CN203663622U - Pneumatic catching device for treatment of PM (Particulate Matters) 2.5 in smoke gas - Google Patents
Pneumatic catching device for treatment of PM (Particulate Matters) 2.5 in smoke gas Download PDFInfo
- Publication number
- CN203663622U CN203663622U CN201320866630.8U CN201320866630U CN203663622U CN 203663622 U CN203663622 U CN 203663622U CN 201320866630 U CN201320866630 U CN 201320866630U CN 203663622 U CN203663622 U CN 203663622U
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- China
- Prior art keywords
- flue gas
- water bath
- venturi scrubber
- pneumatic
- absorption liquid
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
- Y02A50/2351—Atmospheric particulate matter [PM], e.g. carbon smoke microparticles, smog, aerosol particles, dust
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- Treating Waste Gases (AREA)
Abstract
The utility model discloses a pneumatic catching device for the treatment of PM (Particulate Matters) 2.5 in smoke gas, which comprises a Venturi dust remover and a water bath tank; the water bath box is filled with absorption liquid; the Venturi dust remover is installed on the water bath tank, an outlet of the Venturi dust remover is formed in a set height position above a liquid level of the absorption liquid, original smoke gas inlets are formed in the side wall of the upper part of the Venturi dust remover, and a water inlet for injection is formed in the top of the Venturi dust remover; and the absorption liquid is introduced into the water inlet for injection and moves downwards along the Venturi dust remover to inject smoke gas in the original smoke gas inlets into the Venturi dust remover, thereby forming a large-particle particulate matter; and the absorption liquid and the large-particle particulate matter move downwards to impact the liquid level of the absorption liquid in the water bath tank, so that the smoke gas can be caught and absorbed. The pneumatic catching device has the benefits that the pneumatic catching device adopts an ejection pressurized pneumatic dust removal technology which is the most advanced technology for the treatment of the PM2.5 in the smoke gas, the efficiency is high, and the PM2.5 in the smoke gas from oily fume in the catering industry, hospital incinerators, various small-sized kilns and the like can be effectively removed to meet the requirement of controlling the environmental pollution.
Description
Technical field
The utility model relates to catering trade flue gas PM2.5 and administers field, especially a kind of pneumatic capturing device of administering for flue gas PM2.5 such as oil smoke of catering industry, hospital's incinerator, various small-sized kilns.
Background technology
At present, the flue gas that the cooking of Kitchen internal cause produces is to adopt smoke exhaust ventilator and flue directly to discharge substantially, easily atmosphere is produced and is polluted, and grease also easily exerts an influence to surrounding environment, also causes the wasting of resources.The flue gas that hospital's incinerator, various small-sized kilns etc. are got rid of, has also all caused adverse effect to atmosphere.
The particularly cooking fume complicated of catering trade, nose, eye, larynx and lung to people have spread effect, and cooking fume affects oneself and causes the attention of relevant department near resident's kitchen and restaurant.Existing fume treatment device adopts same treating apparatus to process the moisture in flue gas, oil stain and flue gas conventionally, and regularly removes, clears up oil stain wherein, and therefore, sort processor needs numerous and diverse structure to support, and manufacturing cost is high, safeguards inconvenience., click above because oil stain adsorbs for a long time, is deposited in meanwhile, easily result in blockage, reduce operating efficiency.
Utility model content
The problem existing for prior art, the purpose of this utility model is to provide the pneumatic capturing device of administering for flue gas PM2.5 such as oil smoke of catering industry, hospital's incinerator, various small-sized kilns that a kind of cost is low, efficiency is high.
For achieving the above object, a kind of pneumatic capturing device of administering for flue gas PM2.5 of the utility model, comprise venturi scrubber and water bath, wherein in water bath, be filled with a certain amount of absorption liquid, venturi scrubber is arranged on water bath, and the outlet of venturi scrubber is arranged at the set height position of the liquid level top of absorption liquid, in the upper portion side wall of venturi scrubber, be provided with former smoke inlet, the top of venturi scrubber is provided with injection water inlet, this injection is with passing into absorption liquid in water inlet, absorption liquid moves downward the flue gas injection in former smoke inlet to enter in venturi scrubber, to form oarse-grained particle along venturi scrubber, and move downward together the absorption liquid liquid level in impact water bath case, further flue gas is trapped to absorption.
Further, on described venturi scrubber, be circumferentially evenly provided with several former smoke inlets along it.
Further, described former smoke inlet enter tube wall tangential that cigarette direction is described venturi scrubber.
Further, the outlet top of described venturi scrubber is provided with cyclone, and the outlet of described venturi scrubber and the liquid level of described absorption liquid distance are: 0.1～0.5 meter.
Further, described injection is with being provided with the nozzle that produces storing injection power by supercharging on water inlet, and the outlet of described venturi scrubber is provided with trumpet type outlet.
Further, the bottom of described water bath is connected with water inlet with described injection by pipeline, and is provided with circulating pump on pipeline, and this circulating pump is transported to described injection water inlet by the absorption liquid in described water bath and recycles.
Further, on the pipeline between described circulating pump and described water bath, be provided with supplementing water entrance, the bottom of described water bath is also provided with outer drain outlet.
Further, the top of described water bath is provided with centrifugal moisture trap, is provided with and the unit, inclined-plane of discharging clean Gas phase Smoke shock on it, and the outlet of centrifugal moisture trap is arranged on the opposite side of unit, inclined-plane.
Further, the top of described water bath is provided with clean flue gas delivery line, described centrifugal moisture trap is arranged on clean flue gas delivery line, the air inlet place that clean flue gas delivery line is positioned at described water bath is provided with trumpet type air inlet, the end that clean flue gas delivery line is positioned at outside described water bath is provided with half ramp structure, this half ramp structure is identical with angle of inclination, unit, described inclined-plane, the bottom of half ramp structure is provided with the gas outlet of gap type, and the clean flue gas of discharging from this gas outlet directly clashes into unit, described inclined-plane.
Further, described absorption liquid guarantees that by control module liquid level remains on one and exports metastable distance with described venturi scrubber.
The utility model adopts injection supercharging pneumatic dust collection technology, be at present state-of-the-art, for flue gas PM2.5 improvement technology such as oil smoke of catering industry, hospital's incinerator, various small-sized kilns, efficiency is high, can effectively remove the PM2.5 in flue gas, to meet the requirement that controls environment and pollute.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation;
Fig. 2 is clean flue gas delivery line structural representation.
The specific embodiment
Below, with reference to accompanying drawing, the utility model is more fully illustrated, shown in the drawings of exemplary embodiment of the present utility model.But the utility model can be presented as multiple multi-form, and should not be construed as the exemplary embodiment that is confined to narrate here.But, these embodiment are provided, thereby make the utility model comprehensively with complete, and scope of the present utility model is fully conveyed to those of ordinary skill in the art.
For ease of explanation, here can use such as " on ", the space relative terms such as D score " left side " " right side ", the relation for element shown in key diagram or feature with respect to another element or feature.It should be understood that except the orientation shown in figure, spatial terminology is intended to comprise the different azimuth of device in using or operating.For example, if the device in figure is squeezed, be stated as the element that is positioned at other elements or feature D score will be positioned at other elements or feature " on ".Therefore, exemplary term D score can comprise upper and lower orientation both.Device can otherwise be located (90-degree rotation or be positioned at other orientation), and the relative explanation in space used here can correspondingly be explained.
As shown in Figure 1 and Figure 2, the pneumatic capturing device that the utility model is administered for catering trade flue gas PM2.5, comprises venturi scrubber 1, water bath 2, centrifugal moisture trap 14 and clean flue gas delivery line 17.
Wherein, venturi scrubber 1 is arranged on water bath 2, the top of venturi scrubber 1 is provided with water inlet 5 for injection, injection is with being provided with the nozzle 8 that produces storing injection power by supercharging on water inlet 5, in the upper portion side wall of venturi scrubber 1, be provided with several former smoke inlets 4, the outlet top of venturi scrubber 1 is provided with cyclone 7, the outlet of venturi scrubber 1 is provided with trumpet type outlet 9, and the outlet of venturi scrubber 1 is arranged at the set height position of the liquid level top of absorption liquid 3, and its spacing is 0.1～0.5 meter.
In water bath 2, be filled with a certain amount of absorption liquid 3, the bottom of water bath 2 is connected with water inlet 5 with injection by pipeline 10, and on pipeline 10, be provided with circulating pump 11, circulating pump 11 is transported to injection water inlet 5 by the absorption liquid in water bath 23 and recycles.On pipeline between circulating pump 11 and water bath 2, be provided with supplementing water entrance 12, the bottom of water bath 2 is also provided with outer drain outlet 13.
The top of water bath 2 is provided with clean flue gas delivery line 17, and centrifugal moisture trap 14 is installed on it.The air inlet place that clean flue gas delivery line 17 is positioned at water bath 2 is provided with trumpet type air inlet 18, and clean flue gas delivery line 17 is positioned at bottom that end outside water bath 2 is provided with half ramp structure 19, half ramp structures 19 and is provided with the gas outlet 20 of gap type.On centrifugal moisture trap 14, be provided with and the unit, inclined-plane 15 of discharging clean Gas phase Smoke shock, the outlet 16 of centrifugal moisture trap 14 is arranged on the opposite side of unit, inclined-plane 15.Wherein, half ramp structure 19 is identical with 15 angles of inclination, unit, inclined-plane, and the clean flue gas of discharging from gas outlet 20 directly clashes into unit, inclined-plane 15.
In the utility model, venturi scrubber 1 air inlet and water inlet position are different from the rotine positioning of current China for the venturi scrubber 1 of smoke gas treatment.Flue gas is from the venturi front side of venturi scrubber 1 to entering (and conventional mode is for axially entering), and introducing mode is: flue gas is divided into some roads (conventionally adopting 1～4 tunnel), that is: enters in venturi scrubber 1 by several former smoke inlet 4 injections.Several former smoke inlets 4 circumferentially evenly arrange along venturi scrubber 1, and the cigarette direction of entering of former smoke inlet 4 is the tangential of venturi scrubber 1 tube wall.Simultaneously, absorption liquid is from axially the entering of venturi scrubber 1 (and conventional mode is for entering in venturi venturi side direction), and setting has higher pressure and special nozzle 8, the glassware for drinking water that nozzle 8 sprays has speed and tighter spreadability faster, produce stronger injection power, flue gas in flue gas cross over pipe before venturi can be attracted in Venturi tube, at a high speed, high spreadability spray stream the flue gas of introducing is pushed through to venturi, the resistance that makes venturi scrubber 1 be-300～-100Pa(and the resistance of conventional venturi scrubber is 150～500Pa).Because venturi scrubber 1 is installed vertically downward, fume side enters, under go out, absorption liquid is enterprising, under go out, PM2.5 ultrafine dust will be condensed into larger particle in Venturi tube.
Be provided with cyclone 7 by the outlet top at venturi scrubber 1, cyclone 7 is for being arranged on the combining structure of several blades on tube wall, and it forms certain resistance in exit, and the air pressure that guarantees venturi scrubber 1 is uniform state.Cyclone 7 can guarantee that the flue gas exporting from venturi scrubber 1, for evenly discharging, is uniform state by the air pressure that guarantees venturi scrubber 1, and can prevent gas discharge time, local pressure is large, and causes the phenomenon that occurs liquid splash on liquid level 6.By be provided with trumpet type outlet 9 in the outlet of venturi scrubber 1, it is the delivery flow of even flue gas further, simultaneously, while discharging flue gas from outlet, can form at tube wall position negative pressure, the outer of the outside expenditure of trumpet type outlet 9 can prevent that the liquid of being blown by flue gas is back in pipe along tube wall.
Flue gas after water-bath impacting type dust removal process is upwards discharged and is entered centrifugal moisture trap 14 by water bath 2.Centrifugal moisture trap 14 is the gas unhurried current pipelines that clean flue gas delivery line 17 diameters of ratio are larger, flue runs in top, below is flue, flue gas flows downward through cyclone, and flue gas and liquid, under the effect of cyclone, form swirling eddy, the drop of larger particles is thrown toward the wall of unit, inclined-plane 15, because amount of liquid is larger, form downward continuous hollow cone liquid film, be conducive to dedusting; Liquid by wall interception and sedimentation flow back into water bath under Action of Gravity Field, and clean flue gas is by upper discharge.
Claims (10)
1. a pneumatic capturing device of administering for flue gas PM2.5, it is characterized in that, comprise venturi scrubber and water bath, wherein in water bath, be filled with a certain amount of absorption liquid, venturi scrubber is arranged on water bath, and the outlet of venturi scrubber is arranged at the set height position of the liquid level top of absorption liquid, in the upper portion side wall of venturi scrubber, be provided with former smoke inlet, the top of venturi scrubber is provided with injection water inlet, this injection is with passing into absorption liquid in water inlet, absorption liquid moves downward the flue gas injection in former smoke inlet to enter in venturi scrubber, to form oarse-grained particle along venturi scrubber, and move downward together the absorption liquid liquid level in impact water bath case, further flue gas is trapped to absorption.
2. the pneumatic capturing device of administering for flue gas PM2.5 as claimed in claim 1, is characterized in that, on described venturi scrubber, is circumferentially evenly provided with several former smoke inlets along it.
3. the pneumatic capturing device of administering for flue gas PM2.5 as claimed in claim 2, is characterized in that, described former smoke inlet enter tube wall tangential that cigarette direction is described venturi scrubber.
4. the pneumatic capturing device of administering for flue gas PM2.5 as claimed in claim 1, it is characterized in that, the outlet top of described venturi scrubber is provided with cyclone, and the outlet of described venturi scrubber and the liquid level of described absorption liquid distance are: 0.1～0.5 meter.
5. the pneumatic capturing device of administering for flue gas PM2.5 as claimed in claim 1, is characterized in that, described injection is with being provided with the nozzle that produces storing injection power by supercharging on water inlet, and the outlet of described venturi scrubber is provided with trumpet type outlet.
6. the pneumatic capturing device of administering for flue gas PM2.5 as claimed in claim 1, it is characterized in that, the bottom of described water bath is connected with water inlet with described injection by pipeline, and on pipeline, be provided with circulating pump, this circulating pump is transported to described injection water inlet by the absorption liquid in described water bath and recycles.
7. the pneumatic capturing device of administering for flue gas PM2.5 as claimed in claim 6, is characterized in that, on the pipeline between described circulating pump and described water bath, be provided with supplementing water entrance, the bottom of described water bath is also provided with outer drain outlet.
8. the pneumatic capturing device of administering for flue gas PM2.5 as claimed in claim 1, it is characterized in that, the top of described water bath is provided with centrifugal moisture trap, on it, be provided with and the unit, inclined-plane of discharging clean Gas phase Smoke shock, the outlet of centrifugal moisture trap is arranged on the opposite side of unit, inclined-plane.
9. the pneumatic capturing device of administering for flue gas PM2.5 as claimed in claim 8, it is characterized in that, the top of described water bath is provided with clean flue gas delivery line, described centrifugal moisture trap is arranged on clean flue gas delivery line, the air inlet place that clean flue gas delivery line is positioned at described water bath is provided with trumpet type air inlet, the end that clean flue gas delivery line is positioned at outside described water bath is provided with half ramp structure, this half ramp structure is identical with angle of inclination, unit, described inclined-plane, the bottom of half ramp structure is provided with the gas outlet of gap type, the clean flue gas of discharging from this gas outlet directly clashes into unit, described inclined-plane.
10. the pneumatic capturing device of administering for catering trade flue gas PM2.5 as claimed in claim 1, is characterized in that, described absorption liquid guarantees that by control module liquid level remains on one and exports metastable distance with described venturi scrubber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320866630.8U CN203663622U (en) | 2013-12-26 | 2013-12-26 | Pneumatic catching device for treatment of PM (Particulate Matters) 2.5 in smoke gas |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320866630.8U CN203663622U (en) | 2013-12-26 | 2013-12-26 | Pneumatic catching device for treatment of PM (Particulate Matters) 2.5 in smoke gas |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203663622U true CN203663622U (en) | 2014-06-25 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320866630.8U Expired - Fee Related CN203663622U (en) | 2013-12-26 | 2013-12-26 | Pneumatic catching device for treatment of PM (Particulate Matters) 2.5 in smoke gas |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203663622U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103721501A (en) * | 2013-12-26 | 2014-04-16 | 北京布鲁斯盖环保科技发展有限公司 | Pneumatic capture device for governing smoke particulate matter 2.5 (PM2.5) |
-
2013
- 2013-12-26 CN CN201320866630.8U patent/CN203663622U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103721501A (en) * | 2013-12-26 | 2014-04-16 | 北京布鲁斯盖环保科技发展有限公司 | Pneumatic capture device for governing smoke particulate matter 2.5 (PM2.5) |
| CN103721501B (en) * | 2013-12-26 | 2016-04-06 | 北京布鲁斯盖环保科技发展有限公司 | A kind of pneumatic capturing device administered for flue gas PM2.5 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140625 Termination date: 20161226 |
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| CF01 | Termination of patent right due to non-payment of annual fee |