CN208975502U - Sintering device flue gas integrates denitrification apparatus - Google Patents
Sintering device flue gas integrates denitrification apparatus Download PDFInfo
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- CN208975502U CN208975502U CN201821164360.5U CN201821164360U CN208975502U CN 208975502 U CN208975502 U CN 208975502U CN 201821164360 U CN201821164360 U CN 201821164360U CN 208975502 U CN208975502 U CN 208975502U
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Abstract
The utility model belongs to a kind of comprehensive denitrification apparatus of sintering device flue gas, its main feature is that: inner flue is equipped in flue collector, inner flue front end is equipped with preceding fixing closing plate, and its rear end is equipped with rear fixing closing plate, between have inner flue bracket;In high temperature section flue collector side, equipped with 1-5 high-temperature flue mouth, collect and is connected to high-temperature flue, intrinsic blinds baffle plate on floss hole, high-temperature flue is supported by bracket, is connected with SCR reactor head, and SCR reactor bottom tube is connected with flue collector, flue collector is connected with desulfurizing tower, and exhaust fan, ozone blowing area and ozone hybrid reaction area are equipped on flue collector.The device, high temperature section flue gas are directly led out, and enter SCR reactor denitration with ammonia, then through ozone denitration, it can be achieved that in full flue gas NOx minimum discharge, be the comprehensive denitrification apparatus of comparatively ideal sintering device flue gas.
Description
Technical field
The utility model relates to sintering device flue gas processing equipments, are a kind of comprehensive denitrification apparatus of sintering device flue gas.
Background technique
Currently, sintering machine denitration mostly uses SCR denitration, and although this method denitration effect is pretty good, SCR denitration
It is required that flue gas is at 300 DEG C or more, sintered compound flue-gas temperature is low, about only 120-150 DEG C or so, so some is added using coal gas
The mode of heating of exchanging heat again after heat heats up.Equipment needed for this heating means is all very huge, and investment is big, takes up a large area, and transports
Row maintenance cost is high.Chinese patent ZL201720170462.7 in 2017 discloses a kind of " sintering machine SCR denitration system ", takes
High temperature section flue gas carries out SCR denitration, although this technique is fine, only high temperature section denitration is selected to be difficult to realize in full flue gas
The minimum discharge of NOx, in addition, there is a valve on its every smoke pipe, flue-gas temperature is high, and valve is easy to damage, and not easy to repair
And replacement.
Summary of the invention
The purpose of the utility model is to provide a kind of comprehensive denitrification apparatus of sintering device flue gas, are set with solving existing heating means
It is standby all very huge, it takes up a large area, investment is big, and operating cost is high;Sintering machine SCR denitration system, it is difficult to realize NOx in full flue gas
Minimum discharge, have a valve on every smoke pipe, flue-gas temperature is high, and valve is easy to damage, and not easy to repair and replacement
Problem.
Purpose of the utility model is realized as follows: the sintering device flue gas integrates denitrification apparatus, comprising: sintering owner's cigarette
Road, inner flue, side smoke tube, ammonia system processed, SCR reactor, exhaust fan, ozone blowing area, ozone hybrid reaction area, ozone processed are set
Standby, desulfurizing tower and ash-discharging device, its main feature is that: inner flue is equipped in flue collector, inner flue front end is equipped with preceding fixing closing plate,
Rear end is equipped with rear fixing closing plate, between have an inner flue bracket, the side smoke tube point left and right sides, every side has 23, and 1-3 is section of igniting,
4-15 is high temperature section, and 16-23 is cooling section, the flue collector side between side smoke tube 4 to 15, is equipped with 1-5 high-temperature flue mouth,
Blinds baffle plate is equipped on high-temperature flue mouth, high-temperature flue mouth, which collects, is connected to high-temperature flue, and high-temperature flue is supported by bracket,
It is connected with SCR reactor head, SCR reactor bottom tube is connected with flue collector, and flue collector is connected with desulfurizing tower, in flue collector
It is equipped with exhaust fan, ozone blowing area and ozone hybrid reaction area.
Working principle;High-temperature flue gas removes bulky grain dust, is mixed into along high-temperature flue and ammonia through blinds baffle plate
SCR reactor, after denitration with ignite section and cooling section flue gas mixes, enter ozone blowing area and smelly along flue collector through exhaust fan
Oxygen hybrid reaction area, the lower valency NOx in flue gas is oxidized to high-valence state NOx soluble easily in water, into desulfurizing tower and hydroxide
Calcium reacts, and after the NOx in flue gas absorbs removal in desulfurizing tower, is discharged through desulfurizing tower chimney.
The blinds and vertical axis angle of blinds baffle plate are 45 ° -60 °.
The utility model has the advantage that (1) high temperature section flue gas is directly led out compared with prior art, anti-into SCR
Device denitration is answered, heated by gas is not had to, compared with heating means simple process, saves heating equipment, occupied area is small, small investment, energy consumption
It is low, operating cost is low;(2) compared with sintering machine SCR denitration system, eliminate valve, it is easy to damage to solve valve, and it is not easy to repair more
It changes, it is difficult to realize the minimum discharge problem of NOx in full flue gas.
Detailed description of the invention
Fig. 1 is the comprehensive denitrification apparatus structural schematic diagram of sintering device flue gas;
Fig. 2 is A-A cross-sectional view.
Specific embodiment
In Fig. 1: Main Gas Flue of Sintering Machine 1, inner flue 4, side smoke tube 2, the side smoke tube point left and right sides, every side have 23,1-3
For section of igniting, 4-15 is high temperature section, and 16-23 is cooling section, ammonia system 6 processed, SCR reactor 8, exhaust fan 14, ozone devices processed
12, ozone blowing area 9, ozone hybrid reaction area 10, desulfurizing tower 11 and ash-discharging device 16.These are identical with the prior art,
Except that: inner flue 4 is equipped in flue collector, inner flue front end is equipped with preceding fixing closing plate 3, after inner flue end is equipped with
Fixing closing plate 5, between have inner flue bracket 17, the high temperature section flue collector side between side smoke tube 4 to 15, be equipped with it is 1-5 high
Warm floss hole collects and is connected to high-temperature flue 7, and intrinsic blinds baffle plate 18, blinds are with vertical axis angle on each floss hole
45°-60°.High-temperature flue is supported by bracket 15 to be connected with SCR reactor head, and ammonia system processed is connected with high-temperature flue, draws
The NH entered3It is mixed into SCR reactor with high-temperature flue gas, bottom tube is connected with flue collector, and side smoke tube 1-3 ignites section and 16-23
Cooling section is connected with flue collector 1, exhaust fan 14 is equipped on flue collector, ozone is blown area 9, ozone hybrid reaction area 10, master
Flue is connected with desulfurizing tower 11.High-temperature flue gas enters SCR reactor, 70- under the action of exhaust fan, along high-temperature flue 7
80% NOx is divested, then with ignite section and cooling section low-temperature mixed flue gas 13 mixes, enter ozone blowing along inner flue
Area, ozone hybrid reaction area, the low price NOx in flue gas is oxidized to high price NOx soluble easily in water, into desulfurizing tower and hydroxide
Calcium reaction, to achieve the purpose that smoke comprehensive denitration, the neat stress after denitration is discharged from desulfurizing tower chimney.
Claims (2)
1. a kind of comprehensive denitrification apparatus of sintering device flue gas, comprising: Main Gas Flue of Sintering Machine (1), inner flue (4), side smoke tube (2), system
Ammonia system (6), SCR reactor (8), exhaust fan (14), ozone are blown area (9), ozone hybrid reaction area (10), ozone devices processed
(12), desulfurizing tower (11) and ash-discharging device (16), it is characterised in that: inner flue is equipped in flue collector, inner flue front end is equipped with
Preceding fixing closing plate (3), its rear end are equipped with rear fixing closing plate (5), between have inner flue bracket (17), side smoke tube (2) is divided to or so two
Side, every side have 23, and 1-3 is section of igniting, and 4-15 is high temperature section, and 16-23 is cooling section, the main cigarette between side smoke tube 4 to 15
Road side is equipped with 1-5 high-temperature flue mouth, blinds baffle plate (18) is equipped on high-temperature flue mouth, high-temperature flue mouth collects company
It passes to high-temperature flue (7) high-temperature flue to be supported by bracket (15), be connected with SCR reactor head, SCR reactor bottom tube and master
Flue (1) is connected, and flue collector is connected with desulfurizing tower, and it is mixed that exhaust fan, ozone blowing area and ozone are equipped on flue collector (1)
Close reaction zone.
2. the comprehensive denitrification apparatus of sintering device flue gas according to claim 1, it is characterised in that: the blinds of blinds baffle plate (18)
It is 45 ° -60 ° with vertical axis angle.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201821164360.5U CN208975502U (en) | 2018-07-16 | 2018-07-16 | Sintering device flue gas integrates denitrification apparatus |
Applications Claiming Priority (1)
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CN201821164360.5U CN208975502U (en) | 2018-07-16 | 2018-07-16 | Sintering device flue gas integrates denitrification apparatus |
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CN208975502U true CN208975502U (en) | 2019-06-14 |
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2018
- 2018-07-16 CN CN201821164360.5U patent/CN208975502U/en active Active
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GR01 | Patent grant | ||
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TR01 | Transfer of patent right |
Effective date of registration: 20210929 Address after: 102600 507, 5th floor, building 2, courtyard 11, Tianhua North Street, Daxing District Economic and Technological Development Zone, Beijing (Yizhuang group, high end industrial area, Beijing Pilot Free Trade Zone) Patentee after: BEIJING HUIPU ENVIRONMENTAL PROTECTION TECHNOLOGY Co.,Ltd. Address before: 056002 Block B, Shenghai Blue County, 516 Lianfeng East Road, Congtai District, Handan City, Hebei Province, 2001 Patentee before: Bian Fulin |
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TR01 | Transfer of patent right |