CN211384172U - Multi-pipe cyclone adjustable separator - Google Patents
Multi-pipe cyclone adjustable separator Download PDFInfo
- Publication number
- CN211384172U CN211384172U CN201922066637.1U CN201922066637U CN211384172U CN 211384172 U CN211384172 U CN 211384172U CN 201922066637 U CN201922066637 U CN 201922066637U CN 211384172 U CN211384172 U CN 211384172U
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- Prior art keywords
- chamber
- cyclone
- air inlet
- cyclones
- exhaust
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- 238000000926 separation method Methods 0.000 claims abstract description 26
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000011148 porous material Substances 0.000 claims abstract description 5
- 230000002457 bidirectional effect Effects 0.000 claims description 2
- 238000007789 sealing Methods 0.000 claims description 2
- 239000007788 liquid Substances 0.000 description 7
- 239000007787 solid Substances 0.000 description 4
- 239000000428 dust Substances 0.000 description 3
- 230000008901 benefit Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 230000009471 action Effects 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 238000011143 downstream manufacturing Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 210000001503 joint Anatomy 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
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Abstract
The utility model discloses a multi-cyclone adjustable separator, which comprises a tank body and a plurality of cyclones, wherein the tank body is internally divided into an exhaust chamber, a separation air inlet chamber and a collection chamber from top to bottom in sequence through an upper tube plate and a lower tube plate; the plurality of cyclones are arranged in the separation air inlet chamber, exhaust ports of the cyclones extend to the exhaust chamber, and collecting ports of the cyclones extend to the collecting chamber; the separation air inlet chamber is provided with an air inlet, and the air inlet is provided with a pore plate gas distributor; the upper end of the exhaust chamber is connected with an upper cover with an exhaust port through a flange, and the lower end of the collection chamber is connected with a lower cover with a collection port through a flange.
Description
Technical Field
The utility model relates to an industrial gas clarification plant field especially relates to an adjustable separator of multitube whirlwind.
Background
In the prior art of industrial gas purification, liquid and dust removal and separation, the cyclone technology is mainly adopted for cyclone separation with a simple tangential inlet, as shown in figure 1, the structural device has low separation precision and cannot meet the requirements of a separator; the operation elasticity ratio is small and unadjustable, the influence of air flow fluctuation is large, the stability and the reliability are poor, and the safe and stable operation of downstream processes and equipment is affected; because of the structure problem, the container has large tangential holes, the container can only be used for dust removal and liquid removal under the working conditions of low pressure or normal pressure, and under the working conditions of high pressure, the container cannot be used due to the strength problem and the safety.
SUMMERY OF THE UTILITY MODEL
The utility model provides a not enough to prior art, the utility model provides an adjustable separator of multitube whirlwind aims at solving current tangential cyclone and is not suitable for high-pressure environment, and the separation precision is not high, inefficiency, and operation elasticity is little can not be adjusted, poor stability's problem.
In order to achieve the above object, the utility model provides a following technical scheme: a multi-pipe cyclone adjustable separator comprises a tank body and a plurality of cyclones, wherein the tank body is internally divided into an exhaust chamber, a separation air inlet chamber and a collection chamber from top to bottom in sequence through an upper tube plate and a lower tube plate; the plurality of cyclones are arranged in the separation air inlet chamber, exhaust ports of the cyclones extend to the exhaust chamber, and collecting ports of the cyclones extend to the collecting chamber;
the separation air inlet chamber is provided with an air inlet, and the air inlet is provided with a pore plate gas distributor; the upper end of the exhaust chamber is connected with an upper cover with an exhaust port through a flange, and the lower end of the collection chamber is connected with a lower cover with a collection port through a flange.
Further, still include the installing support that is used for supporting the jar body.
Furthermore, a sealing ring is padded at the butt joint of the flanges.
Preferably, the cyclone is arranged on the lower tube plate and the upper tube plate.
Preferably, the cyclone is composed of a conical cyclone separation part, a tangential inlet part and a gas lifting exhaust pipe, the tangential inlet part is arranged on the side surface of the upper part of the conical cyclone separation part, and the lower end of the gas lifting exhaust pipe extends below the tangential inlet part.
Preferably, the tangential inlet section is a centrosymmetric bidirectional tangential inlet section.
The utility model has the advantages that: the container is not provided with a large tangential opening and can be used in a high-pressure process section; the separation efficiency is high, and the operation elasticity is big, can carry out nimble regulation, greatly reduced investment and running cost, improve the economic benefits of enterprise, the operation is stable, long service life.
Drawings
Fig. 1 is a schematic structural diagram of a conventional apparatus.
Fig. 2 is a schematic structural diagram of the present invention.
Fig. 3 is a schematic structural view of the cyclone.
Fig. 4 is a top view of the cyclone.
Detailed Description
As shown in fig. 2, 3 and 4, the multi-cyclone adjustable separator comprises a tank body and a plurality of cyclones 2, wherein the tank body is internally divided into an exhaust chamber 5, a separation air inlet chamber 6 and a collection chamber 7 from top to bottom by an upper tube plate 4 and a lower tube plate 1; the plurality of cyclones 2 are arranged in the separation air inlet chamber 6, the exhaust ports of the cyclones 2 extend to the exhaust chamber 5, and the collecting ports of the cyclones 2 extend to the collecting chamber 7;
the separation air inlet chamber 6 is provided with an air inlet, and the air inlet is provided with a pore plate gas distributor 3; the upper end of the exhaust chamber 5 is connected with an upper cover with an exhaust port through a flange 8, and the lower end of the collection chamber 7 is connected with a lower cover with a collection port through a flange 8.
The exhaust chamber 5 and the collection chamber 7 of the utility model can be made into an openable flange 8 structure, when the air flow is in minimum air flow operation, the exhaust chamber 5 and the collection chamber 7 are respectively opened, the upper and lower ports of a certain amount of cyclones 2 are respectively blocked by a plug or a cover which is designed in a matching way, and the air flow can normally operate under the working condition of minimum air flow; when the cyclone separator needs to operate under the working condition of large air quantity, the cyclone separator can normally operate by opening the upper and lower ports of the cyclone separator 2; can flexibly adjust according to different gas volumes without changing the structure of equipment or redesigning and manufacturing new equipment, thereby reducing the investment and the operation cost of enterprises.
Meanwhile, the distributor 3 with the pore plate is arranged at the air inlet, the distributor 3 can select a disc-shaped distributor which avoids the air lifting exhaust pipe 23, so that the mixed medium is uniformly filled in the whole separation air inlet chamber 6, the uneven air inlet of the internal rotor 2 is avoided, the air inlet of some cyclone sub-units is too much under the condition of different working conditions, the flow speed is high and even exceeds the upper limit of the elasticity ratio of the cyclone sub-units 2, the air inlet of some cyclone sub-units 2 is too small to reach the due air inlet amount, the flow speed is too low, and the separation effect and the efficiency of the whole separator are improved. So that the medium in the whole gas inlet chamber 6 of the separator uniformly and orderly flows from top to bottom and then enters the cyclone 2.
The principle of the cyclone is as follows: when gas medium containing liquid and dust particles enters the cyclone subunit from the A, B port in a tangential direction, then the medium rotates at high speed in the cyclone separation area part 21, because the gas, the liquid and the solid have different densities, so the gas and the solid have different centrifugal forces, the liquid and the solid have larger densities, the obtained larger inertial centrifugal force is thrown onto the inner wall of the cyclone separation area part 21, liquid drops are continuously thrown onto the wall, and the solid particles flow downwards along the inner wall due to the action of gravity and then are discharged from a lower port; in the center of the cyclone separation section 21, since the gas rotates at a high speed to form a low pressure region, the gas having a low density after separation is discharged from the gas-lift gas discharge pipe 23 in a swirling flow with a low center pressure, thereby completing the solid-liquid separation of the gas.
The above description is only exemplary of the present invention and should not be taken as limiting the scope of the present invention, as any modification, equivalent replacement or improvement made within the spirit and principle of the present invention should be included in the present invention.
Claims (6)
1. A multi-cyclone adjustable separator comprises a tank body and a plurality of cyclones (2), and is characterized in that the tank body is sequentially divided into an exhaust chamber (5), a separation air inlet chamber (6) and a collection chamber (7) from top to bottom through an upper tube plate (4) and a lower tube plate (1); the plurality of cyclones (2) are arranged in the separation air inlet chamber (6), the exhaust ports of the cyclones (2) extend to the exhaust chamber (5), and the collecting ports of the cyclones (2) extend to the collecting chamber (7);
the separation air inlet chamber (6) is provided with an air inlet, and the air inlet is provided with a pore plate gas distributor (3); the upper end of the exhaust chamber (5) is connected with an upper cover with an exhaust port through a flange (8), and the lower end of the collection chamber (7) is connected with a lower cover with a collection port through a flange (8).
2. A multi-cyclone adjustable separator according to claim 1, further comprising a mounting bracket for supporting the vessel.
3. A multi-cyclone adjustable separator according to claim 1, wherein the abutment of the flanges (8) is gasketed with a sealing ring.
4. A multi-cyclone adjustable separator according to claim 1, wherein the cyclones (2) are mounted in a lower tube sheet (1) and an upper tube sheet (4).
5. A multi-cyclone adjustable separator as claimed in claim 1, wherein the cyclone (2) is composed of a conical cyclone separating part (21), a tangential inlet part (22) and a lift gas exhaust pipe (23), the upper side of the conical cyclone separating part (21) is provided with the tangential inlet part (22), and the lower end of the lift gas exhaust pipe (23) extends below the tangential inlet part (22).
6. A multi-cyclone adjustable separator according to claim 5, wherein the tangential inlet section (22) is a centrosymmetric bidirectional tangential inlet section.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922066637.1U CN211384172U (en) | 2019-11-26 | 2019-11-26 | Multi-pipe cyclone adjustable separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201922066637.1U CN211384172U (en) | 2019-11-26 | 2019-11-26 | Multi-pipe cyclone adjustable separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211384172U true CN211384172U (en) | 2020-09-01 |
Family
ID=72218413
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201922066637.1U Expired - Fee Related CN211384172U (en) | 2019-11-26 | 2019-11-26 | Multi-pipe cyclone adjustable separator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN211384172U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114984673A (en) * | 2022-04-29 | 2022-09-02 | 中冶长天国际工程有限责任公司 | Dust remover and dust removing method |
-
2019
- 2019-11-26 CN CN201922066637.1U patent/CN211384172U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114984673A (en) * | 2022-04-29 | 2022-09-02 | 中冶长天国际工程有限责任公司 | Dust remover and dust removing method |
| CN114984673B (en) * | 2022-04-29 | 2023-09-01 | 中冶长天国际工程有限责任公司 | Dust remover and dust removing method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20200901 |