CN104645768B - A kind of Wet type cyclone dust arrester - Google Patents
A kind of Wet type cyclone dust arrester Download PDFInfo
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- CN104645768B CN104645768B CN201510069283.XA CN201510069283A CN104645768B CN 104645768 B CN104645768 B CN 104645768B CN 201510069283 A CN201510069283 A CN 201510069283A CN 104645768 B CN104645768 B CN 104645768B
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Abstract
The present invention relates to a kind of dust arrester, particularly relate to a kind of Wet type cyclone dust arrester, belong to technical field of environment protection equipment, described Wet type cyclone dust arrester includes being sequentially connected conditioning Tower, gas-liquid coupler, Venturi tube and the cyclone separator connect, it is provided with spray equipment in described conditioning Tower, ash-laden gas enters from conditioning Tower, neat stress is discharged from cyclone separator, compared with prior art, the present invention is by being combined several dust collection methods, and reasonable in design is compact, takes up an area little, cost is low, and installation and repairing is convenient；Dust removal efficiency is up to 99.9%；Equipment loss is little, and service life is long.
Description
Technical field
The present invention relates to a kind of dust arrester, particularly relate to a kind of Wet type cyclone dust arrester, belong to technical field of environment protection equipment.
Background technology
At present, domestic dedusting technology is mainly electric precipitation, bag dedusting, wet dust removal, dust removal with machine etc., and wherein electricity removes
Dirt and bag dedusting are respectively provided with the shortcomings such as occupation of land is big, cost is high, operating cost is high；Equipment is easily caused corrosion by wet dust removal, loss
Greatly；The efficiency of dust collection of dust removal with machine is the highest.In order to make up the defect of various method self, have and several method is used in combination with
Situation, but the cost combining the cleaner of several method in prior art is high, and structure is complicated, installs inconvenience, maintenance difficult,
Operating cost is high.
The patent of Application No. 97225432.3 discloses a kind of Wet desulfurization cyclone dust collectors, and its structure includes whirlwind, venturi
Pipe and wet dust collector, although it combines several cleaner, but it arranges fountain head at the contraction section of Venturi tube, makes literary composition
The loss of venturi is accelerated, and needs in actual applications to regularly replace Venturi tube, and use cost is higher；Meanwhile, this technology
Sewage disposal burden weight, the operating cost of whole device is high.
Summary of the invention
It is an object of the invention to for the deficiencies in the prior art, it is provided that a kind of Wet type cyclone dust arrester.
The present invention solves the technical scheme of problem: provide a kind of Wet type cyclone dust arrester, including be sequentially connected connect conditioning Tower,
Gas-liquid coupler, Venturi tube and cyclone separator；Described conditioning Tower is provided with ash-laden gas entrance and spray equipment, described spray
Device includes water inlet pipe, control valve and some hydraulic spray nozzles；Described gas-liquid coupler includes some sheathed water conservancy diversion being fixed together
Cylinder and the multiple blades being arranged between adjacent guide cylinder；Described Venturi tube includes contraction section, throat and diffuser；Described rotation
Wind separator includes cyclone inlet, cyclone separator body, ash cylinder, ash discharging hole, central row trachea, filter and clean
Exhanst gas outlet；The contraction section of described Venturi tube is connected with gas-liquid coupler, the diffuser of described Venturi tube and cyclone separator
Entrance is connected.
Further, described some hydraulic spray nozzles for be uniformly placed equidistant, the opening direction of described hydraulic spray nozzle the most horizontally toward gas
Liquid bonder, i.e. consistent with air-flow inflow direction, advantageously ensure that dusty gas is still unsaturated gas, it is to avoid supersaturated gas
In dust adhesion downstream equipment on and cause inconvenience removal.
Further, the blade of described gas-liquid coupler is the most radially uniform is in tilted layout.
Further, described cyclone separator is the reverse-flow cylinder cone separator with tangential inlet.
Further, described cyclone separator body includes that shell portion and conical section, described conical section are positioned at described cylinder
The lower section of part, and be combined as a whole.
Preferably, the height of described cyclone separator body is 4～4.5:1 with the ratio of the diameter of its shell portion, is conducive to carrying
High efficiency of dust collection.
Further, the lower section of described conical section is ash cylinder, and the end of described ash cylinder is ash discharging hole.
Preferably, the lower edge of described central row trachea and described cyclone inlet is lower along concordant.
Further, the top of the centrally disposed exhaustor of described filter, the lower section of neat stress outlet.
Further, the internal structure of described dust arrester all applies anticorrosive coat, prevents the dusty gas corrosion to equipment.
Dust arrester of the present invention provides the benefit that:
1. described in, dust arrester reasonable in design is compact, takes up an area little, and cost is low, and installation and repairing is convenient；
2. dust arrester described in by several dust collection methods are combined, especially conditioning Tower, gas-liquid coupler, Venturi tube
With the orderly combination of cyclone separator, chalk dust removing, dust removal efficiency is conducive to be up to 99.9%；
3. by humidification ring layout is designed humidifying equipment, and anticorrosion before Venturi tube rather than in Venturi tube
The design of layer, makes equipment loss little, and service life is long.
Accompanying drawing explanation
Fig. 1 is the structural representation of Wet type cyclone dust arrester of the present invention.
Fig. 2 is the left view of the gas-liquid coupler of Wet type cyclone dust arrester of the present invention.
In figure: 1-conditioning Tower, 11-ash-laden gas entrance, 12-spray equipment, 121-water inlet pipe, 122-control valve, 123-water smoke
Nozzle；2-gas-liquid coupler, 21-guide shell, 22-blade；3-Venturi tube, 31-contraction section, 32-throat, 33-diffuser；
4-cyclone separator, 41-cyclone inlet, 42-cyclone separator body, 43-ash cylinder, 44-ash discharging hole, the aerofluxus of 45-center
Pipe, the outlet of 46-filter, 47-neat stress.
Detailed description of the invention
The present invention is described further below in conjunction with the accompanying drawings.
As it is shown in figure 1, Wet type cyclone dust arrester of the present invention include being sequentially connected connect conditioning Tower 1, gas-liquid coupler 2, Wen Qiu
In pipe 3 and cyclone separator 4；Described conditioning Tower 1 is provided with ash-laden gas entrance 11 and spray equipment 12, described spray equipment
12 include water inlet pipe 121, control valve 122 and some hydraulic spray nozzles 123；Described gas-liquid coupler 2 includes some sheathed fixing
Guide shell 21 together and the multiple blades 22 being arranged between adjacent guide cylinder 21；Described Venturi tube 3 includes contraction section
31, throat 32 and diffuser 33；Described cyclone separator 4 include cyclone inlet 41, cyclone separator body 42,
Ash cylinder 43, ash discharging hole 44, central row trachea 45, filter 46 and neat stress outlet 47；The contraction section of described Venturi tube 3
31 are connected with gas-liquid coupler 2, and the diffuser 33 of described Venturi tube 3 is connected with cyclone inlet 41.
Described some hydraulic spray nozzles 123 for be uniformly placed equidistant, the opening direction the most horizontally toward gas-liquid of described hydraulic spray nozzle 123
Bonder 2, i.e. consistent with air-flow inflow direction.
The blade 22 of described gas-liquid coupler 2 is the most radially uniform to be in tilted layout.
Described cyclone separator 4 is the reverse-flow cylinder cone separator with tangential inlet.
Described cyclone separator body 42 includes that shell portion and conical section, described conical section are positioned under described shell portion
Side, and be combined as a whole.
The height of described cyclone separator body 42 is 4～4.5:1 with the ratio of the diameter of shell portion, is conducive to improving dedusting effect
Rate.
The lower section of described conical section is ash cylinder 43, and the end of described ash cylinder 43 is ash discharging hole 44.
The lower edge of described central row trachea 45 is lower along concordant with described cyclone inlet 41.
The top of the described centrally disposed exhaustor of filter 46 45, the lower section of neat stress outlet 47.
The all devices in inside of described dust arrester, all apply anticorrosive coat, prevent the dusty gas corrosion to equipment.
The work process of Wet type cyclone dust arrester of the present invention is as follows:
Dusty gas enters conditioning Tower by ash-laden gas entrance, and the hydraulic spray nozzle in conditioning Tower sprays into wellatomized in gas
Water；Dusty gas after humidification, through gas-liquid coupler, increases the mixing homogeneity of atomized water further, and dust is in gas-liquid simultaneously
Bonder blade surface can clash into, assemble so that particle diameter is increased；Then dusty gas enters Venturi tube, at venturi
In pipe, owing to the flow area of gas reduces, the volume of gas is compressed, the powder during gas compression, in gas
Dirt is collided, is bondd, particle diameter increases further, due to the work of water sprinkling for better material moisture of upstream so that the adhesiveness of dust increases, thus
It is more easy to be agglomerated into the dust that particle diameter is bigger；The dusty gas of flow through venturi compression tangentially enters cyclone separator, and air-flow is along cylinder
Moving downward twist, grit is being thrown toward wall under the influence of centrifugal force, falls to entering ash cylinder along wall；The gas rotated
Stream to center flow at cyclone separator body contract, is upwardly formed secondary vortex flow and enters filter through central row trachea, pass through
Gas after filter is discharged through neat stress outlet.
The present invention is not limited to above-mentioned embodiment, in the case of without departing substantially from the flesh and blood of the present invention, those skilled in the art
It is contemplated that any deformation, improve, replace and each fall within protection scope of the present invention.
Claims (8)
1. a Wet type cyclone dust arrester, it is characterised in that include being sequentially connected conditioning Tower, gas-liquid coupler, Venturi tube and the cyclone separator connect；Described conditioning Tower is provided with ash-laden gas entrance and spray equipment, and described spray equipment includes water inlet pipe, control valve and some hydraulic spray nozzles；Described gas-liquid coupler includes some sheathed guide shells being fixed together and the multiple blades being arranged between adjacent guide cylinder；Described Venturi tube includes contraction section, throat and diffuser；Described cyclone separator includes cyclone inlet, cyclone separator body, ash cylinder, ash discharging hole, central row trachea, filter and neat stress outlet；Described gas-liquid coupler is arranged on spray equipment downstream direction, described some hydraulic spray nozzles are arranged in ash-laden gas entrance, described some hydraulic spray nozzles are for be uniformly placed equidistant, the opening direction of described hydraulic spray nozzle the most horizontally toward gas-liquid coupler, the contraction section of described Venturi tube is connected with gas-liquid coupler, the diffuser of described Venturi tube is connected with cyclone inlet, and the height of described cyclone separator body is 4～4.5:1 with the ratio of the diameter of its shell portion.
Wet type cyclone dust arrester the most according to claim 1, it is characterised in that the blade of described gas-liquid coupler is the most radially uniform to be in tilted layout.
Wet type cyclone dust arrester the most according to claim 1, it is characterised in that described cyclone separator is the reverse-flow cylinder cone separator with tangential inlet.
Wet type cyclone dust arrester the most according to claim 1, it is characterised in that described cyclone separator body includes that shell portion and conical section, described conical section are positioned at the lower section of described shell portion, and are combined as a whole.
Wet type cyclone dust arrester the most according to claim 4, it is characterised in that the lower section of described conical section is ash cylinder, the end of described ash cylinder is ash discharging hole.
Wet type cyclone dust arrester the most according to claim 1, it is characterised in that the lower edge of described central row trachea is lower along concordant with described cyclone inlet.
Wet type cyclone dust arrester the most according to claim 1, it is characterised in that the top of the centrally disposed exhaustor of described filter, the lower section of neat stress outlet.
Wet type cyclone dust arrester the most according to claim 1, it is characterised in that the internal structure of described dust arrester all applies anticorrosive coat.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201510069283.XA CN104645768B (en) | 2015-02-10 | 2015-02-10 | A kind of Wet type cyclone dust arrester |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201510069283.XA CN104645768B (en) | 2015-02-10 | 2015-02-10 | A kind of Wet type cyclone dust arrester |
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| CN104645768B true CN104645768B (en) | 2016-08-31 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US11850606B2 (en) | 2020-09-09 | 2023-12-26 | Industrial Technology Research Institute | Particles capturing system |
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| CN106310835B (en) * | 2016-10-11 | 2020-03-27 | 中国北方车辆研究所 | Dust collecting device for air filter test |
| CN106964224A (en) * | 2017-01-24 | 2017-07-21 | 北京利德衡环保工程有限公司 | A kind of dedusting demister and its water circulation system |
| CN108479198B (en) * | 2018-06-11 | 2023-10-27 | 兰州大学 | Dust remover and dust removing equipment |
| CN108786385B (en) * | 2018-07-25 | 2024-04-19 | 江苏新宏大集团有限公司 | Brush type washer |
| CN111744314A (en) * | 2020-08-04 | 2020-10-09 | 沈金鹏 | Venturi cyclone dust collector |
| CN111888874B (en) * | 2020-08-19 | 2022-01-14 | 宁国环创环保科技有限公司 | Venturi cyclone dust collector |
| CN113856381B (en) * | 2021-10-09 | 2022-09-02 | 山东格瑞德活性炭有限公司 | New process route and system for purifying hazardous waste disposal flue gas |
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| CN2286428Y (en) * | 1997-01-06 | 1998-07-22 | 梁绍庚 | Vertical and wet type desulfurizing and dust removing equipment |
| CN2298055Y (en) * | 1997-06-14 | 1998-11-25 | 曹云鹏 | Wet desulfurization cyclone dust collectors |
| CN2822752Y (en) * | 2005-06-07 | 2006-10-04 | 孙克勤 | Flue gas besulfurization absorption column |
| RU2325218C1 (en) * | 2006-10-13 | 2008-05-27 | Олег Савельевич Кочетов | Kochetov's centrifugal dust extracter |
| CN202191836U (en) * | 2011-08-02 | 2012-04-18 | 何平 | Gas-liquid coupler for wet desulphurization device and wet desulphurization device |
| CN204502684U (en) * | 2015-02-10 | 2015-07-29 | 北京中能诺泰节能环保技术有限责任公司 | A kind of Wet type cyclone dust arrester |
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2015
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2286428Y (en) * | 1997-01-06 | 1998-07-22 | 梁绍庚 | Vertical and wet type desulfurizing and dust removing equipment |
| CN2298055Y (en) * | 1997-06-14 | 1998-11-25 | 曹云鹏 | Wet desulfurization cyclone dust collectors |
| CN2822752Y (en) * | 2005-06-07 | 2006-10-04 | 孙克勤 | Flue gas besulfurization absorption column |
| RU2325218C1 (en) * | 2006-10-13 | 2008-05-27 | Олег Савельевич Кочетов | Kochetov's centrifugal dust extracter |
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| CN204502684U (en) * | 2015-02-10 | 2015-07-29 | 北京中能诺泰节能环保技术有限责任公司 | A kind of Wet type cyclone dust arrester |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| US11850606B2 (en) | 2020-09-09 | 2023-12-26 | Industrial Technology Research Institute | Particles capturing system |
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