CN205760573U - A kind of boiler flue gas desulfurization depurator - Google Patents
A kind of boiler flue gas desulfurization depurator Download PDFInfo
- Publication number
- CN205760573U CN205760573U CN201620744558.5U CN201620744558U CN205760573U CN 205760573 U CN205760573 U CN 205760573U CN 201620744558 U CN201620744558 U CN 201620744558U CN 205760573 U CN205760573 U CN 205760573U
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- Prior art keywords
- depurator
- flue gas
- gas desulfurization
- boiler flue
- air inlet
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Abstract
This utility model relates to field of Environment Protection, it is specially a kind of boiler flue gas desulfurization depurator, it is characterized by that depurator is internal and be divided into dehydration outer row room 12 by water fender 11 from top to bottom, surge chamber 13, spray process chamber 14, minor air cell 15, bathing in a common bathing pool collecting chamber 16, described spray process chamber 14 includes flue gas shunting plate 131, smoke air inlet 142, it is positioned at two grades of spray equipments 143 of smoke air inlet 142 periphery, it is positioned at the one-level spray equipment 144 of smoke air inlet 142 bottom, smoke air inlet 142 and the inclined room 145 of one-level spray equipment 144 periphery, water fender 11 fixing on spray process chamber 14 inwall and inclined room 145 outer wall；Described minor air cell 15 includes that the eddy current baffle plate 151 being fixed on water fender 11, described eddy current baffle plate 151 are semicircle, and decurvation.By boiler flue gas desulfurization depurator structure is transformed and optimized, further increase purification efficiency and desulfuration efficiency, and this utility model simple in construction, low cost of manufacture, be suitable to popularization and application.
Description
Technical field
This utility model relates to field of Environment Protection, is specially a kind of boiler flue gas desulfurization depurator.
Background technology
Acid rain be we face now, one of significantly more air quality problems.Acidic materials and resulting in
The compound of acidic materials, generates when burning mineral fuel generates electricity and provides transport.These materials are mainly from sulfur
The acid that oxide and nitrogen oxides derive, the essential measure of control of acid rain is to reduce sulfur dioxide and the row of nitrogen oxides
Put.In order to reduce the various strategical decisions of acid rain, the investment of tens dollars may be needed every year, due to costly, so
Must stop, from fume emission, the source that acid rain generates, boiler flue gas desulfurization depurator can be good at flue gas ash removal, desulfurization,
And purifying smoke enters air.But desulfurizing purifier udst separation efficiency and desulfuration efficiency are not ideal enough at present.
Summary of the invention
This utility model, by boiler flue gas desulfurization depurator structure being transformed, improves purification efficiency and desulfurization effect
Rate.
For achieving the above object, the following technical scheme of this utility model offer:
A kind of boiler flue gas desulfurization depurator, including shell 1, is characterized by that the internal water fender 11 that passes through of depurator is from up to
Under be divided into dehydration outer row room 12, surge chamber 13, spray process chamber 14, minor air cell 15, bathing in a common bathing pool collecting chamber 16, arrange room outside described dehydration
12 are positioned at depurator top, including the dehydrations being positioned at the clean gas outlet 121 of depurator top, clean gas outlet 121 connects below
Device 122；Described surge chamber 13 includes water fender 11 fixing on flue gas shunting plate 131, process chamber inwall；Described spray processes
Room 14 includes flue gas shunting plate 131, smoke air inlet 142, is positioned at two grades of spray equipments 143, positions of smoke air inlet 142 periphery
One-level spray equipment 144, smoke air inlet 142 and the inclined room of one-level spray equipment 144 periphery in smoke air inlet 142 bottom
145, water fender 11 fixing on process chamber 14 inwall and inclined room 145 outer wall is sprayed；Described minor air cell 15 includes being fixed on dash
Eddy current baffle plate 151 on plate 11, described eddy current baffle plate 151 is semicircle, and decurvation；Described bathing in a common bathing pool collecting chamber 16 includes
The sewage draining exit 161 of bottom and valve 162.
Optimization of the present utility model, according to a kind of boiler flue gas desulfurization depurator described above, it is characterized by described only
Change device inwall and be provided with corrosion-proof lining.
Further, according to a kind of boiler flue gas desulfurization depurator described in the top, it is characterized by described one-level spray dress
Putting 144 is atomizer.
Further, according to a kind of boiler flue gas desulfurization depurator described in the top, it is characterized by described two grades of spray dresses
Putting 143 is atomizer.
Further, according to a kind of boiler flue gas desulfurization depurator described in the top, it is characterized by described two grades of spray dresses
Putting 143 hydrojets is sodium hydroxide, sodium carbonate, the inorganic aqueous alkali of sodium bicarbonate class.
Further, according to a kind of boiler flue gas desulfurization depurator described in the top, it is characterized by described flue gas shunting plate
131 is cone cover body.
Further, according to a kind of boiler flue gas desulfurization depurator described in the top, it is characterized by described bathing in a common bathing pool collecting chamber
16 is inverted cone.
Further, according to a kind of boiler flue gas desulfurization depurator described in the top, it is characterized by described bathing in a common bathing pool collecting chamber
16 and the outer side of junction, minor air cell 15 the internal phase of spill box 163, spill box 163 outlet and depurator is set
Logical.
Further, according to a kind of boiler flue gas desulfurization depurator described in the top, it is characterized by described a kind of boiler
Gas vulcanizing-cleaning apparatus, is characterized by that described dehydration device 122 is carbon adsorption layer.
Operation principle of the present utility model is: dusty gas enters in desulfurizing purifier, with cigarette by smoke air inlet 142
The one-level spray equipment 144 of gas air inlet 142 sprays liquid and forward contacts, and flue gas is carried out primary purification process, and then flue gas changes
Change direction downwards directly to impact the water surface at a high speed, make the micronic dust particle in flue gas and SO2Adsorbed completely by water, precipitate, then flue gas
Through eddy current baffle plate 151 and water surface path clearance, enter the two inclined rooms of sidewind 145, flue gas and two grades of spray equipment 143 injections
Being formed containing alkali liquor seethes with excitement to swash spatters washing state, is fully contacted mixing, makes flue gas obtain after-treatment, and then flue gas rises, then with
Two top, sidewind inclined rooms doctor solution after spray atomizing inversely contacts, adsorbs, and makes flue gas obtain three purified treatment, desulfurization
Flue gas after purification reduces air velocity in entering flue gas surge chamber 13, more purified device outlet dehydrating demisting device 12 removes cigarette
Entering air through chimney after fine droplet in gas, the dust of depurator collection and desulfurization product are subsequently in bathing in a common bathing pool collecting chamber 16
Sedimentation, is periodically discharged by sewage draining exit 161, and the absorption serosity beyond working water level is discharged by overflow pipe 163.
The beneficial effects of the utility model are: a kind of boiler flue gas desulfurization depurator is by by boiler flue gas desulfurization depurator
Structure is transformed and has been optimized, and further increases purification efficiency and desulfuration efficiency, and this utility model simple in construction, system
Make low cost, be suitable to popularization and application.
Accompanying drawing explanation
Fig. 1 is front view of the present utility model；
In figure: shell-1, water fender-11, dehydration be outer arrange room-12, clean gas outlet-121, dehydration device-122, surge chamber-
13, flue gas shunting plate-131, spray process chamber-14, smoke air inlet-142, two grades of spray equipments-143, one-level spray equipment-
144, inclined room-145, minor air cell-15, eddy current baffle plate-151, bathing in a common bathing pool collecting chamber-16, sewage draining exit-161, valve-162, overflow water
Case-163.
Detailed description of the invention
Below in conjunction with the accompanying drawing in this utility model embodiment, the technical scheme in this utility model embodiment is carried out
Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of this utility model rather than whole
Embodiment.Based on the embodiment in this utility model, those of ordinary skill in the art are not under making creative work premise
The every other embodiment obtained, broadly falls into the scope of this utility model protection.
A kind of embodiment that this utility model provides: refer to Fig. 1,
A kind of boiler flue gas desulfurization depurator, including shell 1, is characterized by that the internal water fender 11 that passes through of depurator is from up to
Under be divided into dehydration outer row room 12, surge chamber 13, spray process chamber 14, minor air cell 15, bathing in a common bathing pool collecting chamber 16, arrange room outside described dehydration
12 are positioned at depurator top, including the dehydrations being positioned at the clean gas outlet 121 of depurator top, clean gas outlet 121 connects below
Device 122；Described surge chamber 13 includes water fender 11 fixing on flue gas shunting plate 131, process chamber inwall；Described spray processes
Room 14 includes flue gas shunting plate 131, smoke air inlet 142, is positioned at two grades of spray equipments 143, positions of smoke air inlet 142 periphery
One-level spray equipment 144, smoke air inlet 142 and the inclined room of one-level spray equipment 144 periphery in smoke air inlet 142 bottom
145, water fender 11 fixing on process chamber 14 inwall and inclined room 145 outer wall is sprayed；Described minor air cell 15 includes being fixed on dash
Eddy current baffle plate 151 on plate 11, described eddy current baffle plate 151 is semicircle, and decurvation；Described bathing in a common bathing pool collecting chamber 16 includes
The sewage draining exit 161 of bottom and valve 162.
Wherein said depurator inwall is provided with corrosion-proof lining；144, two grades of spray equipments 143 of described one-level spray equipment are
Atomizer；Described two grades of spray equipment 143 hydrojets are sodium hydroxide, sodium carbonate, the inorganic aqueous alkali of sodium bicarbonate class；Described flue gas
Flow distribution plate 131 is cone cover body；Described bathing in a common bathing pool collecting chamber 16 is inverted cone；Described bathing in a common bathing pool collecting chamber 16 and minor air cell 15 hand over
The outer side at the place of connecing arranges spill box 163, and spill box 163 outlet communicates with inside depurator；Described dehydration dress
Put 122 for carbon adsorption layer.
This utility model is not limited to the details of above-mentioned one exemplary embodiment, and without departing substantially from spirit of the present utility model or
In the case of basic feature, it is possible to realize this utility model in other specific forms.Therefore, no matter from the point of view of which point, all
Should regard embodiment as exemplary, and be nonrestrictive, scope of the present utility model is by claims not
It is that described above limits, it is intended that all changes fallen in the implication of equivalency and scope of claim are included
In this utility model.Should not be considered as limiting involved claim by any reference in claim.
Claims (9)
1. a boiler flue gas desulfurization depurator, including shell (1), is characterized by that the internal water fender (11) that passes through of depurator is from upper
It is divided under to outside dehydration and arranges room (12), surge chamber (13), spray process chamber (14), minor air cell (15), bathing in a common bathing pool collecting chamber (16), institute
Arranging room (12) is positioned at depurator top outward to state dehydration, exports (121), the outlet of clean gas including the clean gas being positioned at depurator top
(121) the dehydration device (122) connected below；Described surge chamber (13) includes on flue gas shunting plate (131), process chamber inwall solid
Fixed water fender (11)；Described spray process chamber (14) includes flue gas shunting plate (141), smoke air inlet (142), is positioned at flue gas
Two grades of spray equipments (143) of air inlet (142) periphery, it is positioned at the one-level spray equipment of smoke air inlet (142) bottom
(144), smoke air inlet (142) and one-level spray equipment (144) periphery inclined room (145), spray process chamber (14) inwall and
Partially fixing on room (145) outer wall water fender (11)；Described minor air cell (15) includes the eddy current gear being fixed on water fender (11)
Plate (151), described eddy current baffle plate (151) is semicircle, and decurvation；Described bathing in a common bathing pool collecting chamber (16) includes the row of bottom
Dirty mouth (161) and valve (162).
A kind of boiler flue gas desulfurization depurator the most according to claim 1, is characterized by that described depurator inwall is provided with anti-
Rotten liner.
A kind of boiler flue gas desulfurization depurator the most according to claim 1, is characterized by described one-level spray equipment (144)
It it is atomizer.
A kind of boiler flue gas desulfurization depurator the most according to claim 1, is characterized by described two grades of spray equipments (143)
It it is atomizer.
A kind of boiler flue gas desulfurization depurator the most according to claim 4, is characterized by described two grades of spray equipments (143)
Hydrojet is sodium hydroxide, sodium carbonate, the inorganic aqueous alkali of sodium bicarbonate class.
A kind of boiler flue gas desulfurization depurator the most according to claim 1, is characterized by that described flue gas shunting plate (131) is
Cone cover body.
A kind of boiler flue gas desulfurization depurator the most according to claim 1, is characterized by that described bathing in a common bathing pool collecting chamber (16) is
Inverted cone.
A kind of boiler flue gas desulfurization depurator the most according to claim 1, it is characterized by described bathing in a common bathing pool collecting chamber (16) and
The outer side of minor air cell (15) junction is arranged inside spill box (163), spill box (163) outlet and depurator
Communicate.
A kind of boiler flue gas desulfurization depurator the most according to claim 1, is characterized by that described dehydration device (122) is carbon
Adsorption layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620744558.5U CN205760573U (en) | 2016-07-15 | 2016-07-15 | A kind of boiler flue gas desulfurization depurator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620744558.5U CN205760573U (en) | 2016-07-15 | 2016-07-15 | A kind of boiler flue gas desulfurization depurator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205760573U true CN205760573U (en) | 2016-12-07 |
Family
ID=58122518
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620744558.5U Expired - Fee Related CN205760573U (en) | 2016-07-15 | 2016-07-15 | A kind of boiler flue gas desulfurization depurator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205760573U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107551789A (en) * | 2017-09-28 | 2018-01-09 | 苏州百硕自动化环保设备有限公司 | A kind of centrifugal smoke eliminator |
| CN111821833A (en) * | 2020-08-11 | 2020-10-27 | 苏州仕净环保科技股份有限公司 | Extension turbulent desulfurization and denitrification integrated device |
| CN116899369A (en) * | 2023-09-14 | 2023-10-20 | 泉州兴跃机械有限公司 | Flue gas treatment system of asphalt mixing plant and working method thereof |
-
2016
- 2016-07-15 CN CN201620744558.5U patent/CN205760573U/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107551789A (en) * | 2017-09-28 | 2018-01-09 | 苏州百硕自动化环保设备有限公司 | A kind of centrifugal smoke eliminator |
| CN107551789B (en) * | 2017-09-28 | 2023-09-15 | 池州市琼琚信息技术服务有限公司 | Centrifugal type flue gas purifying device |
| CN111821833A (en) * | 2020-08-11 | 2020-10-27 | 苏州仕净环保科技股份有限公司 | Extension turbulent desulfurization and denitrification integrated device |
| CN116899369A (en) * | 2023-09-14 | 2023-10-20 | 泉州兴跃机械有限公司 | Flue gas treatment system of asphalt mixing plant and working method thereof |
| CN116899369B (en) * | 2023-09-14 | 2023-12-01 | 泉州兴跃机械有限公司 | Flue gas treatment system of asphalt mixing plant and working method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 115000 Dongcheng Office of Gaizhou City, Liaoning Province, white fruit Village Patentee after: Liaoning Zhiyuan Environmental Protection Engineering Co. Ltd. Address before: 115000 Dongcheng Office of Gaizhou City, Liaoning Province, white fruit Village Patentee before: YINGKOU HUIYUAN BOILER EQUIPMENTS MANUFACTURING CO., LTD. |
|
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20161207 Termination date: 20190715 |