CN218637610U - Cooling multi-pipe dust remover - Google Patents
Cooling multi-pipe dust remover Download PDFInfo
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- CN218637610U CN218637610U CN202221438014.8U CN202221438014U CN218637610U CN 218637610 U CN218637610 U CN 218637610U CN 202221438014 U CN202221438014 U CN 202221438014U CN 218637610 U CN218637610 U CN 218637610U
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- Prior art keywords
- dust
- dust removal
- removal case
- heat exchanger
- baffle
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- 239000000428 dust Substances 0.000 title claims abstract description 176
- 238000001816 cooling Methods 0.000 title claims abstract description 26
- 238000010521 absorption reaction Methods 0.000 claims abstract description 7
- 238000001179 sorption measurement Methods 0.000 claims description 10
- 238000003466 welding Methods 0.000 claims description 4
- 238000000034 method Methods 0.000 abstract description 20
- 230000000694 effects Effects 0.000 abstract description 6
- 239000007789 gas Substances 0.000 description 33
- 239000002956 ash Substances 0.000 description 25
- 230000008569 process Effects 0.000 description 16
- 238000007599 discharging Methods 0.000 description 11
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 10
- 239000003546 flue gas Substances 0.000 description 10
- 238000005192 partition Methods 0.000 description 9
- 239000000779 smoke Substances 0.000 description 9
- 238000005265 energy consumption Methods 0.000 description 6
- 238000000746 purification Methods 0.000 description 4
- 230000003068 static effect Effects 0.000 description 4
- 238000001514 detection method Methods 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 239000010882 bottom ash Substances 0.000 description 2
- 238000004887 air purification Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000003500 flue dust Substances 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 230000004941 influx Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 1
- 238000011897 real-time detection Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
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Abstract
The utility model discloses a cooling multitube dust remover, including dust removal case, supporting leg, tubular heat exchanger and intake pipe, dust removal bottom four corners department all installs the supporting leg, dust removal case a lateral wall upper end is connected with tubular heat exchanger, tubular heat exchanger bottom one side is provided with the intake pipe, the dust removal incasement is provided with the baffle, the baffle top is provided with the air-purifying chamber, the baffle below is provided with the clean room, be provided with cyclone on the baffle side by side. Has the advantages that: the utility model discloses a set up electrostatic generator and electrostatic absorption board, at the ash discharge in-process, electrostatic generator can adsorb the collection to the dust fast with the electrostatic absorption board, and then prevents that its velocity of flow is lower and the quality is lighter and adsorbed by cyclone again, guarantees the dust collection efficiency and the dust removal effect of device, improves the device practicality.
Description
Technical Field
The utility model relates to a multitube dust remover technical field specifically relates to a cooling multitube dust remover.
Background
The multi-tube dust remover is mainly used for collecting dust from boiler and industry, and is composed of several cyclones combined in a sealed box for removing dust from fume.
Present cooling multi-tube dust remover separates flue gas and dust through cyclone in the use, make the dust rely on self gravity to discharge through the ash removal fill, but because cyclone's ash discharge mouth and ash removal fill have certain distance, simultaneously because the dust quality is lighter, and then at the ash removal in-process, the dust can lead to partial dust to permeate in the dust removal room because the velocity of flow is lower, and then lead to it to be collected by cyclone again, influence the dust collection efficiency of device, reduce the device practicality, furthermore, present cooling multi-tube dust remover is in the use because can't detect the flue gas volume of influx dust removal incasement, and then lead to the device all to throw the cyclone all the time and use to remove dust the flue gas, lead to the energy consumption of device great, reduce the device functionality.
SUMMERY OF THE UTILITY MODEL
Technical problem to be solved
In order to overcome the prior art not enough, a cooling multi-tube dust remover is provided, the problem that the existing cooling multi-tube dust remover separates smoke and dust through a cyclone dust remover in the using process, the dust is discharged through an ash discharge hopper by means of self gravity, but the ash discharge port of the cyclone dust remover has a certain distance with the ash discharge hopper, meanwhile, the dust quality is light, and further in the ash discharge process, the dust can be diffused into a dust removing chamber due to the fact that the flow rate is low, and further the dust can be collected by the cyclone dust remover again, the dust removal efficiency of the device is influenced, the practicability of the device is reduced, the smoke amount flowing into a dust removing box can not be detected in the using process of the existing cooling multi-tube dust remover, and further the device is enabled to throw all the cyclone dust remover to remove dust of the smoke all the time, the energy consumption of the device is large, and the functionality of the device is reduced is solved.
(II) technical scheme
The utility model discloses a following technical scheme realizes: the utility model provides a cooling multitube dust remover, including dust removal case, supporting leg, tubular heat exchanger and intake pipe, dust removal bottom four corners department all installs the supporting leg, dust removal case lateral wall upper end is connected with tubular heat exchanger, tubular heat exchanger bottom one side is provided with the intake pipe, the dust removal incasement is provided with the baffle, the baffle top is provided with the air-purifying chamber, the baffle below is provided with the clean room, be provided with cyclone on the baffle side by side, cyclone's quantity has threely, dust removal bottom is provided with the dust hopper, dust removal case another lateral wall upper end is provided with the blast pipe, be provided with the electrostatic absorption board on the dust hopper inner wall, be provided with the electrostatic generator on the dust hopper lateral wall, be provided with gas flow sensor on tubular heat exchanger's the gas outlet, be provided with the display screen on the gas flow sensor, be provided with operating panel on the case of department.
Further, the tubular heat exchanger with the dust removal case passes through bolted connection, the intake pipe with the tubular heat exchanger passes through bolted connection.
Through adopting above-mentioned technical scheme, the flue gas warp the intake pipe gets into tubular heat exchanger carries out the heat transfer cooling, and the flue gas after the cooling gets into the dust removal incasement removes dust.
Further, the baffle with the dust removal case welding, the air-purifying chamber and the dust removal chamber all take shape in the dust removal incasement portion.
Through adopting above-mentioned technical scheme, the baffle will dust removal incasement portion divide into the air-purifying chamber and dust removal chamber two parts.
Furthermore, the cyclone dust collector is connected with the partition plate through screws, the ash discharge hopper is welded with the dust removal box, one end of the ash discharge hopper extends into the interior of the dust removal box, and the exhaust pipe is welded with the dust removal box.
By adopting the technical scheme, the cyclone dust collector adsorbs the flue gas in the dust removal chamber to remove dust in the dust removal chamber, and in the dust removal process, the dust is discharged through the bottom ash discharge port and finally passes through the ash discharge hopper discharge device, and the gas after dust removal is discharged into the air purification chamber through the top end and finally is discharged through the exhaust pipe.
Furthermore, the electrostatic absorption plate is connected with the ash discharge hopper through screws, the electrostatic generator is electrically connected with the electrostatic absorption plate, and the electrostatic generator is connected with the ash discharge hopper through screws.
Through adopting above-mentioned technical scheme, at the ash discharge in-process, the electrostatic generator with the electrostatic absorption board can adsorb the collection to the dust fast, and then prevents that its velocity of flow is lower and the quality is lighter and quilt again cyclone adsorbs, guarantees the dust collection efficiency and the dust removal effect of device, improves the device practicality.
Furthermore, the gas flow sensor is connected with the tubular heat exchanger through a flange, and the display screen is electrically connected with the gas flow sensor.
By adopting the technical scheme, in the air inlet process, the gas flow sensor detects the flow of gas in real time and displays the detection data through the display screen, and the number of the cyclone separators which are put into the gas flow sensor is controlled and determined by workers according to the detection data, so that the whole device is prevented from being put into the gas flow sensor all the time, the energy consumption of the device is saved, and the functionality of the device is improved.
Further, the operation panel is electrically connected with the electrostatic generator, the cyclone dust collector and the gas flow sensor.
Through the technical scheme, the operation panel controls the operation of the device.
(III) advantageous effects
Compared with the prior art, the utility model, following beneficial effect has:
1. in order to solve the problems that the smoke and dust are separated by a cyclone dust collector in the use process of the existing cooling multi-tube dust collector, the dust is discharged by a dust discharging hopper by means of the gravity of the dust, but the dust discharging port of the cyclone dust collector has a certain distance with the dust discharging hopper, and meanwhile, the dust quality is light, so that in the dust discharging process, part of dust can be diffused in a dust removing chamber due to low flow velocity of the dust, and then the dust is collected by the cyclone dust collector again, the dust removing efficiency of the device is influenced, and the practicability of the device is reduced, the utility model discloses a static generator and a static adsorption plate are arranged, in the dust discharging process, the static generator and the static adsorption plate can quickly adsorb and collect the dust, so that the dust is prevented from being adsorbed by the cyclone dust collector again due to low flow velocity and light mass, the dust removing efficiency and the dust removing effect of the device are ensured, and the practicability of the device is improved;
2. because can't detect the flue gas volume of flowing into the dust removal incasement for solving current cooling multitube dust remover in the use, and then lead to the device all to throw all the time with cyclone and use to remove dust the flue gas, the energy consumption that leads to the device is great, reduces the functional problem of device, the utility model discloses a set up gas flow sensor and display screen, at the in-process of admitting air, gas flow sensor real-time detection gas's flow and will detect data and pass through the display screen demonstration, the staff controls the quantity of surely throwing into cyclone according to the data that detect, avoids all the investments all the time, and saving device's energy consumption improves the device functionality.
Drawings
FIG. 1 is a front view of a multi-tube cooling dust collector of the present invention;
FIG. 2 is a main sectional view of a dust box in the multi-tube cooling dust collector of the present invention;
fig. 3 is an enlarged view of a position a in the multi-tube cooling dust collector of the present invention.
The reference numerals are illustrated below:
1. supporting legs; 2. an ash discharge hopper; 3. an operation panel; 4. an air inlet pipe; 5. a tubular heat exchanger; 6. a gas flow sensor; 7. a display screen; 8. a dust removal box; 9. an exhaust pipe; 10. a gas purification chamber; 11. a partition plate; 12. a cyclone dust collector; 13. a dust chamber; 14. an electrostatic generator; 15. and (4) an electrostatic adsorption plate.
Detailed Description
In order to make the technical solution and advantages of the present invention more clearly understood, the present invention is further described in detail below with reference to the accompanying drawings and embodiments. It should be understood that the specific embodiments described herein are for purposes of illustration only and are not intended to limit the invention.
As shown in figures 1-3, the cooling multi-tube dust collector in the embodiment comprises a dust collection box 8, supporting legs 1, a tube heat exchanger 5 and an air inlet tube 4, wherein the supporting legs 1 are all installed at four corners of the bottom end of the dust collection box 8, the tube heat exchanger 5 is connected with the upper end of one side wall of the dust collection box 8, the air inlet tube 4 is arranged at one side of the bottom end of the tube heat exchanger 5, flue gas enters the tube heat exchanger 5 through the air inlet tube 4 for heat exchange and cooling, the cooled flue gas enters the dust collection box 8 for dust collection, a partition plate 11 is arranged in the dust collection box 8, a gas purification chamber 10 is arranged above the partition plate 11, a dust collection chamber 13 is arranged below the partition plate 11, the partition plate 11 divides the interior of the dust collection box 8 into two parts, namely a gas purification chamber 10 and a dust collection chamber 13, cyclone dust collectors 12 are arranged on the partition plate 11 side by side, three cyclone dust collectors 12 are arranged at the bottom end of the dust collection box 8, an exhaust pipe 2 is arranged at the upper end of the other side wall of the dust collection box 8, the cyclone dust collector 12 absorbs the smoke in the dust removing chamber 13 and removes the dust in the interior thereof, in the dust removing process, the dust is discharged through the bottom ash discharging port and finally passes through the ash discharging hopper 2 discharging device, the gas after dust removing is discharged into the air purifying chamber 10 through the top end and finally is discharged through the exhaust pipe 9, the inner wall of the ash discharging hopper 2 is provided with the electrostatic adsorption plate 15, the outer side wall of the ash discharging hopper 2 is provided with the electrostatic generator 14, in the ash discharging process, the electrostatic generator 14 and the electrostatic adsorption plate 15 can quickly adsorb and collect the dust, so as to prevent the dust from being adsorbed by the cyclone dust collector 12 again due to low flow velocity and light weight, the dust removing efficiency and the dust removing effect of the device are ensured, the gas flow sensor 6 is arranged on the gas outlet of the tubular heat exchanger 5, the display 7 is arranged on the gas flow sensor 6, in the gas inlet process, the gas flow sensor 6 detects the flow of the gas in real time and displays the detected data through the display 7, the staff controls the quantity of confirming the cyclone that drops into according to the data that detect, avoids all dropping into all the time, and the energy consumption of saving device is provided with operating panel 3 on the dust box 8, and operating panel 3 controlling means's work.
As shown in fig. 1 to 3, in this embodiment, the tubular heat exchanger 5 is connected to the dust removing box 8 by bolts, the air inlet pipe 4 is connected to the tubular heat exchanger 5 by bolts, the partition plate 11 is welded to the dust removing box 8, the air purifying chamber 10 and the dust removing chamber 13 are both formed inside the dust removing box 8, the cyclone 12 is connected to the partition plate 11 by screws, the ash discharge hopper 2 is welded to the dust removing box 8, one end of the ash discharge hopper 2 extends into the dust removing box 8, and the exhaust pipe 9 is welded to the dust removing box 8.
As shown in fig. 1 to fig. 3, in this embodiment, the electrostatic adsorption plate 15 is connected to the ash bucket 2 by screws, the electrostatic generator 14 is electrically connected to the electrostatic adsorption plate 15, the electrostatic generator 14 is connected to the ash bucket 2 by screws, the gas flow sensor 6 is connected to the tubular heat exchanger 5 by flanges, the display 7 is electrically connected to the gas flow sensor 6, and the operation panel 3 is electrically connected to the electrostatic generator 14, the cyclone 12, and the gas flow sensor 6.
The specific implementation process of this embodiment is as follows: the device is connected with corresponding pipelines outside and connected with an external power supply, then the device works through an operation panel 3, in the working process of the device, smoke enters a tubular heat exchanger 5 through an air inlet pipe 4 to carry out heat exchange and temperature reduction, the cooled smoke enters a dust removal box 8 to carry out dust removal, when the smoke enters the dust removal box 8, smoke in a dust removal chamber 13 is adsorbed by a cyclone dust collector 12 to enter the interior of the dust removal chamber to carry out dust removal, in the dust removal process, dust is discharged through a bottom dust discharge port and finally passes through an ash discharge hopper 2 discharge device, the dedusted gas is discharged into a gas purification chamber 10 through the top end and finally is discharged through an exhaust pipe 9, in the ash discharge process, an electrostatic generator 14 and an electrostatic adsorption plate 15 can quickly adsorb and collect the dust, further, the dust is prevented from being adsorbed by the cyclone dust collector 12 again due to low flow rate and light weight, the dust removal efficiency and the dust removal effect of the device are ensured, in addition, the air inlet process, a gas flow sensor 6 detects the flow of the gas and displays the detection data to determine the quantity of the cyclone separator according to control, the investment of the quantity of the gas is avoided, and the investment of the device is all the investment is saved.
The previous description of the disclosed embodiments is provided to enable any person skilled in the art to make or use the present invention. Various modifications to these embodiments will be readily apparent to those skilled in the art, and the generic principles defined herein may be applied to other embodiments without departing from the spirit or scope of the invention. Thus, the present invention is not intended to be limited to the embodiments shown herein but is to be accorded the widest scope consistent with the principles and novel features disclosed herein.
Claims (7)
1. The utility model provides a cooling multitube dust remover which characterized in that: including dust removal case (8), supporting leg (1), tubular heat exchanger (5) and intake pipe (4), dust removal case (8) bottom four corners department all installs supporting leg (1), dust removal case (8) a lateral wall upper end is connected with tubular heat exchanger (5), tubular heat exchanger (5) bottom one side is provided with intake pipe (4), be provided with baffle (11) in dust removal case (8), baffle (11) top is provided with clean air chamber (10), baffle (11) below is provided with clean room (13), be provided with cyclone (12) on baffle (11) side by side, the quantity of cyclone (12) has threely, dust removal case (8) bottom is provided with dust exhaust hopper (2), dust removal case (8) another lateral wall upper end is provided with blast pipe (9), be provided with electrostatic absorption board (15) on dust exhaust hopper (2) inner wall, be provided with electrostatic generator (14) on dust exhaust hopper (2) the lateral wall, be provided with gas flow sensor (6) on the gas flow sensor (6), be provided with display panel (7) on dust removal case (3).
2. A cooling manifold as claimed in claim 1, wherein: the tubular heat exchanger (5) is connected with the dust removal box (8) through bolts, and the air inlet pipe (4) is connected with the tubular heat exchanger (5) through bolts.
3. A cooling manifold as defined in claim 1 wherein: baffle (11) with dust removal case (8) welding, air-purifying chamber (10) and dust removal chamber (13) all take shape in inside dust removal case (8).
4. A cooling manifold as claimed in claim 1, wherein: cyclone (12) with baffle (11) pass through the screw connection, dust exhaust bucket (2) with dust removal case (8) welding, dust exhaust bucket (2) one end extends to inside dust removal case (8), blast pipe (9) with dust removal case (8) welding.
5. A cooling manifold as defined in claim 1 wherein: the electrostatic adsorption plate (15) is connected with the ash discharge hopper (2) through screws, the electrostatic generator (14) is electrically connected with the electrostatic adsorption plate (15), and the electrostatic generator (14) is connected with the ash discharge hopper (2) through screws.
6. A cooling manifold as defined in claim 1 wherein: the gas flow sensor (6) is connected with the tubular heat exchanger (5) through a flange, and the display screen (7) is electrically connected with the gas flow sensor (6).
7. A cooling manifold as claimed in claim 1, wherein: the operation panel (3) is electrically connected with the electrostatic generator (14), the cyclone dust collector (12) and the gas flow sensor (6).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221438014.8U CN218637610U (en) | 2022-06-09 | 2022-06-09 | Cooling multi-pipe dust remover |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202221438014.8U CN218637610U (en) | 2022-06-09 | 2022-06-09 | Cooling multi-pipe dust remover |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN218637610U true CN218637610U (en) | 2023-03-17 |
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ID=85489239
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202221438014.8U Active CN218637610U (en) | 2022-06-09 | 2022-06-09 | Cooling multi-pipe dust remover |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN218637610U (en) |
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2022
- 2022-06-09 CN CN202221438014.8U patent/CN218637610U/en active Active
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20240827 Address after: 271000 north of luyigu street, Ningyang Economic Development Zone, Tai'an City, Shandong Province, west of Huapu boiler company and east of Heyi heavy industry company Patentee after: Tai'an Huanyu Dedusting Technology Co.,Ltd. Country or region after: China Address before: No. 2517, Building 8, No. 69, Zengcheng Avenue, Licheng Street, Zengcheng District, Guangzhou City, Guangdong Province, 511300 Patentee before: Guangzhou Dongrun Energy Co.,Ltd. Country or region before: China |