CN205886561U - Ozone flow field injection apparatus - Google Patents

Ozone flow field injection apparatus Download PDF

Info

Publication number
CN205886561U
CN205886561U CN201620723440.4U CN201620723440U CN205886561U CN 205886561 U CN205886561 U CN 205886561U CN 201620723440 U CN201620723440 U CN 201620723440U CN 205886561 U CN205886561 U CN 205886561U
Authority
CN
China
Prior art keywords
nozzle
arm
branch pipe
adjacent
ozone
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.)
Active
Application number
CN201620723440.4U
Other languages
Chinese (zh)
Inventor
李银娣
庞凯博
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jiangsu Tian Tian Environmental Protection Engineering Co Ltd
Original Assignee
Jiangsu Tian Tian Environmental Protection Engineering Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Jiangsu Tian Tian Environmental Protection Engineering Co Ltd filed Critical Jiangsu Tian Tian Environmental Protection Engineering Co Ltd
Priority to CN201620723440.4U priority Critical patent/CN205886561U/en
Application granted granted Critical
Publication of CN205886561U publication Critical patent/CN205886561U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Treating Waste Gases (AREA)

Abstract

The utility model discloses an ozone flow field injection apparatus, including house steward, intercommunication the branch pipe and the setting of house steward's a plurality of just equidistant settings that are parallel to each other are in the ascending a plurality of nozzles of branch pipe axle, the branch pipe stretch into in the flue section and perpendicular to flue section is arranged, the nozzle set up along the branch pipe axial equidistantly, the nozzle is located one side towards the flue gas incoming flow of branch pipe, the mutual -Offset of nozzle on the adjacent branch pipe, are the spray direction of nozzle and the contained angle between the flue gas flow direction 100 175 the degree, is distance between the adjacent branch pipe 100mm 200mm, is the interval that adjacent nozzle was gone up to every spinal branch pipe 200mm 300mm, the device makes ozone distribute in the flue evenly, increase substantially ozone oxidation nitrogen oxide's efficiency.

Description

A kind of ozone flow field injection apparatus
Technical field
The utility model belongs to the air contaminant treatment field of discharged from coal-fired boiler, particularly to a kind of injection of ozone flow field Device.
Background technology
noxImprovement be always the emphasis of world's most countries environmental protection, its produced pollutant even more causes me One of greatest contamination source of state's environmental destruction, has had become as the task of top priority of China's air pollution treatment at present.
For the improvement of nox, mainly adopt denitrating flue gas selective catalytic reduction (abbreviation scr), selectivity both at home and abroad Noncatalytic reduction (abbreviation sncr), wherein, the denitration principle of scr technique is to adopt nh3(liquefied ammonia, ammoniacal liquor or ureaclastic Ammonia) as reducing agent, it is injected to after dilution in denitration reactor inlet flue, nox when by catalyst layer and in flue gas React n2 and h2o generating non-secondary pollution with fume emission, and sncr technique, compared with scr technique, using nh3Make Spray in the high-temperature region of burner hearth for reducing agent, without catalyst, both technique denitration efficiencies are high, non-secondary pollution, extensively should For in various combustion apparatus, but both technique cannot realize the deep removal of nitrogen oxides, but also there is the escaping of ammonia.
Patent cn200510061120.3 discloses a kind of ozone oxidation and denitration method of boiler flue gas, using alkali lye as absorption Agent, absorbs the nitrogen oxides through to a certain degree aoxidizing, its main thought is using ozone o3Nitric oxide is part or all of After being oxidized to nitrogen dioxide, nitrogen peroxide or dinitrogen pentoxide, then using alkali lye to nox adsorption, remove in flue gas Oxynitrides;For oxidizing and denitrating ozone, spraying into of ozone is one of core technology of this technique.
Utility model content
The utility model provides a kind of ozone flow field injection apparatus, so that ozone is evenly distributed in flue, significantly carries The efficiency of high ozone antioxidant nitroxide.
In order to solve the above problems, the utility model be employed technical scheme comprise that a kind of such, ozone flow field injection Device, including house steward, connects some arms being parallel to each other and arranging at equal intervals of described house steward and is arranged on described Some nozzles in pipe axial direction, described arm stretches in flue section and perpendicular to flue section arrangement, described nozzle along Pipe is axially equally spacedly arranged, and nozzle is located at the side to flow towards flue gas of arm, the nozzle mutual dislocation on adjacent arm Arrangement, the angle between the injection direction of nozzle and flow of flue gas direction is in 100-175 degree, and the distance between adjacent arm is 100mm-200mm, on every arm, the spacing of adjacent nozzle is 200mm-300mm;
Preferably, the injection direction of the nozzle and ozone angle between flow direction in arm is in 120 degree, adjacent The distance between pipe is 140mm, and the spacing along the axially adjacent nozzle of arm is 200 mm.
Preferably, arm is arranged at temperature is 50-100 DEG C of flue section.
Beneficial effect: the nozzle mutual dislocation arrangement on adjacent arm of the present utility model is so that injection is more uniform, separately In outer the utility model device the distance between the angle between the injection direction of nozzle and flow of flue gas direction, adjacent arm and On every arm, the spacing of adjacent nozzle is optimized the ozone injection conditions it is determined that optimal to these factors, so that ozone is existed It is evenly distributed in flue, using minimum ozone, reach the efficiency that maximum increases substantially ozone oxidation nitrogen oxides.
Brief description
Fig. 1 is front view of the present utility model;
Fig. 2 is side view of the present utility model.
Specific embodiment
In order to deepen, to understanding of the present utility model, below in conjunction with embodiment and accompanying drawing, the utility model to be made further Describe in detail, this embodiment is only used for explaining the utility model, does not constitute the restriction to the utility model protection domain.
Embodiment 1
Referring to Fig. 1 and Fig. 2, a kind of ozone injection apparatus, including house steward 1, connect some of described house steward and be parallel to each other And the arm 2 that arranges and be arranged on some nozzles 3 in described arm 2 axial direction at equal intervals, described nozzle 3 is along arm 2 Axially equally spacedly arrange, the nozzle 3 mutual dislocation arrangement on adjacent arm 2, wherein, described arm 2 stretches in flue section 4 And arrange for 50-100 DEG C of flue section 4 perpendicular to temperature, nozzle 3 is located at the side to flow towards flue gas of arm 2, described spray The injection direction of the mouth 3 and ozone angle between flow direction in arm is in 120 degree, and the distance between adjacent arm 2 is 140mm, the spacing along the axially adjacent nozzle 3 of arm 2 is 200mm.
The foregoing is only preferred embodiment of the present utility model, not in order to limit the utility model, all this Within the spirit of utility model and principle, any modification, equivalent substitution and improvement made etc., should be included in the utility model Protection domain within.

Claims (3)

1. a kind of ozone flow field injection apparatus it is characterised in that include house steward, connect some of described house steward be parallel to each other and The arm that arranges at equal intervals and be arranged on some nozzles in described arm axial direction, described arm stretches in flue section and vertical Directly in flue section arrangement, described nozzle is axially equally spacedly arranged along arm, and nozzle is located at flowing towards flue gas of arm Side, the nozzle mutual dislocation arrangement on adjacent arm, the angle between the injection direction of nozzle and flow of flue gas direction is in 100-175 degree, the distance between adjacent arm is 100mm-200mm, and on every arm, the spacing of adjacent nozzle is 200mm- 300mm.
2. a kind of ozone flow field injection apparatus according to claim 1 is it is characterised in that the injection direction of nozzle and ozone Angle between flow direction in arm is in 120 degree, and the distance between adjacent arm is 140mm, along arm axial direction phase The spacing of adjacent nozzle is 200 mm.
3. a kind of ozone flow field injection apparatus according to claim 1 is it is characterised in that it is 50- that arm is arranged at temperature 100 DEG C of flue sections.
CN201620723440.4U 2016-07-11 2016-07-11 Ozone flow field injection apparatus Active CN205886561U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620723440.4U CN205886561U (en) 2016-07-11 2016-07-11 Ozone flow field injection apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620723440.4U CN205886561U (en) 2016-07-11 2016-07-11 Ozone flow field injection apparatus

Publications (1)

Publication Number Publication Date
CN205886561U true CN205886561U (en) 2017-01-18

Family

ID=57771963

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620723440.4U Active CN205886561U (en) 2016-07-11 2016-07-11 Ozone flow field injection apparatus

Country Status (1)

Country Link
CN (1) CN205886561U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020007163A1 (en) * 2018-07-02 2020-01-09 广东佳德环保科技有限公司 Device for uniformly distributing apparatus

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2020007163A1 (en) * 2018-07-02 2020-01-09 广东佳德环保科技有限公司 Device for uniformly distributing apparatus

Similar Documents

Publication Publication Date Title
WO2017059820A1 (en) Reduction and oxidation combined denitration system and denitration method therefor
CN104162349B (en) A kind of low-temperature denitration catalyst SO that suppresses2Poisoning method
CN101439260B (en) System for removing nitrous oxides in low-temperature flue gas and technique thereof
JP6970470B2 (en) Ozone-stepped oxidation-absorption denitration system and method for sintered flue gas
CN103406006A (en) SCR (Selective Catalytic Reduction) denitration device for NOx control of rotary cement kiln
CN103977681A (en) Denitration method for high-concentration nitric oxide flue gas
CN203494378U (en) SCR (Selective Catalytic Reduction) denitration device for controlling NOx of rotary cement kiln
CN205886561U (en) Ozone flow field injection apparatus
CN104399370A (en) Lower temperature flue gas SCR (Selective Catalytic Reduction) denitration system and process
CN205073858U (en) DeNOx systems is united with oxidation to reduction
CN106039959A (en) Ozone oxidation denitrification technology
CN109316952A (en) A kind of the flue gas minimum discharge equipment and technique of non-electrical domain
CN202844873U (en) Annular nitric oxide waste gas purifier
CN107715672A (en) A kind of ozone flow field bioactive molecule distributor
CN102698600A (en) System for intelligently controlling flue gas denitrification of cement plant based on selective catalytic reduction (SCR) method
KR102310469B1 (en) Method and system for removing particulate matter and hazardous compounds from flue gas using ceramic filter with SCR catalyst
CN106039958A (en) Novel method for denitrifying coke oven waste gas
CN206660927U (en) A kind of coal-burning boiler low-temperature flue gas processing unit with ozone denitrification apparatus
CN205586812U (en) A ozone mixing flue gas systematic distribution device for organic catalytic denitrification of low temperature
CN204563937U (en) A kind of low-temperature smoke air SCR denitrating system
CN206787283U (en) A kind of drying calciner for inactivation SCR denitration catalyst regeneration
CN212440698U (en) Flue gas denitration device
KR102359124B1 (en) Method and system for removing hazardous compounds from flue gases using fabric filter bags with SCR catalyst
CN203829902U (en) Pyrolysis denitration system device capable of achieving white smoke concentration less than 50 milligrams
EP3285912A1 (en) Method and system for selective noncatalytic nox reduction

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant