CN207680335U - A kind of waste incinerator flue denitrating system - Google Patents

A kind of waste incinerator flue denitrating system Download PDF

Info

Publication number
CN207680335U
CN207680335U CN201721588892.7U CN201721588892U CN207680335U CN 207680335 U CN207680335 U CN 207680335U CN 201721588892 U CN201721588892 U CN 201721588892U CN 207680335 U CN207680335 U CN 207680335U
Authority
CN
China
Prior art keywords
flue
spray gun
input port
compressed gas
waste incinerator
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
CN201721588892.7U
Other languages
Chinese (zh)
Inventor
袁磊
柴建伟
韩俊胜
石军武
郭康
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.)
China (beijing) Energy Saving And Environmental Protection Engineering Co Ltd
Original Assignee
China (beijing) Energy Saving And 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 China (beijing) Energy Saving And Environmental Protection Engineering Co Ltd filed Critical China (beijing) Energy Saving And Environmental Protection Engineering Co Ltd
Priority to CN201721588892.7U priority Critical patent/CN207680335U/en
Application granted granted Critical
Publication of CN207680335U publication Critical patent/CN207680335U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Chimneys And Flues (AREA)
  • Treating Waste Gases (AREA)

Abstract

The utility model discloses a kind of waste incinerator flue denitrating systems, including waste incinerator, the flue gas of waste incinerator is through flue whereabouts waste heat boiler, the flue is divided into the first flue, the second flue and third flue, first flue is the flue that section is rectangle, at least three row's spray guns are respectively set on three side walls of the rectangular flue, wherein:Neighbouring two rows of spray guns in two opposing sidewalls in spray gun are staggered, with opposing sidewalls alignment is arranged vertically adjacent to the spray gun on side wall up and down, the compressed gas source includes compressor and voltage stabilizing air accumulator, and the voltage stabilizing air accumulator is connected to the compressed gas input port of spray gun by a pressure reducing valve.It is low that the utility model solves nozzle service life, and rational nozzle layout eliminates injection dead zone, improves denitration efficiency 10% 15%, not only ensure that DS NOx Est reaches 2010 standard of European Union, and delayed the service life of equipment, reduce equipment failure rate and maintenance frequency, improves denitration efficiency.

Description

A kind of waste incinerator flue denitrating system
Technical field
The utility model is related to a kind of waste incinerator flue denitrating systems.
Background technology
SNCR denitration technology has been widely used in garbage incinerating power plant at present, is diluted in flue by spraying Ammoniacal liquor realize denitration, reduce the discharge of nitrogen oxides, but with people's standard higher and higher to surrounding air, and face Increasingly severeer Environmental Protection Situation, higher for the degree of purification requirement of garbage incinerating power plant flue gas emission, local government exists To requiring nitrogen oxide emission to be less than 200mg/m in garbage incinerating power plant project environmental impact assessment3Or even some districts and cities require nitrogen Oxide uses minimum discharge standard, discharge capacity to be less than or equal to 100mg/m3.Can also it go out sometimes in current garbage incinerating power plant Existing denitrating flue gas is unstable, and nozzle life is short, and corrosion is washed away seriously, so as to cause the low problem of denitration efficiency.Therefore, it is necessary to adopt Take stringenter technical measures, in the flue gas emission of garbage incinerating power plant ensure denitration stabilization and efficiently.
Invention content
The purpose of this utility model is to propose a kind of waste incinerator flue denitrating system, passes through the pipe conveyed in reducing agent Increase voltage stabilizing air accumulator in road, and the nozzle of stainless steel is replaced with into the technical measures such as silicon nitride ceramics nozzle, improves cigarette Qi exhaustion nitre stability, extends the service life of nozzle, ensure denitrating flue gas stabilization and efficiently.
To achieve the goals above, the technical solution of the utility model is:
A kind of waste incinerator flue denitrating system, including waste incinerator, the flue gas of waste incinerator is through flue whereabouts Waste heat boiler, the flue are divided into three-level, and respectively the first flue, the second flue and third flue, flue gas sequence is through the first cigarette Road, the second flue and third flue enter waste heat boiler, between second flue and third flue by setting it is vertical to Under water-cooled wall partition wall separate, first flue be section be rectangle flue, in the side wall upper edge cigarette of rectangular flue The flue gas trend in road is provided with multiple rows of spray gun for denitration, and spray gun has reducing agent input port and compressed gas input port, reducing agent Input port connects reducing agent input source, and compressed gas input port is connected with compressed gas source, and the compression inputted from compressed gas input port is empty Gas sprays the reducing agent inputted from reducing agent input port in spray gun from the nozzle of spray gun after mixed aerosol;In the rectangle cigarette At least three row's spray guns are respectively set on three side walls in road, wherein:Neighbouring two rows of sprays in two opposing sidewalls in spray gun Rifle is staggered, and arranges alignment up and down vertically adjacent to the spray gun on side wall with opposing sidewalls, the compressed gas source includes compression Machine and voltage stabilizing air accumulator, the voltage stabilizing air accumulator are connected to the compressed gas input port of spray gun, voltage stabilizing gas storage by a pressure reducing valve The gas storage pressure of tank is at least 1.5 times of spray gun compressed gas input port air pressure.
Scheme is further:The reducing agent input source includes:The urea liquid preparation tank that is linked in sequence, urea liquid storage It deposits tank, urea liquid supply unit, metering mixed cell and a dilution soft water storage tank and soft water supply unit, soft water is defeated Unit connection metering mixed cell, metering mixed cell is sent to inject spray gun reducing agent by mixed reducing agent is measured by metering pump Input port.
Scheme is further:The nozzle of the spray gun is silicon nitride ceramics nozzle, and the spray angle of nozzle is 120 degree of level Angle.
Scheme is further:The admission pressure of the compressed gas input port of the spray gun is 0.5Mpa.
The utility model has the beneficial effects that:
It is low to solve nozzle service life, rational nozzle layout eliminates injection dead zone and carried under same conditions of mixture ratios High denitration efficiency 10%-15%, not only ensures that DS NOx Est reaches 2010 standard of European Union, but also delayed the service life of equipment, reduces Equipment failure rate and maintenance frequency, improve denitration efficiency.The silicon nitride ceramics nozzle that this denitration in the stove uses can be Domestic garbage burning electricity generation is widelyd popularize, and the low big output of input has ensured burning power plant monolithic stability, safe and environment-friendly fortune Row.
The utility model is described in detail with reference to the accompanying drawings and examples.
Description of the drawings
Fig. 1 is the utility model structure section schematic diagram;
Fig. 2 is the utility model reducing agent input source connection relation structural schematic diagram.
Specific implementation mode
A kind of waste incinerator flue denitrating system is the flue denitrating system for the application of waste incinerator waste heat, such as Shown in Fig. 1 and Fig. 2, including waste incinerator 1, through flue whereabouts waste heat boiler, the flue is divided into the flue gas of waste incinerator Three-level, respectively the first flue 2, the second flue 3 and third flue 4, flue gas sequence is through the first flue, the second flue and third cigarette Road enters waste heat boiler, passes through the water-cooled wall partition wall 5 vertically downward of setting between second flue and third flue It separates, collection ash of the water-cooled wall partition wall for flue gas collects the ash collection slot 6 that the ash falls into following settings, flue gas is in the first cigarette Road carries out denitration, and therefore, first flue is the flue that section is rectangle, i.e. square flue, on the side wall of rectangular flue Flue gas trend along flue is provided with multiple rows of spray gun 7 for denitration, and spray gun structure is the prior art, and spray gun has reducing agent input Mouth and compressed gas input port, reducing agent input port connect reducing agent input source, and compressed gas input port is connected with compressed gas source, from pressure Contracting gas input port input compressed air by the reducing agent inputted from reducing agent input port in spray gun after mixed aerosol from spray gun Nozzle spray;Wherein, in order to improve, only there are denitration effects to pay no attention to for setting spray gun on two adjacent walls in the prior art At least three row's spray guns are respectively set in the present situation thought, the present embodiment on three side walls of the rectangular flue, in order to overcome injection Dead angle, wherein:Neighbouring two rows of spray guns in two opposing sidewalls in spray gun are staggered, with opposing sidewalls vertically adjacent to side Spray gun on wall arranges alignment up and down, and distance between row and row is at 1.5 to 2.5 meters;Also, the compressed gas source includes pressure Contracting machine 8 and voltage stabilizing air accumulator 9, the voltage stabilizing air accumulator are connected to the compressed gas input port of spray gun by a pressure reducing valve 10, surely The gas storage pressure of pressure air accumulator is at least 1.5 times of spray gun compressed gas input port air pressure.
In embodiment:As shown in Fig. 2, the reducing agent input source includes:The urea liquid preparation tank 11 that is linked in sequence, urine Plain solution storage tanks 12, urea liquid supply unit 13, metering mixed cell 14 and a dilution soft water storage tank 15 and soft water Supply unit 16, soft water supply unit connect metering mixed cell, metering mixed cell going back metering mixing by metering pump Former agent injection spray gun reducing agent input port.
Denitration nozzle is chronically in hot environment, and sour corrosion is than more serious, the nozzle of general 316L materials, at most As soon as operation year or so is just corroded and washes away very serious, nozzle reduces once being corroded and washing away atomizing effect, and droplet dew phenomenon is tight Weight reduces so as to cause denitration efficiency.For this purpose, in the present embodiment:The nozzle of the spray gun is silicon nitride ceramics nozzle, nitridation The main constituent of silicon ceramics is Si3N4, this is a kind of elevated temperature strength height, high rigidity, wear-resisting, corrosion-resistant and energy self-lubricating high temperature Ceramics, linear expansion coefficient is minimum in various ceramics, and temperature in use is up to 1400 DEG C, has fabulous corrosion resistance, dehydrogenation fluorine It is sour outer, the corrosion of various other acid, and alkaline-resisting, the various corrosions of metal of energy are resistant to, and there is excellent electrical insulating property and resistance to spoke Penetrating property.The spray angle of nozzle is 120 degree of angles of level.
In embodiment:The admission pressure of the compressed gas input port of the spray gun is 0.5Mpa.Two Fluid sprayers selected, NH3 water atomizations are atomized using compressed air, and NH3 water mists are melted into the thin of 50 microns of average diameter or more by the compressed air of 0.5Mpa Mist produces N2 and H2O by NH3 and reaction of nitrogen oxides.It is best that compressed air is maintained at 0.5Mpa atomizing effects, but general electricity Factory's air branching ratio is more, and the compressed air pressure of same pipeline fluctuates larger, compressed air pressure influence of fluctuations atomizing effect, If uniformly mixing, denitration efficiency can be substantially reduced for flue gas and the reaction of NH3 water.Therefore, using in compressed air in embodiment Increase compressed air vacuum tank before air inlet, ensure that compressed air pressure maintains 0.5Mpa or so, ensure nebulization efficiency, improves de- Nitre efficiency.
It is low that the present embodiment solves nozzle service life, improves denitration efficiency 10%-15%, the nitrogen for making waste incineration generate What oxide was stablized maintains 200mg/m per hour3

Claims (4)

1. a kind of waste incinerator flue denitrating system, including waste incinerator, the flue gas of waste incinerator is through more than flue whereabouts Heat boiler, the flue are divided into three-level, respectively the first flue, the second flue and third flue, flue gas sequence through the first flue, Second flue and third flue enter waste heat boiler, between second flue and third flue by setting vertically downward Water-cooled wall partition wall separates, and first flue is the flue that section is rectangle, in the side wall upper edge flue of rectangular flue Flue gas trend is provided with multiple rows of spray gun for denitration, and spray gun has reducing agent input port and compressed gas input port, reducing agent input Mouth connection reducing agent input source, compressed gas input port are connected with compressed gas source, and the compressed air inputted from compressed gas input port will The reducing agent inputted from reducing agent input port sprays after mixed aerosol from the nozzle of spray gun in spray gun;It is characterized in that, institute It states and at least three row's spray guns is respectively set on three side walls of rectangular flue, wherein:Phase up and down in two opposing sidewalls in spray gun Adjacent two rows spray gun is staggered, and alignment, the compressed gas source are arranged up and down vertically adjacent to the spray gun on side wall with opposing sidewalls Including compressor and voltage stabilizing air accumulator, the voltage stabilizing air accumulator is connected to the compressed gas input port of spray gun by a pressure reducing valve, The gas storage pressure of voltage stabilizing air accumulator is at least 1.5 times of spray gun compressed gas input port air pressure.
2. waste incinerator flue denitrating system according to claim 1, which is characterized in that the reducing agent input source packet It includes:The urea liquid preparation tank that is linked in sequence, urea liquid holding vessel, urea liquid supply unit, metering mixed cell, and One dilution soft water storage tank and soft water supply unit, soft water supply unit connection metering mixed cell, metering mixed cell pass through Metering pump will measure mixed reducing agent injection spray gun reducing agent input port.
3. waste incinerator flue denitrating system according to claim 1, which is characterized in that the nozzle of the spray gun is nitrogen The spray angle of SiClx ceramic nozzle, nozzle is 120 degree of angles of level.
4. waste incinerator flue denitrating system according to claim 1, which is characterized in that the compressed gas of the spray gun is defeated The admission pressure of entrance is 0.5Mpa.
CN201721588892.7U 2017-11-24 2017-11-24 A kind of waste incinerator flue denitrating system Active CN207680335U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721588892.7U CN207680335U (en) 2017-11-24 2017-11-24 A kind of waste incinerator flue denitrating system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721588892.7U CN207680335U (en) 2017-11-24 2017-11-24 A kind of waste incinerator flue denitrating system

Publications (1)

Publication Number Publication Date
CN207680335U true CN207680335U (en) 2018-08-03

Family

ID=62999059

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721588892.7U Active CN207680335U (en) 2017-11-24 2017-11-24 A kind of waste incinerator flue denitrating system

Country Status (1)

Country Link
CN (1) CN207680335U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109539264A (en) * 2018-12-21 2019-03-29 北京高安屯垃圾焚烧有限公司 Garbage incinerating system and garbage incineration method
CN112240556A (en) * 2020-10-20 2021-01-19 江苏天楹等离子体科技有限公司 Flue gas waste heat utilization device of garbage incinerator

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109539264A (en) * 2018-12-21 2019-03-29 北京高安屯垃圾焚烧有限公司 Garbage incinerating system and garbage incineration method
CN109539264B (en) * 2018-12-21 2024-04-05 北京高安屯垃圾焚烧有限公司 Garbage incineration equipment and garbage incineration method
CN112240556A (en) * 2020-10-20 2021-01-19 江苏天楹等离子体科技有限公司 Flue gas waste heat utilization device of garbage incinerator

Similar Documents

Publication Publication Date Title
CN207680335U (en) A kind of waste incinerator flue denitrating system
CN203043817U (en) Selective catalytic reduction (SCR) denitration system capable of increasing flue gas temperature by utilizing high-temperature steam
CN205235766U (en) Automatic control SCR flue gas denitration urea pyrolysis system
CN103463977A (en) SCR (Selective Catalytic Reduction) denitration device for directly spraying ammonium hydroxide
CN205027203U (en) Online chemical cleaning device of air heater
CN202860407U (en) Full mixing-type ammonia spraying component
CN211799959U (en) Ammonia SNCR (Selective non catalytic reduction) denitration system for tower boiler
CN104941446A (en) Ammonia spraying grating anti-blocking device for SCR denitration system
CN108905567B (en) Flue gas treatment system for ceramic production
CN202844862U (en) Smoke denitration device
CN206965500U (en) Fire coal boiler fume denitrating system
CN204447709U (en) A kind of SNCR denitration system
CN110787609A (en) Flue gas denitration device for tank furnace and denitration method thereof
CN106139868A (en) A kind of remove the system of sulfur trioxide in flue gas in power station boiler
CN210356699U (en) Novel ammonia diluting device
CN102626589B (en) SNCR (Selective Non Catalytic Reduction) denitrification gun spraying system of large boiler and use method thereof
CN208449035U (en) A kind of SNCR denitration system
CN211896058U (en) Urea pyrolysis system
CN203678250U (en) Selective non-catalytic reduction (SNCR) denitration reactor provided with double-fluid spray gun
CN113019109A (en) Selective non-catalytic reduction desulfurization method
CN206444437U (en) Boiler SNCR urea method denitrating systems
CN111482083A (en) Dangerous waste incineration SCR (Selective catalytic reduction) equipment without external energy consumption
CN216321047U (en) SNCR + SCR coupling deNOx systems based on high low temperature flue gas mixes
CN106268269A (en) The device of a kind of nitrogen oxides in controlling to burn and control method
CN204768279U (en) A ammonia injection grid prevents stifled device for SCR deNOx systems

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant