CN202096878U - Preposed rectification static mixer in SCR denitration system - Google Patents

Preposed rectification static mixer in SCR denitration system Download PDF

Info

Publication number
CN202096878U
CN202096878U CN 201120143707 CN201120143707U CN202096878U CN 202096878 U CN202096878 U CN 202096878U CN 201120143707 CN201120143707 CN 201120143707 CN 201120143707 U CN201120143707 U CN 201120143707U CN 202096878 U CN202096878 U CN 202096878U
Authority
CN
China
Prior art keywords
ammonia
static mixer
flue
utility
scr
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 - Lifetime
Application number
CN 201120143707
Other languages
Chinese (zh)
Inventor
邢聪
曾毅夫
周益辉
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.)
Aerospace Kaitian Environmental Technology Co Ltd
Original Assignee
Kaitian Environmental Technology 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 Kaitian Environmental Technology Co Ltd filed Critical Kaitian Environmental Technology Co Ltd
Priority to CN 201120143707 priority Critical patent/CN202096878U/en
Application granted granted Critical
Publication of CN202096878U publication Critical patent/CN202096878U/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Landscapes

  • Treating Waste Gases (AREA)

Abstract

The utility model relates to a preposed rectification static mixer in an SCR (Selective Catalyctic Reduction) denitration system. The static mixer comprises a plurality of C-shaped chips and support racks, which are mounted in a flue duct. The support racks are arranged parallelly below ammonia convey pipelines, and ammonia jet nozzles on the ammonia convey pipelines correspond to the C-shaped chips on the support racks in position. By adopting the utility model, not only the full mixing of flue and ammonia can be ensured, but also the post mixing space is saved, the mixing uniformity is improved, a great pressure drop is not caused, the conversion rate inside an SCR reactor vessel is improved, and the denitration efficiency is raised.

Description

A kind of preposition rectification static mixer of SCR denitrating system
Technical field
The utility model relates to thermal power plant or glass furnace SCR (SCR) denitrating flue gas field, particularly a kind of preposition rectification static mixer of SCR denitrating system.
Background technology
At present, the SCR gas denitrifying technology is widely used in the denitration field.Existing denitrating system flue is arranged very compact, flue gas stream skewness, flue gas generally occur and mixes unequal phenomenon with ammonia, causes that denitration efficiency is low, the escapement ratio of ammonia is big.
In order to guarantee that flue gas mixes with the even of ammonia, be provided with static mixer behind the ammonia-gas spraying device mostly, but reduced the space that flue gas mixes with ammoniacal liquor.In fact, most ammonia-gas spraying devices are positioned at the flue after the turning, and just there is the situation of skewness in the air-flow itself before the ammonia-gas spraying device of flowing through.Find through the CFD numerical simulation, the air-flow after the turning a quite long segment distance internal memory outside effluent speed be higher than inboard phenomenon, promptly outside flow is on the high side.In such environment, spray into quantitative ammonia, will exist flue gas and ammoniacal liquor to mix uneven phenomenon, directly get into the SCR reactor in the case, denitration efficiency is not high.
Therefore, need at present that design is a kind of simply, static mixer efficiently badly, flue gas and ammonia were mixed before getting into the SCR reactor, and then raising SCR denitrating flue gas efficient.
Technology contents
The purpose of the utility model is to solve the deficiency of prior art and a kind of raising denitration efficiency is provided, and reduces the escaping of ammonia rate, makes flue gas and ammonia at the preposition rectification static mixer that gets into the SCR denitrating system that the SCR reactor mixes before.
A kind of preposition rectification static mixer of SCR denitrating system; Comprise a plurality of C shape sheets and the bracing frame that are installed in the flue; Support frame as described above is set in parallel in the below of ammonia conveyance conduit, and the position at the ammonia nozzle of each said ammonia conveyance conduit on the support frame as described above is equipped with C shape sheet.
In the utility model, said C shape sheet is wrapped in said ammonia conveyance conduit and said ammonia nozzle opening direction outer and said C shape sheet is corresponding with said ammonia jet expansion direction.
In the utility model, the consistent and direction that all move of all said C shape sheet opening directions back to said flue gas.
Adopt such scheme, the utlity model has following advantage:
1, before the rectification static mixer is placed on ammonia-gas spraying device, for flue gas and mixing of ammonia provide more spaces;
2, C shape be designed with the generation that is beneficial to eddy current, pressure drop is low;
3, can play rectified action to the air-flow of skewness before the ammonia-gas spraying device of flowing through;
4, strengthen NH 3/ NO XMixing, be beneficial to the raising denitration efficiency, reduce the escaping of ammonia rate.
In sum, adopt the utility model not only can guarantee fully mixing of flue gas and ammonia, can also save the blending space of its back; Can improve the uniformity of mixing again; And can not produce very big pressure drop, promote the conversion ratio in the SCR reactor, improve denitration efficiency.
Description of drawings
Fig. 1 is the utility model and flue front view.
Fig. 2 is axle figure such as the utility model and flue.
Fig. 3 is the structural representation of the utility model.
Fig. 4 is the utility model example structure sketch map.
In the accompanying drawing 1,2,3,4,1-ammonia nozzle, 2-ammonia conveyance conduit, 3-C shape sheet, 4-bracing frame, 5-flow deflector, 6-flue.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is described further.
Like Fig. 1,3 said; The utility model is a kind of static mixer of SCR flue gas denitrification system; Comprise a plurality of C shape sheets 3 and bracing frame 4 that are installed in the flue 6; Support frame as described above 4 is set in parallel in the below of ammonia conveyance conduit 2, and support frame as described above 4 is equipped with C shape sheet 3 on the position of the ammonia nozzle 1 of each said ammonia conveyance conduit 2.Said C shape sheet 3 is wrapped in outside said ammonia conveyance conduit 2 and the said ammonia nozzle 1, and the opening direction of said C shape sheet 3 is corresponding with said ammonia nozzle 1 Way out.Consistent and the direction that all move of all said C shape sheet 3 opening directions back to said flue 6 interior flue gases.
Embodiment:
Below view shows be the integral form of the static mixer used in certain SCR of power plant denitrating flue gas; Described flue 6 is made up of air preheater outlet bend pipe (in be provided with described flow deflector 5) and vertical gas pass; For the blending space of sufficient flue gas and ammonia is provided, ammonia-gas spraying device is arranged in the vertical gas pass.Ammonia-gas spraying device adopts the described ammonia conveyance conduit 2 of four rows, and the arrangement form of 4*4 described nozzle 1 is equidistantly arranged.
Select the described C shape sheet 3 with quantity such as described nozzle 1 for use, and described C shape sheet 3 is fixed on the described bracing frame 4, described C shape sheet 3 all is consistent with the opening of described nozzle 1, more described bracing frame 4 is fixed in the flue 6.Described C shape sheet 3 all can adopt carbon steel or stainless steel material to process with described bracing frame 4.
As shown in Figure 4,2D≤d 1≤4D, 3D≤d 2≤5D, the general d that adopts in the above-mentioned scope 1=2.5D, d 2=3.5D.
Flue gas flows into flue with the direction of representing among Fig. 1.As shown in Figure 2, adjust the uniformity of flue gas with preposition rectification static mixer.Flue gas described C shape sheet 3 backs of flowing through produce the toll bar vortexs, and the ammonia that drives ejection from described nozzle 1 carries out strong disturbance, mixing.So far, in short space, accomplish two actions that mix of rectification and flue gas with the ammonia of flue gas.
The above-mentioned accompanying drawing that combines has carried out exemplary description to the utility model patent, but the concrete realization of the utility model patent does not receive the restriction of aforesaid way.As long as adopted the design of the utility model patent and the improvement of the various unsubstantialities that technical scheme is carried out; Or the design of the utility model patent and technical scheme are directly applied to other occasion without improving, all within the protection domain of the utility model patent.

Claims (3)

1. the preposition rectification static mixer of a SCR denitrating system; It is characterized in that: comprise a plurality of C shape sheets (3) and the bracing frame (4) that are installed in the flue (6); Support frame as described above (4) is set in parallel in the below of ammonia conveyance conduit (2), and support frame as described above (4) is gone up in the position of the ammonia nozzle (1) of each said ammonia conveyance conduit (2) C shape sheet (3) is installed.
2. the preposition rectification static mixer of SCR denitrating system according to claim 1 is characterized in that: said C shape sheet (3) is wrapped in said ammonia conveyance conduit (2) and said ammonia nozzle (1) opening direction outer and said C shape sheet (3) is corresponding with said ammonia nozzle (1) Way out.
3. the preposition rectification static mixer of SCR denitrating system according to claim 2 is characterized in that: the consistent and direction that all move back to the interior flue gas of said flue (6) of all said C shape sheet (3) opening directions.
CN 201120143707 2011-05-06 2011-05-06 Preposed rectification static mixer in SCR denitration system Expired - Lifetime CN202096878U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 201120143707 CN202096878U (en) 2011-05-06 2011-05-06 Preposed rectification static mixer in SCR denitration system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 201120143707 CN202096878U (en) 2011-05-06 2011-05-06 Preposed rectification static mixer in SCR denitration system

Publications (1)

Publication Number Publication Date
CN202096878U true CN202096878U (en) 2012-01-04

Family

ID=45382914

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 201120143707 Expired - Lifetime CN202096878U (en) 2011-05-06 2011-05-06 Preposed rectification static mixer in SCR denitration system

Country Status (1)

Country Link
CN (1) CN202096878U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105381715A (en) * 2015-12-15 2016-03-09 浙江百能科技有限公司 Counter-current ammonia spraying mixer

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105381715A (en) * 2015-12-15 2016-03-09 浙江百能科技有限公司 Counter-current ammonia spraying mixer

Similar Documents

Publication Publication Date Title
CN102626585B (en) V-type ammonia spraying and mixing system for SCR (Selective Catalytic Reduction) smoke denitrification device
US10507427B2 (en) Flue ozone distributor applied in low-temperature oxidation denitrification technology and arrangement manner thereof
CN202146712U (en) Smoke catalytic reduction denitration device capable of mixing uniformly, equalizing and guiding flow
CN102389727B (en) SCR (Selective Catalytic Reduction) denitration four-corner tangent circle type ammonia-fume gas uniformly-mixing device
CN202860405U (en) Flue gas denitration device capable of uniformly mixing guiding flow
CN103657411A (en) Vortex mixing device for SCR (silicon controlled rectification) flue gas denitration system
CN101987280A (en) SCR (silicon controlled rectifier) denitration reactor of coal fuel gas
CN203577639U (en) Swirl mixing device for SCR (selective catalytic reduction) flue gas denitrification system
CN101306325A (en) Flue gas even distribution device of selective catalytic reduction reaction denitration reactor
CN203916479U (en) Be arranged at gas mixer in gas passage and the gas mixer of composition thereof
CN207980871U (en) Rectangular nozzle formula ammonia-spraying grid suitable for flue gas SCR denitration technique ammonia spraying system
CN202909629U (en) Reversed-injection ammonia injection element
CN201244479Y (en) Ejection apparatus and injection grille containing the ejection apparatus
CN103933858A (en) Tangential double vortex SCR mixer
CN109289573B (en) Gas mixing device and method applied to denitration system
CN105797582B (en) A kind of the differentiation spray ammonia reactor and spray ammonia method of SCR denitration
CN201244443Y (en) Device for even distribution of pneumatic flow field
CN202096879U (en) Front secondary rectification static mixer of SCR (silicon controlled rectifier) denitration system
CN102078767A (en) V-shaped mixing grille for selective-catalytic-reduction denitration device
CN202096878U (en) Preposed rectification static mixer in SCR denitration system
CN206391869U (en) A kind of SCR denitration system eddy flow chip static mixer
CN211274167U (en) Flue gas denitration gas-air mixing device
CN204034566U (en) A kind of SCR denitration gas approach
CN103055734A (en) SCR (Selective Catalytic Reduction) static mixer of semi-flexible willow-leaf-shaped blade
CN204710083U (en) A kind of ozone denitrification apparatus

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CP03 Change of name, title or address

Address after: No. 59, nanzhuyuan Road, Changsha Economic and Technological Development Zone, Changsha City, Hunan Province

Patentee after: AEROSPACE KAITIAN ENVIRONMENTAL TECHNOLOGY Co.,Ltd.

Address before: 410100 Xingsha Road, Changsha Economic Development Zone, Hunan, No. 15

Patentee before: KAITIAN ENVIRONMENTAL TECH. Co.,Ltd.

CP03 Change of name, title or address
CX01 Expiry of patent term

Granted publication date: 20120104

CX01 Expiry of patent term