CN220677861U - Boiling type mixer - Google Patents
Boiling type mixer Download PDFInfo
- Publication number
- CN220677861U CN220677861U CN202322076337.8U CN202322076337U CN220677861U CN 220677861 U CN220677861 U CN 220677861U CN 202322076337 U CN202322076337 U CN 202322076337U CN 220677861 U CN220677861 U CN 220677861U
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- China
- Prior art keywords
- pressure equalizing
- mixing
- pressure
- mixing chamber
- pipeline
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- 238000009835 boiling Methods 0.000 title claims abstract description 20
- 239000002994 raw material Substances 0.000 claims abstract description 22
- 238000009826 distribution Methods 0.000 claims abstract description 15
- 210000001503 joint Anatomy 0.000 claims abstract description 4
- 238000002347 injection Methods 0.000 claims description 17
- 239000007924 injection Substances 0.000 claims description 17
- 239000003814 drug Substances 0.000 claims description 13
- 239000000463 material Substances 0.000 abstract description 14
- 239000002912 waste gas Substances 0.000 abstract description 4
- 230000009471 action Effects 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 239000002699 waste material Substances 0.000 abstract description 3
- 238000003756 stirring Methods 0.000 description 6
- 239000007788 liquid Substances 0.000 description 4
- 239000012254 powdered material Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000007246 mechanism Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000010923 batch production Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Abstract
The utility model discloses a boiling mixer, which comprises a screw feeder, wherein a raw material inlet funnel is arranged at the inlet of the screw feeder, a blanking pipeline is arranged below the outlet of the screw feeder, the outlet of the blanking pipeline is in butt joint with a mixing chamber, a pressure equalizing air chamber is arranged at the lower side of the mixing chamber, and the center of the lower end of the pressure equalizing air chamber is connected with a product outlet pipeline; four material returning pipelines are arranged on the outer side of the mixing chamber, and a separator is arranged at the top of each material returning pipeline; the separators are connected in pairs through pipelines and then are converged at the center of the mixer, and an air outlet pipeline is arranged at the upper end of the converged position; the raw materials are rolled in the mixing chamber and move up and down through the action of the pressure equalizing air chamber and the air distribution system, so that the mixing rate is improved, a small amount of finer raw materials are separated through the separator and enter the mixing chamber again for mixing, the yield is improved, and the waste caused by incomplete mixing is reduced; meanwhile, the mixing rate is improved, so that the generation of waste gas in the reaction is reduced, and the green and environment-friendly production is realized.
Description
Technical Field
The utility model relates to the technical field of mechanical equipment, in particular to a boiling mixer.
Background
Mixing of powdered materials is a problem that many industries need to face. For a powder material mixing device, the principle commonly used at present is mainly to mix materials by two modes of rotation and stirring. For the device for mixing materials in a rotary mode, the device is mainly aimed at objects of small-batch production, and the material to be mixed is required to have high fluidity and not easy to agglomerate. For the device for mixing materials in a stirring manner, the materials to be mixed are mainly stirred through some stirring mechanisms, so that the materials can be mixed, but when a large amount of materials are faced, the condition of uneven stirring exists, and the cleaning of the stirring mechanisms is difficult. Because of the high mixing requirements of the powdered materials, which are agglomerated, it is often difficult to mix the different powdered materials sufficiently. The contact area between the mixing equipment and the powdery material is large in a rotation mode or a stirring mode, so that large friction is generated, heat is generated by friction, and the inflammable powdery material is extremely easy to reach an ignition point, so that danger is caused. This requires a more efficient and safe device to meet the mixing requirements of the powdered material.
Disclosure of Invention
The present utility model aims to solve the above problems and to provide a boiling mixer.
The boiling mixer comprises a screw feeder, wherein a raw material inlet funnel is arranged at the inlet of the screw feeder, a blanking pipeline is arranged below the outlet of the screw feeder, the outlet of the blanking pipeline is in butt joint with a mixing chamber, a pressure equalizing air chamber is arranged at the lower side of the mixing chamber, and the center of the lower end of the pressure equalizing air chamber is connected with a product outlet pipeline; four material returning pipelines are arranged on the outer side of the mixing chamber, and a separator is arranged at the top of each material returning pipeline; the separators are connected in pairs through pipelines and then are converged at the center of the mixer, and an air outlet pipeline is arranged at the upper end of the converged position.
Further, according to the boiling mixer, the raw material inlet funnel and the screw feeder are erected above the inlet of the blanking pipeline by using the rectangular structure, and the screw feeder is erected to effectively improve feeding efficiency.
Further, the upper end of the pressure equalizing air chamber is further provided with eight high-pressure medicament injection devices, wherein every four high-pressure medicament injection devices are in the same plane, two groups are added, the injection ends of the high-pressure medicament injection devices are located right above the mixing chamber, and the high-pressure medicament injection devices can atomize liquid so as to fully mix the liquid with raw materials.
Further, the boiling mixer further comprises a high-pressure air blower connected to the bottom of the pressure equalizing air chamber, wherein an air inlet pipeline of the high-pressure air blower enters the pressure equalizing air chamber in the horizontal direction, and the air inlet is not directly aligned to the pressure equalizing air chamber, so that the air pressure can be reduced, and the pressure equalizing effect is better.
Further, the boiling mixer further comprises a wind distribution system arranged at the upper end of the pressure equalizing air chamber, and the wind distribution system is positioned between the mixing chamber and the pressure equalizing air chamber.
Further, the boiling mixer further comprises an air distribution system, wherein the air distribution system is formed by uniformly and vertically arranging a plurality of pressure equalizing hoods on the same plane.
The utility model has the beneficial effects that: according to the utility model, the raw materials are rolled and move up and down in the mixing chamber under the action of the pressure equalizing air chamber and the air distribution system, so that the mixing rate is improved, a small amount of finer raw materials are separated by the separator and enter the mixing chamber again for mixing, the yield is improved, and the waste caused by incomplete mixing is reduced; meanwhile, the mixing rate is improved, so that the generation of waste gas in the reaction is reduced, and the green and environment-friendly production is realized.
Drawings
FIG. 1 is a front view of a boiling mixer;
FIG. 2 is a top view of a boiling mixer;
fig. 3 is a schematic diagram of a boiling mixer high pressure medicament injection apparatus.
In the figure: 1-raw material inlet funnel, 2-screw feeder, 3-blanking pipeline, 4-mixing chamber, 5-air distribution system, 6-pressure equalizing air chamber, 7-product outlet pipeline, 8-high pressure blower, 9-pressure equalizing hood, 10-high pressure medicament injection device, 11-return pipeline, 12-separator and 13-air outlet pipeline.
Detailed Description
Further advantages and effects of the present utility model will become apparent to those skilled in the art from the disclosure of the present specification, by describing the embodiments of the present utility model with specific examples. While the description of the utility model will be described in connection with the preferred embodiments, it is not intended to limit the inventive features to the implementation. Rather, the purpose of the utility model described in connection with the embodiments is to cover other alternatives or modifications, which may be extended by the claims based on the utility model. The following description contains many specific details for the purpose of providing a thorough understanding of the present utility model. The utility model may be practiced without these specific details. Furthermore, some specific details are omitted from the description in order to avoid obscuring the utility model. It should be noted that, in the case of no conflict, the embodiments and features in the embodiments may be combined with each other. It should be noted that in this specification, like reference numerals and letters denote like items in the following figures, and thus once an item is defined in one figure, no further definition or explanation thereof is necessary in the following figures.
Unless defined otherwise, technical or scientific terms used herein should be given the ordinary meaning as understood by one of ordinary skill in the art to which this utility model belongs. The terms "first," "second," and the like, as used herein, do not denote any order, quantity, or importance, but rather are used to distinguish one element from another. Likewise, the terms "a" or "an" and the like do not denote a limitation of quantity, but rather denote the presence of at least one. The terms "disposed," "connected," and the like are to be construed broadly and may be, for example, fixedly connected, detachably connected, or integrally connected; can be mechanically or electrically connected; either directly or indirectly through intermediaries, or in communication with the interior of two elements, the specific meaning of the terms in this embodiment will be understood by those of ordinary skill in the art. The orientation or positional relationship indicated by "upper", "lower", "left", "right", "inner", "bottom", etc. is based on the orientation or positional relationship shown in the drawings, or the orientation or positional relationship in which the inventive product is conventionally put in use, is merely for convenience in describing the present utility model and simplifying the description, and is not indicative or implying that the apparatus or element in question must have a specific orientation, be constructed and operated in a specific orientation, and therefore should not be construed as limiting the present utility model.
For the purpose of making the objects, technical solutions and advantages of the present utility model more apparent, embodiments of the present utility model will be described in further detail below with reference to the accompanying drawings.
In the embodiment, as shown in fig. 1-3, a boiling mixer comprises a screw feeder 2, wherein a raw material inlet funnel 1 is arranged at the inlet of the screw feeder 2, a blanking pipeline 3 is arranged below the outlet of the screw feeder 2, the outlet of the blanking pipeline 3 is in butt joint with a mixing chamber 4, a pressure equalizing air chamber 6 is arranged at the lower side of the mixing chamber 4, and a product outlet pipeline 7 is connected at the center of the lower end of the pressure equalizing air chamber 6; four return pipelines 11 are arranged outside the mixing chamber 4, and a separator 12 is arranged at the top of each return pipeline; the separators 12 are connected in pairs through pipelines and then are converged at the center of the mixer, and an air outlet pipeline 13 is arranged at the upper end of the converged position.
The raw material inlet funnel 1 and the screw feeder 2 are erected above the inlet of the blanking pipeline 3 by using a rectangular structure, and the screw feeder is erected to effectively improve the feeding efficiency.
Eight high-pressure medicament injection devices 10 are further arranged at the upper end of the pressure equalizing air chamber 6, wherein every four high-pressure medicament injection devices 10 are in one group on the same plane, two groups are added, the injection ends of the high-pressure medicament injection devices 10 are located right above the mixing chamber 4, and the high-pressure medicament injection devices 10 can atomize liquid so as to fully mix the raw materials. The device also comprises a high-pressure air blower 8 connected to the bottom of the pressure equalizing air chamber 6, wherein an air inlet pipeline of the high-pressure air blower 8 enters the pressure equalizing air chamber 6 in the horizontal direction, and an air inlet is not directly aligned to the pressure equalizing air chamber, so that the air pressure can be reduced, and the pressure equalizing effect is better.
The mixing device also comprises a pressure equalizing air chamber 6, wherein the upper end of the pressure equalizing air chamber 6 is provided with an air distribution system 5, and the air distribution system 5 is positioned between the mixing chamber 4 and the pressure equalizing air chamber 6. The wind distribution system 5 is formed by uniformly and vertically arranging a plurality of pressure equalizing hoods 9 on the same plane.
The specific operation process is that firstly raw materials enter a screw feeder 2 through a raw material inlet funnel 1 and are conveyed to a blanking port of a blanking pipeline 3 by the screw feeder, and a mixing chamber 4 is kept at a certain height. The high-pressure blower 8 is started, high-pressure air generated by the high-pressure blower 8 enters the pressure equalizing air chamber 6 to distribute air quantity through the air distribution system 5, and the pressure equalizing hood 9 are utilized to blow the raw materials to roll and move up and down. As shown in fig. 3, the high-pressure chemical injection device 10 quantitatively injects a mist liquid to mix and react with the raw materials. A small amount of finer raw materials and an air mixture move upwards to enter 4 separators 12 for separation, the raw materials separated by wind enter a mixing chamber 4 again for reaction through a return pipeline 11, waste gas is discharged through an air outlet pipeline 13 and enters environmental protection equipment for treatment, and finally, a finished product is discharged through a product outlet pipeline 7.
The utility model has the beneficial effects that: according to the utility model, the raw materials are rolled and move up and down in the mixing chamber under the action of the pressure equalizing air chamber and the air distribution system, so that the mixing rate is improved, a small amount of finer raw materials are separated by the separator and enter the mixing chamber again for mixing, the yield is improved, and the waste caused by incomplete mixing is reduced; meanwhile, the mixing rate is improved, so that the generation of waste gas in the reaction is reduced, and the green and environment-friendly production is realized.
The foregoing has shown and described the basic principles and main features of the present utility model and the advantages of the present utility model. It will be understood by those skilled in the art that the present utility model is not limited to the embodiments described above, and that the above embodiments and descriptions are merely illustrative of the principles of the present utility model, and various changes and modifications may be made without departing from the spirit and scope of the utility model, which is defined in the appended claims. The scope of the utility model is defined by the appended claims and equivalents thereof.
Claims (6)
1. The boiling mixer is characterized by comprising a screw feeder (2), wherein a raw material inlet funnel (1) is arranged at the inlet of the screw feeder (2), a blanking pipeline (3) is arranged below the outlet of the screw feeder (2), the outlet of the blanking pipeline (3) is in butt joint with a mixing chamber (4), a pressure equalizing air chamber (6) is arranged at the lower side of the mixing chamber (4), and a product outlet pipeline (7) is connected at the center of the lower end of the pressure equalizing air chamber (6); four return pipelines (11) are arranged on the outer side of the mixing chamber (4), and a separator (12) is arranged at the top of each return pipeline; the separators (12) are connected in pairs through pipelines and then are converged at the center of the mixer, and an air outlet pipeline (13) is arranged at the upper end of the converged position.
2. A boiling mixer according to claim 1, characterized in that the raw material inlet funnel (1) and the screw feeder (2) are erected above the inlet of the blanking pipe (3) using rectangular structural shelves.
3. A boiling mixer according to claim 1, characterized in that eight high-pressure medicament injection devices (10) are further arranged at the upper end of the pressure equalizing air chamber (6), wherein every four high-pressure medicament injection devices (10) are arranged in one group on the same plane, two groups are total, and the injection ends of the high-pressure medicament injection devices (10) are positioned right above the mixing chamber (4).
4. The boiling mixer according to claim 1, further comprising a high-pressure blower (8) connected to the bottom of the pressure equalizing air chamber (6), wherein the air inlet pipe of the high-pressure blower (8) enters the pressure equalizing air chamber (6) in the horizontal direction.
5. A boiling mixer according to claim 1, further comprising a wind distribution system (5) arranged at the upper end of the pressure equalizing air chamber (6), wherein the wind distribution system (5) is arranged between the mixing chamber (4) and the pressure equalizing air chamber (6).
6. A boiling mixer according to claim 5, further comprising an air distribution system (5) formed by a plurality of pressure equalizing hoods (9) uniformly and vertically arranged on the same plane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322076337.8U CN220677861U (en) | 2023-08-03 | 2023-08-03 | Boiling type mixer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322076337.8U CN220677861U (en) | 2023-08-03 | 2023-08-03 | Boiling type mixer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220677861U true CN220677861U (en) | 2024-03-29 |
Family
ID=90372942
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322076337.8U Active CN220677861U (en) | 2023-08-03 | 2023-08-03 | Boiling type mixer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220677861U (en) |
-
2023
- 2023-08-03 CN CN202322076337.8U patent/CN220677861U/en active Active
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| GR01 | Patent grant |