CN211057059U - Continuous extraction tank for spice - Google Patents
Continuous extraction tank for spice Download PDFInfo
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- CN211057059U CN211057059U CN201921684088.8U CN201921684088U CN211057059U CN 211057059 U CN211057059 U CN 211057059U CN 201921684088 U CN201921684088 U CN 201921684088U CN 211057059 U CN211057059 U CN 211057059U
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Abstract
The utility model provides a spices continuous extraction jar, includes extraction jar, auger delivery ware, center pin, motor, feeding and discharge gate, steam inlet and steam outlet, and the extraction jar is the airtight jar body that is equipped with the heat preservation, is equipped with the auger delivery ware of fixing on the center pin in the extraction jar, and the extraction jar is equipped with the motor that links to each other with the center pin, drives auger delivery ware around the center rotation will follow natural spices and carry the other end by the one end of extraction jar. The opposite sides of the two ends of the extraction tank are respectively provided with a feed inlet and a discharge outlet, a steam outlet and a steam inlet, the feed inlet and the steam outlet are respectively arranged at the same end of the extraction tank, the discharge outlet and the steam inlet are respectively arranged at the other same end of the extraction tank, so that the perfume and the gas are in countercurrent contact, and the extracted fragrance is carried from the steam outlet to leave the extraction tank and enter the gas storage tank. The utility model has the advantages of simple structure, but continuous production is suitable for and carries out continuous extraction to a large amount of spices, and the countercurrent extraction design has promoted extraction efficiency, can extract the aromatic substance of spices high-efficiently.
Description
Technical Field
The utility model relates to a natural perfume draws equipment, especially relates to a natural perfume's continuous extraction jar.
Background
The natural perfume has a long history of use in human activities, and ancient people use aromatic parts of animals and plants as raw materials to prepare original-state perfume materials through simple processing, and most of the shapes of the natural perfume materials keep some inherent appearance characteristics of the animals and plants, such as incense wood blocks, incense wood pieces, incense powder and the like; the aromatic substances separated from natural raw materials by physical methods (steam distillation, extraction, squeezing, etc.) in modern times are in the forms of essential oil, extract, absolute oil, balm, tincture, isolated natural perfume, etc., such as rose oil, vanilla tincture, jasmine extract, ylang essential oil, litsea cubeba oil, osmanthus absolute oil, menthol, etc. Conventional perfume extraction techniques include steam distillation, leaching and pressing, among others.
The steam distillation comprises various forms of water distillation, direct steam distillation, rotary cone stripping distillation and the like, and is suitable for extracting some natural perfumes with low aroma component boiling points, for example, the current high-quality rose essential oil is still extracted by using the steam distillation.
The extraction method is suitable for raw materials whose aroma components are easily deteriorated when heated, or some aroma components are dissolved in water and are not suitable for steam extraction. The most common is a volatile solvent extraction method, and the used solvent is petroleum ether, benzene, dichloroethane or a mixed solvent and the like; when carbon dioxide is used as a solvent, a supercritical extraction method can be adopted, the solvent is not required to be removed by heating at a lower temperature, the processing and extraction of food flavors are extremely suitable, the product fragrance is closer to natural raw materials, and no solvent residue exists. But the industrial application is not wide due to large equipment investment and higher technical requirement.
The squeezing method has wide application range, and is only suitable for extracting essential oil of citrus pericarp, such as sweet orange oil, lemon oil, shaddock oil, orange oil, etc.
The adsorption method is used as early as 18 th century, and is a method for absorbing aromatic components in fresh flowers by refined oil, replacing the flowers after a period of time, saturating the oil absorbing the aromatic components of the fresh flowers after replacing for many times, and then removing the aromatic components absorbed balsam by alcohol; at present, activated carbon, novel porous polymer and the like are mostly used as adsorbents, and then alcohol or supercritical carbon dioxide is used for desorption, so that the quality and the yield of essential oil are obviously improved.
The existing common extraction method mainly uses a medium or a solvent to carry out aroma components, and then concentrates or removes the solvent to obtain the aroma extract, so that the influence of the extraction process and the solvent on aroma is reduced as much as possible, and the aroma components in the natural aroma are completely and completely extracted.
However, these methods of extracting a perfume have disadvantages in extracting a perfume from a solid or viscous paste having a low water content, a strong fragrance, or a high boiling point of the fragrance component. Particularly, for some natural perfumes, the traditional production mode has limited yield and cannot meet the market demand. Therefore, it is desirable to design a way to rapidly produce perfume extracts in large quantities while ensuring the quality of the perfume extracts.
Disclosure of Invention
An object of the utility model is to the weak point that exists among the prior art, provide a device that can carry out continuous extraction to natural spices, can improve the output of natural spices extraction product, be applicable to the extensive extraction of natural essential oil.
In order to realize the above-mentioned purpose, the utility model provides a spices continuous extraction jar, including extraction jar, auger delivery ware, the center pin, including a motor, an end cap, a controller, and a cover plate, feeding and discharge gate, steam inlet and steam outlet, the airtight jar body of its characterized in that extraction jar for being equipped with the heat preservation, be equipped with the auger delivery ware of fixing on the center pin in the extraction jar, the one end of extraction jar is equipped with the motor, this motor links to each other with the center pin and drives the auger delivery ware of fixing on the center pin and around the center is rotatory to will enter into the internal natural spices of jar from the feed inlet and. The opposite sides of the two ends of the extraction tank are respectively provided with a feed inlet and a discharge outlet, a steam outlet and a steam inlet, the feed inlet and the steam outlet are respectively arranged at the same end of the extraction tank, the discharge outlet and the steam inlet are respectively arranged at the other same end of the extraction tank, natural perfume and gas are in countercurrent contact in the extraction tank, the steam enters the tank body from the steam inlet, and the extraction operation of the perfume is started until the extraction is finished, the extracted perfume components are carried from the steam outlet to separate the continuous extraction tank, and then the extracted perfume components enter a gas storage tank connected with the steam outlet.
The extraction tank is horizontal, the feed inlet is arranged on the upper side face of one end of the extraction tank, and the discharge outlet is arranged on the lower side face of the other end of the extraction tank. The extraction tank can also be vertical or inclined, and the inclination angle of the extraction tank is 0-90 degrees.
The length of the extraction tank is 1-20 m; the diameter is 10 cm-1 m.
The screw conveyer arranged in the extraction tank is tightly contacted with the inner wall of the extraction tank, the blade spacing of the screw conveyer is 10 cm-50 cm, and the rotating speed is 1-60 r/min.
The extraction tank can be used for extracting solid and viscous pasty raw materials.
The utility model has the advantages that:
1. the device has the advantages of simple structure, low cost, convenient cleaning and continuous production.
2. The screw conveyor in the extraction tank can convey natural perfume, increase the contact area and contact time of the perfume and extraction steam, and improve the extraction efficiency.
3. The extraction tank is flexible to operate. The residence time of the natural perfume in the extractor can be controlled by controlling the rotation speed of the screw conveyor, and the thermal decomposition and loss of the recovered aroma substances can be avoided by matching with proper extraction temperature control.
Drawings
FIG. 1 is a schematic structural view of the present invention;
in the figure: 1. the device comprises a screw conveyor, a feed inlet 2, a discharge outlet 3, a steam inlet 4, a steam outlet 5, a heat insulation layer 6, a motor 7, a central shaft 8 and an extraction tank 9.
Detailed Description
The embodiments of the present invention will be further explained with reference to the accompanying drawings:
referring to fig. 1, the continuous extraction tank for perfume of the present embodiment includes an extraction tank 9, a screw conveyor 1, a central shaft 8, a motor 7, a feed inlet 2, a discharge outlet 3, a steam inlet 4 and a steam outlet 5, the extraction tank 9 is a closed tank body, the extraction tank 9 is provided with a heat insulation layer 6, the extraction tank may be horizontal or vertical or inclined, an inclination angle of the extraction tank 9 is 0 ° to 90 °, and the length of the extraction tank 9 is 1 m to 20 m; the diameter is 10 cm-1 m. The extraction tank 9 of this example is horizontal, and the length of the extraction tank 9 is 10 meters, and the diameter is 0.3 meter. The extraction tank 9 is internally provided with a screw conveyor 1, the screw conveyor 1 is fixed on a central shaft 8, the screw conveyor 1 is tightly contacted with the inner wall of the extraction tank 9, the blade pitch of the screw conveyor 1 is 10 cm-50 cm, and the rotating speed is 1 r/min-60 r/min. The pitch of the blades of the screw conveyor 1 of this embodiment is 20 cm and the rotational speed is 2 revolutions per minute. The extraction tank 9 is provided with a feed inlet 2, and the feed inlet 2 is connected with a storage tank (not shown in the figure). One end of the extraction tank 9 is provided with a motor 7, the motor 7 is connected with a central shaft 8 to drive a screw conveyor 1 fixed on the central shaft 8 to rotate around the center, and the solid natural spice entering the tank body from the feed port 2 is conveyed to the other end from one end of the extraction tank 9. The opposite sides of the two ends of the extraction tank 9 are respectively provided with a feed inlet 2, a discharge outlet 3, a steam outlet 5 and a steam inlet 4. In this embodiment, the feed inlet 2 and the vapor outlet 5 are respectively disposed at the same end of the extraction tank 9, and the feed inlet 2 is disposed on the upper side surface of the extraction tank 9. The discharge port 3 and the steam inlet 4 are respectively arranged at the other same end of the extraction tank 9, the discharge port 3 is arranged at the lower side surface of the extraction tank 9, and the steam outlet 5 is connected with a gas storage tank (not shown in the figure), so that natural perfume and gas are in countercurrent contact in the extraction tank 9, the steam enters the tank body from the steam inlet 4, and the perfume is extracted until the extraction is finished, and the extracted perfume components carried by the steam outlet 5 are separated from the continuous extraction tank 9 and enter the gas storage tank connected with the steam outlet 5 for storage.
When in use, the spice stored in the spice storage tank is continuously fed into the extraction tank 9 from the feed inlet 2, and a solvent can be optionally added as an extraction solvent. The perfume is pushed by the blades of the screw conveyor 1 to move towards the other end, and the temperature of the extraction tank is controlled to be the set temperature, so that the aroma components in the perfume are separated. Introducing extraction steam through the steam inlet 4 to make the natural perfume and steam gas contact in countercurrent in the extraction tank 9, extracting the aroma components until the extraction is completed, allowing the extracted aroma components to leave the continuous extraction tank 9 from the steam outlet 5 and enter the aroma collection tank for recovery, and allowing the extracted perfume waste to enter a waste tank (not shown in the figure).
The utility model discloses a spices continuous extraction jar can combine with conventional spices extraction system, constitutes efficient spices continuous extraction device. The temperature of the extraction tank, the rotation speed of the screw conveyor and which solvent is selected as the extraction solvent can be determined according to the physical properties of the perfume and the requirements of products.
Claims (5)
1. The utility model provides a spices continuous extraction jar, including the extraction jar, the auger delivery ware, the center pin, including a motor, an end cap, a controller, and a cover plate, feed inlet and discharge gate, steam inlet and steam outlet, its characterized in that extraction jar is the airtight jar body that is equipped with the heat preservation, be equipped with the auger delivery ware of fixing on the center pin in the extraction jar, the one end of extraction jar is equipped with the motor, this motor links to each other with the center pin and drives the auger delivery ware of fixing on the center pin and revolve around the center, the both ends opposite side of extraction jar is equipped with feed inlet and discharge gate respectively, steam outlet and steam inlet, feed inlet and steam outlet establish the same end of extraction jar respectively, another same end at the.
2. The continuous extraction tank of claim 1, wherein the extraction tank is horizontal, the inlet is disposed on the upper side of one end of the extraction tank, and the outlet is disposed on the lower side of the other end of the extraction tank.
3. The continuous extraction tank of claim 1, wherein the extraction tank is vertical or inclined, and the inclination angle of the extraction tank is 0 ° to 90 °.
4. The continuous extraction tank of claim 1, wherein the extraction tank has a length of 1-20 m; the diameter is 10 cm-1 m.
5. The continuous extraction tank of claim 1, wherein the extraction tank is provided with a screw conveyor closely contacting the inner wall of the extraction tank, the screw conveyor has a blade pitch of 10 cm to 50 cm and a rotation speed of 1 rpm to 60 rpm.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201921684088.8U CN211057059U (en) | 2019-10-10 | 2019-10-10 | Continuous extraction tank for spice |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201921684088.8U CN211057059U (en) | 2019-10-10 | 2019-10-10 | Continuous extraction tank for spice |
Publications (1)
Publication Number | Publication Date |
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CN211057059U true CN211057059U (en) | 2020-07-21 |
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CN201921684088.8U Active CN211057059U (en) | 2019-10-10 | 2019-10-10 | Continuous extraction tank for spice |
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CN (1) | CN211057059U (en) |
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2019
- 2019-10-10 CN CN201921684088.8U patent/CN211057059U/en active Active
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Inventor after: Kang Weijun Inventor after: Zhang Weibing Inventor after: Zhuang Weiqiang Inventor after: Mao Fuyan Inventor after: Liu Wei Inventor before: Kang Weijun Inventor before: Zhang Weibing Inventor before: Zhuang Weiqiang Inventor before: Mao Fuyan Inventor before: Liu Wei |
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CB03 | Change of inventor or designer information |