CN202415508U - System device for extracting radix asparagi seed oil - Google Patents
System device for extracting radix asparagi seed oil Download PDFInfo
- Publication number
- CN202415508U CN202415508U CN2011205121004U CN201120512100U CN202415508U CN 202415508 U CN202415508 U CN 202415508U CN 2011205121004 U CN2011205121004 U CN 2011205121004U CN 201120512100 U CN201120512100 U CN 201120512100U CN 202415508 U CN202415508 U CN 202415508U
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- radix asparagi
- tank
- seed oil
- connects
- transfer lime
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Abstract
The utility model discloses a system device for extracting radix asparagi seed oil, which comprises a CO2 tank, a pressure regulating device, a temperature regulating device, an extraction tank, a separation tank, a discharging hole, a separating tank, a high-pressure tank, a high-pressure pump, a condenser, a feeding hole and a conveying pipe. During the use, radix asparagi seed powder is fed into the extraction tank through the feeding hole, the CO2 tank is opened, CO2 enters the extraction tank by passing through the condenser, the high-pressure pump, the temperature regulating device and the pressure regulating device through the conveying pipe, and the radix asparagi seed powder is dissolved when the CO2 reaches a supercritical state, and then the dissolved radix asparagi seed powder enters the separating tank for primary separation, so that the supercritical oil is obtained, the radix asparagi seed oil continuously enters a secondary separating tank for secondary separation, so that the radix asparagi seed oil is obtained, and the separated CO2 reflows into the condensing the tank for recycling. The utility model has the beneficial effects that the radix asparagi seed oil is high in recycling rate and good in quality; the system device has a simple structure, and is easy to operate; and the economic benefit is increased, and the labor intensity is lowered.
Description
Technical field
The extraction plant that the utility model relates to and a kind of plant seed is oily, particularly a kind of system and device that extracts the Radix Asparagi seed oil.
Background technology
Radix Asparagi Asparagus cochinchinensis (Lour.) Merr. has another name called asparagus fern, for the evergreen vine of Liliaceae, is used as medicine with the piece root.Main product in Guizhou, ground such as Guangxi, Yunnan, Gansu, Anhui, Henan, Hunan, Hubei, Sichuan and Jiangxi.The asparagus fern beginning is stated from Shennong's Herbal, and the successive dynasties book on Chinese herbal medicine is all on the books.Its flavor is sweet, bitter, cold in nature, returns the lung kidney channel, the ability nourishing YIN to relieve dryness, and clearing lung-heat is promoted the production of body fluid; Cure mainly that dryness of the lung dry cough, cough due to consumptive disease, Tianjin wound are thirsty, disease such as the numerous insomnia of the heart, interior heat are quenched one's thirst, the dry constipation of intestines.Can also treat dry throat and mouth, cough caused by dryness phlegm is sticking, spitting of blood, Whooping cough, pharyngeal diphtheria, rhinitis sicca etc.Asparagus fern contains compositions such as aspartic acid, N, β-Gu Zaichun, steroid saponin, asparagus fern polysaccharide, phlegmatic temperament, Stigmasterol, 5-methoxymethyl furfural, alditol, lactones, flavones, anthraquinone, cardiotonic glycoside, rhamnosyl, wood sugar and glucose.Also contain abundant VITAMINs, inorganic elements etc. in addition.Since ancient times, people Radix Asparagi as the good merchantable brand of promoting longevity, thereby being in great demand to Radix Asparagi.
Research for Radix Asparagi at present mainly concentrates on its rhizome; And very few to the research of seed, be rich in wax in fact in the Radix Asparagi seed, its wax is a composition very important in the Chinese medicine; Obtaining the Radix Asparagi seed oil at present all is to adopt traditional pressing method; Not only workload is big, and the recovery is very low, causes the waste of efficient resource.
Adopt supercritical CO
2Extracting process is one well to be selected, but relevant device is more popular at present, also is not fit to the device of extraction Radix Asparagi seed oil.
The utility model content
The utility model technical problem to be solved provides a kind of special-purpose supercritical CO of Radix Asparagi seed oil that extracts
2Extraction plant is to simplify technical process, reduce labour intensity, the height that improves the quality of products, to improve the extraction yield of Radix Asparagi seed oil.
For solving the problems of the technologies described above, the technical scheme that the utility model adopted is the system and device of extraction Radix Asparagi seed oil, comprises CO
2Gas tank, voltate regulator, thermosistor, extractor, separating tank
, discharge port, separating tank
, HPP, condensing surface, dog-house and transfer lime, it is characterized in that CO
2Gas tank connects condensing surface through transfer lime; Condensing surface connects HPP through transfer lime, and HPP connects thermosistor through transfer lime, and thermosistor connects voltate regulator through transfer lime; Voltate regulator connects extractor through transfer lime; Dog-house is housed on the extractor, and the other end of extractor connects thermosistor and voltate regulator through transfer lime, connects separating tank again
, separating tank
There is discharge port the lower end, and the upper end connects voltate regulator through transfer lime and connects separating tank again
, separating tank
There is discharge port the lower end, and the upper end connects condensing surface through transfer lime.
During use, Radix Asparagi kind powder of seeds is dropped into extractor from dog-house, envelope is tight, opens CO
2Gas tank, CO
2Get into extractor, CO through transfer lime through condensing surface, HPP, thermosistor and voltate regulator
2Be issued to supercritical state at relevant pressure and temperature, when the Radix Asparagi seed oil is dissolved in supercritical CO
2Get into separating tank through transfer lime through thermosistor and voltate regulator behind the fluid
, under relevant pressure and temperature, carry out flash trapping stage, obtain the Radix Asparagi seed oil; Supercritical CO then
2Fluid continues to get into the secondary separating tank through transfer lime through voltate regulator
, under relevant pressure and temperature, carry out secondary and separate, obtain the Radix Asparagi seed oil, the CO that separates simultaneously
2Be back in the drainer, recycle.
The beneficial effect of the utility model is that the recovery of Radix Asparagi seed oil is high, and quality is good, and equipment is simple, and easy handling has improved economic benefit, has reduced labour intensity.
Description of drawings
Accompanying drawing is the system and device synoptic diagram of the utility model extraction Radix Asparagi seed oil.
Among the figure: 1, CO
2Gas tank, 2, voltate regulator, 3, thermosistor, 4, extractor, 5, separating tank
, 6, discharge port, 7, separating tank
, 8, HPP, 9, condensing surface, 10, dog-house, 11, transfer lime.
Embodiment
Below in conjunction with accompanying drawing and embodiment the utility model is described further.
With CO
2Gas tank 1 connects condensing surface 9 through transfer lime 11; Condensing surface 9 connects HPP 8 through transfer lime 11, and HPP 8 connects thermosistor 3 through transfer lime 11, and thermosistor 3 connects voltate regulator 2 through transfer lime 11; Voltate regulator 2 connects extractor 4 through transfer lime 11; Dog-house 10 is installed on extractor 4, the other end of extractor 4 is connected thermosistors 3 and voltate regulators 2 through transfer lime 11, connect separating tank again
5, separating tank
Discharge port 6 is installed in 5 lower ends, and the upper end connects voltate regulator 2 through transfer lime 11 and connects separating tank again
7, separating tank
Discharge port 6 is installed in 7 lower ends, and the upper end connects condensing surface 9 through transfer lime 11, so just has been mounted to the system and device of extraction Radix Asparagi seed oil.
Get Radix Asparagi kind powder of seeds 100kg, drop in the extractor 4, CO is opened in sealing
2 Gas tank 1, CO
2Arrive extractor 4 through condensing surface 9, HPP 8, at pressure 30MPa, 45 ℃ of temperature, CO
2Extract under the flow 20kg/h condition; When the Radix Asparagi seed oil is dissolved in supercritical CO
2Get into the flash trapping stage jar behind the fluid
5, at pressure 8MPa, carry out flash trapping stage under 40 ℃ of conditions of temperature, obtain the Radix Asparagi seed oil; Supercritical CO
2Fluid continues to get into the secondary separating tank
In 7,, carry out secondary under 40 ℃ of conditions of temperature and separate, obtain the Radix Asparagi seed oil, from separating tank at pressure 6MPa
The CO that separates in 7
2Get back in the drainer 9, obtain Radix Asparagi seed oil 7.25kg behind the dynamic operation 90min.
Claims (1)
1. the system and device of extraction Radix Asparagi seed oil comprises CO
2Gas tank (1), voltate regulator (2), thermosistor (3), extractor (4), separating tank
(5), discharge port (6), separating tank
(7), HPP (8), condensing surface (9), dog-house (10) and transfer lime (11), it is characterized in that CO
2Gas tank (1) connects condensing surface (9) through transfer lime (11); Condensing surface (9) connects HPP (8) through transfer lime (11); HPP (8) connects thermosistor (3) through transfer lime (11); Thermosistor (3) connects voltate regulator (2) through transfer lime (11), and voltate regulator (2) connects extractor (4) through transfer lime (11), and dog-house (10) is housed on the extractor (4); The other end of extractor (4) connects thermosistor (3) and voltate regulator (2) through transfer lime (11), connects separating tank again
(5), separating tank
(5) there is discharge port (6) lower end, and the upper end connects voltate regulator (2) through transfer lime (11) and connects separating tank again
(7), separating tank
(7) there is discharge port (6) lower end, and the upper end connects condensing surface (9) through transfer lime (11).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205121004U CN202415508U (en) | 2011-12-11 | 2011-12-11 | System device for extracting radix asparagi seed oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2011205121004U CN202415508U (en) | 2011-12-11 | 2011-12-11 | System device for extracting radix asparagi seed oil |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202415508U true CN202415508U (en) | 2012-09-05 |
Family
ID=46740289
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2011205121004U Expired - Fee Related CN202415508U (en) | 2011-12-11 | 2011-12-11 | System device for extracting radix asparagi seed oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202415508U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103421599A (en) * | 2013-07-31 | 2013-12-04 | 安徽省霍山县聚一科技有限公司 | Camellia oil preparation system and operation method thereof |
-
2011
- 2011-12-11 CN CN2011205121004U patent/CN202415508U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103421599A (en) * | 2013-07-31 | 2013-12-04 | 安徽省霍山县聚一科技有限公司 | Camellia oil preparation system and operation method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20120905 Termination date: 20151211 |
|
| EXPY | Termination of patent right or utility model |