CN205360931U - Degree of depth defogging dust collector - Google Patents
Degree of depth defogging dust collector Download PDFInfo
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- CN205360931U CN205360931U CN201521122749.XU CN201521122749U CN205360931U CN 205360931 U CN205360931 U CN 205360931U CN 201521122749 U CN201521122749 U CN 201521122749U CN 205360931 U CN205360931 U CN 205360931U
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- filter bed
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- dust arrester
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Abstract
The utility model discloses a degree of depth defogging dust collector, include: the smoke box that admits air dams and adsorbs the droplet and the rotatory filter bed of smoke and dust in the smoke box that admits air, receives the smoke box of giving vent to anger through the gas of rotatory filter bed, the water cleanness subassembly of rotatory filter bed one end of submergence and washing rotation filter bed. The utility model provides a superfine droplet and dust, separation efficiency be up to more than 90% that is used for the degree of depth defogging dust collector that the fume emission was handled behind the wet flue gas desulfurization, more than this device can desorption 3um reaches.
Description
Technical field
This utility model relates to field of environment protection equipment, particularly a kind of smoke eliminator.
Background technology
Containing certain density droplet (the general 75mg/Nm of flue fog drip concentration in heat-engine plant wet desulfurization fume exhaust3), being entrained with in Gypsum Fibrosum (Gypsum Fibrosum accounts for 20%), the particularly droplet of big particle diameter gypsum content in droplet more can not be ignored, and the dust in smoke evacuation there are about half and carries secretly from droplet.In order to reduce dust emission further, reaching " the ultra-clean discharge of flue dust " requirement, it is necessary for arranging high efficiency demister at desulfurizing tower rear portion flue.
Existing mist separator of desulfurization (no matter being demister or tower external flue formula demister in tower) is only effective to big droplet, and the little droplet of below 20um cannot be removed.In order to reduce soot emissions further, it is common practice to arrange wet electrical dust precipitator after desulfurizing tower, removed flue dust and droplet by the mode of extra electric field.
It is the droplet of more than 20um that conventional desulfurization demister is only capable of elimination particle diameter, and the little droplet of below 20um is helpless, and rinses frequently, and water consumption is big.Although wet electrical dust precipitator is higher except mist, efficiency of dust collection, but floor space is big, it is necessary to high voltage supply, and power consumption is high, and water consumption is big, and cost is high.Although screen type demister demisting efficiency is higher, but not easily rinses, it is easy to blocking, desulphurization system is difficult to application；Prior art is unresolved such problem also.
Utility model content
For solving the deficiencies in the prior art, the purpose of this utility model is in that to provide a kind of degree of depth for wet-method desulfurized fume emission treatment except mist dust arrester, and this device can remove 3um and above ultra-fine droplet and dust, and demisting efficiency is up to more than 90%.
In order to realize above-mentioned target, this utility model adopts the following technical scheme that:
The degree of depth removes mist dust arrester, including air inlet smoke box, dams and the rotation filter bed of the droplet that adsorb in air inlet smoke box and flue dust, receives the smoke box of giving vent to anger of gas through over-rotation filter bed, and submergence rotates filter bed one end and also cleans the water cleaning assemblies of rotation filter bed.
The aforesaid degree of depth removes mist dust arrester, and rotating filter bed composition has: be connected to air inlet smoke box, the housing of smoke box of giving vent to anger, and is placed in the cyclic transfer assembly in housing, the filter bed of parcel cyclic transfer assembly.
The aforesaid degree of depth removes mist dust arrester, rotates filter bed and is at least one.
The aforesaid degree of depth removes mist dust arrester, and cyclic transfer assembly composition has: two drive sprockets being placed in filter bed two ends, connects the chain of drive sprocket, is connected to drive sprocket the driven sprocket driving filter bed to move.
The aforesaid degree of depth removes mist dust arrester, and filter bed composition has: at least one piece of silk screen intercepter plate, connects the otic placode between silk screen intercepter plate and chain, is connected to the PTFE flexible cloth between silk screen intercepter plate.
The aforesaid degree of depth removes mist dust arrester, and silk screen intercepter plate composition has: silk screen layer, the framework of carrying silk screen layer；Silk screen layer is made up of at least one of which silk screen, and the thickness of silk screen layer is 5-100mm.
The aforesaid degree of depth removes mist dust arrester, and water cleaning assemblies includes: bottom tank, connects the internal pipeline between the tank of bottom, is placed in the nozzle on the tank of bottom.
The aforesaid degree of depth removes mist dust arrester, also includes: be connected to the water circulation use assembly of water cleaning assemblies.
The aforesaid degree of depth removes mist dust arrester, and the flow direction of flue gas is perpendicular to rotation filter bed.
The aforesaid degree of depth removes mist dust arrester, also includes: be placed in air inlet smoke box and the airflow uniform distribution plate rotated between filter bed.
Of the present utility model having the beneficial effect that 1) this device arranges and rotates filter bed and invade the water cleaning assemblies not rotated bottom filter bed, not only make filter bed be cleaned in time, and realize dynamic dedusting except mist；The flow direction of flue gas is vertical with filter bed, relies on " air-flow conveying+filter bed retains+moisture film absorption, adhesion " combined effect, makes gas cleaning；Smoke content < 5mg/Nm after process3, reach the requirement of minimum discharge；The sulfuric acid mist of elimination major part simultaneously, reduces the risk of successor devices corrosion and blocking, extension device service life；This device can remove 3um and above ultra-fine droplet and dust, and demisting efficiency is up to more than 90%.2) water cleaning assemblies be connected to outside water circulation use assembly, compared with existing purifier, volume be only its 30%, take up an area space little, cost economize, resistance is low, and water consumption is few, wastewater flow rate is little.3) Maintenance and Repair of this device are convenient, except can only silk screen layer be replaced when fog effect is deteriorated.
Accompanying drawing explanation
Fig. 1 is the structural representation of a kind of embodiment of the present utility model；
Fig. 2 is the structural representation of a kind of embodiment of this utility model silk screen intercepter plate；
The implication of accompanying drawing labelling in figure:
1 air inlet smoke box, 2 airflow uniform distribution plates, 3 housings, 4 drive sprockets, 5 chains, 6 filter beds, 7 give vent to anger smoke box, 8 driven sprockets, 9 water cleaning assemblies, 10 frameworks, 11 silk screen intercepter plates, 12PTFE flexible cloth, 13 otic placodes.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, this utility model done concrete introduction.
The degree of depth removes mist dust arrester, including air inlet smoke box 1, dams and the rotation filter bed 6 of the droplet that adsorb in air inlet smoke box 1 and flue dust, receives the smoke box 7 of giving vent to anger of gas through over-rotation filter bed 6, and submergence rotates filter bed 6 one end and also cleans the water cleaning assemblies 9 of rotation filter bed 6.
Rotate filter bed 6 composition to have: be connected to air inlet smoke box 1, the housing 3 of smoke box 7 of giving vent to anger, be placed in the cyclic transfer assembly in housing 3, the filter bed 6 of parcel cyclic transfer assembly.In order to allow flue gas uniformly enter rotation filter bed 6, improve filter efficiency, between air inlet smoke box 1 and rotation filter bed 6, be provided with airflow uniform distribution plate 2.The number rotating filter bed 6 is indefinite, rotates filter bed 6 and is at least one, can increase and decrease as required.Cyclic transfer assembly composition has: two drive sprockets 4 being placed in filter bed 6 two ends, connects the chain 5 of drive sprocket 4, is connected to drive sprocket 4 driven sprocket 8 driving filter bed 6 to move.Motor drives drive sprocket 4 to rotate, and drives chain 5 and driven sprocket 8 to transmit, and driven sprocket 8 is connected in filter bed 6, thus driving filter bed 6 transmission.When filter bed 6 moves to the position of bottom tank, it is achieved clean, the flow direction of flue gas is perpendicular to rotation filter bed 6, so ensure that the filter bed 6 of contact flue gas is all clean, and bedewed water, rely on " air-flow conveying+filter bed 6 retains+moisture film absorption, adhesion " combined effect, make gas cleaning.The lower submerged of filter bed 6, in the tank of bottom, had both facilitated the flushing of filter bed 6, also made bottom water seal air tight simultaneously.Tank is provided with nozzle, makes filter bed 6 rinse cleaning.
Filter bed 6 composition has: at least one piece of silk screen intercepter plate 11, connects the otic placode 13 between silk screen intercepter plate 11 and chain 5, is connected to the PTFE flexible cloth 12 between silk screen intercepter plate 11；Silk screen intercepter plate 11 composition has: silk screen layer, the framework 10 of carrying silk screen layer；Silk screen layer is made up of at least one of which silk screen, and the thickness of silk screen layer is 5-100mm.Such design makes polylith silk screen intercepter plate about 11 coaxial rotating, is linked to be seamless entirety by PTFE filter cloth between silk screen intercepter plate 11.
Water cleaning assemblies 9 includes: bottom tank, connects the internal pipeline between the tank of bottom, is placed in the nozzle on the tank of bottom；In order to saving water resource, the degree of depth removes mist dust arrester, also includes: be connected to the water circulation use assembly of water cleaning assemblies 9.
The work process of this device is: after (a) flue gas enters device, after air inlet smoke box 1 and air-flow uniform board 2, and droplet and flue dust are along with the flowing " hitting " of flue gas is to rotating filter bed 6；B () flue gas flows through rotation filter bed 6 after, droplet and flue dust are dammed and are absorbed；In adsorption process, it is filled with, owing to silk screen intercepter plate 11 is internal, the droplet absorbed, enhances filtration and the absorbability of silk screen intercepter plate 11 so that during normal operation, the degree of depth increases substantially except the mist rate of removing of mist dust arrester, it is possible to effectively remove by minimum droplet；C (), under the drive of drive sprocket 4 and chain 5, filter bed 6 rotates along (inverse) hour hands.Rotate to silk screen intercepter plate 11 entrance of bottom tank to clean specially, after rinsing well, return flue gas flow channel；D the pollutant in () flushing water, are processed by external water circulation use assembly, the clean also reuse of the water after process；It should be noted that water circulation use assembly is that the half being commercially available on market recycles assembly.Through such process, this device droplet clearance >=90% to more than 3um, filter bed 6 drag overalls≤300Pa.
This device arranges and rotates filter bed 6 and invade the water cleaning assemblies 9 not rotated bottom filter bed 6, not only makes filter bed 6 be cleaned in time, and realizes dynamic dedusting except mist；The flow direction of flue gas is vertical with filter bed 6, relies on " air-flow conveying+filter bed 6 retains+moisture film absorption, adhesion " combined effect, makes gas cleaning；Smoke content < 5mg/Nm after process3, reach the requirement of minimum discharge；The sulfuric acid mist of elimination major part simultaneously, reduces the risk of successor devices corrosion and blocking, extension device service life；This device can remove 3um and above ultra-fine droplet and dust, and demisting efficiency is up to more than 90%.Water cleaning assemblies 9 be connected to outside water circulation use assembly, compared with existing purifier, volume be only its 30%, take up an area space little, cost economize, resistance is low, and water consumption is few, wastewater flow rate is little.The Maintenance and Repair of this device are convenient, except can only silk screen layer be replaced when fog effect is deteriorated.
Of the present utility model ultimate principle, principal character and advantage have more than been shown and described.Skilled person will appreciate that of the industry, above-described embodiment does not limit this utility model in any form, and all employings are equal to the technical scheme that the mode of replacement or equivalent transformation obtains, and all fall within protection domain of the present utility model.
Claims (10)
1. the degree of depth removes mist dust arrester, it is characterized in that, including air inlet smoke box, dam and the rotation filter bed of the droplet that adsorbs in above-mentioned air inlet smoke box and flue dust, receiving the smoke box of giving vent to anger of gas through above-mentioned rotation filter bed, the water cleaning assemblies of above-mentioned rotation filter bed is also cleaned in submergence above-mentioned rotation filter bed one end.
2. the degree of depth according to claim 1 removes mist dust arrester, it is characterised in that above-mentioned rotation filter bed composition has: is connected to the housing of above-mentioned air inlet smoke box, smoke box of giving vent to anger, is placed in the cyclic transfer assembly in above-mentioned housing, wraps up the filter bed of above-mentioned cyclic transfer assembly.
3. the degree of depth according to claim 2 removes mist dust arrester, it is characterised in that above-mentioned rotation filter bed is at least one.
4. the degree of depth according to claim 2 removes mist dust arrester, it is characterized in that, above-mentioned cyclic transfer assembly composition has: two drive sprockets being placed in filter bed two ends, connects the chain of above-mentioned drive sprocket, is connected to above-mentioned drive sprocket the driven sprocket driving above-mentioned filter bed to move.
5. the degree of depth according to claim 4 removes mist dust arrester, it is characterised in that above-mentioned filter bed composition has: at least one piece of silk screen intercepter plate, connects the otic placode between above-mentioned silk screen intercepter plate and chain, is connected to the PTFE flexible cloth between above-mentioned silk screen intercepter plate.
6. the degree of depth according to claim 5 removes mist dust arrester, it is characterised in that above-mentioned silk screen intercepter plate composition has: silk screen layer, carries the framework of above-mentioned silk screen layer；Above-mentioned silk screen layer is made up of at least one of which silk screen, and the thickness of above-mentioned silk screen layer is 5-100mm.
7. the degree of depth according to claim 1 removes mist dust arrester, it is characterised in that above-mentioned water cleaning assemblies includes: bottom tank, connects the internal pipeline between the tank of above-mentioned bottom, is placed in the nozzle on the tank of above-mentioned bottom.
8. the degree of depth according to claim 1 removes mist dust arrester, it is characterised in that also include: be connected to the water circulation use assembly of above-mentioned water cleaning assemblies.
9. the degree of depth according to claim 1 removes mist dust arrester, it is characterised in that the flow direction of flue gas is perpendicular to above-mentioned rotation filter bed.
10. the degree of depth according to claim 1 removes mist dust arrester, it is characterised in that also include: be placed in above-mentioned air inlet smoke box and the airflow uniform distribution plate rotated between filter bed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521122749.XU CN205360931U (en) | 2015-12-31 | 2015-12-31 | Degree of depth defogging dust collector |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521122749.XU CN205360931U (en) | 2015-12-31 | 2015-12-31 | Degree of depth defogging dust collector |
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| Publication Number | Publication Date |
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| CN205360931U true CN205360931U (en) | 2016-07-06 |
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| CN201521122749.XU Active CN205360931U (en) | 2015-12-31 | 2015-12-31 | Degree of depth defogging dust collector |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105664629A (en) * | 2015-12-31 | 2016-06-15 | 国电南京自动化股份有限公司 | Deep fog and dust removal apparatus |
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2015
- 2015-12-31 CN CN201521122749.XU patent/CN205360931U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105664629A (en) * | 2015-12-31 | 2016-06-15 | 国电南京自动化股份有限公司 | Deep fog and dust removal apparatus |
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