CN210846093U - Aggregate mixing device - Google Patents
Aggregate mixing device Download PDFInfo
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- CN210846093U CN210846093U CN201921210738.5U CN201921210738U CN210846093U CN 210846093 U CN210846093 U CN 210846093U CN 201921210738 U CN201921210738 U CN 201921210738U CN 210846093 U CN210846093 U CN 210846093U
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- transition section
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- shaped transition
- feed inlet
- mixing device
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Abstract
The utility model discloses a granular material mixing device, which comprises a near-end storage tank, a far-end storage tank and a homogenizing tank; a T-shaped transition section is arranged at the feed inlet of the homogenizing tank; the discharge hole of the near-end storage tank is communicated with the first port of the T-shaped transition section through a transmission pipeline; the discharge port of the far-end storage tank is connected with one end of a spiral delivery pump through a pipeline, and the other end of the spiral delivery pump is communicated with a second port of the T-shaped transition section through a transmission pipeline; a third port of the T-shaped transition section is communicated with a feed inlet of the homogenizing tank, and the T-shaped transition section is provided with a connecting port connected with the blower; just being equipped with the buffer disc to the feed inlet of homogenization jar, the central axis of buffer disc coincides with the central axis of homogenization jar, the buffer disc bottom is connected with driving motor electricity, homogenization jar bottom is equipped with the discharge gate, the discharge gate passes through the pipe connection with the negative pressure delivery pump. The utility model provides a be convenient for remote transmission, the complete aggregate mixing arrangement of homogenization.
Description
Technical Field
The utility model relates to a conveying equipment technical field, concretely relates to aggregate mixing arrangement.
Background
Because there are product performance that the product performance is undulant greatly in the single line product, and product performance is unstable scheduling phenomenon, in order to make the product more even, the performance is more stable, needs carry out homogenization treatment to the product of 3 ~ 4 production lines at least. Therefore, there is a need to address the process of transporting several lines of product to the homogenization tank for processing.
Because some products are close to the homogenizing tank and some products are far from the homogenizing tank, the operation of transferring the granular materials of the production line at a remote position into the homogenizing tank is difficult, and the problem of incomplete product homogenization of different specific production lines can also occur.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to overcome the defect that exists among the prior art, provide a be convenient for remote transmission, the complete aggregate mixing arrangement of homogenization.
In order to achieve the purpose, the technical scheme of the utility model is to design a granular material mixing device, which is characterized by comprising a near-end storage tank, a far-end storage tank and a homogenizing tank; a T-shaped transition section is arranged at the feed inlet of the homogenizing tank; the discharge hole of the near-end storage tank is communicated with the first port of the T-shaped transition section through a transmission pipeline; the discharge port of the far-end storage tank is connected with one end of a spiral delivery pump through a pipeline, and the other end of the spiral delivery pump is communicated with a second port of the T-shaped transition section through a transmission pipeline; a third port of the T-shaped transition section is communicated with a feed inlet of the homogenizing tank, and the T-shaped transition section is provided with a connecting port connected with the blower; just being equipped with the buffer disc to the feed inlet of homogenization jar, the central axis of buffer disc coincides with the central axis of homogenization jar, the buffer disc bottom is connected with driving motor electricity, homogenization jar bottom is equipped with the discharge gate, the discharge gate passes through the pipe connection with the negative pressure delivery pump.
Set up "T" type changeover portion in the feed inlet department of homogenization jar, make things convenient for the material of different distances to carry out the mixing, the time spent in near-end storage tank to the homogenization jar is short, and long time spent in the distal end storage tank sets up the changeover portion consequently, begins the mixing when the material of near-end storage tank and distal end storage tank all gets into the changeover portion. In addition, ventilation in the T-shaped transition section is helpful for the materials to rapidly enter the homogenizing tank on one hand, and the materials are mixed in advance on the other hand.
As an optimized technical scheme, a material storage groove is arranged in the middle of the buffer disc, and material guide grooves are radially arranged on the periphery of the material storage groove. The buffer disc is rotatory under the drive of motor, and the material gets into from the feed inlet and beats the buffer disc on, further mixing, on the lateral wall of homogenizing tank was thrown out along the baffle box after the mixing, followed the lateral wall and flowed from the discharge gate, carried out abundant mixing. Compared with the prior art, the mixer is adopted for mixing, the heat generation in the mixing process is reduced, and the product quality is improved.
As a preferable technical scheme, the air outlet position in the T-shaped transition section is the intersection A of the first port and the second port. The air outlet position is arranged on the intersection point of the near-end storage tank and the far-end storage tank, so that the wind power is mixed more fully.
As a preferred technical scheme, the feed inlet of the homogenizing tank is provided with guide vanes, the top view of the guide vanes is arranged in a net shape, and the length of the guide vanes is matched with the depth of the feed inlet. Due to the arrangement of the flow deflectors, the materials fall into the storage groove of the buffer disc to the maximum extent, and the materials are prevented from bouncing after being impacted with the buffer disc.
As a preferred technical scheme, the flow deflector is flexible rubber.
As a preferred technical scheme, a screw is arranged between the buffer disc and the motor, and stirring blades are arranged on the screw. So that the stirring is more sufficient.
As the preferred technical scheme, a first gate valve is arranged between the T-shaped transition section and the homogenizing tank, and a second gate valve is arranged between the discharge port of the homogenizing tank and the negative pressure delivery pump.
The utility model has the advantages and the beneficial effects that: the utility model discloses a mixing arrangement can carry out the homogeneous mixing with the material of near-end storage tank and distal end storage tank for the material performance is more stable and even, adopts the utility model discloses the product quality of production is more stable.
Drawings
Fig. 1 is a schematic structural diagram of the present invention;
FIG. 2 is a schematic view of a structure of a buffer tray;
in the figure: 1. a proximal storage tank; 2. a remote material storage tank; 3. a homogenization tank; 4. a T-shaped transition section; 5. a screw delivery pump; 6. a blower; 7. a buffer tray; 8. a drive motor; 9. a negative pressure delivery pump; 10. a flow deflector; 11. a stirring blade; 12. a first gate valve; 13. a second gate valve; 14. a material storage groove; 15. a material guide groove.
Detailed Description
The following description will further describe embodiments of the present invention with reference to the accompanying drawings and examples. The following examples are only for illustrating the technical solutions of the present invention more clearly, and the protection scope of the present invention is not limited thereby.
A granular material mixing device comprises a near-end storage tank 1, a far-end storage tank 2 and a homogenizing tank 3; a T-shaped transition section 4 is arranged at the feed inlet of the homogenizing tank; the discharge hole of the near-end storage tank is communicated with the first port of the T-shaped transition section through a transmission pipeline; the discharge port of the far-end storage tank is connected with one end of a spiral delivery pump 5 through a pipeline, and the other end of the spiral delivery pump is communicated with a second port of the T-shaped transition section through a transmission pipeline; a third port of the T-shaped transition section is communicated with a feed inlet of the homogenizing tank, and the T-shaped transition section is provided with a connecting port connected with the blower 6; just being equipped with buffer disk 7 to the feed inlet of homogenization jar, the central axis of buffer disk and the coincidence of the central axis of homogenization jar, buffer disk bottom is connected with driving motor 8 electricity, homogenization jar bottom is equipped with the discharge gate, the discharge gate passes through the pipe connection with negative pressure delivery pump 9.
A material storage groove 14 is formed in the middle of the buffer disc, and material guide grooves 15 are radially formed in the periphery of the material storage groove.
The air outlet position in the T-shaped transition section is the intersection A of the first port and the second port.
The homogenizing tank is characterized in that a flow deflector 10 is arranged at the feed inlet of the homogenizing tank, the flow deflectors are arranged in a net shape in a top view, and the length of each flow deflector is matched with the depth of the feed inlet.
The flow deflector is flexible rubber.
And a screw rod is arranged between the buffer disc and the motor, and stirring blades 11 are arranged on the screw rod.
A first gate valve 12 is arranged between the T-shaped transition section and the homogenizing tank, and a second gate valve 13 is arranged between the discharge port of the homogenizing tank and the negative pressure delivery pump.
The foregoing is only a preferred embodiment of the present invention, and it should be noted that, for those skilled in the art, a plurality of improvements and decorations can be made without departing from the technical principle of the present invention, and these improvements and decorations should also be regarded as the protection scope of the present invention.
Claims (7)
1. The granular material mixing device is characterized by comprising a near-end storage tank, a far-end storage tank and a homogenizing tank; a T-shaped transition section is arranged at the feed inlet of the homogenizing tank; the discharge hole of the near-end storage tank is communicated with the first port of the T-shaped transition section through a transmission pipeline; the discharge port of the far-end storage tank is connected with one end of a spiral delivery pump through a pipeline, and the other end of the spiral delivery pump is communicated with a second port of the T-shaped transition section through a transmission pipeline; a third port of the T-shaped transition section is communicated with a feed inlet of the homogenizing tank, and the T-shaped transition section is provided with a connecting port connected with the blower; just being equipped with the buffer disc to the feed inlet of homogenization jar, the central axis of buffer disc coincides with the central axis of homogenization jar, the buffer disc bottom is connected with driving motor electricity, homogenization jar bottom is equipped with the discharge gate, the discharge gate passes through the pipe connection with the negative pressure delivery pump.
2. The pellet mixing device according to claim 1, wherein a storage trough is provided in the middle of the buffer tray, and guide chutes are radially provided around the storage trough.
3. The pellet mixing device of claim 2, wherein the air outlet of the T-shaped transition section is located at the intersection a of the first port and the second port.
4. The pellet mixing device according to claim 3, wherein the feed inlet of the homogenizing tank is provided with flow deflectors, the flow deflectors are arranged in a net shape, and the length of each flow deflector is matched with the depth of the feed inlet.
5. The pellet mixing device of claim 4, wherein said deflector is a flexible rubber.
6. The pellet mixing device as claimed in claim 5, wherein a screw is provided between said buffer disc and said motor, and said screw is provided with stirring blades.
7. The pellet mixing device according to claim 6, wherein a first gate valve is provided between the T-shaped transition section and the homogenizing tank, and a second gate valve is provided between the discharge port of the homogenizing tank and the negative pressure delivery pump.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201921210738.5U CN210846093U (en) | 2019-07-30 | 2019-07-30 | Aggregate mixing device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201921210738.5U CN210846093U (en) | 2019-07-30 | 2019-07-30 | Aggregate mixing device |
Publications (1)
Publication Number | Publication Date |
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CN210846093U true CN210846093U (en) | 2020-06-26 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201921210738.5U Active CN210846093U (en) | 2019-07-30 | 2019-07-30 | Aggregate mixing device |
Country Status (1)
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CN (1) | CN210846093U (en) |
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2019
- 2019-07-30 CN CN201921210738.5U patent/CN210846093U/en active Active
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