CN220048556U - High-efficiency separation cyclone - Google Patents
High-efficiency separation cyclone Download PDFInfo
- Publication number
- CN220048556U CN220048556U CN202321471642.0U CN202321471642U CN220048556U CN 220048556 U CN220048556 U CN 220048556U CN 202321471642 U CN202321471642 U CN 202321471642U CN 220048556 U CN220048556 U CN 220048556U
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- Prior art keywords
- fixedly connected
- cyclone
- pipe
- discharge pipe
- powder
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- 238000000926 separation method Methods 0.000 title claims abstract description 34
- 239000000843 powder Substances 0.000 claims abstract description 50
- 230000003014 reinforcing effect Effects 0.000 claims description 4
- 238000013461 design Methods 0.000 claims description 3
- 239000004744 fabric Substances 0.000 claims description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract description 34
- 238000007599 discharging Methods 0.000 abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 5
- 239000002245 particle Substances 0.000 abstract description 4
- 238000000034 method Methods 0.000 abstract description 2
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 abstract description 2
- 229910021645 metal ion Inorganic materials 0.000 description 4
- 239000008187 granular material Substances 0.000 description 3
- 230000000903 blocking effect Effects 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Landscapes
- Cyclones (AREA)
Abstract
The utility model discloses a high-efficiency separation cyclone, which belongs to the technical field of cyclones and comprises a cyclone main body, wherein one side of the cyclone main body is fixedly connected with a feeding pipe, the top of the cyclone main body is fixedly connected with a water discharging pipe, the inside of the cyclone main body is obliquely and fixedly connected with a baffle, the bottom of the cyclone main body is fixedly connected with a powder discharging pipe, the bottom of the powder discharging pipe is fixedly connected with a separating box through a bolt, one side of the separating box is fixedly connected with a coarse powder discharging pipe, and the bottom of the separating box is fixedly connected with a fine powder discharging pipe; according to the utility model, the separation box, the coarse powder discharge pipe, the separation screen and the fine powder discharge pipe are arranged, so that the iron powder can be immediately screened after the cyclone separates the iron powder, larger iron powder particles which do not meet the standard are discharged through the coarse powder discharge pipe on one side, and qualified iron powder is collected through the fine powder discharge pipe on the bottom, so that the separation efficiency of the iron powder can be improved, and the method is worthy of popularization and use.
Description
Technical Field
The utility model relates to the technical field of cyclones, in particular to a high-efficiency separation cyclone.
Background
The cyclone is a common separation and classification device, the working principle of which is centrifugal sedimentation, and the basic principle of the cyclone is to separate liquid-liquid, liquid-solid, liquid-gas and other two-phase mixtures with certain density difference under the action of centrifugal force. When the two-phase mixed liquid to be separated enters the cyclone tangentially from the periphery of the cyclone at a certain pressure, different centrifugal forces are generated to separate the two phases.
The utility model patent of publication No. CN215541859U proposes a cyclone with high-efficient separation function, including a cylindrical feeding barrel, a tangential feeding pipe is arranged on one side of the cylindrical feeding barrel, a conical barrel is fixedly connected with the bottom end of the cylindrical feeding barrel, an underflow pipe is fixedly connected with the bottom end of the conical barrel, an overflow pipe is arranged in the central cavity of the cylindrical feeding barrel, the cylindrical feeding barrel is communicated with the overflow pipe, a plurality of first electromagnets are arranged on the outer side wall of the cylindrical feeding barrel, and a plurality of second electromagnets are arranged on the outer side wall of the conical barrel. According to the utility model, metal ions with larger solution density fly to the inner walls of the cylindrical feeding barrel and the conical barrel under the action of centrifugal force, the metal ions are attached to the inner walls of the cylindrical feeding barrel and the conical barrel through the first electromagnet and the second electromagnet after being electrified, and the first electromagnet and the second electromagnet are powered off, so that the demagnetizing attraction of the metal ions drops downwards, and finally the metal ions are guided out through the underflow pipe, thereby improving the separation efficiency and the separation effect of the solution.
In the practical use process of the case, as the large-particle iron powder which does not meet the factory requirements exists in the iron powder screened by the diverter, the large-particle iron powder also needs to be discharged into other equipment for screening, the efficiency is low, time and labor are wasted, the equipment cost is increased, and therefore the efficient separation cyclone is provided.
Disclosure of Invention
Aiming at the defects of the prior art, the utility model provides a high-efficiency separation cyclone, overcomes the defects of the prior art and aims at solving the problems in the prior art.
In order to achieve the above purpose, the present utility model provides the following technical solutions: the utility model provides a high-efficient separation swirler, includes the swirler main part, one side fixedly connected with inlet pipe of swirler main part, the top fixedly connected with drain pipe of swirler main part, the inside slope fixedly connected with baffle of swirler main part, the bottom fixedly connected with of swirler main part arranges the powder pipe, the bottom bolt that arranges the powder pipe installs the separator box, one side fixedly connected with coarse powder discharge pipe of separator box, the bottom fixedly connected with fine powder discharge pipe of separator box, the inside fixedly connected with separation screen cloth of separator box.
As a preferable technical scheme of the cyclone separator, the baffle is positioned at one side of the feeding pipe, and spiral lines are formed in the cyclone main body.
By adopting the technical scheme, the material with treatment can flow completely along the spiral lines.
As a preferable technical scheme of the utility model, the outside of the cyclone main body is fixedly connected with reinforcing ribs.
By adopting the technical scheme, the overall strength of the cyclone can be enhanced.
As a preferable technical scheme of the utility model, the top of the separation box is provided with a connecting hole which is fixedly communicated with the powder discharge pipe.
By adopting the technical scheme, the separated iron powder can be discharged into the separation box below.
As a preferable mode of the utility model, the separating screen is designed to be inclined, the coarse powder discharge pipe is positioned at one side of the separating screen, and the fine powder discharge pipe is positioned right below the separating screen
Through adopting above-mentioned technical scheme, can screen out large granule's iron powder to the subsequent processing of iron powder is convenient for.
The utility model has the beneficial effects that: through setting up separator box, coarse powder discharge pipe, separating screen and fine powder discharge pipe, can screen immediately after the swirler separates out the iron powder, will not accord with the great iron powder granule of standard and pass through the coarse powder discharge pipe discharge of one side to collect qualified iron powder through the fine powder discharge pipe of bottom, and then can improve the separation efficiency of iron powder, be worth using widely.
Drawings
FIG. 1 is a front view of the present utility model;
FIG. 2 is a partial front cross-sectional view of the present utility model;
fig. 3 is a top view of the mid-cyclone body of the present utility model.
In the figure: 1. a cyclone body; 2. a feed pipe; 3. a drain pipe; 4. a baffle; 5. reinforcing ribs; 6. a powder discharge pipe; 7. a separation box; 8. a coarse powder discharge pipe; 9. separating the screen; 10. and a fine powder discharge pipe.
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, a high-efficiency separation cyclone comprises a cyclone main body 1, wherein one side of the cyclone main body 1 is fixedly connected with a feed pipe 2, the top of the cyclone main body 1 is fixedly connected with a drain pipe 3, the inside of the cyclone main body 1 is obliquely and fixedly connected with a baffle 4, the baffle 4 is positioned on one side of the feed pipe 2, spiral lines are formed in the inside of the cyclone main body 1, the outside of the cyclone main body 1 is fixedly connected with a reinforcing rib 5, and the bottom of the cyclone main body 1 is fixedly connected with a powder discharge pipe 6; the water flow containing iron powder inside is input into the cyclone main body 1 through the feed pipe 2, is input into the spiral line in the cyclone main body 1 through the blocking of the baffle plate 4, is separated through centrifugal force, is discharged through the drain pipe 3 at the top, and granular iron powder is discharged through the powder discharge pipe 6 at the bottom for subsequent operation.
In addition, a separating box 7 is arranged at the bottom end bolt of the powder discharging pipe 6, a coarse powder discharging pipe 8 is fixedly connected to one side of the separating box 7, a fine powder discharging pipe 10 is fixedly connected to the bottom end of the separating box 7, a separating screen 9 is fixedly connected to the inside of the separating box 7, a connecting hole is formed in the top of the separating box 7 and fixedly communicated with the powder discharging pipe 6, the separating screen 9 is of an inclined design, the coarse powder discharging pipe 8 is positioned on one side of the separating screen 9, and the fine powder discharging pipe 10 is positioned right below the separating screen 9; the iron powder is input to the inside of the separation box 7 through the powder discharge pipe 6 and the connecting hole, and fall to the top of the separation screen 9, the separation screen 9 of slope design makes the iron powder at top roll, the iron powder that the size is qualified can pass through the sieve mesh and fall to the inside of the fine powder discharge pipe 10 and discharge, coarser iron powder rolls down one side of the coarse powder discharge pipe 8 along the separation screen 9 of slope, and discharge through the coarse powder discharge pipe 8, and then can pass through the coarse powder discharge pipe 8 of one side with the great iron powder granule that does not accord with the standard and discharge, and collect qualified iron powder through the fine powder discharge pipe 10 of bottom, and then can improve the separation efficiency of iron powder, be worth using widely.
Working principle: the water flow containing iron powder inside is input into the cyclone main body 1 through the feeding pipe 2, the water flow is input into the spiral line inside the cyclone main body 1 through the blocking of the baffle plate 4, separation is carried out through centrifugal force, the fluid is discharged through the water discharge pipe 3 at the top, granular iron powder is discharged through the powder discharge pipe 6 at the bottom for subsequent operation, the iron powder is input into the separation box 7 through the powder discharge pipe 6 and the connecting hole and falls to the top of the separation screen 9, the iron powder at the top is enabled to roll through the inclined separation screen 9, the iron powder with qualified size can pass through the sieve mesh and fall to the inner part of the fine powder discharge pipe 10 for discharge, the coarser iron powder rolls to one side of the coarse powder discharge pipe 8 along the inclined separation screen 9 and is discharged through the coarse powder discharge pipe 8, and further larger iron powder particles which do not meet the standard can be discharged through the coarse powder discharge pipe 8 at one side, and the qualified iron powder is collected through the fine powder discharge pipe 10 at the bottom, further the separation efficiency of the iron powder can be improved, and the separation efficiency of the iron powder is worth popularizing and using.
The foregoing description is only a preferred embodiment of the present utility model, and the present utility model is not limited thereto, but it is to be understood that modifications and equivalents of some of the technical features described in the foregoing embodiments may be made by those skilled in the art, although the present utility model has been described in detail with reference to the foregoing embodiments. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present utility model should be included in the protection scope of the present utility model.
Claims (6)
1. The utility model provides a high-efficient separation swirler, includes swirler main part (1), its characterized in that, one side fixedly connected with inlet pipe (2) of swirler main part (1), the top fixedly connected with drain pipe (3) of swirler main part (1), the inside slope fixedly connected with baffle (4) of swirler main part (1), the bottom fixedly connected with of swirler main part (1) arranges powder pipe (6), the bottom bolt of arranging powder pipe (6) installs separator box (7), one side fixedly connected with coarse powder discharge pipe (8) of separator box (7), the bottom fixedly connected with fine powder discharge pipe (10) of separator box (7), the inside fixedly connected with separation screen cloth (9) of separator box (7).
2. A high efficiency separating cyclone as claimed in claim 1, wherein the baffle (4) is located at one side of the feed pipe (2).
3. A high efficiency separating cyclone as claimed in claim 1, wherein the cyclone body (1) is internally provided with spiral threads.
4. A high efficiency separating cyclone as claimed in claim 1, wherein the cyclone body (1) is fixedly connected with reinforcing ribs (5) at the outside.
5. A high efficiency separating cyclone as claimed in claim 1, wherein the top of the separating box (7) is provided with a connecting hole which is fixedly communicated with the powder discharge pipe (6).
6. A high efficiency separating cyclone as claimed in claim 1, wherein the separating screen (9) is of an inclined design, the coarse powder discharge pipe (8) is located at one side of the separating screen (9), and the fine powder discharge pipe (10) is located directly below the separating screen (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321471642.0U CN220048556U (en) | 2023-06-10 | 2023-06-10 | High-efficiency separation cyclone |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202321471642.0U CN220048556U (en) | 2023-06-10 | 2023-06-10 | High-efficiency separation cyclone |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220048556U true CN220048556U (en) | 2023-11-21 |
Family
ID=88786423
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202321471642.0U Active CN220048556U (en) | 2023-06-10 | 2023-06-10 | High-efficiency separation cyclone |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220048556U (en) |
-
2023
- 2023-06-10 CN CN202321471642.0U patent/CN220048556U/en active Active
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