CN214715705U

CN214715705U - Flue denitration ammonia injection uniform distribution device and denitration ammonia injection system

Info

Publication number: CN214715705U
Application number: CN202120939199.XU
Authority: CN
Inventors: 耿明山; 任乐; 郑文学; 金锐; 向继涛
Original assignee: Capital Engineering & Research Inc Ltd
Current assignee: Capital Engineering & Research Inc Ltd
Priority date: 2021-04-30
Filing date: 2021-04-30
Publication date: 2021-11-16
Anticipated expiration: 2031-04-30

Abstract

The utility model relates to a flue denitration ammonia spraying uniform distribution device and a denitration ammonia spraying system, wherein the device comprises an annular distribution pipe and at least 2 mutually independent ammonia spraying structures; the annular distribution pipe is communicated with an ammonia gas inlet pipeline; a plurality of ammonia structures of spouting are even and adjacent to be set up in the flue, each ammonia structure of spouting is through spouting ammonia branch pipe intercommunication annular distribution pipe, each ammonia structure of spouting all includes I shape branch pipe structure, I shape branch pipe structure can with spout ammonia branch pipe intercommunication, I shape branch pipe structure goes up the intercommunication has a plurality of distributors, connect a plurality of sprayers on each distributor, the injection direction of each sprayer is perpendicular setting with the center pin of sprayer, and the ammonia air current that a plurality of sprayers of connecting on each distributor sprayed can form the rotatory air current in center. The utility model discloses a reasonable arrangement realizes spouting the optimization of ammonia device, optimizes ammonia and flue gas nitrogen oxide's homogeneous mixing effect, improves denitration efficiency to reduce the ammonia escape rate. The operability is strong, the operation economic benefit is improved, and the practical engineering application can be met.

Description

Flue denitration ammonia injection uniform distribution device and denitration ammonia injection system

Technical Field

The utility model relates to a flue gas or industry tail gas denitration technical field especially relates to a flue denitration spouts ammonia equipartition device and denitration and spouts ammonia system.

Background

The treatment of air pollution is an important component of environmental treatment, and people increasingly pay more attention to environmental problems and atmospheric environmental protection problems along with the development of industry and the improvement of living standard.

Nitrogen oxides (NOx) are a major class of atmospheric pollutants, and are responsible for the formation of acid rain, photochemical smog, and PM_2.5One of the main factors of contamination. At present, the industrial source NOx emission in China accounts for more than 70% of the total NOx emission amount, and the technology for controlling the emission of NOx in industrial flue gas mainly comprises a combustion control technology and a post-combustion control technology. The combustion control techniques include low nitrogen combustion techniques, reburning techniques, and flue gas recirculation techniques. Among the post-combustion control techniques, Selective Catalytic Reduction (SCR), selective non-catalytic reduction (SNCR), and SCR-SNCR hybrid techniques are the main techniques, and these techniques are most applied in japan. Selective catalytic reduction is the most effective NOx post-control technology from both economic and technical efficiency points of view.

The energy structure of China mainly takes coal as main material, and a large amount of SO is generated in the coal burning process₂And NOx and other atmospheric pollutants cause serious atmospheric pollution and economic loss. Pollutants in the smoke discharged by the industries of thermal power, steel and the like are various, and the newly issued smoke discharge standards of thermal power, steel and the like have provided strict requirements for the emission of NOx. Threshing deviceThe purpose of the nitrate is mainly to remove Nitric Oxide (NO) and nitrogen dioxide (NO)₂) The proportion of Nitric Oxide (NO) in flue gas to nitrogen oxides (NOx) is very high, often above 90%.

Nitric oxide is a pollutant gas, and after nitric oxide is directly discharged into the atmosphere, nitric oxide easily pollutes the atmosphere, soil and water sources, so when a factory discharges flue gas, particularly when the discharged flue gas contains nitric oxide, denitration treatment needs to be carried out on the flue gas. The existing flue gas denitration technology mainly comprises a dry method and a wet method, and compared with the wet flue gas denitration technology, the dry flue gas denitration technology has the main advantages of low basic investment, simple equipment and process, and NO removal_XThe efficiency is higher, no wastewater and waste treatment is caused, and secondary pollution is not easy to cause.

In SO₂And NOx removal is greater than SO removal₂Therefore, the simultaneous desulfurization and denitrification techniques can be roughly classified into two types from the viewpoint of NOx. The first type is a catalytic reduction method, which mainly utilizes a catalyst, a reducing agent and the like to reduce NOx so as to realize simultaneous desulfurization and denitrification; the second type is oxidation absorption method, which mainly uses various strong oxidants and active free radicals to oxidize NO insoluble in water to generate NO₂，SO₂And NO₂Subsequent simultaneous absorption, strong oxidants include NaClO₂、ClO₂、HClO₃、KMnO₄、H₂O₂Etc., the free radicals include O₂ ^-、OH^-、O₃And the like, and the generation technologies thereof include electron beam technology, pulsed corona discharge, and radical cluster lamp. The nitrogen oxide is difficult to remove, and the nitrogen dioxide is easy to remove. Therefore, the technology for converting nitric oxide into nitrogen dioxide is more critical.

At present, the desulfurization and denitrification technologies widely used at home and abroad comprise wet limestone and gypsum Flue Gas Desulfurization (FGD) and NH₃A combination of selective catalytic reduction denitration technology (SCR) and an activated carbon adsorption catalysis method.

The selective catalytic reduction SCR method for denitration adopts ammonia, CO or hydrocarbon and the like as a reducing agent in the presence of a catalyst and in the presence of oxygenReducing NO in the flue gas to N in the presence of gas₂. NH can be used as a reducing agent of the SCR reaction₃、CO、H₂And methane, ethylene, propane, propylene, and the like. Among them, the removal efficiency of NO obtained when ammonia is used as the reducing gas is the highest.

Wherein the SCR is widely applied to denitration of coal-fired power plants, a temperature window of 300-400 ℃ is needed, and NOx is in a catalyst and NH₃Is reduced to N₂The denitration efficiency can reach more than 90%; the activated carbon adsorption catalysis method utilizes the adsorption and catalysis effects of activated carbon, the application temperature is about 200 ℃, and the denitration efficiency is about 50-70% under the condition of ammonia spraying; in the field of low-temperature denitration, SCR needs to heat flue gas, and the technical cost of activated carbon is high.

Although the desulfurization and denitrification efficiency of the technology is high, the investment and operation cost are high, the requirements of the catalyst in the SCR denitrification process on the process conditions are strict, the special requirements including the flue gas temperature and the dust characteristics in the flue gas exist, and the catalyst is easy to be poisoned and failed, so that the operation cost of an SCR system is high.

For a selective catalytic reduction method, two performance parameters of denitration efficiency and ammonia escape rate are mainly improved by two means: 1. the catalytic reduction capability of the catalyst is improved; 2. improving the flue gas distribution and NOx/NH at the inlet of the catalyst layer₃(NOx means nitrogen oxide, NH)₃Representing ammonia) uniformity.

The catalytic reduction capability of the catalyst is improved mainly by means of improving the formula of the catalyst, increasing the dosage of the catalyst and the like; and catalyst layer inlet flue gas distribution and NOx/NH₃The uniformity of the ammonia injection grid is realized by optimizing a flue guide plate of the denitration device and adjusting the design of the ammonia injection grid, wherein the ammonia injection grid is used for treating NOx/NH in flue gas of the denitration device₃Is particularly critical.

In an SCR flue gas denitration system, the injection and mixing of a reducing agent ammonia gas are important components of the whole system. Usually, the ammonia injection and mixing adopts an ammonia injection grid or a static mixer so as to achieve the purpose of uniformly mixing the ammonia gas and the flue gas. In the design of a denitration system, the sufficient mixing of ammonia and nitrogen oxides is a key factor, and the uneven mixing can cause lower denitration rate or higher escape ammonia amount. The effect of this mixing is only a rough type of control, while the distribution of ammonia is significantly uneven and cannot be controlled locally and fine tuned.

However, the flue gas distribution in the denitration reactor at the present stage basically adopts the distribution grid in the reactor, so that the flue gas distribution in the denitration reactor is not uniform, dead angles exist in the flue gas distribution in the denitration reactor, the flue gas is not uniformly mixed with ammonia gas, the catalytic reaction efficiency is low, and the denitration efficiency is influenced.

Among the current SCR deNOx systems, the flue gas flue adopts the rectangle flue more, reductant ammonia/empty gas mixture spouts the flue through Ammonia Injection Grid (AIG) and mixes the back with waste gas, get into SCR denitration reactor, the ammonia injection grid is arranged into the rectangle structure according to the flue form, adopt house steward and branch pipe distribution, the ammonia injection grid of rectangle form is because of the structural reason, lead to spouting ammonia volume and spouting ammonia position and can not control, lead to reductant ammonia and flue gas to mix inhomogeneous, and then influence the denitration efficiency in the denitration reactor, and lead to the tail gas ammonia escape after the denitration too high. The flue of part circular cross section adopts the mode of many injection branch pipe trompils, can't realize the accurate control of local ammonia volume of spouting, and the ammonia flow of each jet orifice has great deviation simultaneously, can't satisfy the flue gas maldistribution and lead to the demand of local ammonia volume dynamic control of spouting.

The ammonia injection grid commonly used in the prior art is composed of a plurality of parallel ammonia injection pipes, and each ammonia injection pipe is provided with a plurality of ammonia gas nozzles. In actual industrial production, the ammonia spraying amount of different ammonia nozzles on different ammonia spraying pipes is greatly different, and the distribution of ammonia on the cross section of a flue is extremely uneven due to the influence of comprehensive factors such as on-way resistance of a pipeline and uneven distribution of flue gas flow velocity on the cross section of the flue, so that the denitration efficiency is seriously influenced, and the ammonia escape rate is increased.

The common ammonia injection device configuration type of current SCR denitrification facility is the ammonia injection grid of equipartition formula. The basic principle is that a plurality of subareas with the same size are designed and planned in the denitration inlet flue, and a plurality of groups of nozzles are uniformly distributed in the subareas. Each partition corresponds to an ammonia injection branch pipe, and a valve is arranged on the ammonia injection branch pipe and used for manual adjustment.

However, with the increasing of the national environmental protection requirement, the requirement of ultra-clean and even ultra-clean flue gas denitration is provided, when the requirement of the flue gas denitration device on the denitration efficiency is more than 90%, the efficiency can not be further improved by simply increasing the dosage of the catalyst, and the NOx/NH must be treated₃Higher requirements for uniformity, NH₃/NO_XThe deviation of the molar ratio distribution needs to be up to + -3% or even less.

In the face of such high NH₃/NO_XThe requirement for the deviation of the molar ratio distribution, the current ammonia-injection grid pattern, begins to expose its disadvantages:

1. when the deviation of the flue gas flow field is large, the ammonia gas flow required by a plurality of local injection branch pipes is too large or too small and exceeds the adjustment range; the flow rate of the locally sprayed ammonia gas is too much or too little relative to the flow rate of the flue gas, so that the denitration efficiency is not high.

2. Ammonia is unevenly distributed on the cross section, and the dynamic adjustment of local ammonia flow cannot be realized; the ordinary stop valve that the valve of ammonia injection branch pipe adopted, the regulation performance is relatively poor, can't satisfy the regulation required precision.

3. The flow distribution of each nozzle on a single branch pipe is uneven, the air flow velocity near the inlet of the branch pipe is high, the flow is high, and the air flow velocity at the tail end of the branch pipe is low and the air flow is insufficient.

4. Flue gas and ammonia gas are not well mixed in laminar flow and turbulent flow states.

5. The spoiler is arranged, so that resistance loss of air flow is increased, the equipment is high in processing and manufacturing difficulty, high in mounting precision requirement and inconvenient to maintain and overhaul.

6. The mode of adopting the tapered branch pipe can only be suitable for gas distribution under a certain flow condition, the gas distribution under different flow conditions still has nonuniformity, the processing and manufacturing difficulty of the branch pipe is large, and the precision requirement is high.

The increase of the escape rate of ammonia not only reduces the denitration efficiency, but also causes the blockage and corrosion of the denitration device. Therefore, a new ammonia injection grid which is reasonable in design and suitable for application is urgently needed, the uniform mixing of ammonia gas and nitric oxide in a flue is ensured, the denitration efficiency is further improved, and the ammonia escape rate is reduced.

Therefore, the inventor provides a flue denitration ammonia injection uniform distribution device and a denitration ammonia injection system by experience and practice of related industries for many years so as to overcome the defects of the prior art.

SUMMERY OF THE UTILITY MODEL

An object of the utility model is to provide an ammonia system is spouted in flue denitration ammonia equipartition device and denitration, overcomes the problem that exists among the prior art, the utility model discloses can divide into the flue cross-section the same region of a plurality of, realize spouting the optimization of ammonia device through reasonable arranging, utilize the nozzle to form the whirl effect, optimize ammonia and flue gas nitrogen oxide's homogeneous mixing effect, improve denitration efficiency to reduce the ammonia escape rate. The operability is strong, the operation economic benefit is improved, and the practical engineering application can be met.

The utility model aims at realizing the above, a flue denitration ammonia spraying uniform distribution device comprises an annular distribution pipe and at least 2 mutually independent ammonia spraying structures; the annular distribution pipe is arranged on the outer side of the flue in a surrounding manner, and the annular distribution pipe is communicated with an ammonia gas inlet pipeline; a plurality of ammonia structures of spouting are even and adjacent to be set up in the flue, each spout the ammonia structure through spouting ammonia branch pipe intercommunication annular distribution pipe, each spout the ammonia structure and all include I shape branch pipe structure, I shape branch pipe structure can with spout ammonia branch pipe intercommunication, I shape branch pipe structure is last to be communicated with a plurality of distributors, each connect a plurality of sprayers on the distributor, each the injection direction of sprayer is perpendicular setting with the center pin of sprayer, and each the ammonia air current that a plurality of sprayers connected on the distributor sprayed can form the rotatory air current in center.

The utility model discloses an in a preferred embodiment, each the sprayer includes the connecting pipe, the first end of connecting pipe with the distributor intercommunication, the second end of connecting pipe is through the vertical pipe of transition pipe intercommunication, the one end that transition pipe was kept away from to vertical pipe sets up the arc guide plate, evenly set up a plurality of injection holes that link up along circumference on the lateral wall of vertical pipe, the center pin of vertical pipe constitutes the center pin of sprayer, the center pin of injection hole with the center pin of vertical pipe is perpendicular setting.

In a preferred embodiment of the present invention, the i-shaped branch pipe structure includes a plurality of first-stage i-shaped branch pipes, each of the first-stage i-shaped branch pipes includes a first-stage central pipe, two ends of the first-stage central pipe are respectively communicated with 1 first-stage transverse branch pipe, a first inlet is disposed at a symmetrical center of the first-stage central pipe, two ends of each of the first-stage transverse branch pipes are respectively provided with a first outlet, the first inlet can be communicated with the ammonia injection branch pipes, and each of the first outlets is respectively communicated with one of the distributors; the distributor is arranged in an X shape, a second inlet is arranged at the symmetrical center of the distributor and communicated with the first outlet, a second outlet is respectively arranged at each end of the distributor, and the second outlets are respectively communicated with the ejectors.

In a preferred embodiment of the present invention, each of the distributors is provided with 4 second outlets, each of the second outlets is respectively communicated with one of the ejectors, a central horizontal line of the 4 ejectors on each of the distributors forms a rectangle, one set of opposite sides is set as a first datum line, and the other set of opposite sides is set as a second datum line; the side wall of the vertical pipe is uniformly provided with 4 penetrating jet holes along the circumferential direction, one jet hole is set as a first jet hole, a jet hole adjacent to the first jet hole is set as a second jet hole, the central axis of the first jet hole and the first datum line form a first included angle, the central axis of the second jet hole and the second datum line form a second included angle, and the first included angle and the second included angle are arranged in an equal manner.

In a preferred embodiment of the present invention, the first included angle ranges from 10 ° to 80 °, and the second included angle ranges from 10 ° to 80 °.

The utility model discloses an in a preferred embodiment, the diameter of connecting pipe is less than the diameter setting of vertical pipe, the transition pipe is the toper pipe, the diameter of transition pipe is gradual increase setting from bottom to top.

In a preferred embodiment of the present invention, the i-shaped branch pipe structure comprises 3 first-stage i-shaped branch pipes, the i-shaped branch pipe structure further comprises a transition connection pipe, the transition connection pipe is provided with 3 third outlets, and each third outlet is respectively communicated with the first inlets of the 3 first-stage i-shaped branch pipes; and a third inlet is arranged on the transition connecting pipe, and the third inlet is communicated with the ammonia spraying branch pipe.

The utility model discloses an in the preferred embodiment, I shape branch pipe structure includes 4 one-level I shape branch pipe, I shape branch pipe structure still includes second grade I shape branch pipe, and the symmetry center department of second grade I shape branch pipe sets up the fourth entry, and each tip of second grade I shape branch pipe sets up the fourth export respectively, the fourth entry with spout ammonia branch pipe intercommunication, each the fourth export communicates with each first entry respectively.

In a preferred embodiment of the present invention, each ammonia injection branch pipe is provided with a first regulating valve and a flow meter.

In a preferred embodiment of the present invention, the annular distribution pipe is at least connected to 2 ammonia gas inlet pipes, and the 2 ammonia gas inlet pipes are designed to have a symmetrical structure; the cross-sectional area of the annular distribution pipe is more than 2 times of the sum of the cross-sectional areas of the ammonia injection branch pipes; and a second regulating valve is arranged on each ammonia gas inlet pipeline.

The purpose of the utility model can be realized in such a way that a denitration ammonia spraying system comprises a denitration front flue, a denitration treatment flue and a control system, wherein the first end of the denitration front flue is provided with a flue gas inlet, the first end of the denitration treatment flue is provided with a flue gas outlet, and the second end of the denitration front flue and the second end of the denitration treatment flue are in sealed communication arrangement; the denitration front flue and the denitration treatment flue are communicated with each other and provided with a heat exchanger; an SCR denitration reactor is arranged between the second end of the denitration treatment flue and the heat exchanger; at least 1 flue denitration ammonia spraying uniform distribution device is arranged between the second end of the denitration front flue and the heat exchanger, and the flue denitration ammonia spraying uniform distribution device is vertically arranged with the central shaft of the denitration front flue; a rotational flow mixing structure is arranged between the flue denitration ammonia-spraying uniform distribution device and the heat exchanger; an ammonia gas analyzer is arranged between the heat exchanger and the SCR denitration reactor and used for detecting the amount of ammonia gas in flue gas subjected to denitration treatment by the SCR denitration reactor, the ammonia gas analyzer is provided with a plurality of sampling measurement points, and each sampling measurement point is in one-to-one correspondence with each distributor of the flue denitration ammonia spraying and uniformly distributing device.

In a preferred embodiment of the present invention, 2 of the flue denitration ammonia injection equispaced devices are axially arranged in parallel at an interval between the second end of the flue and the heat exchanger before denitration, and each of the flue denitration ammonia injection equispaced devices comprises an annular distribution pipe and at least 2 mutually independent ammonia injection structures; each it all includes I shape branch pipe structure to spout the ammonia structure, I shape branch pipe structure includes a plurality of one-level I shape branch pipes, each one-level I shape branch pipe includes one-level center tube and one-level horizontal branch pipe, 2 circumference contained angle between the one-level center tube of flue denitration ammonia injection equipartition device is the third contained angle.

In a preferred embodiment of the present invention, the third included angle ranges from 30 ° to 60 °.

The utility model discloses an in a preferred embodiment, whirl mixed structure includes that a plurality of neighbours lean on the whirl blender that sets up, and is a plurality of whirl blender pass through fixed knot structure connect in flue before the denitration, two liang adjacent 3 whirl blender's center line is equilateral triangle.

In a preferred embodiment of the present invention, each of the swirl mixers includes an annular frame, the annular frame is provided with a connecting ring at a coaxial and radial interval, the annular frame is provided with a plurality of inclined first swirl blades at a circumferential interval between the connecting rings, and each of the first swirl blades is provided with an equal fourth angle between the central axes of the connecting rings.

In a preferred embodiment of the present invention, the number of the first swirl vanes in each of the swirl mixers is 3 to 15, and the range of the fourth included angle is 15 to 70 °.

The utility model discloses a in a preferred embodiment, each swirl mixer includes ring frame respectively, coaxial and radial interval set up the go-between in the ring frame, coaxial and radial interval set up the centre ring in the go-between, ring frame with the circumference interval sets up the second whirl blade of a plurality of slopes between the go-between, the go-between with the circumference interval sets up the third whirl blade of a plurality of slopes between the centre ring, third whirl blade with second whirl blade's whirl direction is opposite setting, each second whirl blade with fifth contained angle between the center pin of go-between is equal setting, each third whirl blade with sixth contained angle between the center pin of go-between is equal setting.

In a preferred embodiment of the present invention, the number of the second swirl vanes in each swirl mixer is 6 to 36, and the range of the fifth included angle is 25 to 70 °; the number of the third swirl vanes in each swirl mixer is 3-24, and the range of the sixth included angle is 15-65 degrees.

From above, the utility model provides a flue denitration spouts ammonia equipartition device and denitration and spouts ammonia system has following beneficial effect:

(1) the utility model provides an among the flue denitration ammonia spraying equal cloth device, a plurality of mutually independent ammonia spraying structures divide the flue into a plurality of independent ammonia spraying areas, realize the subregion independent control and spout the ammonia volume, satisfy different areas because the flue gas distributes unevenly and causes the required ammonia volume of spouting to have the requirement of difference, eliminate traditional ammonia spraying grid local ammonia concentration too big, cause the phenomenon that ammonia escape volume exceeds standard; each area is provided with an I-shaped branch pipe structure, a distributor and an injector, each ammonia spraying branch pipe is provided with a first regulating valve and a flowmeter, and the ammonia spraying amount of each subarea can be respectively regulated and controlled through the first regulating valve and the flowmeter, so that the ammonia spraying amount can be regulated in subareas on the cross section of the flue, the uniform mixing effect of ammonia and nitrogen oxides in air is optimized, the denitration efficiency is improved, and the ammonia escape rate is effectively reduced; the distribution pipes are annularly arranged, so that the uniformity of ammonia spraying can be ensured, and the blockage and corrosion can be effectively prevented;

(2) the utility model provides an among the flue denitration ammonia spraying equal cloth device, respectively spout the connection mode that the ammonia structure adopted I shape branch pipe structure, distributor and sprayer, realize that the on-the-way resistance loss of all sprayers is equal, realize that flow, the pressure of each sprayer of every ammonia spraying area are equal, eliminate the difference between each sprayer, realize the even distribution of the ammonia volume of spouting in the subregion, eliminate and have great flow inhomogeneity between the traditional ammonia spraying grid sprayer;

(3) the utility model provides an among the flue denitration ammonia spraying equal cloth device, the distributor adopts the X type to arrange in each subregion, and the distributor end sets up the sprayer, realizes in each subregion, and all sprayers can realize the equality of sprayer interval in horizontal and vertical homoenergetic, realize the sprayer evenly distributed, realize that the region that each sprayer covers is equal, realize the even distribution in space of the ammonia volume that each sprayer sprays; the ejector is used for forming a rotational flow effect, so that the uniform mixing effect of ammonia and nitrogen oxides in the flue gas is optimized, the denitration efficiency is improved, and the ammonia escape rate is reduced;

(4) the utility model provides a denitration ammonia-spraying system, which is provided with a flue denitration ammonia-spraying uniform distribution device, because the distribution of the flue gas in the flue is not uniform and the flue gas flow of a local area is larger, the flue gas velocity measuring instrument, the flue gas analyzer and the ammonia gas analyzer are utilized to realize that the load quantity of the nitrogen oxide is calculated according to the flow of the flue gas aiming at the ammonia spraying subarea corresponding to the area with larger local flue gas flow, the required ammonia spraying quantity is calculated according to the load quantity of the nitrogen oxide of the subarea, the partition ammonia injection amount is adjusted and flow monitoring is carried out according to the required ammonia injection amount, automatic setting, automatic adjustment and automatic detection of the ammonia injection amount in each area are realized, dynamic control of the ammonia injection amount is realized, ideal removal of nitrogen oxides is realized, the requirement of adjusting the ammonia injection amount in real time under different flue gas working conditions is met, the residual ammonia amount of the flue gas is monitored, and the exceeding of the ammonia escape amount in the discharged flue gas is avoided;

(5) the denitration ammonia injection system provided by the utility model can be transformed on the basis of the original denitration system, thereby saving investment, reducing cost and ensuring higher denitration efficiency;

(6) in the denitration ammonia spraying system provided by the utility model, the flue denitration ammonia spraying uniform distribution device has simple structure and convenient adjustment, and ammonia gas and flue gas are mixed more uniformly, thereby improving the removal efficiency of nitrogen oxide;

(7) the utility model discloses processing preparation, installation are simple and convenient, easy to carry out.

Drawings

The drawings are only intended to illustrate and explain the present invention and do not limit the scope of the invention. Wherein:

FIG. 1: do the utility model discloses a flue denitration ammonia injection equipartition device's schematic diagram.

FIG. 2: is the structure diagram of the ejector of the utility model.

FIG. 3: is a view along a direction in fig. 2.

FIG. 4: is a cross-sectional view B-B in fig. 2.

FIG. 5: is the structure chart of the distributor of the utility model.

FIG. 6: is a cross-sectional view of C-C in fig. 5.

FIG. 7: is the ammonia spraying schematic diagram of a plurality of ejectors on a distributor of the utility model.

FIG. 8: do the utility model discloses a schematic diagram of one-level I shape branch connection distributor.

FIG. 9: the structure chart of the ammonia spraying structure of the utility model comprises 3 one-level I-shaped branch pipes.

FIG. 10: the structure chart of the ammonia spraying structure of the utility model comprises 4 one-level I-shaped branch pipes.

FIG. 11: do the utility model discloses a structural schematic diagram of ammonia system is spouted in denitration.

FIG. 12: shown in cross-section at D-D in fig. 11.

FIG. 13: shown in cross-section E-E in fig. 11.

FIG. 14: is an enlarged view at I in FIG. 11.

FIG. 15: do the utility model discloses a whirl mixed structure's top view.

FIG. 16: does the utility model discloses a layout of 3 whirl blenders in the whirl mixed structure.

FIG. 17: is a top view of a particular embodiment of the swirl mixer of the present invention.

FIG. 18: is a front view of a particular embodiment of the swirl mixer of the present invention.

FIG. 19: is a top view of another embodiment of the swirl mixer of the present invention.

FIG. 20: is a front view of another embodiment of the swirl mixer of the present invention.

In the figure:

200. a denitration ammonia injection system;

100. flue denitration ammonia spraying uniform distribution device;

1. an annular distribution pipe;

2. an ammonia spraying structure;

3. an ammonia gas inlet pipe; 31. a second regulating valve;

4. an ammonia injection branch pipe; 41. a first regulating valve; 42. a flow meter;

5. a distributor;

6. an ejector;

61. a connecting pipe; 62. a transition duct; 63. a vertical tube; 64. an arc-shaped guide plate; 65. an injection hole; 651. a first injection hole; 652. a second injection hole;

7. an I-shaped branch pipe structure;

71. a first-stage I-shaped branch pipe; 711. a primary center tube; 712. a first-stage transverse branch pipe;

72. a second-stage I-shaped branch pipe;

73. a transition connecting pipe;

8. a rotational flow mixing structure;

81. a swirl mixer; 811. an annular frame; 812. a connecting ring; 813. a first swirl vane; 814. a center ring; 815. a second swirl vane; 816. a third swirl vane;

82. a fixed structure;

91. a denitration front flue; 911. a flue gas inlet; 92. denitration treatment of the flue; 921. a flue gas outlet; 93. a heat exchanger; 94. an SCR denitration reactor; 95. a flue gas analyzer; 96. a flue gas speed measuring instrument; 97. a spoiler; 98. a flame burner; 99. an ammonia gas analyzer.

Detailed Description

In order to clearly understand the technical features, objects, and effects of the present invention, embodiments of the present invention will be described with reference to the accompanying drawings.

The specific embodiments of the present invention described herein are for the purpose of explanation only and should not be construed as limiting the invention in any way. Given the teachings of the present invention, the skilled person can conceive of any possible variants based on the invention, which should all be considered as belonging to the scope of the invention. It will be understood that when an element is referred to as being "disposed on" another element, it can be directly on the other element or intervening elements may also be present. When an element is referred to as being "connected" to another element, it can be directly connected to the other element or intervening elements may also be present. The terms "mounted," "connected," and "connected" are to be construed broadly and may include, for example, mechanical or electrical connections, communications between two elements, direct connections, indirect connections through intermediaries, and the like. The terms "vertical," "horizontal," "upper," "lower," "left," "right," and the like as used herein are for illustrative purposes only and do not denote a unique embodiment.

Unless defined otherwise, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this application belongs. The terminology used herein in the description of the present application is for the purpose of describing particular embodiments only and is not intended to be limiting of the application. As used herein, the term "and/or" includes any and all combinations of one or more of the associated listed items.

The utility model relates to a fire coal, fuel and gas power plant selective catalytic reduction flue gas denitration system, denitration reductant ammonia spray and mix application technique, be applicable to the flue gas or the industry tail gas denitration field of trades such as power plant, steam power plant, metallurgy, chemical industry, fodder.

As shown in fig. 1 to 10, the utility model provides a flue denitration ammonia-spraying uniform distribution device 100, which comprises an annular distribution pipe 1 and at least 2 mutually independent ammonia-spraying structures 2; the annular distribution pipe 1 is arranged on the outer side of the flue in a surrounding manner, and the annular distribution pipe 1 is communicated with an ammonia gas inlet pipeline 3; a plurality of ammonia structures 2 of spouting evenly and adjacent setting in the flue, each ammonia structure 2 of spouting communicates annular distribution pipe 1 through spouting ammonia branch pipe 4, each ammonia structure 2 of spouting all includes I shape branch pipe structure, I shape branch pipe structure can with spout ammonia branch pipe 4 intercommunication, I shape branch pipe structure goes up the intercommunication has a plurality of distributors 5, connect a plurality of sprayers 6 on each distributor 5, the injection direction of each sprayer 6 is perpendicular setting with the center pin of sprayer, and each the ammonia air current that a plurality of sprayers of connecting sprayed on the distributor can form the rotatory air current in center.

In the flue denitration ammonia spraying uniform distribution device provided by the utility model, a plurality of mutually independent ammonia spraying structures divide the interior of the flue into a plurality of independent ammonia spraying areas, and the distribution pipes are arranged in an annular shape, so that the uniformity of ammonia spraying can be ensured, and the blockage prevention and corrosion prevention can be effectively realized;

the ammonia spraying structures adopt a connection mode of an I-shaped branch pipe structure, a distributor and the ejectors, so that the on-way resistance losses of all the ejectors are equal, the flow and the pressure of each ejector in each ammonia spraying area are equal, the difference among the ejectors is eliminated, the ammonia spraying amount in the subareas is uniformly distributed, and the large flow nonuniformity among the traditional ammonia spraying grid ejectors is eliminated;

the ejector is utilized to form a rotational flow effect, the uniform mixing effect of ammonia and nitrogen oxides in flue gas is optimized, the denitration efficiency is improved, and the ammonia escape rate is reduced.

Further, as shown in fig. 2, 3, and 4, each injector 6 includes a connecting pipe 61, a first end of the connecting pipe 61 is communicated with the distributor 5, a second end of the connecting pipe 61 is communicated with a vertical pipe 63 through a transition pipe 62, an arc-shaped guide plate 64 is disposed at one end of the vertical pipe 63 far away from the transition pipe 62, and an arc-shaped surface of the arc-shaped guide plate 64 far away from the vertical pipe 63 is opposite to the flow direction of the flue gas. In fig. 2, the direction a is the flow direction of the flue gas. A plurality of penetrating injection holes 65 are uniformly arranged on the side wall of the vertical pipe 63 along the circumferential direction, the central axis of the vertical pipe 63 forms the central axis of the injector, and the central axes of the injection holes and the central axis of the vertical pipe are arranged perpendicularly. The flue is vertical setting, and flue denitration ammonia injection equipartition device 100 is the level setting, and the center pin of jet orifice is the level setting. The direction of injection of each injector 6 is shown by the arrow in fig. 4.

The utility model provides an among the flue denitration ammonia spraying equal cloth device, the axial of the perpendicular flue of jet orifice of each sprayer sets up the arc guide plate at the free end of sprayer, realizes the even diffusion distribution of air current, and the arc guide plate promotes the misce bene of flue gas and ammonia, reduces the flue gas and erodes the sprayer wearing and tearing.

Further, as shown in fig. 8, the i-shaped branch pipe structure 7 includes a plurality of first-stage i-shaped branch pipes 71, each first-stage i-shaped branch pipe 71 includes a first-stage central pipe 711, two ends of the first-stage central pipe 711 are respectively communicated with 1 first-stage transverse branch pipe 712, a first inlet is arranged at the symmetrical center of the first-stage central pipe 711, two ends of each first-stage transverse branch pipe 712 are respectively provided with a first outlet, the first inlet can be communicated with the ammonia injection branch pipe 4, and each first outlet is respectively communicated with a distributor 5; the distributor 5 is arranged in an X shape, a second inlet is arranged at the symmetrical center of the distributor 5 and is communicated with the first outlet, each end of the distributor 5 is respectively provided with a second outlet, and each second outlet is respectively communicated with an ejector 6.

As shown in fig. 5 and 6, the distributor 5 is arranged in an X shape, the injectors 6 are arranged at the tail ends of the distributor 5, the equal distance between the injectors can be realized in the transverse direction and the longitudinal direction of all the injectors, the uniform distribution of the injectors is realized, the equal coverage area of each injector is realized, and the uniform distribution of the ammonia amount sprayed by each injector in the space is realized.

Further, as shown in fig. 7, each distributor 5 is provided with 4 second outlets, each second outlet is communicated with one ejector, the center horizontal connecting lines of the 4 ejectors on each distributor form a rectangle, one group of opposite sides are set as first reference lines, and the other group of opposite sides are set as second reference lines; the side wall of the vertical pipe is uniformly provided with 4 penetrating jet holes 65 along the circumferential direction, a first jet hole is set as a first jet hole 651, a jet hole adjacent to the first jet hole is set as a second jet hole 652, the central axis of the first jet hole 651 is arranged at a first included angle alpha with a first datum line, the central axis of the second jet hole 652 is arranged at a second included angle beta with a second datum line, and the first included angle alpha and the second included angle beta are arranged equally.

Further, the range of the first included angle alpha is 10-80 degrees, and the preferable ranges are 15-30 degrees and 60-75 degrees; the second included angle beta is in the range of 10-80 degrees, and the preferable ranges are 15-30 degrees and 60-75 degrees. The value ranges of the first included angle alpha and the second included angle beta directly influence the rotation direction of the central rotating airflow, and the rotation direction of the central rotating airflow can be clockwise or anticlockwise.

Further, the diameter of the connecting pipe 61 is smaller than that of the vertical pipe 63, the transition pipe 62 is a tapered pipe, and the diameter of the transition pipe 62 is gradually increased from bottom to top.

Further, the ammonia spraying structure 2 can adopt a mode of combining 3 first-stage I-shaped branch pipes 71 and also can adopt a mode of combining 4 first-stage I-shaped

branch pipes

71 and 1 second-stage I-shaped branch pipe 72, and the flue denitration ammonia spraying uniform distribution device 100 carries out different ammonia spraying structure combination modes according to the section size of the flue, so that the ammonia spraying units in the flue are uniformly distributed.

As shown in fig. 9, in an embodiment of the present invention, the i-shaped branch structure includes 3 first-stage i-shaped branch pipes 71, the i-shaped branch structure 7 further includes a transition connection pipe 73, the transition connection pipe 73 is provided with 3 third outlets, and each third outlet is respectively communicated with the first inlets of the 3 first-stage i-shaped branch pipes 71; the transition connecting pipe 73 is provided with a third inlet which is communicated with the ammonia spraying branch pipe 4.

As shown in fig. 10, in another embodiment of the present invention, the i-shaped branch structure includes 4 first-level i-shaped branch pipes 71, the i-shaped branch structure 7 further includes a second-level i-shaped branch pipe 72, a fourth inlet is disposed at the symmetric center of the second-level i-shaped branch pipe 72, a fourth outlet is disposed at each end of the second-level i-shaped branch pipe 72, the fourth inlet is communicated with the ammonia spraying branch pipe 4, and each fourth outlet is communicated with each first inlet. The first-stage I-shaped branch pipe 71 is communicated with 4 distributors, the distance between one ejector and 2 adjacent ejectors (which are adjacent along the length direction of the first-stage central pipe 711 and the length direction of the first-stage transverse branch pipe 712) is d, and the preferred range of the distance d is 200-800 mm.

Further, as shown in fig. 1, each ammonia injection branch pipe 4 is provided with a first regulating valve 41 and a flow meter 42. The ammonia spraying amount of each ammonia spraying structure 2 can be respectively adjusted and controlled through the first adjusting valve 41 and the flowmeter 42, so that the ammonia spraying amount can be adjusted in a partition mode on the cross section of a flue, the uniform mixing effect of nitrogen oxides in ammonia and air is optimized, the denitration efficiency is improved, and the ammonia escape rate is effectively reduced.

Further, the annular distribution pipe 1 is at least communicated with 2 ammonia gas inlet pipelines 3, and the 2 ammonia gas inlet pipelines 3 are designed in a symmetrical structure; the annular distribution pipe 1 is designed by adopting a circular pipeline, the cross section area of the annular distribution pipe 1 is more than 2 times of the sum of the cross section areas of all the ammonia spraying branch pipes 4, and the ammonia flow rate of each ammonia spraying branch pipe 4 is uniform and stable; a second regulating valve 31 is arranged on the ammonia gas inlet pipeline 3 to regulate the ammonia gas inlet amount.

In the present embodiment, the annular distribution pipe 1 and the ammonia injection branch pipe 4 are connected by flanges.

Further, flue denitration ammonia injection uniform distribution device 100 still includes the control assembly, is connected with first governing valve 41 and second governing valve 31. The embodiment of the utility model provides an in first governing valve 41 and second governing valve 31 are the aperture governing valve, including executor and electromagnetic flow control valve body, the execution is used for receiving the aperture signal from the control assembly and adjusts the aperture of electromagnetic flow control valve body, realizes spouting the automatically regulated of ammonia volume.

As shown in fig. 11 to 20, the utility model also provides an ammonia system 200 is spouted in denitration, including flue 91, denitration treatment flue 92 and control system (not shown in the figure) before denitration, the first end of flue 91 sets up flue gas inlet 911 before denitration, and the first end of denitration treatment flue 92 sets up flue gas outlet 921, and the second end of flue 91 and the second end of denitration treatment flue 92 are sealed and communicated and set up before denitration; a heat exchanger 93 is communicated with the denitration front flue 91 and the denitration treatment flue 92; an SCR denitration reactor 94 is arranged between the second end of the denitration treatment flue 92 and the heat exchanger 93; the heat exchanger 93 preheats the low-temperature flue gas before the denitration with lower temperature before entering the SCR denitration reactor by using the high-temperature denitration high-temperature flue gas after the denitration by the SCR denitration reactor, fully utilizes the waste heat, and reduces the energy consumption required by the heating of the flue gas before the denitration.

At least 1 flue denitration ammonia-spraying uniform distribution device 100 is arranged between the second end of the denitration front flue 91 and the heat exchanger 93, and the flue denitration ammonia-spraying uniform distribution device 100 is vertically arranged with the central shaft of the denitration front flue 91; a rotational flow mixing structure 8 is arranged between the flue denitration ammonia-spraying uniform distribution device 100 and the heat exchanger 93; an ammonia gas analyzer 99 is arranged between the heat exchanger 93 and the SCR denitration reactor 94, and the ammonia gas analyzer 99 is used for detecting the amount of ammonia gas in the flue gas subjected to denitration treatment by the SCR denitration reactor. The ammonia gas analyzer 99 is provided with a plurality of sampling measurement points, and each sampling measurement point is arranged in one-to-one correspondence with each distributor 5 of the flue denitration ammonia spraying and uniformly distributing device 100.

A flue gas analyzer 95 and a flue gas speed measuring instrument 96 are arranged between the heat exchanger 93 and the flue denitration ammonia injection uniform distribution device 100, and a spoiler 97 and a flame burner 98 are arranged between the flue denitration ammonia injection uniform distribution device 100 and the second end of the denitration front flue 91. The flue gas analyzer 95 is used for measuring the content of nitrogen oxides in the flue gas, and the flue gas velocity measuring instrument 96 is used for measuring the flue gas velocity in the flue before denitration; the flue gas analyzer 95, the flue gas velocity measuring instrument 96 and the ammonia gas analyzer 99 are all electrically connected with the control system. The number of the flame burners 98 is more than or equal to 2, and the flame burners burn combustible gas and combustion-supporting gas to realize the temperature rise of flue gas and ammonia gas, meet the flue gas temperature requirement required by SCR reaction and realize the expected denitration reaction. The spoiler 97 may have a V-shaped long groove structure, a groove structure, or a spiral blade structure.

The flue gas velocity measuring instrument, the flue gas analyzer and the ammonia gas analyzer are utilized to realize automatic setting, automatic adjustment and automatic detection of ammonia spraying amount in each area, realize dynamic control of ammonia spraying amount, meet the requirement that ammonia spraying amount can be adjusted in real time under different flue gas working condition conditions, monitor residual ammonia amount of flue gas and avoid exceeding the ammonia escape amount in discharged flue gas.

The utility model provides an among the denitration ammonia injection system, adopt flue denitration to spout ammonia equipartition device, divide into a plurality of the same regions with the cross-section of flue before the denitration, realize spouting the optimization of ammonia through reasonable arrangement, both can guarantee to spout the homogeneity of ammonia, can effectively prevent stifled anticorrosion again, utilize the sprayer to form the whirl effect, optimize the even mixed effect of ammonia and flue gas nitrogen oxide, improve denitration efficiency, and reduce the ammonia escape rate; meanwhile, the ammonia introducing amount can be adjusted according to the concentration of nitrogen oxides in the flue gas, the operability is high, the operation economic benefit is improved, and the practical engineering application can be met.

Further, as shown in fig. 14, 2 flue denitration ammonia-spraying uniform distribution devices 100 are axially arranged in parallel and at intervals between the second end of the front flue 91 for denitration and the heat exchanger 93, and each flue denitration ammonia-spraying uniform distribution device 100 comprises an annular distribution pipe 1 and at least 2 ammonia-spraying structures 2; each ammonia injection structure 2 comprises an i-shaped branch pipe structure 7, each i-shaped branch pipe structure 7 comprises a plurality of first-stage i-shaped branch pipes 71, each first-stage i-shaped branch pipe 71 comprises a first-stage central pipe 711 and a first-stage transverse branch pipe 712, and as shown in fig. 12 and 13, a circumferential included angle between the first-stage central pipes of the 2 flue denitration ammonia injection uniform distribution devices 100 is a third included angle. The setting that is certain circumference contained angle between 2 flue denitration ammonia injection equipartition device 100's the one-level center tube for each flue denitration ammonia injection equipartition device 100's sprayer is the setting that staggers of circumference, realizes that the ammonia of spouting in each independent subregion is more even.

The central axis of the annular distribution pipe 1 is coincident with the central axis of the denitration front flue 91, and each ammonia spraying branch pipe 4 penetrates through the side wall of the denitration front flue 91 in a sealing manner to be communicated with each ammonia spraying structure 2.

Further, the third angle ranges from 30 ° to 60 °, and a preferred angle is 45 °.

Further, as shown in fig. 15 and 16, the swirl mixing structure 8 includes a plurality of swirl mixers 81 adjacently abutted against each other, the plurality of swirl mixers 81 are connected to the denitration front flue 91 through a fixing structure 82, and the central connecting line of every two adjacent 3 swirl mixers 81 is an equilateral triangle. The length of the central connecting line is equal to the diameter of the swirl mixer, so that the maximization of the swirl action area of the flue gas in the flue is realized, and the area of the flue gas which can not be swirled is reduced.

The fixing structure 82 includes a plurality of fixing rods capable of being fixedly connected to the inside of the denitration front flue 91, and a distance between adjacent fixing rods is smaller than a diameter dimension of the swirl mixer 81.

Furthermore, the swirl mixer can adopt various structural forms.

As shown in fig. 17 and 18, in an embodiment of the present invention, each swirl mixer 81 includes an annular frame 811, a connecting ring 812 is disposed coaxially and radially in the annular frame 811, a plurality of inclined first swirl vanes 813 are disposed at circumferential intervals between the annular frame 811 and the connecting ring 812, and a fourth included angle between each first swirl vane 813 and the central axis of the connecting ring 812 is equal.

Further, the number of the first swirl vanes 813 in each swirl mixer 81 is 3-15, and the range of the fourth included angle is 15-70 °.

As shown in fig. 19 and 20, in another embodiment of the present invention, each swirl mixer 81 includes an annular frame 811, a connecting ring 812 is coaxially and radially spaced in the annular frame 811, a center ring 814 is coaxially and radially spaced in the connecting ring 812, and a blind plate is disposed at an end of the center ring 814. A plurality of inclined second swirl blades 815 are circumferentially arranged between the annular frame 811 and the connecting ring 812 at intervals, a plurality of inclined third swirl blades 816 are circumferentially arranged between the connecting ring 812 and the central ring 814 at intervals, the swirl directions of the third swirl blades 816 and the second swirl blades 815 are opposite, a fifth included angle between each second swirl blade 815 and the central axis of the connecting ring is equal, and a sixth included angle between each third swirl blade 816 and the central axis of the connecting ring is equal. The second swirl blades 815 form outer swirl blades, the third swirl blades 816 form inner swirl blades, swirl of flue gas flow is achieved by means of the inner swirl blades and the outer swirl blades, mixing of the flue gas and ammonia gas is promoted, the blind plate can prevent the air flow from flowing through the central ring, the flue gas flows from gaps of the swirl plates, and mixing of the flue gas swirl is promoted.

Further, the number of second swirl vanes in each swirl mixer is 6-36, and the range of a fifth included angle is 25-70 degrees; the number of the third swirl vanes in each swirl mixer is 3-24, and the range of the sixth included angle is 15-65 degrees.

Further, the control system comprises a flue gas speed measuring module, a flue gas component measuring module, an ammonia injection amount calculating module, an ammonia injection amount monitoring module and a measured data summarizing and analyzing module; the speed measuring module is used for measuring the flue gas flow speed in different areas in a flue, the flue gas component analyzing module is used for measuring the content of nitrogen oxides in the flue gas, the removal load of the nitrogen oxides is calculated by utilizing a computer program, the measured data summarizing and analyzing module is used for calculating the load of the nitrogen oxides according to the flue gas flow and the flue gas components of each area, the ammonia injection amount required by each area is calculated according to the nitrogen oxide load, the ammonia injection amount of each area is regulated by a first regulating valve 41 (electrically or pneumatically) on an ammonia injection branch pipe 4, and the actual ammonia injection amount is monitored according to a flow meter 42 on the ammonia injection branch pipe 4; the ammonia gas monitoring module is used for detecting the amount of unreacted ammonia at the downstream of the SCR denitration reactor, controlling the ammonia spraying amount according to the ammonia escape amount in each area in a feedback mode, and when the ammonia escape amount exceeds a set value, the system prompts that the ammonia spraying amount of the corresponding area is too large, so that the ammonia spraying amount of the area is correspondingly reduced, and the minimum ammonia consumption and the minimum ammonia escape amount are realized.

The utility model discloses an ammonia system 200 is spouted in denitration's use as follows:

the original flue gas (flue gas before unpurified denitration) enters the denitration ammonia spraying system 200 of the utility model from the flue gas inlet 911, firstly, the flue gas is preheated and heated through the heat exchanger 93, the heated flue gas flows through the flue gas analyzer 95 and the flue gas velocity measuring instrument 96, the flue denitration ammonia spraying and distributing device 100 is used for spraying ammonia, the sprayed ammonia is mixed with the flue gas, the flue gas continuously rises, the streaming mixing is carried out through the spoiler 97, the further mixing of the ammonia and the flue gas is promoted, the high-efficiency combustion of combustible gas and combustion air is carried out in the flame burner, the temperature of the flue gas and the mixed gas of the ammonia is further improved, the flue gas is guided by the steering elbow and the guide plate, the further mixing of the flue gas and the ammonia is realized, the mixing of energy is carried out simultaneously, the uniformity of the temperature of the flue gas is realized, the rectification function of the flue gas and the mixed gas of the ammonia through the rectification grating is carried out on the flue gas and the mixed gas, the mixed gas of the flue gas and the ammonia gas can uniformly and vertically enter the inside of the catalyst of the SCR denitration reactor, so that the high-efficiency, rapid and uniform reaction of the nitrogen oxide and the ammonia gas in the flue gas under the catalytic effect of the catalyst is realized;

the flue gas mixed gas after passing through the catalyst of the SCR denitration reactor flows through an ammonia analyzer 99, the ammonia analyzer 99 detects the ammonia content in the mixed gas, the ammonia concentration is controlled to be lower than a set value, if the ammonia content exceeds the set value, the ammonia content is fed back to a control system, the ammonia injection amount of the flue denitration ammonia injection uniform distribution device 100 is reset, meanwhile, the ammonia injection amount of the ammonia injection structure 2 is adjusted by controlling a first adjusting valve through the control system, the residual ammonia content at the downstream of the SCR denitration reactor is continuously monitored and meets the set value, and the denitrated mixed gas enters a heat exchanger 93 and then flows through a flue gas outlet 921 to enter a downstream dust remover (prior art).

The above description is only exemplary of the present invention, and is not intended to limit the scope of the present invention. Any person skilled in the art should also realize that such equivalent changes and modifications can be made without departing from the spirit and principles of the present invention.

Claims

1. A flue denitration ammonia injection uniform distribution device is characterized by comprising an annular distribution pipe and at least 2 mutually independent ammonia injection structures; the annular distribution pipe is communicated with an ammonia gas inlet pipeline; a plurality of ammonia structures of spouting are even and adjacent to be set up in the flue, each spout the ammonia structure through spouting ammonia branch pipe intercommunication annular distribution pipe, each spout the ammonia structure and all include I shape branch pipe structure, I shape branch pipe structure can with spout ammonia branch pipe intercommunication, I shape branch pipe structure is last to be communicated with a plurality of distributors, each connect a plurality of sprayers on the distributor, each the injection direction of sprayer is perpendicular setting with the center pin of sprayer, and each the ammonia air current that a plurality of sprayers connected on the distributor sprayed can form the rotatory air current in center.

2. The flue denitration ammonia-spraying uniform distribution device as claimed in claim 1, wherein each injector comprises a connecting pipe, a first end of the connecting pipe is communicated with the distributor, a second end of the connecting pipe is communicated with a vertical pipe through a transition pipe, an arc-shaped guide plate is arranged at one end of the vertical pipe far away from the transition pipe, a plurality of penetrating injection holes are uniformly arranged on the side wall of the vertical pipe along the circumferential direction, the central shaft of the vertical pipe forms a central shaft of the injector, and the central shafts of the injection holes and the central shaft of the vertical pipe are vertically arranged.

3. The flue denitration ammonia-spraying uniform distribution device of claim 2, wherein the I-shaped branch pipe structure comprises a plurality of first-stage I-shaped branch pipes, each first-stage I-shaped branch pipe comprises a first-stage central pipe, two ends of each first-stage central pipe are respectively communicated with 1 first-stage transverse branch pipe, a first inlet is arranged at the symmetrical center of each first-stage central pipe, two ends of each first-stage transverse branch pipe are respectively provided with a first outlet, each first inlet can be communicated with the ammonia-spraying branch pipe, and each first outlet is respectively communicated with one distributor; the distributor is arranged in an X shape, a second inlet is arranged at the symmetrical center of the distributor and communicated with the first outlet, a second outlet is respectively arranged at each end of the distributor, and the second outlets are respectively communicated with the ejectors.

4. The flue denitration ammonia-spraying uniform distribution device as claimed in claim 3, wherein each of said distributors is provided with 4 of said second outlets, each of said second outlets is respectively communicated with one of said ejectors, the central horizontal connecting lines of the 4 ejectors on each of said distributors form a rectangle, one set of opposite sides is set as a first reference line, and the other set of opposite sides is set as a second reference line; the side wall of the vertical pipe is uniformly provided with 4 penetrating jet holes along the circumferential direction, one jet hole is set as a first jet hole, a jet hole adjacent to the first jet hole is set as a second jet hole, the central axis of the first jet hole and the first datum line form a first included angle, the central axis of the second jet hole and the second datum line form a second included angle, and the first included angle and the second included angle are arranged in an equal manner.

5. The flue denitration ammonia injection uniform distribution device of claim 4, wherein the range of the first included angle is 10 degrees to 80 degrees, and the range of the second included angle is 10 degrees to 80 degrees.

6. The flue denitration ammonia injection uniform distribution device of claim 2, wherein the diameter of the connecting pipe is smaller than that of the vertical pipe, the transition pipe is a conical pipe, and the diameter of the transition pipe is gradually increased from bottom to top.

7. The flue denitration ammonia-spraying uniform distribution device as claimed in claim 3, wherein the I-shaped branch pipe structure comprises 3 first-stage I-shaped branch pipes, the I-shaped branch pipe structure further comprises a transition connecting pipe, 3 third outlets are arranged on the transition connecting pipe, and each third outlet is respectively communicated with the first inlets of the 3 first-stage I-shaped branch pipes; and a third inlet is arranged on the transition connecting pipe, and the third inlet is communicated with the ammonia spraying branch pipe.

8. The flue denitration ammonia-spraying uniform distribution device as claimed in claim 3, wherein the I-shaped branch pipe structure comprises 4 first-stage I-shaped branch pipes, the I-shaped branch pipe structure further comprises a second-stage I-shaped branch pipe, a fourth inlet is arranged at the symmetrical center of the second-stage I-shaped branch pipe, a fourth outlet is respectively arranged at each end of the second-stage I-shaped branch pipe, the fourth inlet is communicated with the ammonia-spraying branch pipe, and each fourth outlet is respectively communicated with each first inlet.

9. The flue denitration ammonia injection uniform distribution device as claimed in claim 1, wherein each ammonia injection branch pipe is provided with a first regulating valve and a flow meter.

10. The flue denitration ammonia-spraying uniform distribution device of claim 1, wherein the annular distribution pipe is at least communicated with 2 ammonia gas inlet pipelines, and the 2 ammonia gas inlet pipelines adopt a symmetrical structural design; the cross-sectional area of the annular distribution pipe is more than 2 times of the sum of the cross-sectional areas of the ammonia injection branch pipes; and a second regulating valve is arranged on each ammonia gas inlet pipeline.

11. A denitration ammonia injection system comprises a denitration front flue, a denitration treatment flue and a control system, wherein a flue gas inlet is formed in the first end of the denitration front flue, a flue gas outlet is formed in the first end of the denitration treatment flue, and the second end of the denitration front flue and the second end of the denitration treatment flue are in sealed communication; the denitration front flue and the denitration treatment flue are communicated with each other and provided with a heat exchanger; an SCR denitration reactor is arranged between the second end of the denitration treatment flue and the heat exchanger; the denitration ammonia injection and uniform distribution device is characterized in that at least 1 flue denitration ammonia injection and uniform distribution device as set forth in any one of claims 1 to 10 is arranged between the second end of the denitration front flue and the heat exchanger, and the flue denitration ammonia injection and uniform distribution device is vertically arranged with the central shaft of the denitration front flue; a rotational flow mixing structure is arranged between the flue denitration ammonia-spraying uniform distribution device and the heat exchanger; an ammonia gas analyzer is arranged between the heat exchanger and the SCR denitration reactor and used for detecting the amount of ammonia gas in flue gas subjected to denitration treatment by the SCR denitration reactor, the ammonia gas analyzer is provided with a plurality of sampling measurement points, and each sampling measurement point is in one-to-one correspondence with each distributor of the flue denitration ammonia spraying and uniformly distributing device.

12. The denitration ammonia injection system of claim 11, wherein 2 flue denitration ammonia injection equispaced devices are axially arranged in parallel and at intervals on the flue before denitration between the second end of the flue and the heat exchanger, each flue denitration ammonia injection equispaced device comprises an annular distribution pipe and at least 2 mutually independent ammonia injection structures; each it all includes I shape branch pipe structure to spout the ammonia structure, I shape branch pipe structure includes a plurality of one-level I shape branch pipes, each one-level I shape branch pipe includes one-level center tube and one-level horizontal branch pipe, 2 circumference contained angle between the one-level center tube of flue denitration ammonia injection equipartition device is the third contained angle.

13. The denitration ammonia injection system of claim 12, wherein the third included angle is in the range of 30 ° to 60 °.

14. The denitration ammonia injection system of claim 11, wherein the swirl mixing structure comprises a plurality of swirl mixers arranged adjacently in an abutting manner, the swirl mixers are connected to the denitration front flue through a fixing structure, and the central connecting line of every two adjacent 3 swirl mixers is an equilateral triangle.

15. The denitration ammonia injection system of claim 14, wherein each of the swirl mixers comprises an annular frame, the annular frame has a connecting ring disposed therein at a coaxial and radially spaced location, a plurality of first inclined swirl vanes are disposed between the annular frame and the connecting ring at a circumferential spacing, and a fourth included angle between each of the first swirl vanes and a central axis of the connecting ring is equal.

16. The denitration ammonia injection system of claim 15, wherein the number of the first swirl vanes in each swirl mixer is 3-15, and the fourth included angle is in the range of 15-70 °.

17. The denitration ammonia injection system of claim 14, wherein each of the swirl mixers comprises an annular frame, and connecting rings are coaxially and radially spaced in the annular frame, and a central ring is coaxially and radially spaced in the connecting rings, and a blind plate is arranged at an end of the central ring; the annular frame with circumference interval sets up the second whirl blade of a plurality of slopes between the go-between, the go-between with circumference interval sets up the third whirl blade of a plurality of slopes between the centre ring, third whirl blade with the whirl direction of second whirl blade is opposite setting, each the second whirl blade with fifth contained angle between the center pin of go-between is equal setting, each third whirl blade with sixth contained angle between the center pin of go-between is equal setting.

18. The denitration ammonia injection system of claim 17, wherein the number of the second swirl vanes in each swirl mixer is 6-36, and the range of the fifth included angle is 25-70 °; the number of the third swirl vanes in each swirl mixer is 3-24, and the range of the sixth included angle is 15-65 degrees.