CN216224891U - High-efficient whirl replacement device with continuous boiling region - Google Patents
High-efficient whirl replacement device with continuous boiling region Download PDFInfo
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- CN216224891U CN216224891U CN202122820894.7U CN202122820894U CN216224891U CN 216224891 U CN216224891 U CN 216224891U CN 202122820894 U CN202122820894 U CN 202122820894U CN 216224891 U CN216224891 U CN 216224891U
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- wall
- cyclone
- base frame
- continuous boiling
- nozzle
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- 238000009835 boiling Methods 0.000 title claims abstract description 23
- 239000000463 material Substances 0.000 claims abstract description 43
- 239000010410 layer Substances 0.000 claims abstract description 26
- 239000011229 interlayer Substances 0.000 claims abstract description 16
- 238000005192 partition Methods 0.000 claims abstract description 9
- 239000000919 ceramic Substances 0.000 claims abstract description 8
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 claims abstract description 6
- 239000013049 sediment Substances 0.000 claims abstract description 5
- 239000011550 stock solution Substances 0.000 claims description 11
- 238000006073 displacement reaction Methods 0.000 claims description 10
- 239000012530 fluid Substances 0.000 claims description 3
- 239000007788 liquid Substances 0.000 description 5
- 238000000926 separation method Methods 0.000 description 5
- 239000011362 coarse particle Substances 0.000 description 3
- 239000010419 fine particle Substances 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 230000007774 longterm Effects 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- 238000004062 sedimentation Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 238000005299 abrasion Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000005194 fractionation Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
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Abstract
The utility model discloses a high-efficiency rotational flow replacement device with a continuous boiling region.A base frame is provided with cyclones distributed in a circumferential array, each cyclone comprises a vortex chamber, the vortex chamber is provided with a feed inlet, and the outer wall of the feed inlet is sleeved with a buffer tube; the cyclone further comprises a cone body and a material settling nozzle, wherein the material settling nozzle is movably arranged at the lower end of the cone body, an inner interlayer is movably arranged in the material settling nozzle, the lower end of the cone body is provided with a vertically and downwardly extending abutting wall, and the bottom end of the abutting wall is abutted against the upper end of the inner interlayer. The utility model provides a high-efficiency rotational flow replacement device with a continuous boiling region, wherein a spiral layer arranged on the inner wall of a cone body is a ceramic layer, the ceramic layer enables the spiral layer to resist high temperature and can protect the inside of the cone body, a collision wall is arranged at the bottom end of the cone body and abuts against an inner partition layer through the collision wall, so that the inner partition layer is fixed on the inner wall of a material sinking nozzle during working, and sediment is placed into a material sinking bin arranged in a base frame through the material sinking nozzle.
Description
Technical Field
The utility model relates to the technical field of cyclone replacement, in particular to a high-efficiency cyclone replacement device with a continuous boiling zone.
Background
A fluid cyclone is a common separation and fractionation device, and the centrifugal sedimentation principle is commonly used. When the two-phase mixed liquid to be separated enters the cyclone tangentially from the periphery of the cyclone under a certain pressure, strong three-dimensional elliptical strong-rotation shearing turbulent motion is generated. Because the particle size difference exists between the coarse particles and the fine particles, the coarse particles and the fine particles are subjected to different sizes of centrifugal force, centripetal buoyancy, fluid drag force and the like, and under the action of centrifugal sedimentation, most of the coarse particles are discharged through a bottom flow port of the cyclone, and most of the fine particles are discharged through an overflow pipe, so that the purposes of separation and classification are achieved.
In prior art, use to the swirler is the solid-liquid separation that carries on more, all is the use under the normal atmospheric temperature, and swirler application area when boiling in succession is less, improvement to the swirler in the aspect of the high temperature field is less for the time, secondly is more crude to the material that separates the back and deposits, great to machine wearing and tearing, along with the continuous deepening of mechanization degree, application to the machine is popularized gradually, and then also need the essence to the improvement of swirler, when using at normal atmospheric temperature, can use with the whirl replacement when boiling in succession.
To sum up, to the whirl replacement device that can be applied to when boiling in succession among the prior art use less, and the material that precipitates after the separation is mostly rougher, to the great problem of machine wear, be used for solving.
SUMMERY OF THE UTILITY MODEL
The utility model aims to provide an efficient cyclone displacement device with a continuous boiling zone, and aims to solve the problems that less cyclone displacement devices are used for continuous boiling, most of materials deposited after separation are rougher and the abrasion to a machine is larger in the prior art, and the problem is to be solved.
In order to achieve the above purpose, the utility model provides the following technical scheme: a high-efficiency rotational flow replacement device with a continuous boiling region comprises a base frame, wherein cyclones distributed in a circumferential array are arranged on the base frame, each cyclone comprises a vortex chamber, a feed port is arranged on each vortex chamber, and a buffer tube is sleeved on the outer wall of each feed port; the cyclone further comprises a cone and a material sinking nozzle, wherein the material sinking nozzle is movably arranged at the lower end of the cone, an inner interlayer is movably arranged in the material sinking nozzle, a vertically and downwardly extending abutting wall is arranged at the lower end of the cone, and the bottom end of the abutting wall is abutted to the upper end of the inner interlayer.
Preferably, the sinking nozzle is provided with sliding chutes distributed along the circumferential array of the inner wall, the outer wall of the inner partition layer is provided with a convex block matched with the sliding chutes, and the convex block is in sliding connection with the sliding chutes.
Preferably, the base frame is provided with a material containing bin and a stock solution bin respectively, the stock solution bin is positioned outside the material containing bin, the swirler further comprises an upper end pipe, a connecting pipe is arranged between the swirler and the material containing bin, and the stock solution bin is connected with the swirler through the buffer pipe.
Preferably, one end of the connecting pipe is movably connected with the upper end pipe, and the vortex chamber is movably connected with the upper end pipe.
Preferably, the upper end of the vortex chamber is provided with a connecting end, a connecting port is arranged at the circle center of the upper end pipe, and the connecting end extends to the inside of the upper end pipe and is movably connected with the lower end of the connecting port.
Preferably, the inner wall of the vertebral body is provided with a spiral layer, the outer wall of the vertebral body is provided with installation seats, and the installation seats are distributed on the outer wall of the vertebral body in an arc array mode.
Preferably, the inner wall of the spiral layer is provided with a ceramic layer.
Preferably, a material sinking bin is arranged on the base frame, one end of the material sinking nozzle is movably connected with the outer wall of one side of the base frame, and one end of the material sinking nozzle extends into the material sinking bin.
Preferably, a fixing frame is arranged on the base frame, and the mounting seat is movably mounted on the fixing frame.
In the technical scheme, the utility model has the following beneficial effects:
the outer wall of a vortex chamber on the cyclone is provided with a feed inlet, and the cyclone is connected with the base frame through a buffer tube sleeved on the outer wall of the feed inlet, so that the cyclone can be protected;
two, the spiral layer that the centrum inner wall set up is the ceramic layer, when pottery makes spiral layer high temperature resistance, can protect the inside of centrum, be provided with the conflict wall in the bottom of centrum, it offsets with interior interlayer through the conflict wall, make interior interlayer fix the inner wall at the heavy material mouth at the during operation, put the precipitate to the heavy material storehouse that sets up in the bed frame in through heavy material mouth, under long-term use, the wearing and tearing that interior interlayer received easily are great, the cost of direct change heavy material mouth is higher, can only change the interior interlayer this moment, avoid the wasting of resources that direct change heavy material mouth caused.
It is to be understood that both the foregoing general description and the following detailed description are exemplary and explanatory only and are not restrictive of the disclosure.
This document provides an overview of various implementations or examples of the technology described in this disclosure, and is not a comprehensive disclosure of the full scope or all features of the disclosed technology.
Drawings
In order to more clearly illustrate the embodiments of the present application or technical solutions in the prior art, the drawings needed to be used in the embodiments are briefly described below, and it is obvious that the drawings in the following description are only some embodiments described in the present invention, and it is obvious for those skilled in the art to obtain other drawings based on these drawings;
FIG. 1 is a schematic diagram of an overall structure provided in an embodiment of the present invention;
FIG. 2 is a schematic view of a cyclone connection structure provided in an embodiment of the present invention;
fig. 3 is a schematic view of an inner partition installation structure provided in an embodiment of the present invention;
fig. 4 is a schematic view of an internal structure of a material depositing nozzle according to an embodiment of the present invention.
Description of reference numerals:
1. a base frame; 20. a material containing bin; 21. a stock solution bin; 3. a fixed mount; 4. a connecting pipe; 5. a vortex chamber; 6. an upper end pipe; 7. a vertebral body; 70. an abutting wall; 71. a spiral layer; 72. a mounting seat; 8. a material sinking nozzle; 9. a feed inlet; 10. an inner interlayer; 11. a chute; 51. a connecting end; 61. a connecting port; 91. a buffer tube; 100. a cyclone.
Detailed Description
In order to make the technical solutions of the present invention better understood, those skilled in the art will now describe the present invention in further detail with reference to the accompanying drawings.
As shown in fig. 1-4, a high-efficiency cyclone displacement device with a continuous boiling zone comprises a base frame 1, and is characterized in that cyclones 100 distributed in a circumferential array are arranged on the base frame 1, the cyclones 100 comprise a vortex chamber 5, a feed port 9 is arranged on the vortex chamber 5, and a buffer tube 91 is sleeved on the outer wall of the feed port 9; because of the cyclone replacement in the continuous boiling state, the outer wall of the cyclone chamber 5 on the cyclone 100 is provided with the feed port 9, and the cyclone 100 is connected with the base frame 1 through the buffer tube 91 sleeved on the outer wall of the feed port 9, so that the cyclone 100 can be protected; the cyclone 100 further comprises a cone 7 and a material sinking nozzle 8, wherein the material sinking nozzle 8 is movably mounted at the lower end of the cone 7, an inner partition 10 is movably mounted in the material sinking nozzle 8, a vertically and downwardly extending collision wall 70 is arranged at the lower end of the cone 7, and the bottom end of the collision wall 70 is abutted against the upper end of the inner partition 10; the material in the stock solution storehouse 21 that liquid set up from bed frame 1 will get into vortex chamber 5 from buffer pipe 91, the lower extreme of vortex chamber 5 is connected with centrum 7, centrum 7 divide into the upper vertebral body, well centrum and lower centrum, and the spiral layer 71 that the centrum 7 inner wall set up is the ceramic layer, when pottery makes spiral layer 71 high temperature resistance, can protect the inside of centrum 7, be provided with conflict wall 70 in the bottom of centrum 7, it offsets with interior interlayer 10 through conflict wall 70, make interior interlayer 10 fix the inner wall at material sinking mouth 8 at the during operation, put the precipitate to the material sinking storehouse that sets up in bed frame 1 in through material sinking mouth 8, in long-term use, the wearing and tearing that interior interlayer 10 easily received are great, the cost of direct change material sinking mouth 8 is higher, can only change material sinking mouth 10 this moment, avoid the wasting of resources that direct change material sinking mouth 8 caused.
The working principle of the utility model is as follows: because of the rotational flow replacement in the continuous boiling state, the outer wall of the vortex chamber 5 on the cyclone 100 is provided with the feed inlet 9, the cyclone 100 is connected with the base frame 1 through the buffer tube 91 sleeved on the outer wall of the feed inlet 9, the cyclone 100 can be protected, then the liquid enters the vortex chamber 5 from the buffer tube 91 from the raw liquid bin 21 arranged on the base frame 1, the lower end of the vortex chamber 5 is connected with the cone 7, the cone 7 is divided into an upper cone, a middle cone and a lower cone, the spiral layer 71 arranged on the inner wall of the cone 7 is a ceramic layer, the ceramic can protect the inside of the cone 7 while the spiral layer 71 resists high temperature, the bottom end of the cone 7 is provided with the abutting wall 70, the abutting wall 70 abuts against the inner partition layer 10, the inner partition layer 10 is fixed on the inner wall of the sinking nozzle 8 during the work, and the sediment is placed into the sinking bin arranged in the base frame 1 through the sinking nozzle 8, under long-term use, the inner interlayer 10 is easily worn greatly, the cost for directly replacing the sinking nozzle 8 is high, and at the moment, only the inner interlayer 10 can be replaced, so that the resource waste caused by directly replacing the sinking nozzle 8 is avoided; the cyclone 100 is fixed on a fixed frame 3 arranged on the base frame 1 through a mounting seat 72 arranged on the outer wall of the cone 7, a connecting port 61 is arranged in an upper end pipe 6, the lower end of the connecting port 61 is connected with a connecting end 51 arranged at the upper end of the vortex chamber 5, the connecting port 61 is connected with a connecting pipe 4, and separated materials enter the material containing bin 20 through the connecting pipe 4.
While certain exemplary embodiments of the present invention have been described above by way of illustration only, it will be apparent to those of ordinary skill in the art that the described embodiments may be modified in various different ways without departing from the spirit and scope of the utility model. Accordingly, the drawings and description are illustrative in nature and should not be construed as limiting the scope of the utility model.
Claims (9)
1. A high-efficiency rotational flow replacement device with a continuous boiling zone comprises a base frame (1) and is characterized in that cyclones (100) distributed in a circumferential array are arranged on the base frame (1), each cyclone (100) comprises a vortex chamber (5), a feeding hole (9) is formed in each vortex chamber (5), and a buffer tube (91) is sleeved on the outer wall of each feeding hole (9);
swirler (100) still includes centrum (7) and sediment mouth (8), sediment mouth (8) movable mounting be in the lower extreme of centrum (7), movable mounting has interior interlayer (10) in sediment mouth (8), the lower extreme of centrum (7) is provided with vertical downwardly extending's conflict wall (70), the bottom of conflict wall (70) with the upper end of interior interlayer (10) is inconsistent.
2. A high efficiency cyclone displacement apparatus with continuous boiling zone according to claim 1, wherein the sinking nozzle (8) is provided with chutes (11) distributed along the circumferential array of the inner wall, the outer wall of the inner partition layer (10) is provided with protrusions matching with the chutes (11), and the protrusions are connected with the chutes (11) in a sliding manner.
3. The high-efficiency cyclone displacement device with the continuous boiling zone as claimed in claim 1, wherein a stock solution bin (20) and a stock solution bin (21) are respectively arranged on the base frame (1), the stock solution bin (21) is positioned outside the stock solution bin (20), the cyclone (100) further comprises an upper end pipe (6), a connecting pipe (4) is arranged between the cyclone (100) and the stock solution bin (20), and the stock solution bin (21) and the cyclone (100) are connected through the buffer pipe (91).
4. A high efficiency cyclone displacement apparatus with continuous boiling zone according to claim 3 wherein one end of the connecting pipe (4) is movably connected to the upper pipe (6) and the vortex chamber (5) is movably connected to the upper pipe (6).
5. A high efficiency cyclone displacement apparatus with continuous boiling zone according to claim 4, characterized in that the upper end of the vortex chamber (5) is provided with a connection end (51), the center of the upper tube (6) is provided with a connection port (61), the connection end (51) extends to the inside of the upper tube (6) and is movably connected with the lower end of the connection port (61).
6. A high efficiency rotational flow replacement device with continuous boiling region according to claim 5, characterized in that the inner wall of the cone (7) is provided with a spiral layer (71), the outer wall of the cone (7) is provided with mounting seats (72), and the mounting seats (72) are distributed on the outer wall of the cone (7) in an arc array.
7. A high efficiency cyclonic fluid displacement apparatus having successive boiling zones as claimed in claim 6, wherein the inner walls of the spiral layers (71) are provided with a ceramic layer.
8. The high-efficiency cyclone displacement device with the continuous boiling area is characterized in that a material settling bin is arranged on the base frame (1), one end of the material settling nozzle (8) is movably connected with the outer wall of one side of the base frame (1), and one end of the material settling nozzle (8) extends into the material settling bin.
9. A high efficiency cyclone displacement apparatus with continuous boiling zone according to claim 6 wherein the base frame (1) is provided with a fixed frame (3), and the mounting seat (72) is movably mounted on the fixed frame (3).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122820894.7U CN216224891U (en) | 2021-11-17 | 2021-11-17 | High-efficient whirl replacement device with continuous boiling region |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202122820894.7U CN216224891U (en) | 2021-11-17 | 2021-11-17 | High-efficient whirl replacement device with continuous boiling region |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216224891U true CN216224891U (en) | 2022-04-08 |
Family
ID=80944121
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202122820894.7U Active CN216224891U (en) | 2021-11-17 | 2021-11-17 | High-efficient whirl replacement device with continuous boiling region |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN216224891U (en) |
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2021
- 2021-11-17 CN CN202122820894.7U patent/CN216224891U/en active Active
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20240926 Address after: 277000 North of Taizhong Road and West of Huaming Road, Economic Development Zone, Taierzhuang District, Zaozhuang City, Shandong Province Patentee after: Wantu Sirui (Zaozhuang) New Materials Co.,Ltd. Country or region after: China Address before: 211300 No. 103-29, building a, Kechuang service center, Huxin Road, modern agricultural industrial park, Gaochun District, Nanjing, Jiangsu Province Patentee before: Jiangsu wantusiri Environmental Technology Co.,Ltd. Country or region before: China |