CN115449431A - Natural perfume extraction device - Google Patents
Natural perfume extraction device Download PDFInfo
- Publication number
- CN115449431A CN115449431A CN202211063502.XA CN202211063502A CN115449431A CN 115449431 A CN115449431 A CN 115449431A CN 202211063502 A CN202211063502 A CN 202211063502A CN 115449431 A CN115449431 A CN 115449431A
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- distillation tower
- tower body
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- temperature
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- 238000000605 extraction Methods 0.000 title claims abstract description 40
- 239000002304 perfume Substances 0.000 title claims description 12
- 238000004821 distillation Methods 0.000 claims abstract description 94
- 235000013599 spices Nutrition 0.000 claims abstract description 20
- 238000010438 heat treatment Methods 0.000 claims description 34
- 238000006243 chemical reaction Methods 0.000 claims description 25
- 239000007788 liquid Substances 0.000 claims description 21
- 238000009423 ventilation Methods 0.000 claims description 7
- 238000009434 installation Methods 0.000 claims 1
- 238000007599 discharging Methods 0.000 abstract 1
- 239000002994 raw material Substances 0.000 description 23
- 239000003205 fragrance Substances 0.000 description 13
- 238000009835 boiling Methods 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 238000005086 pumping Methods 0.000 description 6
- 241000196324 Embryophyta Species 0.000 description 4
- 241001465754 Metazoa Species 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000010517 secondary reaction Methods 0.000 description 2
- 241001090476 Castoreum Species 0.000 description 1
- 241000402754 Erythranthe moschata Species 0.000 description 1
- 241000282375 Herpestidae Species 0.000 description 1
- 241000209504 Poaceae Species 0.000 description 1
- 235000019568 aromas Nutrition 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000003756 stirring 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
- C11B9/00—Essential oils; Perfumes
- C11B9/02—Recovery or refining of essential oils from raw materials
- C11B9/025—Recovery by solvent extraction
-
- 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
- C11B9/00—Essential oils; Perfumes
- C11B9/02—Recovery or refining of essential oils from raw materials
- C11B9/027—Recovery of volatiles by distillation or stripping
Landscapes
- 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)
- Fats And Perfumes (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention relates to the technical field of natural spice extraction, in particular to a natural spice extraction device which comprises a distillation tower body, wherein the bottom of the distillation tower body is fixedly connected with a supporting leg, the bottom of the supporting leg is fixedly connected with a bottom plate, the top of the distillation tower body is fixedly connected with a feeding hole, the bottom of the distillation tower body is fixedly connected with a discharging hole, the side surface of the distillation tower body is fixedly connected with an air inlet, the top of the distillation tower body is fixedly connected with an air extraction hole, the middle of the top of the distillation tower body is rotatably connected with a rotating shaft and a driving device for driving the rotating shaft to rotate, the rotating shaft is fixedly connected with a rotating cone, the bottom of the rotating cone is provided with a wing plate, the inner wall of the distillation tower body is fixedly connected with a fixed cone, the middle of the distillation tower body is provided with a temperature control section, the air inlet and the air extraction hole are respectively provided with a flow control valve, and one side of the distillation tower body is provided with a pressure display.
Description
Technical Field
The invention relates to the technical field of natural spice extraction, in particular to a natural spice extraction device.
Background
The natural perfume is the perfume which is applied at the earliest in history, and the natural perfume refers to the directly applied animal and plant perfuming parts which are not processed originally; or a perfume which is extracted or refined by a physical method without changing its original ingredients. The natural perfume includes two main types of animal and plant natural perfumes. The most commonly used animal natural perfume is musk, civet, castoreum and ambergris. The plant natural perfume is a mixture of various chemical components extracted from flowers, fruits, leaves, barks, roots, stems, grasses, seeds and the like of plants.
The rotary cone column distillation method is a high-efficiency unique liquid-gas contact distillation technology, can meet the development requirement of extraction processing of modern natural spices, and is widely applied to the industries of foods and natural flavors and fragrances at present. The rotating cone technology is to disperse the liquid dropped on the disc surface into an extremely thin liquid surface by utilizing the centrifugal force of a rotating cone disc, and the liquid is evaporated under the action of a high-speed rotating cone disc and under the heating condition, so that the introduced gas can be fully contacted to complete the gas stripping process.
In the prior art, chinese patent No. CN209645874U discloses a rotating cone distillation tower, which includes a frame and a distillation tower body disposed on the frame, wherein the distillation tower body has a rotating shaft and a driving device for driving the rotating shaft to rotate, the distillation tower body is provided with two sets of inverted cones connected in series, each inverted cone includes a plurality of fixed cones connected to an inner wall of the distillation tower body and a plurality of rotating cones connected to the rotating shaft and axially spaced from the fixed cones, each rotating cone has a wing, each rotating cone has a connecting ring sleeved on an outer wall of the rotating shaft, and the connecting ring is fixed to the rotating shaft through a hough joint.
Chinese patent document No. CN209500829U discloses a rotary evaporator capable of controlling steam rate and contact time, which includes a frame and a distillation tower body arranged on the frame, wherein the distillation tower body is provided with a feed inlet at the upper part and a discharge outlet at the lower part, a blanking channel for material falling is formed between the feed inlet and the discharge outlet, the distillation tower body is provided with a steam inlet at the lower part and a steam outlet at the upper part, the steam inlet and the steam outlet form an airflow channel for steam to rise, the distillation tower body is provided with a centrifugal fan at the bottom, an air outlet of the centrifugal fan is provided with a steam boosting device, the steam boosting device includes a cylinder body connected with the outlet of the centrifugal fan, a cyclone cylinder is arranged in the cylinder body towards one side of the centrifugal fan, and a plurality of circumferentially arranged cyclone sheets are arranged on the inner wall of the cyclone cylinder; the outer wall of the cyclone cylinder is arranged in a clearance with the inner wall of the cylinder body, the steam inlet is positioned on the cylinder body, one side of the cyclone cylinder, which is back to the centrifugal fan, is provided with a conical cylinder, the conical cylinder is provided with an oblique air outlet, and steam is compressed in the clearance between the cyclone cylinder and the cylinder body and is discharged into an airflow channel from the air outlet and the intersection of airflow sprayed by the cyclone sheet.
In the prior art, a steam inlet is formed in the bottom of a distillation tower body, a steam outlet is formed in the upper portion of the distillation tower body, steam enters from the steam inlet and is discharged from the steam outlet, a gas stripping process is completed, and therefore aroma components in raw materials are extracted.
Disclosure of Invention
Technical problem to be solved
Aiming at the defects in the prior art, the invention aims to provide a natural spice extraction device, which solves the problems in the prior art, and solves the problem that the raw material liquid can reach a high boiling point to extract aromas with different boiling points without being heated to a high temperature in the stripping process.
(II) technical scheme
In order to achieve the purpose, the invention provides the following technical scheme: the utility model provides a natural spices extraction device, including the distillation tower body, distillation tower body bottom fixedly connected with landing leg, landing leg bottom fixedly connected with bottom plate, distillation tower body top fixedly connected with feed inlet, distillation tower body bottom fixedly connected with discharge gate, distillation tower body side fixedly connected with air inlet, distillation tower body top fixedly connected with extraction opening, swivelling joint has the rotation axis and drives its rotatory drive arrangement in the middle of the distillation tower body top, the rotatory centrum of rotation axis fixedly connected with, rotatory centrum bottom is equipped with the pterygoid lamina, the fixed centrum of distillation tower body inner wall fixedly connected with, be equipped with the accuse temperature section in the middle of the distillation tower body, air inlet and extraction opening all are equipped with flow control valve, distillation tower body one side is equipped with the pressure display.
Preferably, a reaction cavity is arranged in the middle of the temperature control section, a heating cavity is further arranged between the reaction cavity and the outer wall of the temperature control section, and a heating ring is arranged in the heating cavity.
Preferably, heat conducting oil is arranged in the heating cavity.
Preferably, the side surface of the reaction cavity is provided with an annular channel, the interior of the fixed cone body is hollow and is communicated with the annular channel, and a connecting block is fixedly connected between the top surface and the bottom surface of the annular channel.
Preferably, the top of the distillation tower body is fixedly connected with a temperature sensor, one side of the temperature sensor is also provided with a temperature controller, and the temperature sensor extends into the distillation tower body.
Preferably, the upper part of the distillation tower body is provided with an exhaust section, the exhaust section is communicated with the feed inlet and the extraction opening, and the pressure display is communicated with the exhaust section through a pipeline.
Preferably, the bottom of the distillation tower body is provided with a liquid storage section, and the liquid storage section is communicated with the discharge hole.
Preferably, a ventilation section is arranged between the temperature control section and the liquid storage section, and the ventilation section is communicated with the air inlet.
Preferably, the fixed cone body is an inverted frustum with an opening in the middle, the outer edge of the large circular surface at the top of the fixed cone body is fixedly connected with the inner wall of the reaction cavity, and the diameter of the opening in the middle of the fixed cone body is larger than that of the rotating shaft.
Preferably, the rotating cone body is an inverted cone frustum with an opening in the middle, the opening in the middle of the bottom of the rotating cone body is fixedly connected with the rotating shaft, and the diameter of the outer edge of the large circular surface at the top of the rotating cone body is smaller than that of the outer edge of the large circular surface at the top of the fixed cone body.
(III) advantageous effects
1. The invention provides a natural spice extraction device, which controls the pressure in a distillation tower body to be negative pressure through a flow control valve and a pressure display, heats heat-conducting oil through a heating ring, transfers heat to a reaction cavity, and controls the temperature in the reaction cavity through a temperature sensor and a temperature controller, thereby realizing the reduction of the boiling point of raw materials in a low vacuum environment, leading the raw materials to extract fragrances with different boiling points at lower temperature, leading the secondary reaction to be small, leading the polar volatile substances with larger proportion to be extracted, and leading the fragrance to be natural and vivid.
2. The invention provides a natural spice extraction device, which adopts heat conduction oil for heat transfer, so that the heating in a reaction cavity is uniform, and the temperature regulation control is more accurate.
3. The invention provides a natural spice extraction device, which is characterized in that an annular channel is arranged on the side surface of a reaction cavity, the interior of a fixed cone is hollow and is communicated with the annular channel, so that the hollow part of the fixed cone is filled with heat conduction oil, and a raw material liquid is heated when flowing through the surface of the fixed cone, so that the raw material liquid is uniformly heated.
Drawings
Fig. 1 is a schematic structural view of the whole of the present invention.
FIG. 2 is a schematic view of the structure of a distillation column of the present invention.
FIG. 3 is a schematic structural diagram of the temperature control section of the present invention.
Fig. 4 is a schematic structural view of a heating ring according to the present invention.
FIG. 5 is a schematic diagram of the structure of the annular channel of the present invention.
Fig. 6 is a schematic view of the structure inside the tower body according to the invention.
FIG. 7 is a schematic view of the position of a rotating vertebral body and a fixed vertebral body of the present invention.
Fig. 8 is a schematic view of a rotating vertebral body and a fixed vertebral body according to the present invention.
In the figure: 1-a distillation tower body, 2-supporting legs, 3-a bottom plate, 4-a feed inlet, 5-a discharge outlet, 6-an air inlet, 7-an air extraction port, 8-a rotating shaft, 9-a pressure display, 10-a temperature controller, 11-a temperature sensor, 12-a liquid storage section, 13-a ventilation section, 14-a temperature control section, 15-an exhaust section, 16-a heating cavity, 17-a reaction cavity, 18-a heating ring, 19-an annular channel, 20-a connecting block, 21-a fixed cone, 22-a rotating cone and 23-a wing plate.
Detailed Description
The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to fig. 1 to 8 in the embodiments of the present invention, and it is obvious that the described embodiments are only a part of the embodiments of the present invention, and not all embodiments. All other embodiments, which can be obtained by a person skilled in the art without making any creative effort based on the embodiments in the present invention, belong to the protection scope of the present invention.
The invention provides a technical scheme that: a natural perfume extraction device comprises a distillation tower body 1, the distillation tower body 1 is in a cylindrical shape and is hollow inside, the bottom of the distillation tower body 1 is fixedly connected with supporting legs 2, the supporting legs 2 are 3 or more than 3 sloping plates which are uniformly distributed on the side surface of the distillation tower body 1 close to the bottom and are used for supporting the distillation tower body 1, the bottom of the supporting legs 2 is fixedly connected with a bottom plate 3, the bottom plate 3 is flush with the bottom surface, 4 mounting holes are formed in four corners of the bottom plate 3, the mounting holes are fixedly mounted on the bottom surface through bolts, the top of the distillation tower body 1 is fixedly connected with a feed inlet 4, raw material solution for extraction is uniformly injected into the distillation tower body 1, the bottom of the distillation tower body 1 is fixedly connected with a discharge port 5, the solution falling at the bottom of the distillation tower body 1 after air stripping is finished is discharged, the side surface of the distillation tower body 1 is fixedly connected with an air inlet 6, air enters the distillation tower body 1 from the air inlet 6, and volatilized perfume is taken away by upward flow, the top of the distillation tower body 1 is fixedly connected with an air extraction opening 7, the air with fragrance flowing to the upper space of the distillation tower body 1 is extracted to the next enrichment work, the middle of the top of the distillation tower body 1 is rotatably connected with a rotating shaft 8 and a driving device for driving the rotating shaft 8 to rotate, the rotating shaft 8 is fixedly connected with a rotating cone 22, the bottom of the rotating cone 22 is provided with a wing plate 23, the inner wall of the distillation tower body 1 is fixedly connected with a fixed cone 21, a gap formed between the wing plate 23 and the conical surface of the fixed cone 21 is larger than a fluid surface formed by the raw material solution on the conical surface of the fixed cone 21, the driving device drives the rotating shaft 8 to rotate to drive the rotating cone 22 to rotate, the raw material solution falling from the feed inlet 4 falls on the fixed cone 21, the raw material solution flows obliquely downwards along the conical surface, falls into the rotating cone 22 through a circular opening in the middle of the bottom, and the centrifugal force generated by the rotation of the rotating cone 22 is utilized, the raw material solution falling on the rotary cone 22 is dispersed into an extremely thin liquid surface on the conical surface of the rotary cone 22, the temperature control section 14 is arranged in the middle of the distillation tower body 1, the temperature in the distillation tower body 1 is controlled within a certain range, the air inlet 6 and the air extraction opening 7 are both provided with flow control valves, one side of the distillation tower body 1 is provided with a pressure display 9, the pressure display 9 displays the pressure in the distillation tower body 1, the flow control valve of the air inlet 6 is adjusted to reduce the gas entering the distillation tower body 1, the flow control valve of the air extraction opening 7 is adjusted to increase the gas extracted from the distillation tower body 1, so that negative pressure is formed in the distillation tower body 1 to generate a low-vacuum extraction environment, at the moment, the boiling points of various fragrances in the raw material solution are all reduced, the fragrances volatilize into the gas at the control temperature of the temperature control section 14, and then the fragrances are brought into the next enrichment work from the air extraction opening 7.
The middle of the temperature control section 14 is provided with a reaction cavity 17, the reaction cavity 17 is internally provided with an air stripping process for completing gas-liquid contact, a heating cavity 16 is further arranged between the reaction cavity 17 and the outer wall of the temperature control section 14, a heating ring 18 is arranged in the heating cavity 16 and is also provided with heat conducting oil, the heating ring 18 is immersed in the heat conducting oil, the heating ring 18 is connected with an external power supply for power-on heating, through heat conduction, the heat conducting oil is heated by the heating ring 18, the whole heating cavity 16 is heated by the heat conducting oil, the heating cavity 16 heats the reaction cavity 17, the reaction cavity 17 is more uniformly heated, the temperature in the reaction cavity 17 is accurately controlled, the side surface of the reaction cavity 17 is provided with an annular channel 19, the fixed cone 21 is hollow and communicated with the annular channel 19, the hollow part is also filled with the heat conducting oil, the heat conducting oil heats the conical surface of the fixed cone 21, the raw material solution is more uniformly heated, and a connecting block 20 is fixedly connected between the top surface and the bottom surface of the annular channel 19. The connecting block 20 connects the top and bottom surfaces of the annular channel 19 to increase the structural strength of the reaction chamber 17.
The distillation tower body 1 top fixedly connected with temperature sensor 11, temperature sensor 11 one side still is equipped with temperature controller 10, there are temperature display panel and control button on the temperature controller 10 panel, temperature sensor 11 extends into the distillation tower body 1, temperature sensor 11 detects the temperature in the distillation tower body 1, give temperature controller 10 with signal transfer again, the external power source's that temperature controller 10 control heating ring 18 switched on cuts off to the realization is by the accurate temperature in the distillation tower body 1 of control of temperature controller 10.
The upper part of the distillation tower body 1 is provided with an exhaust section 15, the exhaust section 15 is communicated with the feed inlet 4 and the extraction opening 7, the exhaust section 15 enables the upper part of the distillation tower body 1 to have a certain space, the pressure display 9 is communicated with the exhaust section 15 through a pipeline, the pressure display 9 displays the air pressure in the distillation tower body 1, the bottom of the distillation tower body 1 is provided with a liquid storage section 12, the liquid storage section 12 is communicated with the discharge opening 5, a ventilation section 13 is arranged between the temperature control section 14 and the liquid storage section 12, the ventilation section 13 is communicated with the air inlet 6, air enters from the air inlet 6 and flows upwards from the bottom of the reaction cavity 17 to take away fragrance.
The rotating cone 22 is an inverted frustum with an opening in the middle, the opening in the middle of the bottom of the rotating cone is fixedly connected with the rotating shaft 8, the diameter of the outer edge of the large circular surface at the top of the rotating cone 22 is smaller than that of the large circular surface at the top of the fixed cone 21, under the action of centrifugal force generated by rotation of the rotating cone 22, raw material solution falling on the rotating cone 22 is dispersed into an extremely thin liquid surface on the conical surface of the rotating cone 22, thrown out at the outer edge of the large circular surface at the top of the rotating cone 22 and falls onto the next fixed cone 21.
The working principle is as follows: firstly, pumping air from an air pumping hole 7, then pumping air from an air inlet 6 into a distillation tower body 1, adjusting respective flow control valves of the air inlet 6 and the air pumping hole 7 to ensure that the air pumped out from the air pumping hole 7 is larger than the air fed into the air inlet 6, forming negative pressure in the distillation tower body 1 at the moment, observing an air pressure value displayed on a pressure display 9, adjusting the flow control valves according to the observed air pressure value to ensure that the negative pressure generated in the distillation tower body 1 is stable to form a stable low-vacuum extraction environment, setting target temperature and upper and lower limit temperatures for a temperature controller 10, transmitting a temperature signal in the distillation tower body 1 detected by a temperature sensor 11 to the temperature controller 10 in real time, displaying the current temperature on a display board by the temperature controller 10 according to information transmitted by the temperature sensor 11, and controlling a heating ring 18 to be connected with an external power supply to electrify at the moment, wherein the current temperature is lower than the target temperature, the heating ring 18 heats the heat conducting oil through heat conduction, the heat conducting oil is heated by the heating ring 18, the whole heating cavity 16 is heated by the heat conducting oil, the reaction cavity 17 is heated by the heating cavity 16, the temperature in the distillation tower body 1 rises along with the heating of the reaction cavity 17, when the temperature in the distillation tower body 1 rises to a target temperature, the driving device drives the rotating shaft 8 to rotate to drive the rotating cone 22 to rotate, the feed inlet 4 is opened, the raw material solution enters the distillation tower body 1 and falls on the fixed cone 21, the raw material solution flows downwards along the conical surface and falls into the rotating cone 22 through the circular opening in the middle of the bottom, the centrifugal force generated by the rotation of the rotating cone 22 is utilized to disperse the raw material solution falling on the rotating cone 22 into an extremely thin liquid surface on the conical surface of the rotating cone 22, the extremely thin liquid surface is thrown out at the outer edge of the large circular surface at the top of the rotating cone 22 and falls onto the next fixed cone 21, the raw material solution repeatedly flows downwards, a gap formed between the wing plate 23 and the conical surface of the fixed cone 21 is larger than a fluid surface formed by the raw material solution on the conical surface of the fixed cone 21, the wing plate 23 rotates along with the rotating cone 22 to stir surface gas of the fluid surface formed by the conical surface of the fixed cone 21, volatilization of fragrance is accelerated, meanwhile, the gas takes away fragrance volatilized from the raw material solution after reaching a boiling point in the flowing from bottom to top, the gas with fragrance components is pumped out through the air pumping port 7 and then enters the next enrichment work, the device realizes that the raw material extracts fragrance with different boiling points at a lower temperature, secondary reaction is small in the extraction process, a large proportion of polar volatile substances can be extracted, and the produced fragrance is natural and vivid.
In the process, the temperature in the distillation tower body 1 is reduced along with the extraction of the gas carrying heat and aroma, when the current temperature displayed on the display panel of the temperature controller 10 is lower than the set lower limit temperature, the temperature controller 10 controls the heating ring 18 to be connected with an external power supply to be electrified to enter a heating state, when the current temperature reaches the set target temperature, the temperature controller 10 controls the heating ring 18 to be disconnected with the external power supply to stop heating, and the operation is circulated to enter a heat preservation state, so that the temperature in the distillation tower body 1 is always kept between the lower limit temperature and the target temperature.
Claims (10)
1. The utility model provides a natural perfume extraction device, includes distillation tower body (1), distillation tower body (1) bottom fixedly connected with landing leg (2), landing leg (2) bottom fixedly connected with bottom plate (3), distillation tower body (1) top fixedly connected with feed inlet (4), distillation tower body (1) bottom fixedly connected with discharge gate (5), distillation tower body (1) side fixedly connected with air inlet (6), distillation tower body (1) top fixedly connected with extraction opening (7), swivelling joint has rotation axis (8) and drives its rotatory drive arrangement in the middle of distillation tower body (1) top, rotation axis (8) fixedly connected with rotatory centrum (22), rotatory centrum (22) bottom is equipped with pterygoid lamina (23), distillation tower body (1) inner wall fixedly connected with fixed centrum (21), its characterized in that: the distillation tower is characterized in that a temperature control section (14) is arranged in the middle of the distillation tower body (1), flow control valves are arranged on the air inlet (6) and the air suction port (7), and a pressure display (9) is arranged on one side of the distillation tower body (1).
2. The natural spice extraction apparatus of claim 1, wherein: be equipped with reaction chamber (17) in the middle of accuse temperature section (14), reaction chamber (17) with still be equipped with heating chamber (16) between accuse temperature section (14) outer wall, be equipped with heating ring (18) in heating chamber (16).
3. The natural spice extraction apparatus of claim 2, wherein: heat conduction oil is arranged in the heating cavity (16).
4. The natural spice installation of claim 3, wherein: the side surface of the reaction cavity (17) is provided with an annular channel (19), the fixed cone body (21) is hollow and communicated with the annular channel (19), and a connecting block (20) is fixedly connected between the top surface and the bottom surface of the annular channel (19).
5. The natural spice extraction apparatus of claim 4, wherein: distillation tower body (1) top fixedly connected with temperature sensor (11), temperature sensor (11) one side still is equipped with temperature controller (10), temperature sensor (11) extend into in distillation tower body (1).
6. The natural spice extraction apparatus of claim 1, wherein: the distillation tower body (1) upper portion is equipped with exhaust section (15), exhaust section (15) and feed inlet (4), extraction opening (7) intercommunication, pressure display (9) are through pipeline intercommunication exhaust section (15).
7. The natural spice extraction apparatus of claim 6, wherein: the bottom of the distillation tower body (1) is provided with a liquid storage section (12), and the liquid storage section (12) is communicated with the discharge hole (5).
8. The natural spice extraction apparatus of claim 7, wherein: a ventilation section (13) is arranged between the temperature control section (14) and the liquid storage section (12), and the ventilation section (13) is communicated with the air inlet (6).
9. The natural spice extraction apparatus of claim 8, wherein: the fixed cone body (21) is an inverted frustum with an opening in the middle, the outer edge of the large circular surface at the top of the fixed cone body is fixedly connected with the inner wall of the reaction cavity (17), and the diameter of the opening in the middle of the fixed cone body (21) is larger than that of the rotating shaft (8).
10. The natural spice extraction apparatus of claim 8, wherein: the rotary cone body (22) is an inverted frustum with an opening in the middle, the middle opening at the bottom of the rotary cone body is fixedly connected with the rotating shaft (8), and the diameter of the outer edge of the large circular surface at the top of the rotary cone body (22) is smaller than that of the outer edge of the large circular surface at the top of the fixed cone body (21).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202211063502.XA CN115449431A (en) | 2022-09-01 | 2022-09-01 | Natural perfume extraction device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202211063502.XA CN115449431A (en) | 2022-09-01 | 2022-09-01 | Natural perfume extraction device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN115449431A true CN115449431A (en) | 2022-12-09 |
Family
ID=84300144
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202211063502.XA Pending CN115449431A (en) | 2022-09-01 | 2022-09-01 | Natural perfume extraction device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN115449431A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1339328A (en) * | 2000-08-22 | 2002-03-13 | 住友重机械工业株式会社 | Distilling apparatus and distilling method |
| CN208553176U (en) * | 2018-04-25 | 2019-03-01 | 济宁凯特化工有限公司 | A kind of chemical industry distilling apparatus |
| CN209645874U (en) * | 2019-01-15 | 2019-11-19 | 杭州浙大百川生物食品技术有限公司 | Rotating cone destilling tower |
| AU2020104292A4 (en) * | 2020-12-23 | 2021-03-11 | Tianjin University | A new type of internally heat integrated distillation column system device and its use method |
-
2022
- 2022-09-01 CN CN202211063502.XA patent/CN115449431A/en active Pending
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1339328A (en) * | 2000-08-22 | 2002-03-13 | 住友重机械工业株式会社 | Distilling apparatus and distilling method |
| CN208553176U (en) * | 2018-04-25 | 2019-03-01 | 济宁凯特化工有限公司 | A kind of chemical industry distilling apparatus |
| CN209645874U (en) * | 2019-01-15 | 2019-11-19 | 杭州浙大百川生物食品技术有限公司 | Rotating cone destilling tower |
| AU2020104292A4 (en) * | 2020-12-23 | 2021-03-11 | Tianjin University | A new type of internally heat integrated distillation column system device and its use method |
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Application publication date: 20221209 |
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| RJ01 | Rejection of invention patent application after publication |