CN106139791A - Integration Turbulent Flow Type wet-scrubbing equipment - Google Patents
Integration Turbulent Flow Type wet-scrubbing equipment Download PDFInfo
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- CN106139791A CN106139791A CN201510193724.7A CN201510193724A CN106139791A CN 106139791 A CN106139791 A CN 106139791A CN 201510193724 A CN201510193724 A CN 201510193724A CN 106139791 A CN106139791 A CN 106139791A
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- pretreatment unit
- turbulent flow
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- flow type
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Abstract
The present invention solves that technical problem present in known technology provides a kind of integration Turbulent Flow Type wet-scrubbing equipment.The technical solution used in the present invention is: integration Turbulent Flow Type wet-scrubbing equipment, including one-level pretreatment unit, two stage treatment device and blowdown apparatus；Described one-level pretreatment unit is for being converted to turbulent flow by the dusty gas type of flow；Described two stage treatment device is connected to above described one-level pretreatment unit, for the wet dust removal of pretreated dusty gas；Described blowdown apparatus is connected to below described pretreatment unit, the precipitation of sewage and waste disposal after dedusting.The present invention adapts to the working environment of complexity, and efficiency of dust collection is high；Fully and recycle liquid dust removing medium, energy consumption is low；Integrated design, integration of equipmentsization is good, economizes on resources, and makes limited resources make full use of, and easy to use, operation maintenance is simple.
Description
Technical field
The invention belongs to wet-scrubbing equipment technical field, particularly relate to a kind of integration Turbulent Flow Type wet-scrubbing equipment.
Background technology
At present, industrial dust precipitator has a variety of, such as cloth-bag type, electrostatic, cyclone type etc..But due to commercial production mistake
The waste gas produced under a lot of operating modes in journey has the features such as temperature is high, viscosity greatly, easily hardens, and makes raising efficiency of dust collection, fall
Low energy consumption becomes a difficult problem.Fiber bag precipitator efficiency of dust collection is high, but resistance is big, and maintenance cost is high, especially in water content very
Big flue gas occasion, dust hardens and is more easy to appearance, causes resistance to increase, and limits its application.Cyclone dust collector resistance
Little, but efficiency of dust collection is low.Electrostatic precipitator efficiency of dust collection height, but investment is big, floor space is big, and energy consumption is high, maintenance
Costly, it is generally used for the work condition environment of big exhaust gas volumn, the environment of inapplicable little exhaust gas volumn.
Summary of the invention
The present invention solves that technical problem present in known technology provides a kind of integration Turbulent Flow Type wet-scrubbing equipment.
The technical solution used in the present invention is: integration Turbulent Flow Type wet-scrubbing equipment, including one-level pretreatment unit,
Two stage treatment device and blowdown apparatus；Described one-level pretreatment unit is for being converted to turbulent flow by the dusty gas type of flow；
Described two stage treatment device is connected to above described one-level pretreatment unit, and the wet type for pretreated dusty gas is removed
Dirt；Described blowdown apparatus is connected to below described pretreatment unit, the precipitation of sewage and waste disposal after dedusting.
As further improving, also include water circulation system；Described water circulation system includes with described blowdown apparatus successively
Overflow pipe, defecator, spray supply pool, spray supply pump and the spray supply pipe connected；Described spray supply pipe
It is connected with described two stage treatment device, is used for providing wet dust removal shower water.
As preferably, described one-level pretreatment unit includes one-level pretreatment unit cylinder；Described one-level pretreatment unit cylinder
Body sidewall is provided with air inlet near bottom；Some airflow-distribution boards mutually staggered it are provided with in described one-level pretreatment unit.
As preferably, described airflow-distribution board is positioned at above described air inlet, is one with described one-level pretreatment unit axis
Clamp angle；Described airflow-distribution board is provided with passage.
As preferably, described two stage treatment device includes two stage treatment device cylinder；Set in described two stage treatment device cylinder
There is shower；To having nozzle on described shower；It is provided with near top except mist fills in described two stage treatment device cylinder
Put；Described two stage treatment device cylinder top is provided with exhaustor.
As preferably, described two stage treatment device cylinder body bottom is provided with gasification distribution grid；Described gasification distribution grid is provided with micro-
Hole ball float.
As preferably, described nozzle is micro-spray painting nozzle, and atomizing effect is more preferable.
As preferably, described blowdown apparatus include the collection cone bucket that is connected with described one-level pretreatment unit and with described receipts
The taper sedimentation tank that collection cone bucket is connected by blanking pipeline；Described taper sedimentation tank is provided with overfall；Described taper is sunk
Connected by blow-off line below pond, shallow lake and have waste treatment device；Described blowdown apparatus is externally provided with support, is used for supporting whole
Cleaner.
As preferably, described two stage treatment device top is provided with rain-proof type gas outlet.
Owing to the present invention uses as above technical scheme, the dust-laden exhaust gas that the equipment that produces in industrial processes produces send through blower fan
Entering air inlet of the present invention, dust-laden exhaust gas carries out treatment and purification through one-level pretreatment unit and two stage treatment device to dust-laden exhaust gas
After, clean gas upwards discharges air through rain-proof type gas outlet.
In preferred version, it is provided with the airflow-distribution board of band diversion function inside one-level pretreatment unit, makes dusty gas,
The cleaner unit internal gas flow type of flow becomes turbulent flow, and distribution is more reasonable, and the most a part of dust impinges upon on airflow-distribution board
After can fall directly in blowdown apparatus, therefore it also acts the effect of primary purification.It is provided with gas inside two stage treatment device
Changing distribution grid, micropore ball float and spray equipment, spray equipment includes shower and a number of micro-spray painting nozzle, gasification point
Fabric swatch makes dust-laden exhaust gas through two stage treatment device evenly, and distribution grid is provided with a number of ball float with micropore,
Ball float serves disturbance turbulent flow and dustproof function.Dusty gas forms turbulent condition after ball float in cylinder, in air-flow
Minute dusts granule can with on spray equipment micro-spray painting nozzle spray liquid fine particle be sufficiently mixed after, dust
Grain is captured, and waste gas is by double purification.In order to avoid minimum band mist granule enters air, it is provided with W on spray equipment top
Type demister, his special construction can make mist condense into liquid, after convergence, fall inside cleaner unit.Dust-laden gives up
The liquid that gas is formed after being captured, processes after collection cone bucket is collected again, and collection cone bucket bottom is provided with blanking valve,
The switch switching of sewage can be realized, bottom the ash valve that falls, arrange taper sedimentation tank and waste treatment device.Taper precipitates
Cleaner liquid after filtering, with relief function, can be discharged to spray supply pool, the ejecting liquid of spray supply pool by pond
By the effect of spray supply pump, flowing to shower via spray supply pipe, after arriving nozzle, nozzle is made by atomization
With, after atomizing the liquid into, process dusty gas.
The integration more traditional dust removal device of Turbulent Flow Type wet-scrubbing equipment the most of the present invention has the advantage that
1, the working environment of complexity, especially worst hot case are adapted to.
2, efficiency of dust collection is made to increase by improving dust collecting process.
3, fully and recycle liquid dust removing medium, making rational use of resources, energy consumption is low, fully realizes energy-conservation purpose.
4, the flue gas of discharge or the dust concentration of waste gas are low, can be less than country's relevant emission standards.
5, integrated design, integration of equipmentsization is good, economizes on resources, and makes limited resources make full use of, easy to use, runs
Safeguard simple.
Except the technical characteristic that present invention solves the technical problem that, constitute technical scheme described above and by these skills
Outside the advantage that the technical characteristic of art scheme is brought, other technologies problem that die cutting plate storage rack of the present invention can solve,
The advantage that the other technologies feature comprised in technical scheme and these technical characteristics are brought, hereinafter in conjunction with accompanying drawing
It is described in further detail.
Accompanying drawing explanation
Fig. 1 is integration Turbulent Flow Type wet-scrubbing equipment structural representation of the present invention.
In figure: 1, rain-proof type gas outlet；2, two stage treatment device；201, air vent；202, demister；203、
Shower；204, nozzle；205, two stage treatment device cylinder；206, micropore ball float；207, gasification distribution grid；3、
One-level pretreatment unit；301, one-level pretreatment unit cylinder；302, airflow-distribution board；303, air inlet；4, row
Dirty device；401, collection cone bucket；402, support；403, taper sedimentation tank；404, waste treatment device；5, circulation
Water system；501, defecator；502, spray supply pool；503, spray supply pump.
Detailed description of the invention
For the summary of the invention of the present invention, feature and effect can be further appreciated that, hereby enumerate following example, and coordinate accompanying drawing
Describe in detail as follows:
As it is shown in figure 1, the present embodiment is integration Turbulent Flow Type dust arrester, including rain-proof type gas outlet 1, two stage treatment
Device 2, one-level pretreatment unit 3, blowdown apparatus 4 and circulation 5；Wherein two stage treatment device 2 includes aerofluxus
Mouth 201, demister 202, shower 203, micro-spray painting nozzle 204, two stage treatment device cylinder 205, micropore ball float
206, gasification distribution grid 207；Wherein one-level pretreatment unit 3 includes one-level pretreatment unit cylinder 301, air flow method
Plate 302, air inlet 303；Described blowdown apparatus 4 includes collection cone bucket 401, support 402, taper sedimentation tank 403, gives up
Material processing device 404；Described circulation 5 includes overflow pipe, defecator 501, spray supply pool 502, spray
Drench supply pump 503 and spray supply pipe.
The carrying of integration Turbulent Flow Type wet-scrubbing equipment main body is mainly pre-with collection cone bucket 401 or one-level by support 402
The connection of processing means cylinder 301 realizes.Air inlet 303 and one-level pretreatment unit cylinder 301 compact siro spinning technology are without letting out
Leakage, one-level pretreatment unit cylinder 301 is internally provided with a number of airflow-distribution board 302 mutually staggered, described gas
Flow point fabric swatch is positioned at above described air inlet 303, in a certain angle with described one-level pretreatment unit axis；Described air-flow
Distribution grid 302 is provided with passage.
Two stage treatment device cylinder 205 is connected to above one-level pretreatment unit cylinder 301.Near junction, two grades
The internal gasification distribution grid 207 that is provided with of processing means cylinder 205, lays one above gasification distribution grid 207 and has floating and mistake
Filter function micropore ball float 206, gasification distribution grid 207 structure be a kind of have the plate of micropore, grid or according to certain advise
The rule of rule arrangement or irregular device.Two stage treatment device cylinder 205 internal capillary ball float 206 is provided above spray
Shower device, this spray equipment is made up of shower 203 and micro-spray painting nozzle 204, and shower 203 is according to necessarily by pipeline
Regularly arranged pipe network, and it is fixed on inner barrel by fixing device, equipped with micro-spray painting nozzle 204 on shower 203, micro-
Spray painting nozzle 204 is a kind of injection apparatus with spraying liquid function.It is provided with in a certain distance of shower 203 top and removes
Mist device 202, demister 202 is the grid by certain regular distribution, and demister 202 is installed to by hold-down support
Two stage treatment device cylinder 205 is internal near the junction of air vent 201.Air vent 201 is typically tapered and leads to
Crossing close connected mode to be connected with rain-proof type gas outlet 1, rain-proof type gas outlet 1 is the exhaust apparatus with rainproof function,
Outer row for flue gas uses.
Blowdown apparatus 4 includes the collection cone bucket 401 being connected with one-level pretreatment unit cylinder 301, collection cone bucket 401
Bottom is provided with discharge blanking pipe and discharge valve, and discharge valve is that by the manually or automatically valve of on-off function, blanking
What valve bottom was installed is a kind of taper sedimentation tank 403 having and collecting with relief function, realizes dirt by taper sedimentation tank 403
Arrange outside the collection buffering of thing and overflow, bottom taper sedimentation tank 403, be provided with blow-off line and sewage draining valve, sewage draining valve
Realize waste material or the dirt break-make in blow-off line.Waste treatment device 404 is arranged at sewage draining valve bottom, passes through waste disposal
Device 404 realizes collecting waste material or the process of dirt, and waste treatment device 404 is that one has transport function or drying point
Equipment from transportation function.Refuse, the recycling of material or disposal can be realized by it.Taper sedimentation tank 403 is near top
There is overfall side, portion.
Circulation 5 includes the overflow pipe being sequentially connected with overfall, defecator 501, sprays supply pool 502；
Spray supply pool 502 is the casing with savings liquid functional, and spray supply pool 502 is above or liquid internal is provided with spray
Drenching supply pump 503, spray supply pump 503 has frequency modulation function, can more be actually needed setpoint frequency and constant flow supply.
Spray supply pump 503 is connected with shower by spray supply pipe, liquid sprays medium and flows to shower and micro-spray painting
Nozzle 204, is achieved the micro-atomization of spray, purifies dust-laden exhaust gas or the purpose of flue gas.
Above one embodiment of the present of invention is described in detail, but described content has been only presently preferred embodiments of the present invention,
It is not to be regarded as the practical range for limiting the present invention.All impartial changes made according to the present patent application scope and improvement etc.,
Within all should still belonging to the patent covering scope of the present invention.
Claims (9)
1. an integrated Turbulent Flow Type wet-scrubbing equipment, it is characterised in that: include one-level pretreatment unit, two stage treatment
Device and blowdown apparatus；Described one-level pretreatment unit is for being converted to turbulent flow by the dusty gas type of flow；Described two grades
Processing means is connected to above described one-level pretreatment unit, for the wet dust removal of pretreated dusty gas；Described
Blowdown apparatus is connected to below described pretreatment unit, the precipitation of sewage and waste disposal after dedusting.
Integration Turbulent Flow Type wet-scrubbing equipment the most according to claim 1, it is characterised in that: also include that water circulates
System；Described water circulation system includes that the overflow pipe being sequentially connected with described blowdown apparatus, defecator, spray supply
Pond, spray supply pump and spray supply pipe；Described spray supply pipe is connected with described two stage treatment device, is used for providing wet
Formula dedusting shower water.
Integration Turbulent Flow Type wet-scrubbing equipment the most according to claim 1 and 2, it is characterised in that: described one-level
Pretreatment unit includes one-level pretreatment unit cylinder；Described one-level pretreatment unit cylinder lateral wall is provided with air inlet near bottom
Mouthful；Some airflow-distribution boards mutually staggered it are provided with in described one-level pretreatment unit.
Integration Turbulent Flow Type wet-scrubbing equipment the most according to claim 3, it is characterised in that: described air flow method
Plate is positioned at above described air inlet, in a certain angle with described one-level pretreatment unit axis；Set on described airflow-distribution board
There is passage.
Integration Turbulent Flow Type wet-scrubbing equipment the most according to claim 1 and 2, it is characterised in that: described two grades
Processing means includes two stage treatment device cylinder；It is provided with shower in described two stage treatment device cylinder；On described shower
To having nozzle；It is provided with demister near top in described two stage treatment device cylinder；Described two stage treatment device cylinder
Body top is provided with exhaustor.
Integration Turbulent Flow Type wet-scrubbing equipment the most according to claim 5, it is characterised in that: described two stage treatment
Device cylinder body bottom is provided with gasification distribution grid；Described gasification distribution grid is provided with micropore ball float.
Integration Turbulent Flow Type wet-scrubbing equipment the most according to claim 5, it is characterised in that: described nozzle is micro-
Atomizing nozzle.
Integration Turbulent Flow Type wet-scrubbing equipment the most according to claim 1 and 2, it is characterised in that: described blowdown
Device is included the collection cone bucket being connected with described one-level pretreatment unit and is connected by blanking pipeline with described collection cone bucket
The taper sedimentation tank connect；Described taper sedimentation tank is provided with overfall；Below described taper sedimentation tank by blow-off line even
It is connected to waste treatment device；Described blowdown apparatus is externally provided with support.
Integration Turbulent Flow Type wet-scrubbing equipment the most according to claim 1 and 2, it is characterised in that: described two grades
Processing means top is provided with rain-proof type gas outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510193724.7A CN106139791A (en) | 2015-04-22 | 2015-04-22 | Integration Turbulent Flow Type wet-scrubbing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510193724.7A CN106139791A (en) | 2015-04-22 | 2015-04-22 | Integration Turbulent Flow Type wet-scrubbing equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN106139791A true CN106139791A (en) | 2016-11-23 |
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ID=58058971
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510193724.7A Pending CN106139791A (en) | 2015-04-22 | 2015-04-22 | Integration Turbulent Flow Type wet-scrubbing equipment |
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Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000135411A (en) * | 1998-10-29 | 2000-05-16 | Tanabe Kogyo Kk | Exhaust gas treatment device and its manufacture |
| CN2547382Y (en) * | 2002-04-01 | 2003-04-30 | 谭景世 | Wet type dust collector |
| CN101502734A (en) * | 2009-02-13 | 2009-08-12 | 无锡市雪江环境工程设备有限公司 | Spray tower structure for spraying and dedusting |
| CN201410358Y (en) * | 2009-04-29 | 2010-02-24 | 日本环境技术咨询株式会社 | Device for disposing waste gas at high gas speed |
| CN103961996A (en) * | 2014-05-15 | 2014-08-06 | 淮南市明月环保科技有限责任公司 | Fume purification system with tower box |
| CN204656246U (en) * | 2015-04-22 | 2015-09-23 | 天津市璐祥自动化设备有限公司 | Integration Turbulent Flow Type wet-scrubbing equipment |
-
2015
- 2015-04-22 CN CN201510193724.7A patent/CN106139791A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2000135411A (en) * | 1998-10-29 | 2000-05-16 | Tanabe Kogyo Kk | Exhaust gas treatment device and its manufacture |
| CN2547382Y (en) * | 2002-04-01 | 2003-04-30 | 谭景世 | Wet type dust collector |
| CN101502734A (en) * | 2009-02-13 | 2009-08-12 | 无锡市雪江环境工程设备有限公司 | Spray tower structure for spraying and dedusting |
| CN201410358Y (en) * | 2009-04-29 | 2010-02-24 | 日本环境技术咨询株式会社 | Device for disposing waste gas at high gas speed |
| CN103961996A (en) * | 2014-05-15 | 2014-08-06 | 淮南市明月环保科技有限责任公司 | Fume purification system with tower box |
| CN204656246U (en) * | 2015-04-22 | 2015-09-23 | 天津市璐祥自动化设备有限公司 | Integration Turbulent Flow Type wet-scrubbing equipment |
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Application publication date: 20161123 |