CN203316397U - Cyclone - Google Patents
Cyclone Download PDFInfo
- Publication number
- CN203316397U CN203316397U CN2013203745924U CN201320374592U CN203316397U CN 203316397 U CN203316397 U CN 203316397U CN 2013203745924 U CN2013203745924 U CN 2013203745924U CN 201320374592 U CN201320374592 U CN 201320374592U CN 203316397 U CN203316397 U CN 203316397U
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- CN
- China
- Prior art keywords
- powder
- pipe
- sedimentation bucket
- settling hopper
- powder feed
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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Abstract
The utility model discloses a cyclone. The cyclone comprises a settling hopper (1), a powder feeding pipe (2) and a powder discharging pipe (3), wherein the lower end of the settling hopper (1) is provided with a settled substance discharging port (11); the powder feeding pipe (2) is communicated with the settling hopper (1) on the side wall of the settling hopper (1); the powder discharging pipe (3) is communicated with the settling hopper (1) from the top part of the settling hopper (1) and goes deep into the middle part of the settling hopper (1); the opening of the powder discharging pipe (3) is lower than the lower wall of the powder feeding pipe (2); the powder discharging pipe (3) is connected with a centrifugal fan (4). The powder feeding pipe and the powder discharging pipe are arranged on the settling hopper, antimony trioxide powder entering at a high speed rotates in the settling hopper and then is conveyed out of the powder discharging pipe, particle impurities with large mass settle to the bottom part of the settling hopper along the inner wall of the settling hopper, and then the procedure of removing impurities from the antimony trioxide powder is finished.
Description
Technical field
The utility model relates to antimony powder production equipment technical field, particularly a kind of cyclone.
Background technology
In antimony processing industry, in the production and processing operation of antimony oxide powder, there are a lot of operations need to use centrifugal blower.The existing centrifugal blower used is directly to buy from the market, this class blower fan mainly is comprised of Blower Housing and draught fan impeller, its Blower Housing is the chamber of a relative closure, if, when being stained with the adhesive such as dust on the blade of draught fan impeller and need to removing, Blower Housing need to be removed and could be implemented removing.Like this, bring great inconvenience to removing work, the adhesive of removing each time on blade need to expend a large amount of manpowers, and the time that removing work expends is also longer.In the antimony powder production and processing technology, when particularly the antimony powder powder is more moistening, powder is easy to be bonded on blade, need to remove continually the antimony powder powder bondd on blade like this.
In realizing process of the present utility model, the inventor finds that at least there is following problem in prior art: during the adhesive of the existing centrifugal blower used on removing its blade, the side plate of Blower Housing need to be removed and could fall adhesive by spatula.
The utility model content
In order to solve the problem of prior art, the utility model embodiment provides a kind of cyclone.Described technical scheme is as follows:
A kind of cyclone is provided, comprise sedimentation bucket, powder feed pipe and discharge of fine material pipe, described sedimentation bucket is that epimere is the cylinder body that cylindrical shape, hypomere are bucket shape, and the lower end of described sedimentation bucket is provided with the precipitum outlet, and described precipitum outlet place is provided with suitable blanking device; Described powder feed pipe is connected with described sedimentation bucket on the sidewall of described sedimentation bucket, and the upper tube wall of described powder feed pipe and described sedimentation bucket end face have the distance of 1.0～1.5 times of described powder feed pipe calibers; Described discharge of fine material pipe is connected with described sedimentation bucket from the top of described sedimentation bucket, and described discharge of fine material pipe is deep into described sedimentation bucket middle part, and the mouth of pipe of described discharge of fine material pipe is lower than the lower tube wall of described powder feed pipe; Described discharge of fine material Guan Yuyi centrifugal blower is connected.
Further, the nozzle position in the vertical direction of described discharge of fine material pipe is lower than the distance of 0.5～1.5 times of described powder feed pipe caliber of tube wall under described powder feed pipe.
The beneficial effect that the technical scheme that the utility model embodiment provides is brought is:
By the powder feed pipe being set on the sidewall at the sedimentation bucket, at the top of sedimentation bucket, the discharge of fine material pipe being set, like this, from the powder feed pipe, with the antimony oxide powder of coming at a high speed, in the sedimentation bucket, rotatablely move, owing on the discharge of fine material pipe, being provided with centrifugal blower, the antimony oxide powder transfers out from the discharge of fine material pipe under the centrifugal blower effect, the heavier particle impurity of quality is deposited to sedimentation bucket bottom along sedimentation bucket inwall, has so just completed the operation of antimony oxide powder removal of impurities.This cyclone is simple in structure, impurity-eliminating effect is good, dust removal rate is high.
The accompanying drawing explanation
In order to be illustrated more clearly in the technical scheme in the utility model embodiment, in below describing embodiment, the accompanying drawing of required use is briefly described, apparently, accompanying drawing in the following describes is only embodiment more of the present utility model, for those of ordinary skills, under the prerequisite of not paying creative work, can also obtain according to these accompanying drawings other accompanying drawing.
Fig. 1 is the structural representation of the cyclone that provides of the utility model embodiment.
The specific embodiment
For making the purpose of this utility model, technical scheme and advantage clearer, below in conjunction with accompanying drawing, the utility model embodiment is described in further detail.
Embodiment
The present embodiment provides a kind of cyclone, please refer to Fig. 1, this cyclone comprises sedimentation bucket 1, powder feed pipe 2 and discharge of fine material pipe 3, sedimentation bucket 1 is that epimere is the cylinder body that cylindrical shape, hypomere are bucket shape, the lower end of sedimentation bucket 1 is provided with precipitum outlet 11, and precipitum outlet 11 places are provided with suitable blanking device 12; Powder feed pipe 2 is connected with sedimentation bucket 1 on the sidewall of sedimentation bucket 1, and the upper tube wall of powder feed pipe 2 and sedimentation bucket 1 end face have the distance of 1.0～1.5 times of powder feed pipe 2 calibers; Discharge of fine material pipe 3 is connected with sedimentation bucket 1 from the top of sedimentation bucket 1, and discharge of fine material pipe 3 is deep into sedimentation bucket 1 middle part, and the mouth of pipe of discharge of fine material pipe 3 is lower than the lower tube wall of powder feed pipe 2.Discharge of fine material pipe 3 is connected with a centrifugal blower 4.Like this, the antimony oxide powder by powder feed pipe 2 deliver to sedimentation bucket 1 interior after, because speed is very fast, the antimony oxide powder is at the interior High Rotation Speed of sedimentation bucket 1; Further, owing to being provided with centrifugal blower 4 on discharge of fine material pipe 3, centrifugal blower 4 makes the interior top of sedimentation bucket 1 form certain negative pressure, and the antimony oxide powder is discharged from from discharge of fine material pipe 3 after rotation; Yet the particle impurity that other are larger, because the gravity of self is larger, be deposited to sedimentation bucket 1 bottom along sedimentation bucket 1 inwall.Preferably, the upper tube wall of powder feed pipe 2 and sedimentation bucket 1 end face have the distance of 1.0,1.2 or 1.5 times of powder feed pipe 2 calibers.
The nozzle position in the vertical direction of discharge of fine material pipe 3 is lower than the distance of 0.5～1.5 times of powder feed pipe 2 caliber of 2 times tube walls of powder feed pipe.Can avoid impurity to be accompanied by the antimony oxide powder like this, on the one hand directly is discharged from from discharge of fine material pipe 3; On the other hand, such distance can make the antimony oxide powder just be discharged from from discharge of fine material pipe 3.Preferably, the nozzle position in the vertical direction of discharge of fine material pipe 3 is lower than the distance of 0.5,0.8,1.0,1.2 or 1.5 times of powder feed pipe 2 caliber of 2 times tube walls of powder feed pipe.
The foregoing is only preferred embodiment of the present utility model, not in order to limit the utility model, all within spirit of the present utility model and principle, any modification of doing, be equal to replacement, improvement etc., within all should being included in protection domain of the present utility model.
Claims (2)
1. a cyclone, it is characterized in that, comprise sedimentation bucket (1), powder feed pipe (2) and discharge of fine material pipe (3), described sedimentation bucket (1) is that epimere is the cylinder body that cylindrical shape, hypomere are bucket shape, the lower end of described sedimentation bucket (1) is provided with precipitum outlet (11), and described precipitum outlet (11) locates to be provided with suitable blanking device (12);
Described powder feed pipe (2) is connected with described sedimentation bucket (1) on the sidewall of described sedimentation bucket (1), and the upper tube wall of described powder feed pipe (2) and described sedimentation bucket (1) end face have the distance of 1.0～1.5 times of described powder feed pipes (2) caliber; Described discharge of fine material pipe (3) is connected with described sedimentation bucket (1) from the top of described sedimentation bucket (1), described discharge of fine material pipe (3) is deep into described sedimentation bucket (1) middle part, and the mouth of pipe of described discharge of fine material pipe (3) is lower than the lower tube wall of described powder feed pipe (2);
Described discharge of fine material pipe (3) is connected with a centrifugal blower (4).
2. cyclone according to claim 1, is characterized in that, the nozzle position in the vertical direction of described discharge of fine material pipe (3) is lower than the distance of lower 0.5～1.5 times of described powder feed pipe of tube wall (2) caliber of described powder feed pipe (2).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013203745924U CN203316397U (en) | 2013-06-27 | 2013-06-27 | Cyclone |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013203745924U CN203316397U (en) | 2013-06-27 | 2013-06-27 | Cyclone |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203316397U true CN203316397U (en) | 2013-12-04 |
Family
ID=49655795
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013203745924U Expired - Fee Related CN203316397U (en) | 2013-06-27 | 2013-06-27 | Cyclone |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203316397U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110237899A (en) * | 2019-06-19 | 2019-09-17 | 焦作市和兴化学工业有限公司 | Break poly- machine and acetylene carbon black purifier apparatus and high-performance acetylene carbon black production method |
-
2013
- 2013-06-27 CN CN2013203745924U patent/CN203316397U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110237899A (en) * | 2019-06-19 | 2019-09-17 | 焦作市和兴化学工业有限公司 | Break poly- machine and acetylene carbon black purifier apparatus and high-performance acetylene carbon black production method |
| CN110237899B (en) * | 2019-06-19 | 2020-08-18 | 焦作市和兴化学工业有限公司 | Polymer breaker, acetylene black purification equipment and high-performance acetylene black production method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20131204 Termination date: 20140627 |
|
| EXPY | Termination of patent right or utility model |