CN211913610U - Pneumatic stirring device - Google Patents
Pneumatic stirring device Download PDFInfo
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- CN211913610U CN211913610U CN201922275887.6U CN201922275887U CN211913610U CN 211913610 U CN211913610 U CN 211913610U CN 201922275887 U CN201922275887 U CN 201922275887U CN 211913610 U CN211913610 U CN 211913610U
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Abstract
The utility model belongs to the technical field of material mixing device and specifically relates to a through compressed air as stirring power to ambient noise's pneumatic stirring device when effectively reducing the stirring, including the stirring feed bin, stirring feed bin top is provided with the feed inlet, including evenly setting up in the high-pressure intake pipe of stirring feed bin lateral wall face, high-pressure intake pipe will stir feed bin inner chamber and high pressurized air source intercommunication. Compressed air is used as main power to replace a stirrer, so that high-speed airflow is flushed into liquid to drive the liquid material and the solid material to be fully mixed, and the aim of uniformly mixing is fulfilled. Wherein, the high-pressure gas drives the solid-liquid mixed material to move and mix, so as to generate a boiling-like mixing effect, thereby achieving the purpose of uniformly mixing the solid and the liquid. The utility model discloses the noise that produces when the mixing material is minimum, the effectual comfort level that improves operational environment has also improved the efficiency of mixing simultaneously, the utility model discloses be particularly useful for the occasion of solid powder and the more intensive mixing stirring of liquid material.
Description
Technical Field
The utility model belongs to the technical field of material mixing device and specifically relates to a pneumatic stirring device.
Background
A blender is a device commonly used in the industrial field, in particular a device for mixing a powdery solid and a liquid represented by a water level. The common solid-liquid stirring device is characterized in that a motor stirrer is connected in a container with a fixed volume, and a paddle of the stirrer is used for driving liquid to rotate so as to fully and uniformly mix solid liquid. The traditional stirring machine uses electricity as a power source, noise may exist in the stirring process, solid deposition may occur in places where stirring blades cannot reach, the stirring effect is general, and especially, the huge noise generated by the operation of equipment such as a motor during stirring brings great influence on operators in the stirring environment.
SUMMERY OF THE UTILITY MODEL
The utility model aims to solve the technical problem that a pneumatic stirring device through compressed air as stirring power is provided to ambient noise when effectively reducing the stirring.
The utility model provides a technical scheme that its technical problem adopted is: pneumatic agitating unit, including the stirring feed bin, stirring feed bin top is provided with the feed inlet, including evenly setting up in the high-pressure intake pipe of stirring feed bin lateral wall face, high-pressure intake pipe will stir feed bin inner chamber and high pressurized air source intercommunication.
Further, the cross section of the stirring bin is circular.
Furthermore, the high-pressure air inlet pipes are three and are uniformly arranged on the side wall surface of the stirring bin.
Further, the cross section of the stirring bin is rectangular.
Further, the high-pressure air inlet pipes are six, wherein two high-pressure air inlet pipes are respectively arranged on two side wall surfaces in the length direction of the rectangular stirring bin, and one high-pressure air inlet pipe is respectively arranged on two side wall surfaces in the width direction of the rectangular stirring bin.
Further, the gas pressure range of the high-pressure gas source is 0.5-1 MPa.
The utility model has the advantages that: during in-service use, the solid-state material and the liquid material that wait to mix enter into the stirring feed bin through the feed inlet at stirring feed bin top at first in, afterwards, let in high-pressure gas through high-pressure intake pipe. Compressed air is used as main power to replace a stirrer, so that high-speed airflow is flushed into liquid to drive the liquid material and the solid material to be fully mixed, and the aim of uniformly mixing is fulfilled. Wherein, the high-pressure gas drives the solid-liquid mixed material to move and mix, so as to generate a boiling-like mixing effect, thereby achieving the purpose of uniformly mixing the solid and the liquid. The utility model discloses the noise that produces when the mixing material is minimum, the effectual comfort level that improves operational environment has also improved the efficiency of mixing simultaneously, the utility model discloses be particularly useful for the occasion of solid powder and the more intensive mixing stirring of liquid material.
Drawings
Fig. 1 is a top view of a circular stirring silo.
Fig. 2 is a side view of fig. 1.
Fig. 3 is a top view of a rectangular blender bunk.
Fig. 4 is a side view of fig. 3.
Labeled as: stirring feed bin 1, feed inlet 11, high-pressure air inlet pipe 2, high-pressure air inlet pipe export 21.
Detailed Description
The present invention will be further explained with reference to the drawings and examples.
The pneumatic stirring device shown in fig. 1, fig. 2, fig. 3 and fig. 4 comprises a stirring storage bin 1, wherein a feeding hole 11 is formed in the top of the stirring storage bin 1 and comprises a high-pressure air inlet pipe 2 which is uniformly arranged on the side wall surface of the stirring storage bin 1, and the inner cavity of the stirring storage bin 1 is communicated with a high-pressure air source through the high-pressure air inlet pipe 2.
The utility model discloses mainly be applicable to solid powder and the stirring between the liquid material that takes water as the representative mixes, because the characteristics of this device stirring, the mass ratio of generally preferred solid powder and water is no longer than 1:1, and the mass ratio of water surpasses more than half of compounding gross mass promptly to can be abundant when guaranteeing to let in high-pressure gas let the liquid material rolling motion get up, thereby guarantee the quality of mixing. In addition, the solid powder particles are preferably not too large, and the particle size of the solid powder is preferably not more than 10mm, so that the mixed material quality is ensured. The utility model discloses not only the stirring noise is low, still has the effect that stirring effect is good, implementation cost is low simultaneously. In order to ensure the mixing effect of the gas, the gas pressure range of the high-pressure gas source is preferably 0.5-1 MPa.
Generally, the cross section of the stirring bin 1 can be selected to be circular, as shown in fig. 1 and 2, the high-pressure air inlet pipes 2 are three and are uniformly arranged on the side wall surface of the stirring bin 1, so that the effect of air on mixed materials is uniform and effective during material mixing. Based on the same concept, the cross section of the stirring bin 1 can also be selected to be rectangular, as shown in fig. 3 and 4, the number of the high-pressure air inlet pipes 2 is six, wherein two side wall surfaces in the length direction of the rectangular stirring bin 1 are respectively provided with two high-pressure air inlet pipes 2, and two side wall surfaces in the width direction of the rectangular stirring bin 1 are respectively provided with one high-pressure air inlet pipe 2.
Examples
Example 1
Stirring feed bin 1 is columniform pneumatic stirring device, and wherein, 1 diameter 2m in stirring feed bin, 1 height 1m in stirring feed bin, 1 upper end opening in stirring feed bin sets up feed inlet 11, adds water and solid powder from feed inlet 11. The pressure of the introduced compressed air is 0.7Mp, 3 high-pressure air inlet pipes 2 are uniformly arranged around the side wall surface of the stirring storage bin 1, the height of outlets 21 of the high-pressure air inlet pipes is 0.5m, and the high-pressure air inlet pipes 2 are uniformly distributed according to 120 degrees, so that the aim of uniformly stirring can be fulfilled.
Example 2
Pneumatic agitating unit of stirring feed bin 1 rectangle, wherein, 1 long 3m in stirring feed bin, 1 wide 2m in stirring feed bin, 1 high 1.6m in stirring feed bin, 1 upper end opening in stirring feed bin sets up feed inlet 11, directly adds water and solid powder through feed inlet 11. The pressure of the introduced compressed air was 0.65 Mp.
Compressed air intake pipe mounting means: 6 high-pressure air inlet pipes 2 are installed, the high-pressure air inlet pipe outlet 21 is arranged at the height of 0.8m, wherein two high-pressure air inlet pipes 2 are respectively installed at the interval of 1m on each side in the long edge direction of the high-pressure air inlet pipes 2, and 1 high-pressure air inlet pipe 2 is respectively installed in the middle in the short edge direction, so that the aim of uniformly stirring can be fulfilled.
Claims (6)
1. Pneumatic agitating unit, including stirring feed bin (1), stirring feed bin (1) top is provided with feed inlet (11), its characterized in that: including evenly setting up in high-pressure intake pipe (2) of stirring feed bin (1) side wall face, high-pressure intake pipe (2) will stir feed bin (1) inner chamber and high pressurized air source intercommunication.
2. A pneumatic stirring device as set forth in claim 1, characterized in that: the cross section of the stirring bin (1) is circular.
3. A pneumatic stirring device as set forth in claim 2, characterized in that: the high-pressure air inlet pipes (2) are three and are evenly arranged on the side wall surface of the stirring storage bin (1).
4. A pneumatic stirring device as set forth in claim 1, characterized in that: the cross section of the stirring bin (1) is rectangular.
5. A pneumatic stirring device as defined in claim 4, wherein: the high-pressure air inlet pipes (2) are six, wherein two side wall surfaces in the length direction of the rectangular stirring bin (1) are respectively provided with two high-pressure air inlet pipes (2), and two side wall surfaces in the width direction of the rectangular stirring bin (1) are respectively provided with one high-pressure air inlet pipe (2).
6. A pneumatic stirring device as claimed in claim 1, 2, 3, 4 or 5, wherein: the gas pressure range of the high-pressure gas source is 0.5-1 MPa.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922275887.6U CN211913610U (en) | 2019-12-17 | 2019-12-17 | Pneumatic stirring device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922275887.6U CN211913610U (en) | 2019-12-17 | 2019-12-17 | Pneumatic stirring device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211913610U true CN211913610U (en) | 2020-11-13 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201922275887.6U Active CN211913610U (en) | 2019-12-17 | 2019-12-17 | Pneumatic stirring device |
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| Country | Link |
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| CN (1) | CN211913610U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114747654A (en) * | 2022-04-18 | 2022-07-15 | 张成璨 | Sunflower kernel peanut protein vegetarian meat and production device and production method thereof |
-
2019
- 2019-12-17 CN CN201922275887.6U patent/CN211913610U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114747654A (en) * | 2022-04-18 | 2022-07-15 | 张成璨 | Sunflower kernel peanut protein vegetarian meat and production device and production method thereof |
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