CN115353929A - Prickly ash oil edulcoration device - Google Patents
Prickly ash oil edulcoration device Download PDFInfo
- Publication number
- CN115353929A CN115353929A CN202210818836.7A CN202210818836A CN115353929A CN 115353929 A CN115353929 A CN 115353929A CN 202210818836 A CN202210818836 A CN 202210818836A CN 115353929 A CN115353929 A CN 115353929A
- Authority
- CN
- China
- Prior art keywords
- sleeve
- impurity removal
- air
- zanthoxylum oil
- edulcoration
- 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.)
- Granted
Links
- 241000949456 Zanthoxylum Species 0.000 title claims abstract description 59
- 235000007650 Aralia spinosa Nutrition 0.000 title claims description 30
- 239000012535 impurity Substances 0.000 claims abstract description 58
- 238000003756 stirring Methods 0.000 claims abstract description 17
- 230000008878 coupling Effects 0.000 claims abstract description 5
- 238000010168 coupling process Methods 0.000 claims abstract description 5
- 238000005859 coupling reaction Methods 0.000 claims abstract description 5
- 238000001035 drying Methods 0.000 claims description 33
- 238000001914 filtration Methods 0.000 claims description 19
- 238000007599 discharging Methods 0.000 claims description 13
- 230000005540 biological transmission Effects 0.000 claims description 3
- 238000004140 cleaning Methods 0.000 claims description 3
- 238000010438 heat treatment Methods 0.000 claims description 2
- 235000019640 taste Nutrition 0.000 abstract description 4
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 238000002360 preparation method Methods 0.000 abstract description 2
- 235000002566 Capsicum Nutrition 0.000 description 22
- 239000003921 oil Substances 0.000 description 22
- 235000019198 oils Nutrition 0.000 description 22
- 239000006002 Pepper Substances 0.000 description 20
- 241000722363 Piper Species 0.000 description 20
- 235000016761 Piper aduncum Nutrition 0.000 description 20
- 235000017804 Piper guineense Nutrition 0.000 description 20
- 235000008184 Piper nigrum Nutrition 0.000 description 20
- 238000000034 method Methods 0.000 description 18
- 244000089698 Zanthoxylum simulans Species 0.000 description 14
- 239000000428 dust Substances 0.000 description 14
- 239000000463 material Substances 0.000 description 8
- 238000006243 chemical reaction Methods 0.000 description 6
- 230000005484 gravity Effects 0.000 description 6
- 238000010586 diagram Methods 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 239000003205 fragrance Substances 0.000 description 4
- 235000013305 food Nutrition 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 241000758706 Piperaceae Species 0.000 description 2
- 239000008157 edible vegetable oil Substances 0.000 description 2
- 239000000796 flavoring agent Substances 0.000 description 2
- 235000019634 flavors Nutrition 0.000 description 2
- 238000007789 sealing Methods 0.000 description 2
- 244000025254 Cannabis sativa Species 0.000 description 1
- 235000012766 Cannabis sativa ssp. sativa var. sativa Nutrition 0.000 description 1
- 235000012765 Cannabis sativa ssp. sativa var. spontanea Nutrition 0.000 description 1
- 240000007594 Oryza sativa Species 0.000 description 1
- 235000007164 Oryza sativa Nutrition 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 235000009120 camo Nutrition 0.000 description 1
- 235000005607 chanvre indien Nutrition 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000011487 hemp Substances 0.000 description 1
- 235000012149 noodles Nutrition 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 235000009566 rice Nutrition 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 235000019654 spicy taste Nutrition 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11B—PRODUCING, 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
- C11B1/00—Production of fats or fatty oils from raw materials
- C11B1/02—Pretreatment
- C11B1/04—Pretreatment of vegetable raw material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B11/00—Arrangement of accessories in apparatus for separating solids from solids using gas currents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B07—SEPARATING SOLIDS FROM SOLIDS; SORTING
- B07B—SEPARATING SOLIDS FROM SOLIDS BY SIEVING, SCREENING, SIFTING OR BY USING GAS CURRENTS; SEPARATING BY OTHER DRY METHODS APPLICABLE TO BULK MATERIAL, e.g. LOOSE ARTICLES FIT TO BE HANDLED LIKE BULK MATERIAL
- B07B7/00—Selective separation of solid materials carried by, or dispersed in, gas currents
- B07B7/06—Selective separation of solid materials carried by, or dispersed in, gas currents by impingement against sieves
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/001—Drying-air generating units, e.g. movable, independent of drying enclosure
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/74—Recovery of fats, fatty oils, fatty acids or other fatty substances, e.g. lanolin or waxes
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The invention relates to the technical field of zanthoxylum oil production equipment, and particularly discloses a zanthoxylum oil impurity removal device. Including edulcoration cover and the filter sleeve pipe of setting in the edulcoration cover, the edulcoration cover is equipped with a plurality of air guide rings outward, all communicates on every air guide ring to have a plurality of air ducts that are located in the edulcoration cover and rotate with the slagging-off cover and be connected, and the intercommunication rigid coupling has a plurality of air ducts that can drive to have rotated stirring fan blade on the air duct, and one side that stirring fan blade kept away from the air duct all is equipped with a plurality of exhaust nozzle. The invention aims to solve the problem that impurities in the zanthoxylum oil can be incompletely cleaned before the preparation of the traditional zanthoxylum oil, so that the taste of the zanthoxylum oil is poor.
Description
Technical Field
The application relates to the technical field of zanthoxylum oil production equipment, and particularly discloses a zanthoxylum oil impurity removal device.
Background
The zanthoxylum oil is a product which is prepared by extracting substances with fragrance from zanthoxylum and edible oil in edible vegetable oil. The spicy pepper has heavy spicy flavor, thick pepper fragrance and qualitative hemp degree, the Chinese prickly ash has long history, and Tang Dynasty is a tribute product, so the Chinese prickly ash is named as tribute pepper. The original Chinese source pepper is named Qingxi pepper with red color, heavy oil, aromatic and rich fragrance, mellow and spicy taste. Zanthoxylum oil can be used as flavoring oil for food with outstanding numb taste and fragrance. Can enhance the flavor of food. The method can be mainly used for: sichuan dish, cold dish, wheaten food, rice noodle, and chafing dish.
The prickly ash is at the picking in-process, often meet and is being mingled with impurity such as dust, leaf, if do not just begin to carry out the work of preparing of prickly ash with these impurity clean-up, will cause the poor problem of prickly ash oil taste, at present before preparing of prickly ash oil, all can carry out cleaning work, but because water is moist, some dust or leaf still can paste on the prickly ash, influence subsequent prickly ash oil work of preparing, for subsequent work of preparing, after wasing, need use prickly ash drying equipment to carry out drying work, therefore, the inventor is in view of the above-mentioned, a prickly ash oil edulcoration device is provided, so that the above-mentioned problem is solved.
Disclosure of Invention
The invention aims to solve the problem that impurities in the zanthoxylum oil can be incompletely cleaned before the preparation of the traditional zanthoxylum oil, so that the taste of the zanthoxylum oil is poor.
In order to achieve the purpose, the basic scheme of the invention provides a zanthoxylum oil impurity removal device which comprises an impurity removal sleeve and a filtering sleeve arranged in the impurity removal sleeve, wherein a plurality of air guide rings are arranged outside the impurity removal sleeve, each air guide ring is communicated with a plurality of air guide pipes which are arranged in the impurity removal sleeve and are rotationally connected with the slag removal sleeve, a plurality of stirring fan blades which can drive the air guide pipes to rotate are communicated and fixedly connected with the air guide pipes, and a plurality of exhaust nozzles are arranged on one sides of the stirring fan blades, which are far away from the air guide pipes.
The principle and effect of this basic scheme lie in:
1. the prickly ash that will wash the completion drips water to pour into the edulcoration cover from the top of edulcoration cover, then pass the edulcoration cover by self gravity, at this in-process, there is the air heater to let in hot-air for exhaust nozzle, alright effectual stoving prickly ash and mix with various dust and leaves in the prickly ash, the dust will be very easily kicked up this moment, and the leaf is dried and becomes crisp, also becomes the graininess easily.
2. In the use, because exhaust nozzle blowout high-speed air current's in-process can exert reaction force for stirring fan blade, just so can drive air duct and stirring fan blade dwang, at stirring fan blade pivoted in-process, not only can carry out stirring work to the prickly ash that falls into in the edulcoration cover, but also can be continuous pat fragile leaf to make the leaf become and to pass the little graininess of filter sleeve pipe.
3. Therefore, in the process of drying the Chinese prickly ash, the air flow of the exhaust nozzle can enter the filter sleeve, the filter sleeve can also enter hot air from the upper part and discharge the hot air from the lower part, and in the process, the raised dust and leaves which become small particles can be effectively blown into the filter sleeve and then discharged from the filter sleeve, so that the impurity removal work is completed.
4. In the use, because the air in the filter sleeve is from the top down through filter sleeve, steam has been mingled with a large amount of steam simultaneously when passing through half the time, is getting into the latter half, and these steam can be in the same place with the dust and the tiny particle leaf absorption of a large amount of lifts, alright reduce the raise dust condition this moment, improve the quality of edulcoration.
Compared with the prior art, the method can effectively remove dust mixed in the pepper, can also remove leaves with the volume and the weight larger than those of the pepper, is simple to operate, has high feasibility, and is convenient for large-scale popularization.
Further, a drying closing plate and a discharging closing plate are sequentially arranged between the impurity removing sleeve and the filtering sleeve from top to bottom. The impurity removing sleeve is divided into a drying cavity and an impurity removing cavity by utilizing the drying closing plate and the discharging closing plate, the Chinese prickly ash entering the impurity removing sleeve can be firstly accumulated on the drying closing plate, and the time of the Chinese prickly ash in the impurity removing sleeve is prolonged by utilizing the drying closing plate, so that the drying work is facilitated; the prickly ash that the stoving was accomplished falls on arranging the material and closes the board through drying and closing the board, utilizes to arrange the material and closes the board and improve the time of prickly ash in the edulcoration cover, alright effectual improvement dust remove impurity volume.
Furthermore, the bottom of the drying closing plate is provided with a plurality of supporting nozzles communicated with the air guide ring, and the bottom of the discharging closing plate is provided with a plurality of supporting springs communicated with the inner wall of the impurity removing sleeve. The Chinese prickly ash falling on the drying closing plate initially has a large amount of moisture and is heavier, the reaction force of the high-speed airflow sprayed by the supporting nozzles is smaller than the weight of the Chinese prickly ash falling on the drying closing plate, the Chinese prickly ash is supported in the drying closing plate, then the Chinese prickly ash is dried in the using process, the weight is reduced, the reaction force of the high-speed airflow sprayed by the supporting nozzles is larger than the weight of the Chinese prickly ash falling on the drying closing plate, the drying closing plate is pushed open, and the Chinese prickly ash falls on the discharging closing plate; the prickly ash falls into row material and closes the board, and supporting spring's holding power is greater than the gravity of prickly ash this moment, and the prickly ash just stops on arranging material and closing the board, and not only accomplish further stoving this moment, but also can be through the more complete completion edulcoration work of air current, and then the prickly ash piles more, and supporting spring's holding power will the gravity of prickly ash, and row material is closed the board and is just opened this moment, and the edulcoration cover will be discharged to a part prickly ash that is located the below to accomplish the edulcoration work.
Further, the air duct and the filter sleeve pipe rigid coupling, the filter sleeve pipe rotates with the edulcoration cover to be connected, all is equipped with the location ring gear in the air duct ring, all is equipped with the drive gear with location ring gear meshing on the air duct. When the air duct rotates, the air duct and the filtering sleeve can be driven to rotate through the transmission gear and the positioning gear ring, the inner space of the impurity removing sleeve with a larger area can be covered, meanwhile, the outer wall of the filtering sleeve which rotates continuously can continuously rub with pepper, so that impurities adsorbed on the outer wall fall off from the outer wall and enter the filtering sleeve, and therefore higher-quality impurity removing work is finished; in the working process, all the air guide pipes are fixedly connected with the filtering sleeve, so that after a certain air guide pipe is clamped, other air guide pipes rotate and revolve, the filtering sleeve can be driven to rotate at the moment, in the rotating process of the filtering sleeve, the clamped air guide pipes are driven to revolve in reverse, the clamped air guide pipes revolve, the meshing revolution of the positioning gear ring and the transmission gear can be announced, the clamped air guide pipes are driven to rotate, and the occurrence of the clamped air guide pipes can be reduced.
Furthermore, the upper end of the filtering sleeve is rotatably provided with a support ring fixedly connected with the impurity removing sleeve, and the bottom of the filtering sleeve is rotatably provided with a mounting seat. The stable rotation of filter sleeve pipe is convenient for.
Furthermore, a scraper plate capable of cleaning the inner wall of the filter sleeve is arranged in the mounting seat. The inner wall of the filter sleeve can be cleaned by continuously rotating the filter sleeve and the scraper which is relatively static, so that higher-quality impurity removal work is completed.
Furthermore, the upper end of the impurity removing sleeve is fixedly connected with a feed hopper. The feeding work is convenient.
Furthermore, a plurality of heating plates are arranged on the inner side of the impurity removing sleeve. The drying efficiency is improved.
Drawings
In order to more clearly illustrate the technical solutions in the embodiments of the present application, the drawings needed to be used in the description of the embodiments are briefly introduced below, and it is obvious that the drawings in the following description are only some embodiments of the present application, and it is obvious for those skilled in the art to obtain other drawings based on these drawings without creative efforts.
FIG. 1 shows a schematic structural diagram of a zanthoxylum oil impurity removal device provided by the embodiment of the application;
FIG. 2 is a top cross-sectional view of a zanthoxylum oil impurity removing device according to an embodiment of the present application;
FIG. 3 shows a schematic structural diagram of a filtering sleeve in a zanthoxylum oil impurity removal device according to an embodiment of the application;
FIG. 4 is a front sectional view of a zanthoxylum oil impurity removing device provided by the embodiment of the application;
FIG. 5 shows a schematic structural diagram of a positioning toothed ring in a zanthoxylum oil impurity removal device according to an embodiment of the present application;
fig. 6 shows a schematic structural diagram of a drying closing plate in a filtering sleeve in the zanthoxylum oil impurity removing device provided by the embodiment of the application;
fig. 7 shows a schematic structural diagram of a discharging closing plate in the zanthoxylum oil impurity removing device provided by the embodiment of the application.
Detailed Description
To further illustrate the technical means and effects of the present invention adopted to achieve the predetermined objects, the following detailed description of the embodiments, structures, features and effects according to the present invention will be made with reference to the accompanying drawings and preferred embodiments.
Reference numerals in the drawings of the specification include: the device comprises a feed hopper 1, a filtering sleeve 2, an impurity removing sleeve 3, an air guide ring 4, a mounting seat 5, stirring blades 6, a drying closing plate 7, a discharging closing plate 8, a scraping plate 9, a positioning toothed ring moving gear 11, a positioning toothed ring 12, an exhaust nozzle 13, a sealing ring 14, an exhaust nozzle 15, a support ring 16 and a support spring 17.
The embodiment is shown in fig. 1, and edulcoration cover 3 and rotation set up the filter tube 2 in edulcoration cover 3, and edulcoration 3 upper ends of covering have welded a feeder hopper 1, and edulcoration 3 inboards of covering are equipped with a plurality of hot plates, and the rotation of filter tube 2 upper end is equipped with edulcoration 3 welded support rings 16, and the rotation of filter tube 2 bottom has set up a mount pad 5 that is used for supporting filter tube 2, as shown in fig. 4, is equipped with the scraper blade 9 that can clean filter tube 2 inner wall in the mount pad 5.
As shown in fig. 1, fig. 2 and fig. 3, edulcoration cover 3 is equipped with a plurality of air guide rings 4 outward, all communicate on every air guide ring 4 have a plurality of be located edulcoration cover 3 in and with the slagging-off cover rotate the air duct of being connected, the intercommunication rigid coupling has a plurality of air ducts that can drive to rotate stirring fan blade 6 on the air duct, one side that stirring fan blade 6 kept away from the air duct all is equipped with a plurality of exhaust nozzle 13, air guide ring 4 and filter sleeve 2 upper end all communicate has the air heater, as shown in fig. 5, the inboard rotation is equipped with a sealing ring 14 that is used for installing the air duct in the edulcoration cover 3, air duct and filter sleeve 2 rigid coupling, filter sleeve 2 rotates with edulcoration cover 3 to be connected, all be equipped with location ring gear 12 in the air guide ring 4, all be equipped with the drive gear with location ring gear of 12 meshing on the air duct.
As shown in fig. 2, fig. 6 and fig. 7, a drying closing plate 7 and a discharging closing plate 8 are sequentially arranged between the impurity removing sleeve 3 and the filtering sleeve 2 from top to bottom, a plurality of supporting nozzles communicated with the air guide ring 4 are arranged at the bottom of the drying closing plate 7, and a plurality of supporting springs 17 communicated with the inner wall of the impurity removing sleeve 3 are arranged at the bottom of the discharging closing plate 8.
When in use, a plurality of the device is firstly installed on a production line for producing and treating zanthoxylum oil, and the device can be put into use by switching on the air heater and the power supply.
Draining water from the washed pepper, pouring the impurity removal sleeve 3 above the impurity removal sleeve 3, and then enabling the pepper to penetrate through the impurity removal sleeve 3 by self gravity, wherein in the process, hot air is introduced into the exhaust nozzle 13 by an air heater, so that the pepper and various dust and leaves mixed in the pepper can be effectively dried, at the moment, the dust can be easily lifted, and the leaves are dried and become crisp and also easily become small particles; in the use, because exhaust nozzle 13 spouts high velocity air's in-process, can exert reaction force for stirring fan blade 6, just so can drive air duct and stirring fan blade 6 dwang, at stirring fan blade 6 pivoted in-process, not only can carry out stirring work to the prickly ash that falls into in edulcoration cover 3, but also can be continuous pat fragile leaf to make the leaf become the tiny particle form that can pass filter sleeve 2.
Therefore, in the process of drying the Chinese prickly ash, the airflow of the exhaust nozzle 13 enters the filter sleeve 2, the filter sleeve 2 also enters hot air from the upper part and discharges the hot air from the lower part, and in the process, the raised dust and leaves which become small particles can be effectively blown into the filter sleeve 2 and then discharged from the filter sleeve 2, so that the impurity removal work is completed.
In order to improve the impurity removal effect, the peppers entering the impurity removal sleeve 3 can be firstly accumulated on the drying closing plate 7, and the drying closing plate 7 is utilized to improve the time of the peppers in the impurity removal sleeve 3, so that the drying work is facilitated; the dried Chinese prickly ash falls on the discharging closing plate 8 through the drying closing plate 7, and the discharging closing plate 8 is utilized to improve the time of the Chinese prickly ash in the impurity removing sleeve 3, so that the impurity removing amount of dust can be effectively improved; the pepper falling on the drying closing plate 7 initially has a large amount of moisture and is heavier, the reaction force of the high-speed airflow sprayed by the supporting nozzles is smaller than the weight of the pepper falling on the drying closing plate 7, the pepper is supported in the drying closing plate 7, then the pepper is dried and reduced in weight in the using process, the reaction force of the high-speed airflow sprayed by the supporting nozzles is larger than the weight of the pepper falling on the drying closing plate 7, the drying closing plate 7 is pushed open, and the pepper falls into the discharging closing plate 8; the prickly ash falls into row material and closes board 8, and supporting spring 17's holding power is greater than the gravity of prickly ash this moment, and the prickly ash just stops on arranging material and closing board 8, and further stoving not only is accomplished this moment, but also can be through the more complete completion edulcoration work of air current, then the prickly ash piles more, and supporting spring 17's holding power will the gravity of prickly ash, arranges material this moment and closes board 8 and just opens, and some prickly ash that is located the below will discharge edulcoration cover 3 to accomplish the edulcoration work.
The method can effectively remove dust mixed in the pepper, can also remove leaves with the volume and the weight larger than those of the pepper, and is simple to operate, high in feasibility and convenient to popularize in a large range. Although the present invention has been described with reference to the preferred embodiments, it should be understood that various changes, substitutions and alterations can be made herein without departing from the spirit and scope of the invention as defined by the appended claims.
Claims (8)
1. The utility model provides a prickly ash oil edulcoration device which characterized in that: including edulcoration cover and the filter sleeve pipe of setting in the edulcoration cover, the edulcoration cover is equipped with a plurality of air guide rings outward, all communicates on every air guide ring to have a plurality of air ducts that are located in the edulcoration cover and rotate with the slagging-off cover and be connected, and the intercommunication rigid coupling has a plurality of air guides that can drive to rotate stirring fan blade on the air guide, and one side that stirring fan blade kept away from the air guide all is equipped with a plurality of exhaust nozzle, and air guide ring and filter sleeve pipe upper end all communicate there is the air heater.
2. The zanthoxylum oil impurity removal device according to claim 1, wherein a drying closing plate and a discharging closing plate are sequentially arranged between the impurity removal sleeve and the filtering sleeve from top to bottom.
3. The Zanthoxylum oil impurity removing device according to claim 2, wherein the bottom of the drying closing plate is provided with a plurality of supporting nozzles communicated with the air guide ring, and the bottom of the discharging closing plate is provided with a plurality of supporting springs communicated with the inner wall of the impurity removing sleeve.
4. The zanthoxylum oil impurity removal device according to claim 1, wherein the air duct is fixedly connected with the filtering sleeve, the filtering sleeve is rotatably connected with the impurity removal sleeve, positioning gear rings are arranged in the air duct rings, and transmission gears meshed with the positioning gear rings are arranged on the air duct rings.
5. The zanthoxylum oil impurity removal device according to claim 4, wherein the upper end of the filtering sleeve is rotatably provided with a support ring fixedly connected with the impurity removal sleeve, and the bottom of the filtering sleeve is rotatably provided with a mounting seat.
6. The zanthoxylum oil impurity removal device according to claim 5, wherein a scraper capable of cleaning the inner wall of the filter sleeve is arranged in the mounting seat.
7. The Zanthoxylum oil impurity removal device according to claim 1, wherein a feed hopper is fixedly connected with the upper end of the impurity removal sleeve.
8. The zanthoxylum oil impurity removal device according to claim 7, wherein a plurality of heating plates are arranged on the inner side of the impurity removal sleeve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210818836.7A CN115353929B (en) | 2022-07-12 | 2022-07-12 | Zanthoxylum oil edulcoration device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210818836.7A CN115353929B (en) | 2022-07-12 | 2022-07-12 | Zanthoxylum oil edulcoration device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN115353929A true CN115353929A (en) | 2022-11-18 |
| CN115353929B CN115353929B (en) | 2024-03-29 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202210818836.7A Active CN115353929B (en) | 2022-07-12 | 2022-07-12 | Zanthoxylum oil edulcoration device |
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