CN106318634A - Method of extraction of orange blossom essential oil - Google Patents

Method of extraction of orange blossom essential oil Download PDF

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Publication number
CN106318634A
CN106318634A CN201610734541.6A CN201610734541A CN106318634A CN 106318634 A CN106318634 A CN 106318634A CN 201610734541 A CN201610734541 A CN 201610734541A CN 106318634 A CN106318634 A CN 106318634A
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CN
China
Prior art keywords
extraction
orange blossom
fluid
separator
oil
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
Application number
CN201610734541.6A
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Chinese (zh)
Inventor
曾驰
陈力
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Guangxi Hao Yuan Sheng Biotechnology Co Ltd
Original Assignee
Guangxi Hao Yuan Sheng Biotechnology Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Guangxi Hao Yuan Sheng Biotechnology Co Ltd filed Critical Guangxi Hao Yuan Sheng Biotechnology Co Ltd
Priority to CN201610734541.6A priority Critical patent/CN106318634A/en
Publication of CN106318634A publication Critical patent/CN106318634A/en
Pending legal-status Critical Current

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Classifications

    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B9/00Essential oils; Perfumes
    • C11B9/02Recovery or refining of essential oils from raw materials
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B9/00Essential oils; Perfumes
    • C11B9/02Recovery or refining of essential oils from raw materials
    • C11B9/022Refining
    • CCHEMISTRY; METALLURGY
    • C11ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
    • C11BPRODUCING, 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
    • C11B9/00Essential oils; Perfumes
    • C11B9/02Recovery or refining of essential oils from raw materials
    • C11B9/025Recovery by solvent extraction

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  • 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)
  • Medicines Containing Plant Substances (AREA)
  • Cosmetics (AREA)

Abstract

The invention provides a method of extraction of orange blossom essential oil. The method consists of steps 1, sprinkling the entraining agent that is 0.3-0.5% of the weight of fresh orange blossoms into the fresh orange blossoms, adding the fresh orange blossoms to the extraction kettle, and then using hypercritical carbon dioxide fluid for continuous cyclic extraction; the entraining agent is formed, by mass, with 65-70 parts of ethanol, 2-4 parts of triethanolamine, and 0.2-0.4 part of petroleum ether; 2, pouring the carbon dioxide fluid after extraction to a separator for separation; flow of carbon dioxide fluid is 12-15 kg/h, separator pressure is 6-7 MPa, and the temperature is 35-40 oC; extracting the fluid for 1.5-2.5 h, and discharging the extractant from the bottom of the separator to get the orange blossom essential oil through oil and water separation after standing. The orange blossom essential oil obtained using the method in the invention has high purity and long-lasting fragrance.

Description

A kind of extracting method of orange blossom quintessence oil
Technical field
The invention belongs to technical field of plant extraction, be specifically related to the extracting method of a kind of orange blossom quintessence oil.
Background technology
Along with the development of economic society, improving constantly of people's living standard, to the demand of plants essential oil increasingly Greatly, quintessence oil be that a class is volatile, there is intense flavors and abnormal smells from the patient, can be with the general name of vapor distillation oily liquids out.Essence The active composition of oil, is of wide application, such as expelling phlegm for arresting cough, stomach invigorating of dispeling the wind, anthelmintic, wrinkle resistant maintenance etc., the most popular Hydrotherapy (SPA), its marrow is exactly natural plant essence oil.
Summary of the invention
The invention provides the extracting method of a kind of orange blossom quintessence oil.
The present invention provides the extracting method of a kind of orange blossom quintessence oil, and step is as follows:
(1) agent of carrying accounting for orange blossom flower weight 0.3-0.5% is sprayed in orange blossom flower, then orange blossom flower is added extraction In still, carry out continuous cycling extraction with supercritical carbon dioxide fluid, control extraction kettle temperature 35-40 DEG C, extract pressure 18- 22MPa, flow velocity is 16-18kg/h, extraction time 2-4h;Described carry agent and be made up of each component of following mass fraction: ethanol 65-70 part, triethanolamine 2-4 part, petroleum ether 0.2-0.4 part;
(2) CO 2 fluid after extraction being entered separator to separate, the flow of CO 2 fluid is 12-15kg/ H, separator pressure is 6-7MPa, and temperature is 35-40 DEG C, extracts 1.5-2.5h, releases extract from separator bottom, stands After, obtain orange blossom quintessence oil through oil-water separation.
As preferably, step is as follows:
(1) agent of carrying accounting for orange blossom flower weight 0.5% is sprayed in orange blossom flower, then orange blossom flower is added in extraction kettle, Carrying out continuous cycling extraction with supercritical carbon dioxide fluid, control extraction kettle temperature 38 DEG C, extract pressure 20MPa, flow velocity is 17kg/h, extraction time 3h;Described carry agent and be made up of each component of following mass fraction: ethanol 68 parts, triethanolamine 3 parts, Petroleum ether 0.3 part;
(2) CO 2 fluid after extraction being entered separator to separate, the flow of CO 2 fluid is 12kg/h, point Being 6.5MPa from device pressure, temperature is 38 DEG C, extracts 2h, releases extract from separator bottom, after standing, obtains through oil-water separation To orange blossom quintessence oil.
It is high that the method using the present invention extracts the orange blossom quintessence oil purity obtained, and fragrance can be effectively retained.
Detailed description of the invention
Below example facilitates a better understanding of the present invention, but does not limit the present invention.Experiment in following embodiment Method, if no special instructions, is conventional method.Test material used in following embodiment, if no special instructions, is city Sell.
Embodiment 1
The present invention provides the extracting method of a kind of orange blossom quintessence oil, and step is as follows:
(1) agent of carrying accounting for orange blossom flower weight 0.5% is sprayed in orange blossom flower, then orange blossom flower is added in extraction kettle, Carrying out continuous cycling extraction with supercritical carbon dioxide fluid, control extraction kettle temperature 38 DEG C, extract pressure 20MPa, flow velocity is 17kg/h, extraction time 3h;Described carry agent and be made up of each component of following mass fraction: ethanol 68 parts, triethanolamine 3 parts, Petroleum ether 0.3 part;
(2) CO 2 fluid after extraction being entered separator to separate, the flow of CO 2 fluid is 12kg/h, point Being 6.5MPa from device pressure, temperature is 38 DEG C, extracts 2h, releases extract from separator bottom, after standing, obtains through oil-water separation To orange blossom quintessence oil.
Embodiment 2
The present invention provides the extracting method of a kind of orange blossom quintessence oil, and step is as follows:
(1) agent of carrying accounting for orange blossom flower weight 0.4% is sprayed in orange blossom flower, then orange blossom flower is added in extraction kettle, Carrying out continuous cycling extraction with supercritical carbon dioxide fluid, control extraction kettle temperature 40 DEG C, extract pressure 22MPa, flow velocity is 16kg/h, extraction time 4h;Described carry agent and be made up of each component of following mass fraction: ethanol 70 parts, triethanolamine 2 parts, Petroleum ether 0.2 part;
(2) CO 2 fluid after extraction being entered separator to separate, the flow of CO 2 fluid is 15kg/h, point Being 6MPa from device pressure, temperature is 40 DEG C, extracts 2.5h, releases extract from separator bottom, after standing, obtains through oil-water separation To orange blossom quintessence oil.
Embodiment 3
The present invention provides the extracting method of a kind of orange blossom quintessence oil, and step is as follows:
(1) agent of carrying accounting for orange blossom flower weight 0.3% is sprayed in orange blossom flower, then orange blossom flower is added in extraction kettle, Carrying out continuous cycling extraction with supercritical carbon dioxide fluid, control extraction kettle temperature 35 DEG C, extract pressure 18MPa, flow velocity is 18kg/h, extraction time 2h;Described carry agent and be made up of each component of following mass fraction: ethanol 65 parts, triethanolamine 4 parts, Petroleum ether 0.4 part;
(2) CO 2 fluid after extraction being entered separator to separate, the flow of CO 2 fluid is 12kg/h, point Being 7MPa from device pressure, temperature is 35 DEG C, extracts 1.5h, releases extract from separator bottom, after standing, obtains through oil-water separation To orange blossom quintessence oil.
Being compared with ethanol with carrying agent, the orange blossom quintessence oil purity that agent prepares of carrying of application the application improves 3-5%.
Directly carrying out compared with supercritical carbon dioxide extraction reacts with without carrying agent, application the application carries agent system The standby quintessence oil purity obtained improves 5-8%.
Finally it is noted that the foregoing is only the preferred embodiments of the present invention, it is not limited to the present invention, Although being described in detail the present invention with reference to previous embodiment, for a person skilled in the art, it still may be used So that the technical scheme described in foregoing embodiments to be modified, or wherein portion of techniques feature is carried out equivalent. All within the spirit and principles in the present invention, any modification, equivalent substitution and improvement etc. made, should be included in the present invention's Within protection domain.

Claims (2)

1. the extracting method of an orange blossom quintessence oil, it is characterised in that: step is as follows:
(1) agent of carrying accounting for orange blossom flower weight 0.3-0.5% is sprayed in orange blossom flower, then orange blossom flower is added extraction In still, carry out continuous cycling extraction with supercritical carbon dioxide fluid, control extraction kettle temperature 35-40 DEG C, extract pressure 18- 22MPa, flow velocity is 16-18kg/h, extraction time 2-4h;Described carry agent and be made up of each component of following mass fraction: ethanol 65-70 part, triethanolamine 2-4 part, petroleum ether 0.2-0.4 part;
(2) CO 2 fluid after extraction being entered separator to separate, the flow of CO 2 fluid is 12-15kg/ H, separator pressure is 6-7MPa, and temperature is 35-40 DEG C, extracts 1.5-2.5h, releases extract from separator bottom, stands After, obtain orange blossom quintessence oil through oil-water separation.
Method the most according to claim 1, it is characterised in that: step is as follows:
(1) agent of carrying accounting for orange blossom flower weight 0.5% is sprayed in orange blossom flower, then orange blossom flower is added in extraction kettle, Carrying out continuous cycling extraction with supercritical carbon dioxide fluid, control extraction kettle temperature 38 DEG C, extract pressure 20MPa, flow velocity is 17kg/h, extraction time 3h;Described carry agent and be made up of each component of following mass fraction: ethanol 68 parts, triethanolamine 3 parts, Petroleum ether 0.3 part;
(2) CO 2 fluid after extraction being entered separator to separate, the flow of CO 2 fluid is 12kg/h, point Being 6.5MPa from device pressure, temperature is 38 DEG C, extracts 2h, releases extract from separator bottom, after standing, obtains through oil-water separation To orange blossom quintessence oil.
CN201610734541.6A 2016-08-28 2016-08-28 Method of extraction of orange blossom essential oil Pending CN106318634A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610734541.6A CN106318634A (en) 2016-08-28 2016-08-28 Method of extraction of orange blossom essential oil

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Application Number Priority Date Filing Date Title
CN201610734541.6A CN106318634A (en) 2016-08-28 2016-08-28 Method of extraction of orange blossom essential oil

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CN106318634A true CN106318634A (en) 2017-01-11

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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101624557A (en) * 2009-07-31 2010-01-13 重庆市日用化学工业研究所 Method for extracting neroli absolute by supercritical carbon dioxide
CN102504957A (en) * 2011-11-23 2012-06-20 桂林莱茵生物科技股份有限公司 Method for preparing essential oils
CN103589515A (en) * 2013-10-30 2014-02-19 张秋菊 Supercritical carbon dioxide extraction method of high-purity lavender essential oil

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101624557A (en) * 2009-07-31 2010-01-13 重庆市日用化学工业研究所 Method for extracting neroli absolute by supercritical carbon dioxide
CN102504957A (en) * 2011-11-23 2012-06-20 桂林莱茵生物科技股份有限公司 Method for preparing essential oils
CN103589515A (en) * 2013-10-30 2014-02-19 张秋菊 Supercritical carbon dioxide extraction method of high-purity lavender essential oil

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
巫建国等: "超临界CO2萃取橙花精油及GC/MS分析", 《化工技术与开发》 *
毛海舫等: "《天然香料加工工艺学》", 31 January 2006, 中国轻工业出版社 *

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Application publication date: 20170111