CN220176064U - Continuous distillation device with multilayer independent structure - Google Patents
Continuous distillation device with multilayer independent structure Download PDFInfo
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- CN220176064U CN220176064U CN202321694504.9U CN202321694504U CN220176064U CN 220176064 U CN220176064 U CN 220176064U CN 202321694504 U CN202321694504 U CN 202321694504U CN 220176064 U CN220176064 U CN 220176064U
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- Prior art keywords
- distillation
- tank body
- distillation box
- pipe
- box
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- 238000001944 continuous distillation Methods 0.000 title claims abstract description 17
- 238000004821 distillation Methods 0.000 claims abstract description 84
- 239000002994 raw material Substances 0.000 claims abstract description 20
- 238000005485 electric heating Methods 0.000 claims abstract description 6
- 238000003756 stirring Methods 0.000 claims description 23
- 239000007788 liquid Substances 0.000 claims description 4
- OSWPMRLSEDHDFF-UHFFFAOYSA-N methyl salicylate Chemical compound COC(=O)C1=CC=CC=C1O OSWPMRLSEDHDFF-UHFFFAOYSA-N 0.000 abstract description 21
- 239000009637 wintergreen oil Substances 0.000 abstract description 16
- 238000004519 manufacturing process Methods 0.000 abstract description 5
- 238000000746 purification Methods 0.000 abstract description 5
- 239000002699 waste material Substances 0.000 abstract description 4
- 239000000463 material Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 241000196324 Embryophyta Species 0.000 description 2
- 239000000284 extract Substances 0.000 description 2
- 229960001047 methyl salicylate Drugs 0.000 description 2
- 235000007297 Gaultheria procumbens Nutrition 0.000 description 1
- 241000736246 Pyrola Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000017531 blood circulation Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 229940040145 liniment Drugs 0.000 description 1
- 239000000865 liniment Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000001256 steam distillation Methods 0.000 description 1
Landscapes
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to the technical field of distillation equipment, in particular to a continuous distillation device with a multilayer independent structure, which comprises a tank body, wherein two first distillation boxes are fixedly arranged near the upper part of the tank body, a second distillation box is arranged below the first distillation boxes, two electric heating blocks are symmetrically arranged at the bottoms of the first distillation boxes and the second distillation boxes, and the outer annular walls of the first distillation boxes and the second distillation boxes are tightly attached to the inner wall of the tank body; according to the utility model, through the plurality of distillation boxes, the wintergreen oil can be distilled continuously step by step, the purity of distillation and purification can be improved, the use in the wintergreen oil production process is facilitated, and meanwhile, the wintergreen oil in the raw materials can be fully extracted, so that the waste of the raw materials is reduced.
Description
Technical Field
The utility model relates to the technical field of distillation equipment, in particular to a continuous distillation device with a multilayer independent structure.
Background
The wintergreen oil, also called methyl salicylate and methyl salicylate, can be obtained by steam distillation of wintergreen leaves produced in Canada, yunnan and other places in China, and is an external liniment which can be applied on local parts to promote the blood circulation of the parts. The wintergreen oil is purified by a distillation device during production.
Only one distillation bin is arranged in the distillation device in the prior art, so that the same batch of raw materials can be distilled during distillation, the subsequent raw materials need to be added into the distillation tank after the raw materials in the distillation tank are purified, the distillation efficiency can be affected, and meanwhile, the same batch of raw materials are purified only through one-time distillation, so that the time for underutilization or purification of the raw materials is long. In view of this, we propose a continuous distillation apparatus of a multilayer independent structure.
Disclosure of Invention
In order to remedy the above-mentioned shortcomings, the present utility model provides a continuous distillation apparatus of a multi-layer independent structure.
The technical scheme of the utility model is as follows:
the utility model provides a continuous distillation plant of multilayer independent structure, includes the jar body, the internal portion installation of jar is close to upper portion fixed mounting has two first distillation boxes to install the second distillation box in first distillation box below, first distillation box with two electric heating blocks are all symmetrically installed to second distillation box bottom, first distillation box with the outer rampart of second distillation box is all closely laminated with jar internal wall, every an inside unloading pipe is all installed to first distillation box bottom, every all install a first solenoid valve on the inside unloading pipe, the outside unloading pipe that stretches out from jar body bottom is installed to second distillation box bottom, installs the second solenoid valve on the outside unloading pipe.
As the preferable technical scheme, a feeding pipe for adding raw materials is arranged at the top of the tank body, the circumferential outer walls of the tank body are respectively positioned above the two first distillation boxes and the one second distillation box, and an air outlet is formed in the upper part of each first distillation box and the upper part of each second distillation box.
As the preferable technical scheme, the tank body outer wall is equipped with a standpipe, and the intercommunication has the interior extension pipe with three gas outlet intercommunication respectively on the standpipe, interior extension pipe and tank body fixed connection, standpipe top integrated into one piece has the exit tube.
As the preferable technical scheme, at least three supporting legs which are arranged at equal intervals are arranged at the bottom of the tank body and are used for supporting the tank body.
As the preferable technical scheme, the bottom of the first distillation box is conical, so that the speed of liquid in the distillation box flowing to the inner blanking pipe can be increased.
As a preferable technical scheme, a stirring mechanism is arranged in the tank body near the top, and the stirring mechanism is positioned above the first distillation box above the tank body.
As the preferable technical scheme, the stirring mechanism comprises a blade shaft positioned in the first distillation box above and a plurality of blades fixed on the outer wall of the blade shaft, wherein the blade shaft is coaxially fixed with a stirring shaft which is rotatably mounted on the inner wall of the top of the tank body, and the top of the tank body is provided with a stirring motor for driving the stirring shaft to rotate.
Compared with the prior art, the utility model has the beneficial effects that:
according to the utility model, through the plurality of distillation boxes, the wintergreen oil can be distilled continuously step by step, the purity of distillation and purification can be improved, the wintergreen oil can be conveniently used in the production process of the wintergreen oil, meanwhile, the wintergreen oil in the raw materials can be fully extracted, so that the waste of the raw materials is reduced, and simultaneously, three distillation boxes can be used for simultaneously distilling three batches of raw materials.
Drawings
FIG. 1 is a schematic diagram of the overall structure of the present utility model;
FIG. 2 is a schematic diagram of the internal structure of FIG. 1 according to the present utility model;
fig. 3 is a schematic diagram illustrating an internal structure of fig. 1 according to the present utility model.
The meaning of each reference numeral in the figures is:
1. a tank body; 10. an air outlet; 11. a first distillation box; 12. an electric heating block; 13. an internal blanking pipe; 14. a first electromagnetic valve; 15. a second distillation box; 16. an external blanking pipe; 17. a second electromagnetic valve; 2. a support leg; 3. feeding a pipe; 4. a standpipe; 40. an inner extension pipe; 41. a pipe outlet; 5. a stirring motor; 50. a stirring shaft; 51. a blade shaft; 52. and (3) a blade.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
Referring to fig. 1-3, the present utility model provides a technical solution:
the utility model provides a continuous distillation plant of multilayer independent structure, including a jar body 1, jar body 1 internally mounted is close to upper portion fixed mounting has two first distillation box 11, and install second distillation box 15 in first distillation box 11 below, two electric heating blocks 12 are all installed to first distillation box 11 and second distillation box 15 bottom symmetry, the outer rampart of first distillation box 11 and second distillation box 15 is all closely laminated with jar body 1 inner wall, an inside unloading pipe 13 is all installed to every first distillation box 11 bottom, all install a first solenoid valve 14 on every inside unloading pipe 13, the outside unloading pipe 16 that stretches out from jar body 1 bottom is installed to second distillation box 15 bottom, install second solenoid valve 17 on the outside unloading pipe 16. Through a plurality of distillation boxes that set up, can carry out continuous distillation step by step to the wintergreen oil, can improve the purity of distillation purification, be convenient for in the use of wintergreen oil production in-process, also can fully extract the wintergreen oil in the raw and other materials simultaneously to reduce the waste of raw and other materials.
As a preference of this embodiment, the top of the tank 1 is provided with a feeding pipe 3 for feeding raw materials, the feeding pipe 3 is used for feeding raw materials into the tank 1, the circumferential outer wall of the tank 1 is respectively located above two first distillation boxes 11 and one second distillation box 15, and an air outlet 10 is formed, so that the gas distilled from each distillation box can be conveniently sent out through the arranged air outlet 10.
As the preference of this embodiment, the outer wall of the tank body 1 is provided with a standpipe 4, the standpipe 4 is communicated with an inner extension pipe 40 respectively communicated with the three air outlets 10, the inner extension pipe 40 is fixedly connected with the tank body 1, and the top of the standpipe 4 is integrally formed with an outlet pipe 41. The standpipe 4 and the inward pipe 40 are provided for collecting the gas escaping from the gas outlet 10.
Preferably, in this embodiment, at least three supporting legs 2 are installed at the bottom of the tank 1 at equal intervals, so as to support the tank 1.
Preferably, the bottom of the first distillation box 11 is tapered to increase the speed of the liquid flowing into the internal discharging pipe 13 in the first distillation box 11.
Preferably, in this embodiment, a stirring mechanism is mounted inside the tank 1 near the top, and the stirring mechanism is located above the first distillation box 11 located above. Through the rabbling mechanism that sets up can stir raw and other materials, can accelerate the speed that is located the first distillation box 11 of top effectively and heats raw and other materials, and then can improve the efficiency to the distillation of wintergreen oil effectively.
As a preferable mode of this embodiment, the stirring mechanism comprises a blade shaft 51 positioned in the first distillation box 11 positioned above and a plurality of blades 52 fixed on the outer wall of the blade shaft 51, a stirring shaft 50 rotatably mounted on the inner wall of the top of the tank 1 is coaxially fixed on the blade shaft 51, and a stirring motor 5 for driving the stirring shaft 50 to rotate is mounted on the top of the tank 1. When the stirring mechanism is used, the stirring motor 5 drives the stirring shaft 50 to rotate, and then the blade shaft 51 drives the blade 52 to rotate, so that raw materials in the first distillation box 11 can be stirred.
The continuous distillation device with the multilayer independent structure can continuously distill the wintergreen oil step by step through the plurality of distillation boxes, can improve the purity of distillation purification, is convenient for use in the production process of the wintergreen oil, and can fully extract the wintergreen oil in the raw materials so as to reduce the waste of the raw materials;
when the oil tank is used, raw materials of the oil are firstly added into the tank body 1 from the inlet pipe 3, then the electric heating block 12 is electrified to heat the distillation boxes, the raw materials of the oil are successively dropped into the three distillation boxes, the raw materials of the oil are respectively distilled for three times, the two adjacent distillation boxes are communicated through the control of the first electromagnetic valve 14, gas generated in the distillation process is discharged from the gas outlet 10 into the vertical pipe 4 and finally is sent out from the outlet pipe 41, liquid left after distillation is discharged from the external blanking pipe 16, and the external blanking pipe 16 is controlled by the second electromagnetic valve 17.
The foregoing has shown and described the basic principles, principal features and advantages of the utility model. It will be understood by those skilled in the art that the present utility model is not limited to the above-described embodiments, and that the above-described embodiments and descriptions are only preferred embodiments of the present utility model, and are not intended to limit the utility model, and that various changes and modifications may be made therein without departing from the spirit and scope of the utility model as claimed. The scope of the utility model is defined by the appended claims and equivalents thereof.
Claims (7)
1. Continuous distillation plant of multilayer independent structure, including jar body (1), its characterized in that: tank body (1) internally mounted is close to upper portion fixed mounting and has two first distillation box (11) to install second distillation box (15) in first distillation box (11) below, first distillation box (11) with two electric heating blocks (12) are all installed to second distillation box (15) bottom symmetry, first distillation box (11) with the outer annular wall of second distillation box (15) all closely laminates with tank body (1) inner wall, every first distillation box (11) bottom is all installed one inside unloading pipe (13), every all install one first solenoid valve (14) on inside unloading pipe (13), outside unloading pipe (16) that stretch out from tank body (1) bottom are installed to second distillation box (15) bottom, install second solenoid valve (17) on outside unloading pipe (16).
2. The continuous distillation apparatus of multiple independent structures according to claim 1, wherein: the top of the tank body (1) is provided with a feeding pipe (3) for feeding raw materials, and the circumferential outer wall of the tank body (1) is respectively positioned above the two first distillation boxes (11) and the one second distillation box (15) and is provided with an air outlet (10).
3. A continuous distillation apparatus of the multilayer independent structure according to claim 2, wherein: the utility model discloses a jar, including jar body (1), stand pipe (4) are equipped with to jar body (1) outer wall, and the intercommunication has interior extension pipe (40) with three gas outlet (10) intercommunication respectively on stand pipe (4), interior extension pipe (40) and jar body (1) fixed connection, stand pipe (4) top integrated into one piece has exit tube (41).
4. A continuous distillation apparatus having a multi-layered self-contained structure as claimed in claim 3, wherein: at least three supporting legs (2) which are arranged at equal intervals are arranged at the bottom of the tank body (1) and are used for supporting the tank body (1).
5. The continuous distillation apparatus of multiple independent structures according to claim 4, wherein: the bottom of the first distillation box (11) is conical, so that the speed of liquid in the first distillation box (11) flowing to the inner blanking pipe (13) can be increased.
6. The continuous distillation apparatus of multiple independent structures according to claim 5, wherein: and a stirring mechanism is arranged in the tank body (1) near the top, and is positioned above the first distillation box (11) above the tank body.
7. The continuous distillation apparatus of multiple independent structures according to claim 6, wherein: the stirring mechanism comprises a blade shaft (51) positioned in the first distillation box (11) above and a plurality of blades (52) fixed on the outer wall of the blade shaft (51), a stirring shaft (50) rotatably mounted on the inner wall of the top of the tank body (1) is coaxially fixed on the blade shaft (51), and a stirring motor (5) for driving the stirring shaft (50) to rotate is mounted on the top of the tank body (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321694504.9U CN220176064U (en) | 2023-06-30 | 2023-06-30 | Continuous distillation device with multilayer independent structure |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321694504.9U CN220176064U (en) | 2023-06-30 | 2023-06-30 | Continuous distillation device with multilayer independent structure |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220176064U true CN220176064U (en) | 2023-12-15 |
Family
ID=89115725
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321694504.9U Active CN220176064U (en) | 2023-06-30 | 2023-06-30 | Continuous distillation device with multilayer independent structure |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220176064U (en) |
-
2023
- 2023-06-30 CN CN202321694504.9U patent/CN220176064U/en active Active
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