CN204563830U - Cleanse system for soot - Google Patents
Cleanse system for soot Download PDFInfo
- Publication number
- CN204563830U CN204563830U CN201520255613.XU CN201520255613U CN204563830U CN 204563830 U CN204563830 U CN 204563830U CN 201520255613 U CN201520255613 U CN 201520255613U CN 204563830 U CN204563830 U CN 204563830U
- Authority
- CN
- China
- Prior art keywords
- clean room
- air exhauster
- hole
- clean
- communicates
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000004071 soot Substances 0.000 title claims abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 41
- 239000000779 smoke Substances 0.000 claims abstract description 30
- 238000000746 purification Methods 0.000 claims abstract description 19
- 239000003500 flue dust Substances 0.000 claims abstract description 10
- 230000008676 import Effects 0.000 claims abstract description 8
- 230000003020 moisturizing effect Effects 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 18
- 239000003546 flue gas Substances 0.000 abstract description 18
- 239000007789 gas Substances 0.000 abstract description 9
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 8
- 230000000694 effects Effects 0.000 description 4
- 239000012141 concentrate Substances 0.000 description 3
- 239000000428 dust Substances 0.000 description 3
- 239000010865 sewage Substances 0.000 description 3
- 238000003912 environmental pollution Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000010304 firing Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000000630 rising effect Effects 0.000 description 2
- 239000013589 supplement Substances 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 238000005202 decontamination Methods 0.000 description 1
- 230000003588 decontaminative effect Effects 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000001502 supplementing effect Effects 0.000 description 1
Landscapes
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
The utility model belongs to a kind of cleanse system for soot, formed primarily of flue dust import, clean gas outlet, air exhauster and filling pipe.Tank body inner route clapboard is longitudinally separated into several independently clean room sealed against one another, the upper end sidewall of each clean room is at least provided with 2 through holes, each purification locular wall of a corresponding through hole outer end is provided with an air exhauster, the air inlet of each air exhauster communicates with upper end space in the clean room of its lower end, in each clean room of through hole lower end, bottom is marked with filtered water, be provided with in each clean room and lead smoke pipe, stretch out filtered water to be tightly connected with a through hole and the outer end of this through hole communicates with the air outlet of air exhauster in Z-shaped one end of leading smoke pipe, the air inlet of this air exhauster communicates with upper end space in the clean room of its lower end.The utility model effectively can purify flue-gas, has structure simple, and purification cost is low, good purification, advantage environment friendly and pollution-free and easy to use.
Description
Technical field
The utility model belongs to a kind of cleanse system for soot.
Background technology
The firing equipment such as boiler, heating making fuel with coal can produce a large amount of flue-gas containing the polluter such as sulfur dioxide, dust, and these flue-gas directly enter in air along chimney, can cause serious environmental pollution, are detrimental to health.Especially the large-scale firing equipment such as large-sized boiler, industrial boiler and central heating smoke evacuation dust quantity is larger, more serious to gas, environmental pollution.Therefore, must carry out purification treatment to flue-gas, but oneself the purification treatment device structure that has is complicated at present, investment is large, purification treatment is with high costs, clean-up effect is also undesirable.
Summary of the invention
The purpose of this utility model is a kind of cleanse system for soot of design, effectively can purify flue-gas, has structure simple, and purification cost is low, good purification, advantage environment friendly and pollution-free and easy to use.
For this reason, the utility model is primarily of flue dust import, clean gas outlet, air exhauster and filling pipe formed, tank body inner route clapboard is longitudinally separated into several independently clean room sealed against one another, the upper end sidewall of each clean room is at least provided with 2 through holes, each purification locular wall of a corresponding through hole outer end is provided with an air exhauster, the air inlet of each air exhauster communicates with upper end space in the clean room of its lower end, in each clean room of through hole lower end, bottom is marked with filtered water, be provided with in each clean room and lead smoke pipe, stretch out filtered water to be tightly connected with a through hole and the outer end of this through hole communicates with the air outlet of air exhauster in Z-shaped one end of leading smoke pipe, the air inlet of this air exhauster communicates with upper end space in the clean room of its lower end, its remaining part horizontal leading smoke pipe is gathered in filtered water and on it venthole, clean gas outlet is the through hole being positioned at top clean room, the interior upper end of top clean room to be communicated filling pipe by moisturizing valve, the inner bottom part of two neighbouring clean rooms is communicated by the aqueduct of band water guide valve, the air inlet of the air exhauster communicated with lower end clean room through hole communicates flue dust import, the interior bottom of lower end clean room to be communicated blow-off pipe by blowoff valve.
The inner bottom part of described each clean room is provided with convex base plate.The quantity of described clean room is 3 ~ 9.Described convex base plate is the base plate that intermediate altitude is greater than four limit height, the triangular in shape or semicircular in shape of its cross section.The inwall of described each clean room is provided with the preserving timber bed of material.
Said structure reaches the purpose of this utility model.
The utility model effectively can purify flue-gas, has structure simple, and purification cost is low, good purification, advantage environment friendly and pollution-free and easy to use.The utility model can carry out repeatedly water filtration to flue-gas, and the decontamination index of the flue-gas after purification is higher than the discharge index of national regulation, and little power consumption, purification cost is low, and comparatively conventional purification apparatus saves integrated cost is 85%.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is the A-A cross-sectional view of Fig. 1.
Detailed description of the invention
As depicted in figs. 1 and 2, a kind of cleanse system for soot, formed primarily of flue dust import 15, clean gas outlet 1, air exhauster and filling pipe 6.Tank body 3 inner route clapboard 9 is longitudinally separated into several independently clean room sealed against one another.The upper end sidewall of each clean room is at least provided with 2 through holes.Each purification locular wall of a corresponding through hole outer end is provided with an air exhauster.The air inlet of each air exhauster communicates with upper end space in the clean room of its lower end.In each clean room of through hole lower end, bottom is marked with filtered water 18.Be provided with in each clean room and lead smoke pipe 22.Stretch out filtered water to be tightly connected with a through hole and the outer end of this through hole communicates with the air outlet of air exhauster in Z-shaped one end of leading smoke pipe, the air inlet of this air exhauster communicates with upper end space in the clean room of its lower end.Its remaining part horizontal leading smoke pipe is gathered in filtered water and on it venthole.Clean gas outlet is the through hole being positioned at top clean room.The interior upper end of top clean room to be communicated filling pipe by moisturizing valve 5.The inner bottom part of two neighbouring clean rooms is communicated by the aqueduct of band water guide valve 20.The air inlet of the air exhauster communicated with lower end clean room through hole communicates flue dust import 15, and the interior bottom of lower end clean room to be communicated blow-off pipe 25 by blowoff valve 24.
The inner bottom part of described each clean room is provided with convex base plate 23.The quantity of described clean room is 3 ~ 9.Described convex base plate is the base plate that intermediate altitude is greater than four limit height, the triangular in shape or semicircular in shape of its cross section.The inwall of described each clean room is provided with the preserving timber bed of material, as being provided with Anti-corrosion glass layer, in case inner tank wall is corroded.
As depicted in figs. 1 and 2, tank body 3 inner route clapboard 9 of the present utility model is longitudinally separated into four independently the first clean room 13 of clean room 17, second, the 3rd clean room 30 and the 4th clean rooms 2 sealed against one another.The upper end sidewall of each clean room is provided with 2 through holes.In each clean room of through hole lower end, bottom is marked with filtered water 18.Be provided with in each clean room and lead smoke pipe 22.Stretch out filtered water to be tightly connected with a through hole and the outer end of this through hole communicates with the air outlet of air exhauster in Z-shaped one end of leading smoke pipe, its remaining part horizontal leading smoke pipe is gathered in filtered water and on it venthole 19.
First clean room 17 can claim lower end clean room, and the air outlet 14 of (first) air exhauster 16 that a through hole of the first clean room communicates, is provided with in this clean room and leads smoke pipe 22.Stretch out filtered water in Z-shaped one end of leading smoke pipe to communicate with the air outlet of this air exhauster.Its remaining part horizontal leading smoke pipe is gathered in filtered water and on it venthole 19.The communicate interior bottom of flue dust import 15, first clean room (lower end clean room) of the air inlet of this air exhauster to be communicated blow-off pipe 25 by blowoff valve 24.The sewage of discharging from the first clean room inner bottom part can concentrate on cesspool, through chemical neutralization, precipitation, filtration treatment, mechanical centrifugal, clean water can recycle recycling, centrifugal sediment be used as to carry sulphur and it.
The air inlet 27 being positioned at (second) air exhauster 28 on the second clean room 13 lateral wall is communicated with the first clean room 17 upper end space of its lower end by exhaust tube 26.Be provided with in this clean room 13 and lead smoke pipe.Stretch out filtered water in Z-shaped one end of leading smoke pipe to communicate with the air outlet 29 of this air exhauster 28, its remaining part horizontal leading smoke pipe is gathered in filtered water and on it venthole.
The air inlet 12 being positioned at (the 3rd) air exhauster 11 on the 3rd clean room 30 lateral wall is communicated with the second clean room 13 upper end space of its lower end by exhaust tube.Be provided with in this clean room 30 and lead smoke pipe.Stretch out filtered water in Z-shaped one end of leading smoke pipe to communicate with the air outlet 10 of this air exhauster 11, its remaining part horizontal leading smoke pipe is gathered in filtered water and on it venthole.
4th clean room 2 can claim top clean room, and the air inlet 31 being positioned at (the 4th) air exhauster 8 on the 4th clean room's lateral wall is communicated with the 3rd clean room 30 upper end space of its lower end by exhaust tube.Be provided with in this clean room 2 and lead smoke pipe.Stretch out filtered water in Z-shaped one end of leading smoke pipe to communicate with the air outlet 7 of this air exhauster 8, its remaining part horizontal leading smoke pipe is gathered in filtered water and on it venthole.Clean gas outlet 1 is for being positioned at a through hole of top clean room.The interior upper end of top clean room to be communicated filling pipe 6 by moisturizing valve 5, for supplementing filtered water in clean room.
The inner bottom part of two neighbouring clean rooms is communicated by the aqueduct 21 of band water guide valve 20; That is: the 4th clean room communicates by being with the aqueduct of water guide valve with the inner bottom part of the 3rd clean room, 3rd clean room communicates by being with the aqueduct of water guide valve with the inner bottom part of the second clean room, and the second clean room communicates by being with the aqueduct of water guide valve with the inner bottom part of the first clean room.Aqueduct with water guide valve can be one or several.Its effect opens water guide valve to supplement filtered water to the clean room of its lower end by the clean room being positioned at upper end and to hold concurrently draining-off sewage.Inner bottom part due to each clean room is provided with convex base plate, dirt mainly concentrates on the periphery of inner bottom part, the aqueduct opening water guide valve can to supplement filtered water by the clean room being positioned at upper end and to hold concurrently draining-off sewage to the clean room of its lower end, final dirt concentrates on the inner bottom part of the first clean room, and the blow-off pipe communicated by band blowoff valve by bottom in it is entered in cesspool.
During use, by the first air exhauster 16 by the coal-fired flue-gas containing sulfur dioxide and dust from leading in smoke pipe exhaust opening suction first clean room of boiler, and the venthole gathered on it enters in the filtered water that in this clean room, bottom is marked with, the sulfur dioxide in flue gas and dust are blended in filtered water by gas-vapor mix effect.Flue gas rising aqueous vapor is separated.The flue gas body cleaned through first time is arranged in the upper space of the first clean room.Second air exhauster 28 the flue gas body being arranged in first clean room's upper space is extracted out from its air inlet and inject the second clean room from its air outlet lead smoke pipe, and the venthole gathered on it enters in the filtered water that in this clean room, bottom is marked with, the sulfur dioxide in flue gas and dust are blended in filtered water by gas-vapor mix effect.Flue gas rising aqueous vapor is separated, and the flue gas body through cleaning for the second time is arranged in the upper space of the second clean room.The like, the flue gas body through four purifications becomes clean gas and discharges tank body along clean gas outlet.
Each clean room air exhauster used, lead the quantity of smoke pipe and aqueduct, set according to need, therefore be not repeated.
In a word, this practicality newly effectively can purify flue-gas, has structure simple, and purification cost is low, good purification, advantage environment friendly and pollution-free and easy to use.
Claims (5)
1. a cleanse system for soot, primarily of flue dust import, clean gas outlet, air exhauster and filling pipe formed, it is characterized in that: tank body inner route clapboard is longitudinally separated into several independently clean room sealed against one another, the upper end sidewall of each clean room is at least provided with 2 through holes, each purification locular wall of a corresponding through hole outer end is provided with an air exhauster, the air inlet of each air exhauster communicates with upper end space in the clean room of its lower end, in each clean room of through hole lower end, bottom is marked with filtered water, be provided with in each clean room and lead smoke pipe, stretch out filtered water to be tightly connected with a through hole and the outer end of this through hole communicates with the air outlet of air exhauster in Z-shaped one end of leading smoke pipe, the air inlet of this air exhauster communicates with upper end space in the clean room of its lower end, its remaining part horizontal leading smoke pipe is gathered in filtered water and on it venthole, clean gas outlet is the through hole being positioned at top clean room, the interior upper end of top clean room to be communicated filling pipe by moisturizing valve, the inner bottom part of two neighbouring clean rooms is communicated by the aqueduct of band water guide valve, the air inlet of the air exhauster communicated with lower end clean room through hole communicates flue dust import, the interior bottom of lower end clean room to be communicated blow-off pipe by blowoff valve.
2., by cleanse system for soot according to claim 1, it is characterized in that: the inner bottom part of described each clean room is provided with convex base plate.
3., by cleanse system for soot according to claim 1, it is characterized in that: the quantity of described clean room is 3 ~ 9.
4. by cleanse system for soot according to claim 2, it is characterized in that: described convex base plate is the base plate that intermediate altitude is greater than four limit height, the triangular in shape or semicircular in shape of its cross section.
5., by cleanse system for soot according to claim 1, it is characterized in that: the inwall of described each clean room is provided with the preserving timber bed of material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520255613.XU CN204563830U (en) | 2015-04-27 | 2015-04-27 | Cleanse system for soot |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520255613.XU CN204563830U (en) | 2015-04-27 | 2015-04-27 | Cleanse system for soot |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204563830U true CN204563830U (en) | 2015-08-19 |
Family
ID=53856524
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520255613.XU Expired - Fee Related CN204563830U (en) | 2015-04-27 | 2015-04-27 | Cleanse system for soot |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204563830U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109173499A (en) * | 2018-09-07 | 2019-01-11 | 安徽英冉信息咨询有限公司 | The environmental protection equipment absorbed for dust pollution |
| CN111155949A (en) * | 2020-01-04 | 2020-05-15 | 重庆环科源博达环保科技有限公司 | Oil-based drilling cutting treatment method and gas purification device applied to same |
-
2015
- 2015-04-27 CN CN201520255613.XU patent/CN204563830U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109173499A (en) * | 2018-09-07 | 2019-01-11 | 安徽英冉信息咨询有限公司 | The environmental protection equipment absorbed for dust pollution |
| CN109173499B (en) * | 2018-09-07 | 2021-04-09 | 合肥千聚环保科技有限公司 | Environment-friendly equipment for absorbing flying dust pollution |
| CN111155949A (en) * | 2020-01-04 | 2020-05-15 | 重庆环科源博达环保科技有限公司 | Oil-based drilling cutting treatment method and gas purification device applied to same |
| CN111155949B (en) * | 2020-01-04 | 2021-09-24 | 重庆环科源博达环保科技有限公司 | Oil-based drilling cutting treatment method and gas purification device applied to same |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105964124A (en) | Rotary spraying dust removal and desulfurization device | |
| CN206198997U (en) | Flue gas desulfurization denitration dust-removing system | |
| CN204563830U (en) | Cleanse system for soot | |
| CN201192623Y (en) | Integrated equipment with smoke-elimination, dust-removal, desulfurization and denitrification | |
| CN207187376U (en) | A kind of venturi spray water film Multistage desulfuration deduster | |
| CN201880472U (en) | Flue gas desulfurizing and dedusting device for industrial coal-fired boiler | |
| CN105435590A (en) | Purification system of waste gas purification tower | |
| CN203750348U (en) | Secondary smoke dust purification system | |
| CN205216519U (en) | Waste gas purification clean system | |
| CN102489094B (en) | A closed dust and sulfur removal device for boiler flue gas | |
| CN201115812Y (en) | Combined granite dedusting and desulfurization device | |
| CN205461749U (en) | High -efficient dust removal SOx/NOx control device | |
| CN100488599C (en) | Water-absorbing type assembled highly-effective dust-removing desulfurizing device | |
| CN205815393U (en) | Highly effective integration spray column | |
| CN204412054U (en) | A kind of wet flue gas desulfurization tower | |
| CN209752544U (en) | Boiler tail gas treatment equipment | |
| CN203790829U (en) | Purification tower and deep flue gas purification system | |
| CN202823156U (en) | Venturi type siphon atomizing lime method-based desulfurizing emission reduction device | |
| CN203108413U (en) | Oxynitride absorption device | |
| CN104289094A (en) | Waste gas filtering and purifying device | |
| CN207153454U (en) | Water spray tower with multiple flow-disturbing and spraying effect | |
| CN206424787U (en) | Feed Manufacturing exhaust treatment system | |
| CN203108426U (en) | Dust-containing and sulfur-containing flue gas purifying device | |
| CN206310518U (en) | Gas fired-boiler smoke eliminator | |
| CN205569989U (en) | Boiler flue gas dust removal clarifier |
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: 20150819 Termination date: 20190427 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |