.000 description 1
- 239000010977 jade Substances 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 208000019423 liver disease Diseases 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 150000004291 polyenes Chemical class 0.000 description 1
- -1 polyhydrocarbon Chemical class 0.000 description 1
- 229920005862 polyol Polymers 0.000 description 1
- 150000003077 polyols Chemical class 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- IKGXIBQEEMLURG-NVPNHPEKSA-N rutin Chemical compound O[C@@H]1[C@H](O)[C@@H](O)[C@H](C)O[C@H]1OC[C@@H]1[C@@H](O)[C@H](O)[C@@H](O)[C@H](OC=2C(C3=C(O)C=C(O)C=C3OC=2C=2C=C(O)C(O)=CC=2)=O)O1 IKGXIBQEEMLURG-NVPNHPEKSA-N 0.000 description 1
- 230000028327 secretion Effects 0.000 description 1
- 230000036548 skin texture Effects 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 210000002784 stomach Anatomy 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 208000024891 symptom Diseases 0.000 description 1
- 230000008736 traumatic injury Effects 0.000 description 1
- 238000009966 trimming Methods 0.000 description 1
- 230000017260 vegetative to reproductive phase transition of meristem Effects 0.000 description 1
- 235000019154 vitamin C Nutrition 0.000 description 1
- 239000011718 vitamin C Substances 0.000 description 1
Landscapes
- Fats And Perfumes (AREA)
Abstract
The invention discloses a method for extracting rose essential oil with high oil yield, which comprises the following steps: (1) picking rose flowers which are half-cup-shaped and have yellow pistils when the temperature is 5-23 ℃ and the relative air humidity is 55% -70% in the early morning, and selecting full rose petals which are not extruded; (2) putting rose petals and water into a distillation kettle, firstly heating the temperature in the distillation kettle to 70-80 ℃ by using indirect steam, introducing direct steam, and heating to boil, wherein the internal pressure of a distillation device is 0.07-0.09 MPa; (3) and (3) sequentially feeding the mixture of the rose oil and the rose hydrosol generated by distillation and the distillation residue into a condenser and an oil-water separator for condensation and oil-water separation to obtain the rose-water-based fuel. The rose essential oil prepared by the method has high oil yield and low water content, improves the purity of the rose essential oil and is beneficial to preservation.
Description
Technical Field
The invention belongs to the field of plant essential oil extraction, and particularly relates to a method for extracting rose essential oil with high oil yield.
Background
Rose (the scientific name: Rosa rugosa) is a plant of the genus Rosa of the family Rosaceae, and is a generic name of a series of large and gorgeous cultivars of Rosa in daily life. Roses are native to north China, Japan and Korea, and are cultivated in various places in China. In ancient Chinese, the term "rose" originally meant red beautiful jade, and for a long time, rose symbolized beauty and love. The roots and stems of the rose are soft, the rose cannot be made into fresh cut flowers, and the rose petals only have three rounds, so the modern Chinese rose with five rounds of petal flowers, which is obtained by crossing the rose and the Chinese rose, is used as the fresh cut flower rose in the market.
The rose is an ideal flower and tree for urban greening and gardens, is suitable for being used as a hedge, is also a material for greening streets and courtyards, flower beds with flower diameters and various gardens, and is used for trimming and modeling receipts, decorating square lawns, embankments and flower ponds and planting flower clusters in a piece. Besides ornamental value, roses have medicinal value: the roses in the flowering period can secrete phytoncide, kill a large amount of pathogenic bacteria in the air and are beneficial to the health of people; the rose contains more than 300 chemical components, such as aromatic alcohol, aldehyde, fatty acid, phenol and oil and fat containing essence, and the rose product is usually eaten to soften liver and wake stomach, relax qi and activate blood, maintain beauty and keep young and refresh people. The flowers and roots of the rose can be used as medicine, has the functions of regulating qi, promoting blood circulation, astringing and the like, and is mainly used for treating irregular menstruation, traumatic injury, liver qi and stomach pain, breast swelling and pain and other symptoms. The fruit pulp of rose fruit can be made into jam, and has special flavor, and the fruit contains abundant vitamin C and vitamin P, and can be used for preventing acute and chronic infectious diseases, coronary heart disease, liver disease and carcinogen. The rose essential oil extracted from rose petal by distillation has effects of diminishing inflammation, killing bacteria, preventing infectious diseases, inflammation, spasm, promoting cell metabolism and cell regeneration, improving skin texture, promoting blood circulation, and promoting hormone secretion.
The existing distillation method is used for extracting the rose essential oil, the mixture of fresh rose flowers and water is directly heated by high-temperature steam, so that the rose essential oil volatilizes from the mixture of the fresh rose flowers and the water, the rose essential oil slightly has burnt smell, the oil yield is low, and the quality of the essential oil is greatly reduced.
Disclosure of Invention
The invention aims to provide an extraction method of rose essential oil with high oil yield, which can reduce the loss of roses and obtain the rose essential oil with high oil yield, low water content and low cost.
In order to achieve the purpose, the invention adopts the following technical scheme:
a method for extracting rose essential oil with high oil yield comprises the following steps:
(1) picking rose flowers which are half-cup-shaped and have yellow pistils when the temperature is 5-23 ℃ and the relative air humidity is 55% -70% in the early morning, and selecting full rose petals which are not extruded;
(2) putting rose petals and water into a distillation kettle, firstly heating the temperature in the distillation kettle to 70-80 ℃ by using indirect steam, introducing direct steam, and heating to boil, wherein the internal pressure of a distillation device is 0.07-0.09 MPa;
(3) introducing the mixture of rose oil and rose hydrosol and distillation residue into condenser and oil-water separator for condensation and oil-water separation.
The inventor finds that the picking time of the rose is greatly related to the content of the rose essential oil, the oil content of the rose is the highest when the temperature is 5-23 ℃ and the relative humidity of air is 55-70% in the early morning of 5-7, the inventor also finds that the oil content of the rose is different when the flower is opened to half-cup shape and the pistil is yellow, and the oil content of the rose is the highest when the flower is opened to half-cup shape and the pistil is yellow; and after the roses are picked, containers with good ventilation, such as flower baskets and sacks, are used in the transportation process, the roses cannot be extruded, and the loss of oil content due to heat is avoided.
In the specific embodiment of the invention, in the step (2), the volume ratio of the rose petals to the distillation kettle is 1: 1.2-1.7; preferably 1: 1.5.
In a specific embodiment of the present invention, in the step (2), the rose petals: the mass ratio of the water is 1: 3-6, and preferably 1: 4.
In the specific implementation mode of the invention, the temperature rising speed of the indirect steam is 2.5-5 ℃/min.
In the specific embodiment of the invention, the time from the beginning of heating to the boiling of the liquid in the distillation kettle is 30-40 min.
The inventor finds in tests that the existing distillation method extracts rose essential oil, the mixture of fresh rose flowers and water is directly heated by high-temperature steam to volatilize the rose essential oil from the mixture of the fresh rose flowers and the water, the prepared rose essential oil slightly has burnt smell and low oil yield, and the quality of the essential oil is greatly reduced.
In the specific embodiment of the invention, the distillation is continued for 3-4 h, preferably 3-3.5 h after the heating to boiling.
In the specific embodiment of the invention, the condensation temperature is 15-40 ℃, and preferably 20-25 ℃;
the temperature of the oil-water separation is 10-30 ℃, and preferably 10-20 ℃.
In a specific embodiment of the present invention, the extraction method further comprises: continuously feeding the obtained mixture of the rose oil and the rose hydrosol into a distillation still for distillation according to the mode of the step (2);
further, the ratio of water in the distillation kettle: the mass ratio of the mixture of the rose oil and the rose hydrosol is 0.3-0.4: 1.
In the specific embodiment of the invention, the method further comprises the step of storing the rose essential oil in a glass bottle after the oil-water separation;
further, the glass bottle is a brown glass bottle.
The rose essential oil is a mixture of organic matters such as polyol, polyhydrocarbon, polyene and the like, is easily oxidized when exposed to light and affects the quality of aroma, and can be prevented from being oxidized by being bottled with brown glass so as to improve the quality.
In the specific embodiment of the invention, the distillation kettle, the condenser and the oil-water separator are made of red copper; the rose essential oil produced by using a red copper instrument has aromatic flavor, can better solve the peculiar smells of hot smell, rust smell and the like generated in the traditional rose essential oil extraction process, and has higher essential oil quality.
Compared with the prior art, the invention has the following beneficial effects:
(1) the rose essential oil prepared by the method has aromatic flavor, the oil yield is 0.29-0.35 per mill, the oil yield is high, the preservation is facilitated, and the rose essential oil has few impurities and good quality.
(2) The method is convenient and quick, has low production cost, good application value and wide development prospect.
Detailed Description
The technical solutions of the present invention are described clearly and completely below, and it is obvious that the described embodiments are some, not all embodiments of the present invention. All other embodiments, which can be obtained by a person skilled in the art without any inventive step based on the embodiments of the present invention, are within the scope of the present invention.
Example 1
(1) Picking rose flowers which are half-cup-shaped and have yellow pistils when the temperature is 5-7 ℃ and the relative air humidity is 55% in the early morning, and selecting plump rose petals.
(2) The flower basket with good ventilation is used for the picked roses in the transportation process, the roses are not required to be extruded, the heat loss of oil of roses and peanuts is avoided, and the transportation process is less than 2 hours; the processed rose can be temporarily stored, the rose is spread into a thin layer, laid on the ground, frequently turned over, and stored after being dried for later use.
(3) Putting rose petals into a distillation kettle, wherein the barrel body of the distillation kettle is made of red copper, the volume ratio of the flower amount to the volume of the distillation kettle is 2:3, firstly using indirect steam, heating the temperature in the distillation kettle to 70 ℃ at the temperature rising speed of 2.5 ℃/min, then introducing direct steam to heat the distillation kettle to boil, the time from the beginning of heating to the boiling of liquid in the distillation kettle is 30min, continuing to distill for 3h after the liquid is boiled, and the internal pressure of a distillation device is 0.07MPa in the distillation process.
(4) And putting the mixture of the rose oil and the rose hydrosol generated by distillation and the distillation residue into a distillation still for secondary distillation, wherein the mass ratio of the added water to the mixture of the rose oil and the rose hydrosol is 0.3: 1, the distillation conditions are the same as those in the step (3).
(5) Introducing the mixture of rose oil and rose hydrosol and distillation residue generated by distillation into a vertical condenser made of red copper plate for condensation at 15 deg.C, and performing oil-water separation in an oil-water separator made of red copper plate at 10 deg.C to obtain rose essential oil.
(6) The prepared rose essential oil was stored in a brown glass bottle, sealed, and placed in the dark.
Example 2
(1) Picking rose flowers which are half-cup-shaped and have yellow pistils when the temperature is 23 ℃ and the relative air humidity is 70% in the early morning 5-7, and selecting plump rose petals.
(2) The flower basket with good ventilation is used for the picked roses in the transportation process, the roses are not required to be extruded, the heat loss of oil of roses and peanuts is avoided, and the transportation process is less than 2 hours; the processed rose can be temporarily stored, the rose is spread into a thin layer, laid on the ground, frequently turned over, and stored after being dried for later use.
(3) Putting rose petals into a distillation kettle, wherein the barrel body of the distillation kettle is made of red copper, the volume ratio of the flower amount to the volume of the distillation kettle is 2:3, firstly using indirect steam, heating the temperature in the distillation kettle to 80 ℃ at the temperature rising speed of 5 ℃/min, then introducing direct steam to heat the distillation kettle to boil, the time from the beginning of heating to the boiling of liquid in the distillation kettle is 30min, continuing to distill for 4h after the liquid boils, and the internal pressure of a distillation device is 0.09MPa in the distillation process.
(4) And putting the mixture of the rose oil and the rose hydrosol generated by distillation and the distillation residue into a distillation still for secondary distillation, wherein the mass ratio of the added water to the mixture of the rose oil and the rose hydrosol is 0.3: 1, the distillation conditions are the same as those in the step (3).
(5) Introducing the mixture of rose oil and rose hydrosol and distillation residue generated by distillation into a vertical condenser made of red copper plate for condensation at 40 deg.C, and performing oil-water separation in an oil-water separator made of red copper plate at 30 deg.C to obtain rose essential oil.
(6) The prepared rose essential oil was stored in a brown glass bottle, sealed, and placed in the dark.
Example 3
(1) In the early morning, when the temperature is 15 ℃ and the relative air humidity is 60%, picking rose flowers which bloom to be half-cup-shaped and have yellow pistils, and selecting plump rose petals.
(2) The flower basket with good ventilation is used for the picked roses in the transportation process, the roses are not required to be extruded, the heat loss of oil of roses and peanuts is avoided, and the transportation process is less than 2 hours; the processed rose can be temporarily stored, the rose is spread into a thin layer, laid on the ground, frequently turned over, and stored after being dried for later use.
(3) Putting rose petals into a distillation kettle, wherein the barrel body of the distillation kettle is made of red copper, the volume ratio of the flower amount to the volume of the distillation kettle is 2:3, firstly using indirect steam, heating the temperature in the distillation kettle to 75 ℃ at the heating rate of 3.5 ℃/min, then introducing direct steam to heat to boil, the time from the beginning of heating to the boiling of liquid in the distillation kettle is 30min, continuing to distill for 3.5h after the liquid is boiled, and the internal pressure of a distillation device is 0.08MPa in the distillation process.
(4) And putting the mixture of the rose oil and the rose hydrosol generated by distillation and the distillation residue into a distillation still for secondary distillation, wherein the mass ratio of the added water to the mixture of the rose oil and the rose hydrosol is 0.4:1, the distillation conditions are the same as those in the step (3).
(5) Introducing the mixture of rose oil and rose hydrosol and distillation residue generated by distillation into a vertical condenser made of red copper plate for condensation at 25 deg.C, and performing oil-water separation in an oil-water separator made of red copper plate at 20 deg.C to obtain rose essential oil.
(6) The prepared rose essential oil was stored in a brown glass bottle, sealed, and placed in the dark.
The rose essential oil prepared in the embodiments 1 to 3 is rich in compounds such as alcohol, alkene, ester, ketone, aldehyde, ether, alkane, phenols and acids, has strong fragrance, has the natural fragrance of rose, has the oil yield of 0.29-0.35 per mill, is beneficial to preservation, has no impurities such as slag, foam and the like, has good quality, and meets the requirements of international standards.
Comparative example 1
(1) Picking rose flowers which are half-cup-shaped and have yellow pistils when the temperature is 5-7 ℃ and the relative air humidity is 55% in the early morning, and selecting plump rose petals.
(2) The flower basket with good ventilation is used for the picked roses in the transportation process, the roses are not required to be extruded, the heat loss of oil of roses and peanuts is avoided, and the transportation process is less than 2 hours; the processed rose can be temporarily stored, the rose is spread into a thin layer, laid on the ground, frequently turned over, and stored after being dried for later use.
(3) Putting rose petals into a distillation kettle, wherein the barrel body of the distillation kettle is made of iron, the volume ratio of the flower amount to the volume of the distillation kettle is 2:3, introducing direct steam to heat liquid in the distillation kettle to boiling, the time from the beginning of heating to the boiling of the liquid in the distillation kettle is 30min, continuing to distill for 3h after the liquid is boiled, and the internal pressure of a distillation device is 0.07MPa in the distillation process.
(4) And putting the mixture of the rose oil and the rose hydrosol generated by distillation and the distillation residue into a distillation still for secondary distillation, wherein the mass ratio of the added water to the mixture of the rose oil and the rose hydrosol is 0.3: 1, the distillation conditions are the same as those in the step (3).
(5) Introducing the mixture of rose oil and rose hydrosol and distillation residue generated by distillation into a vertical condenser made of iron for condensation at 15 deg.C, and performing oil-water separation in an oil-water separator made of iron at 10 deg.C to obtain rose essential oil.
(6) The prepared rose essential oil was stored in a brown glass bottle, sealed, and placed in the dark.
The rose essential oil prepared by the comparative example has light fragrance, rust taste, oil yield of 0.20 per mill and more impurities such as slag melting, foam and the like.
Comparative example 2
(1) Picking rose flowers and selecting plump rose petals when the temperature is 5-7 ℃ and the relative air humidity is 55% in the early morning.
(2) The flower basket with good ventilation is used for the picked roses in the transportation process, the roses are not required to be extruded, the heat loss of oil of roses and peanuts is avoided, and the transportation process is less than 2 hours; the processed rose can be temporarily stored, the rose is spread into a thin layer, laid on the ground, frequently turned over, and stored after being dried for later use.
(3) Putting rose petals into a distillation kettle, wherein the barrel body of the distillation kettle is made of red copper, the volume ratio of the flower amount to the volume of the distillation kettle is 2:3, firstly using indirect steam, heating the temperature in the distillation kettle to 70 ℃ at the temperature rising speed of 2.5 ℃/min, then introducing direct steam to heat the distillation kettle to boil, the time from the beginning of heating to the boiling of liquid in the distillation kettle is 30min, continuing to distill for 3h after the liquid is boiled, and the internal pressure of a distillation device is 0.07MPa in the distillation process.
(4) Introducing the mixture of rose oil and rose hydrosol and distillation residue generated by distillation into a vertical condenser made of red copper plate for condensation at 60 deg.C, and performing oil-water separation in an oil-water separator made of red copper plate at 10 deg.C to obtain rose essential oil.
(5) The prepared rose essential oil was stored in a brown glass bottle, sealed, and placed in the dark.
The rose essential oil prepared by the comparative example has the natural fragrance of rose, but has light fragrance, the oil yield is 0.21 per mill, and the rose essential oil contains a little of impurities such as melting slag, spray and the like.
Although embodiments of the present invention have been shown and described, it will be appreciated by those skilled in the art that changes, modifications, substitutions and alterations can be made in these embodiments without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (10)
1. The extraction method of the rose essential oil with high oil yield is characterized by comprising the following steps:
(1) picking rose flowers which are half-cup-shaped and have yellow pistils when the temperature is 5-23 ℃ and the relative air humidity is 55% -70% in the early morning, and selecting full rose petals which are not extruded;
(2) putting rose petals and water into a distillation kettle, firstly heating the temperature in the distillation kettle to 70-80 ℃ by using indirect steam, introducing direct steam, and heating to boil, wherein the internal pressure of a distillation device is 0.07-0.09 MPa;
(3) introducing the mixture of rose oil and rose hydrosol and distillation residue into condenser and oil-water separator for condensation and oil-water separation.
2. The extraction method according to claim 1, wherein in the step (2), the volume ratio of the rose petals to the distillation kettle is 1: 1.2-1.7; preferably 1: 1.5.
3. The extraction method according to claim 1, wherein in the step (2), the ratio of the rose petals: the mass ratio of the water is 1: 3-6, and preferably 1: 4.
4. The extraction method according to claim 1, wherein the temperature increase rate of the indirect steam is 2.5 to 5 ℃/min.
5. The extraction method according to claim 1, wherein the time from the start of heating to the boiling of the liquid in the still pot is 30 to 40 min.
6. The extraction method according to claim 1, wherein the distillation is continued for 3-4 h, preferably 3-3.5 h after heating to boiling.
7. The extraction process according to claim 1, characterized in that the condensation temperature is comprised between 15 and 40 ℃, preferably between 20 and 25 ℃;
the temperature of the oil-water separation is 10-30 ℃, and preferably 10-20 ℃.
8. The extraction method according to claim 1, further comprising: continuously feeding the obtained mixture of the rose oil and the rose hydrosol into a distillation still for distillation according to the mode of the step (2);
further, the ratio of water in the distillation kettle: the mass ratio of the mixture of the rose oil and the rose hydrosol is 0.3-0.4: 1.
9. The extraction method according to any one of claims 1 to 8, further comprising the step of storing the rose essential oil in a glass bottle after the oil-water separation;
further, the glass bottle is a brown glass bottle.
10. The extraction method according to claim 1, wherein the distillation still, the condenser and the oil-water separator are made of red copper.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202011615692.2A CN112662476A (en) | 2020-12-30 | 2020-12-30 | Extraction method of rose essential oil with high oil yield |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN202011615692.2A CN112662476A (en) | 2020-12-30 | 2020-12-30 | Extraction method of rose essential oil with high oil yield |
Publications (1)
Publication Number | Publication Date |
---|---|
CN112662476A true CN112662476A (en) | 2021-04-16 |
Family
ID=75411384
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN202011615692.2A Pending CN112662476A (en) | 2020-12-30 | 2020-12-30 | Extraction method of rose essential oil with high oil yield |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN112662476A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112662477A (en) * | 2020-12-30 | 2021-04-16 | 小金县夹金山清多香野生资源开发有限责任公司 | Extraction method of rose essential oil and rose hydrosol |
CN114958487A (en) * | 2022-06-15 | 2022-08-30 | 银谷芳香科技有限公司 | Industrial extraction process method of Roman chamomile oil |
Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1648223A (en) * | 2004-12-27 | 2005-08-03 | 王锦鸣 | Rose oil and its producing process |
CN1651558A (en) * | 2004-12-02 | 2005-08-10 | 西北农林科技大学 | Technology of extracting rose oil by using two step variable distillation type back water distillation method |
CN101280243A (en) * | 2008-06-04 | 2008-10-08 | 杨利民 | Method for extracting rose essence oil and rose absolute by water vapor water distillation technology |
CN102517150A (en) * | 2012-01-06 | 2012-06-27 | 天津聚馥日用品有限公司 | Method for preparing rose extracting stock solution |
CN103897807A (en) * | 2014-04-24 | 2014-07-02 | 四川银谷玫瑰科技有限公司 | Method for extracting rose essential oil |
CN104818122A (en) * | 2015-05-22 | 2015-08-05 | 西昌昌泰香料有限责任公司 | Preparation technique of rose essential oil |
CN105249476A (en) * | 2015-11-13 | 2016-01-20 | 合肥金源生物科技有限公司 | Rose water extract and preparation method thereof |
CN105779133A (en) * | 2016-05-26 | 2016-07-20 | 陕西恒芳玫瑰开发有限公司 | Stage extraction method for rose essential oil |
CN106281700A (en) * | 2016-08-16 | 2017-01-04 | 重庆雅香美源生态农业科技有限公司 | The extraction of Flos Rosae Rugosae quintessence oil and processing method |
CN109554226A (en) * | 2017-09-25 | 2019-04-02 | 宜兴市瑞优娜玫瑰产业有限公司 | A kind of preparation method of Rosa Damascana |
CN112442422A (en) * | 2020-11-12 | 2021-03-05 | 上海番景生物科技有限公司 | Extraction method of fresh saffron crocus juice |
CN112662477A (en) * | 2020-12-30 | 2021-04-16 | 小金县夹金山清多香野生资源开发有限责任公司 | Extraction method of rose essential oil and rose hydrosol |
-
2020
- 2020-12-30 CN CN202011615692.2A patent/CN112662476A/en active Pending
Patent Citations (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1651558A (en) * | 2004-12-02 | 2005-08-10 | 西北农林科技大学 | Technology of extracting rose oil by using two step variable distillation type back water distillation method |
CN1648223A (en) * | 2004-12-27 | 2005-08-03 | 王锦鸣 | Rose oil and its producing process |
CN101280243A (en) * | 2008-06-04 | 2008-10-08 | 杨利民 | Method for extracting rose essence oil and rose absolute by water vapor water distillation technology |
CN102517150A (en) * | 2012-01-06 | 2012-06-27 | 天津聚馥日用品有限公司 | Method for preparing rose extracting stock solution |
CN103897807A (en) * | 2014-04-24 | 2014-07-02 | 四川银谷玫瑰科技有限公司 | Method for extracting rose essential oil |
CN104818122A (en) * | 2015-05-22 | 2015-08-05 | 西昌昌泰香料有限责任公司 | Preparation technique of rose essential oil |
CN105249476A (en) * | 2015-11-13 | 2016-01-20 | 合肥金源生物科技有限公司 | Rose water extract and preparation method thereof |
CN105779133A (en) * | 2016-05-26 | 2016-07-20 | 陕西恒芳玫瑰开发有限公司 | Stage extraction method for rose essential oil |
CN106281700A (en) * | 2016-08-16 | 2017-01-04 | 重庆雅香美源生态农业科技有限公司 | The extraction of Flos Rosae Rugosae quintessence oil and processing method |
CN109554226A (en) * | 2017-09-25 | 2019-04-02 | 宜兴市瑞优娜玫瑰产业有限公司 | A kind of preparation method of Rosa Damascana |
CN112442422A (en) * | 2020-11-12 | 2021-03-05 | 上海番景生物科技有限公司 | Extraction method of fresh saffron crocus juice |
CN112662477A (en) * | 2020-12-30 | 2021-04-16 | 小金县夹金山清多香野生资源开发有限责任公司 | Extraction method of rose essential oil and rose hydrosol |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112662477A (en) * | 2020-12-30 | 2021-04-16 | 小金县夹金山清多香野生资源开发有限责任公司 | Extraction method of rose essential oil and rose hydrosol |
CN114958487A (en) * | 2022-06-15 | 2022-08-30 | 银谷芳香科技有限公司 | Industrial extraction process method of Roman chamomile oil |
CN114958487B (en) * | 2022-06-15 | 2024-03-22 | 银谷芳香科技有限公司 | Industrial extraction process method of Roman chamomile oil |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN112662477A (en) | Extraction method of rose essential oil and rose hydrosol | |
CN101147516B (en) | Method for preparing mulberry tea | |
CN101343603B (en) | Rose liquor wine and preparation thereof | |
CN106929364A (en) | A kind of preparation technology of rose flower wine | |
CN112662476A (en) | Extraction method of rose essential oil with high oil yield | |
CN105861220A (en) | Rose fen-flavor white wine and brewage method thereof | |
CN102391939A (en) | Sweet osmanthus rose wine and preparation method thereof | |
CN109198065A (en) | A kind of production method of black tea | |
CN104365947A (en) | Production method of organic jasmine Kuding tea | |
CN103349132A (en) | Loquat scented tea and preparation method thereof | |
CN104095095A (en) | Lemongrass tea having health-caring function and preparation method thereof | |
CN106957783B (en) | Bozhou chrysanthemum wine and preparation method thereof | |
CN105053402A (en) | Preparation method of jujube black tea | |
CN102391940B (en) | Sophora flower wine and preparation method thereof | |
CN111937970A (en) | Preparation method of spicy rattan pepper oil | |
CN106332633A (en) | Cultivation method of selenium-enriched chrysanthemum | |
CN111248321A (en) | Preparation method of mulberry bud tea | |
CN113303382A (en) | Processing method of flower and fruit flavored white tea rich in clausena lansium fruit flavor | |
CN112314729A (en) | Preparation method of jasmine tea | |
CN107258421A (en) | A kind of method for extending the cercis florescence | |
CN101461558A (en) | Aspergillus bacteriostatic agent and use thereof | |
CN110819486A (en) | Beer and preparation method thereof | |
CN114208915A (en) | Jujube flower tea and preparation method thereof | |
CN106578787A (en) | Preparation method of moringa oleifera health-care beverage | |
CN111802489A (en) | Inflammation-diminishing pain-relieving whitening scented tea and processing method thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20210416 |
|
RJ01 | Rejection of invention patent application after publication |