CN209481617U - A kind of agalloch eaglewood Edgeworthia chrysantha extraction separation equipment - Google Patents

A kind of agalloch eaglewood Edgeworthia chrysantha extraction separation equipment Download PDF

Info

Publication number
CN209481617U
CN209481617U CN201721444775.3U CN201721444775U CN209481617U CN 209481617 U CN209481617 U CN 209481617U CN 201721444775 U CN201721444775 U CN 201721444775U CN 209481617 U CN209481617 U CN 209481617U
Authority
CN
China
Prior art keywords
agalloch eaglewood
equipment
edgeworthia chrysantha
eaglewood edgeworthia
separation
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.)
Active
Application number
CN201721444775.3U
Other languages
Chinese (zh)
Inventor
冯志豪
梁振明
朱力
朱宝璋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Maoming Yufeng Chenxiang Creative Industry Co., Ltd
Original Assignee
GUANGZHOU HAOLI TECHNOLOGY 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 GUANGZHOU HAOLI TECHNOLOGY Co Ltd filed Critical GUANGZHOU HAOLI TECHNOLOGY Co Ltd
Priority to CN201721444775.3U priority Critical patent/CN209481617U/en
Application granted granted Critical
Publication of CN209481617U publication Critical patent/CN209481617U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Extraction Or Liquid Replacement (AREA)
  • Fats And Perfumes (AREA)

Abstract

The utility model discloses a kind of agalloch eaglewood Edgeworthia chrysanthas to extract separation equipment, it is characterised in that is combined supercritical carbon dioxide extraction equipment and molecular distillation equipment, first extracts and obtain the mixing medicinal extract containing agalloch eaglewood Edgeworthia chrysantha, then obtain agilawood essential oil and agalloch eaglewood Edgeworthia chrysantha cream.It is doubled in agilawood essential oil and the yield of agalloch eaglewood Edgeworthia chrysantha cream than other distillating methods using the utility model above, the original fragrance of agalloch eaglewood Edgeworthia chrysantha, solvent-free pollution are utmostly kept in quality, the needs that can satisfy pure natural daily chemical essence exploitation, have broader market prospects.

Description

A kind of agalloch eaglewood Edgeworthia chrysantha extraction separation equipment
Technical field
The utility model relates to natural plant pefumes to purify field, and especially a kind of agalloch eaglewood Edgeworthia chrysantha extracts separation equipment.
Background technique
Agalloch eaglewood trees are Thymelaeceae (Thymelaeaceae) agalloch eaglewood category (Aquilaria) suspension culture of Aquilaria sinensis (Aquilaria Sinensis (Lour.) Gilg) and congener agalloch eaglewood (Aquilria agallocha Roxb.) trees.When its trunk meets with It is bitten by insect and stings, grease will be secreted automatically in trunk after natural calamity or artificial injury, this is also oneself of nature trees More property, secreted grease in nature by certain specific fungal infection after, it is this with the gradually passage of time Grease can give out a kind of unusual fragrance, and this brownish black grease in trunk is exactly agalloch eaglewood Edgeworthia chrysantha.Because of its exclusive fragrance, It is commonly used for preparing fragrance and perfume.
The conventionally employed steam distillation of agalloch eaglewood Edgeworthia chrysantha extracts, and elapsed time is long, effective component is easily destroyed;Also there is use Organic solvent such as ethyl alcohol, gasoline or petroleum ether extract, and there are problems that inflammable and explosive dangerous and organic solvent residual.Therefore, product The unfavorable factors such as matter is low, energy consumption is high and pollution is big, seriously limit the development and application of agalloch eaglewood Edgeworthia chrysantha.
Summary of the invention
In order to overcome the shortcomings of the prior art, the utility model provides a kind of agalloch eaglewood Edgeworthia chrysantha extraction separation equipment, institute The yield for obtaining agilawood essential oil and agalloch eaglewood Edgeworthia chrysantha cream is high, and quality is high.
To achieve the above object, the purpose of this utility model is realized in: a kind of agalloch eaglewood Edgeworthia chrysantha extraction separation equipment, Be characterized in that include:
Supercritical carbon dioxide extraction equipment, extraction kettle and two-stage separation kettle including passing sequentially through pipeline serial communication, Separating still is provided with wire mesh packing;
Pass through the molecular distillation equipment of pipeline and supercritical carbon dioxide extraction equipment serial communication, including at least two-stage Molecular distillation column.
The wire mesh packing is reticulated and stacked and form by metal wire rod braiding.
The separating still includes separation autoclave body, and separation autoclave body bottom is discharge port, and middle and upper part is equipped with gas outlet, separating still The outlet of gas outlet and feeding pipe is separated equipped with wire mesh packing in vivo.
At least 1/2 space is equipped with wire mesh packing in the separating still body, and the outlet of feeding pipe is embedded to metal In wire packing or from top to down through wire mesh packing.
The two-stage separation kettle bottom is connected to molecular distillation equipment, afterbody separating still middle and upper part and recycling dioxy Change the connection of carbon storage tank, recycling carbon dioxide storage tank is successively connected to high-pressure pump, heater, extraction kettle, is formed into a loop.
The molecular distillation equipment includes three-level molecular distillation column.
Compared with prior art, the utility model is combined using supercritical carbon dioxide extraction equipment and molecular distillation equipment Technology is extracted from agalloch eaglewood Edgeworthia chrysantha wood and isolates agilawood essential oil and agalloch eaglewood Edgeworthia chrysantha cream, using this technology, agilawood essential oil and agalloch eaglewood knot The yield of balm doubles above than other distillating methods, and the original perfume (or spice) of agalloch eaglewood Edgeworthia chrysantha is utmostly kept in quality Taste, solvent-free pollution can satisfy the needs of pure natural daily chemical essence exploitation, have broader market prospects.
Detailed description of the invention
Fig. 1 is the flowage structure schematic diagram of the utility model device;
Fig. 2 is the structural schematic diagram of the utility model separating still;
Fig. 3 is the structural schematic diagram of the separating still of another structure type of the utility model.
Specific embodiment
As shown in Figure 1, a kind of agalloch eaglewood Edgeworthia chrysantha of the utility model extracts separation equipment, it include by pipeline serial communication Supercritical carbon dioxide extraction equipment 1 and molecular distillation equipment 2.
Supercritical carbon dioxide extraction equipment 1, extraction kettle 12 and two-stage separation including passing sequentially through pipeline serial communication Kettle 13,14, separating still 13,14 are provided with wire mesh packing 18.
Wire mesh packing 18 is to be woven into the net of different shape, density and specification by metal wire rod and stacked form Type is inert solid material, has many advantages, such as that separative efficiency height, large specific surface area, porosity are high, gas-liquid contact is abundant.It will Wire mesh packing 18 is applied to the separating still 13,14 of supercritical carbon dioxide extraction equipment, separative efficiency can be made to improve, yield It improves.
Separating still 13,14 includes separation autoclave body 19, and separation 19 bottom of autoclave body is discharge port 191, and middle and upper part is equipped with gas outlet 192, separation autoclave body 19 is provided with wire mesh packing 18 and separates gas outlet 192 and the outlet 31 of feeding pipe 3, it is preferred that The space for separating in autoclave body 19 at least 1/2 is equipped with wire mesh packing 18.The outlet 31 of feeding pipe 3 is embedded to wire mesh packing In 18 (as shown in Figure 2) or from top to down run through wire mesh packing 18 (as shown in Figure 3).
Carbon dioxide air source 11 is connected to high-pressure pump 16, heater 17, extraction kettle 12.Two-stage separation kettle 13,14 bottoms with Molecular distillation equipment 2 is connected to, and 14 middle and upper part of afterbody separating still is connected to recycling carbon dioxide storage tank 15, recycles carbon dioxide Storage tank 15 is successively connected to high-pressure pump 16, heater 17, extraction kettle 12, and forming circuit realizes recycling for carbon dioxide.
Molecular distillation equipment 2 includes at least two-stage molecular distillation column.Preferred molecular distillation equipment 2 as shown in Figure 1 Including three-level molecular distillation column.Two-stage separation kettle 13,14 bottoms are connected to the mixing medicinal extract storage tank 21 of molecular distillation equipment 2, are mixed Medicinal extract storage tank 21 is closed successively to be connected to three-level molecular distillation column 22,23,24 again.

Claims (5)

1. a kind of agalloch eaglewood Edgeworthia chrysantha extracts separation equipment, characterized by comprising:
Supercritical carbon dioxide extraction equipment, extraction kettle and two-stage separation kettle including passing sequentially through pipeline serial communication, separation Kettle is provided with wire mesh packing;
Pass through the molecular distillation equipment of pipeline and supercritical carbon dioxide extraction equipment serial communication, including at least two-stage molecule Distillation column.
2. agalloch eaglewood Edgeworthia chrysantha according to claim 1 extracts separation equipment, it is characterised in that: the wire mesh packing by Metal wire rod braiding reticulates and stacked and form.
3. agalloch eaglewood Edgeworthia chrysantha according to claim 1 extracts separation equipment, it is characterised in that: the separating still includes separation Autoclave body, separation autoclave body bottom are discharge port, and middle and upper part is equipped with gas outlet, wire mesh packing are housed by gas outlet in separating still body Outlet with feeding pipe separates.
4. agalloch eaglewood Edgeworthia chrysantha according to claim 3 extracts separation equipment, it is characterised in that: in the separating still body at least 1/2 space is equipped with wire mesh packing, and the outlet of feeding pipe is embedded in wire mesh packing or runs through from top to down metal Wire packing.
5. agalloch eaglewood Edgeworthia chrysantha according to claim 1 extracts separation equipment, it is characterised in that: the molecular distillation equipment packet Include three-level molecular distillation column.
CN201721444775.3U 2017-11-01 2017-11-01 A kind of agalloch eaglewood Edgeworthia chrysantha extraction separation equipment Active CN209481617U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721444775.3U CN209481617U (en) 2017-11-01 2017-11-01 A kind of agalloch eaglewood Edgeworthia chrysantha extraction separation equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721444775.3U CN209481617U (en) 2017-11-01 2017-11-01 A kind of agalloch eaglewood Edgeworthia chrysantha extraction separation equipment

Publications (1)

Publication Number Publication Date
CN209481617U true CN209481617U (en) 2019-10-11

Family

ID=68109576

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721444775.3U Active CN209481617U (en) 2017-11-01 2017-11-01 A kind of agalloch eaglewood Edgeworthia chrysantha extraction separation equipment

Country Status (1)

Country Link
CN (1) CN209481617U (en)

Similar Documents

Publication Publication Date Title
CN107828512A (en) A kind of agalloch eaglewood Edgeworthia chrysantha extraction separation method and equipment
CN100415126C (en) Method for extracting tobacco essence perfume
CN103263370B (en) Production method for jasmine flower perfume
CN103386215B (en) The method of supercritical continuous carbon dioxide extraction Taiwan Cortex seu Flos Hibisci taiwanenss active ingredient
CN100367975C (en) Supercritical CO2 extraction method of ganderoma lucium oil
CN103351954A (en) Process for extracting eaglewood essential oil by using supercritical carbon dioxide
CN108004026A (en) A kind of efficiently agalloch eaglewood extraction system
CN101317649B (en) Method for preparing glossy ganoderma spore oil
CN209481617U (en) A kind of agalloch eaglewood Edgeworthia chrysantha extraction separation equipment
CN101863764B (en) Method for extracting and separating coixenolide and coix seed oil step-by-step by using supercritical CO2
CN103468409A (en) Method for extracting Xinyang maojian tea extractum by utilizing subcritical technology
CN103305343A (en) Method for removing pesticide residue in citrus essential oil
CN101530447A (en) Method for extracting oleoresin rich in lutein in marigold by Supercritical CO2
CN106620008B (en) The technique that tank group ultrasound dynamic countercurrent prepares belladonna liquid extract
CN102533446B (en) Method for removing furocoumarins from citrus essential oil
CN105441194A (en) Purification method for jasmine essential oil
CN104547286A (en) Method for preparing Chinese Eaglewood leaf extract
CN107375400A (en) The supercritical extract of semen momordicae deoils technique
CN103540408B (en) Method for preparing fructus amomi volatile oil
CN109207263B (en) Method for preparing airiness flower essential oil by propylene glycol adsorption method
CN207236016U (en) A kind of spice many body system extracts integrated apparatus
CN108559635B (en) Extraction process of perilla oil
CN207605392U (en) A kind of qinghaosu supercritical extraction unit
CN205556601U (en) High -efficient tea -seed oil filter equipment
CN104694245A (en) A method for obtaining Chinese wolfberry seed oil by supercritical carbon dioxide extraction

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20191121

Address after: 525426 No.25, hebeibei village, committee, Darong village, Guanzhu Town, Dianbai District, Maoming City, Guangdong Province

Patentee after: Maoming Yufeng Chenxiang Creative Industry Co., Ltd

Address before: 510440 interesting creative community A102 in crane long street, Guangzhou Baiyun District, Guangdong

Patentee before: Guangzhou Haoli Technology Co., Ltd.