CN210021685U - Ammonia spraying grid for SNCR denitration of zinc oxide rotary kiln - Google Patents

Ammonia spraying grid for SNCR denitration of zinc oxide rotary kiln Download PDF

Info

Publication number
CN210021685U
CN210021685U CN201920633639.1U CN201920633639U CN210021685U CN 210021685 U CN210021685 U CN 210021685U CN 201920633639 U CN201920633639 U CN 201920633639U CN 210021685 U CN210021685 U CN 210021685U
Authority
CN
China
Prior art keywords
pipeline
zinc oxide
rotary kiln
distribution
kiln body
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
CN201920633639.1U
Other languages
Chinese (zh)
Inventor
郭明明
周兵利
郑雪萍
吴占军
刘海涛
张大力
陈晓飞
杨锡娟
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.)
Luoyang Hollysys Environmental Protection Engineering Co., Ltd
Original Assignee
Luoyang Helishi Environmental Protection Technology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Luoyang Helishi Environmental Protection Technology Co Ltd filed Critical Luoyang Helishi Environmental Protection Technology Co Ltd
Priority to CN201920633639.1U priority Critical patent/CN210021685U/en
Application granted granted Critical
Publication of CN210021685U publication Critical patent/CN210021685U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Images

Landscapes

  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Treating Waste Gases (AREA)

Abstract

The utility model belongs to the technical field of zinc oxide rotary kiln flue gas is administered, a ammonia injection grid for zinc oxide rotary kiln SNCR denitration is proposed. The ammonia spraying grid for SNCR denitration of the zinc oxide rotary kiln is provided with a conveying pipeline arranged in a settling chamber; the ammonia injection grid is also provided with a flow pipeline in the kiln body; the circulating pipeline is arranged along the length direction of the kiln body; one end of the circulating pipeline extends out of the kiln body and is communicated with a conveying pipeline positioned in the settling chamber, the other end of the circulating pipeline extends into a reaction area of the kiln body, and a distribution disc is arranged at the end head of the circulating pipeline; a plurality of distribution pipes communicated with the distribution disc are arranged on the circumference of the distribution disc; the distribution pipes are arranged in a star shape, each distribution pipe is provided with a plurality of spray heads, and the mounting directions of two adjacent spray heads are opposite; a plurality of inclined struts for supporting the circulation pipeline are arranged corresponding to the circulation pipeline. The utility model provides an application difficult problem of SNCR in the zinc oxide rotary kiln, reduced the denitration cost of zinc oxide rotary kiln.

Description

Ammonia spraying grid for SNCR denitration of zinc oxide rotary kiln
Technical Field
The utility model belongs to the technical field of industrial kiln flue gas treatment, mainly relate to an ammonia injection grid for zinc oxide rotary kiln SNCR denitration.
Background
The ammonia spraying grid is one of key equipment of the SNCR denitration device of the zinc oxide rotary kiln; the well-designed ammonia injection grid needs to have the medium uniform distribution effect as large as possible, so that the denitration agent and the flue gas are fully mixed, the equipment cost is low, the stability is high, and the special working condition of the zinc oxide rotary kiln can be adapted; in the zinc oxide smelting process, because the kiln body is constantly doing the rotation, traditional flue gas denitration is with spouting ammonia grid can't effectually fix and utilize, consequently, the research design can adapt to the ammonia-spraying grid of zinc oxide rotary kiln operating mode and have certain practical meaning.
Disclosure of Invention
The utility model aims at providing an ammonia injection grid for zinc oxide rotary kiln SNCR denitration makes its nitrogen oxide in effectively getting rid of the flue gas, does not influence zinc oxide product quality simultaneously.
The utility model adopts the following technical proposal to complete the invention task:
an ammonia injection grid for SNCR denitration of a zinc oxide rotary kiln is provided with a conveying pipeline arranged in a settling chamber; the ammonia injection grid is also provided with a flow pipeline in the kiln body; the circulating pipeline is arranged along the length direction of the kiln body; one end of the circulating pipeline extends out of the kiln body and is communicated with a conveying pipeline positioned in the settling chamber, the other end of the circulating pipeline extends into a reaction area of the kiln body, and a distribution disc is arranged at the end head of the circulating pipeline; a plurality of distribution pipes communicated with the distribution disc are arranged on the circumference of the distribution disc; the distribution pipes are arranged in a star shape, each distribution pipe is provided with a plurality of spray heads, and the mounting directions of two adjacent spray heads are opposite; a plurality of inclined struts for supporting the circulation pipeline are arranged corresponding to the circulation pipeline; the inclined strut is fixed on the blanking pipe, and the blanking pipe is fixed on the settling chamber through the reinforcing pipe.
The diameter of the flow conduit is smaller than the diameter of the delivery conduit.
The utility model provides an ammonia injection grid for zinc oxide rotary kiln SNCR denitration adopts above-mentioned technical scheme, has following beneficial effect: when the ammonia injection grid works, the connecting pipe can extend into the kiln body due to the fixing and supporting functions of the inclined strut, so that the SNCR reaction is ensured to be carried out in a reasonable temperature interval; the pressure flow of the distribution disc and the pressure flow of the distribution pipe are uniformly distributed, so that the flow balance of each nozzle is ensured, and the mixing effect of the flue gas and the denitrifying agent is improved; due to the atomization effect of the nozzle, the turbulent flow state between the flue gas and the denitrifier is enhanced, the denitration reaction is favorably and rapidly carried out, and the denitration efficiency is improved; meanwhile, the ammonia injection grid is simple in structure and small in fluid circulation resistance, and has no adverse effect on the collection and product quality of zinc oxide rotary kiln products.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
Fig. 2 is a schematic structural view of the distribution pipe and the nozzle of the present invention.
In the figure: 1. conveying pipeline, 2, circulation pipeline, 3, distribution disc, 4, bracing, 5, stand, 6, distribution pipe, 7, shower nozzle, 8, settling chamber, 9, kiln body, 10, unloading pipe.
Detailed Description
The invention is described in connection with the accompanying drawings and the embodiments:
as shown in fig. 1, and in combination with fig. 2, an ammonia injection grid for SNCR denitration of a zinc oxide rotary kiln is provided with a conveying pipe 1 arranged in a settling chamber 8; the ammonia injection grid is also provided with a flow pipeline 2 in the kiln body 9; the circulation pipeline 2 is arranged along the length direction of the kiln body 9; the diameters of the conveying pipeline 1 and the circulating pipeline 2 are determined by the treated flue gas volume and the concentration of nitrogen oxides, the diameter of the circulating pipeline 2 is smaller than that of the conveying pipeline 1, the length of the conveying pipeline 1 is determined by the specification of a settling chamber, and the length of the circulating pipeline 2 is determined by the flue gas temperature of a rotary kiln; one end of the circulation pipeline 2 extends out of the kiln body 9 and is communicated with the conveying pipeline 1 positioned in the settling chamber 8, the other end of the circulation pipeline 2 extends into the reaction area of the kiln body 9, the end head of the circulation pipeline is provided with a distribution disc 3, and the denitration agent is conveyed to the reaction area at 800-1100 ℃ through the circulation pipeline in the kiln body; a plurality of distribution pipes 6 communicated with the distribution disc 3 are arranged on the circumference of the distribution disc; the diameter of the distribution disc 3 is determined by the dosage of the denitrifier, and the length of the distribution disc is 300 mm; the length and the number of the distribution pipes 6 are determined by the diameter of the rotary kiln, and the diameter of the distribution pipes 6 is determined by the dosage of the denitrifier; the distribution pipes 6 are arranged in a star shape, each distribution pipe 6 is provided with a plurality of spray heads 7, and the installation directions of two adjacent spray heads 7 are opposite; the specification of the spray nozzles 7 is determined by the flow rate of the flue gas, and the number of the spray nozzles 7 is determined by the amount of the flue gas; a plurality of inclined struts 4 for supporting the circulation pipeline are arranged corresponding to the circulation pipeline; the inclined strut is fixed on the blanking pipe 10, and the blanking pipe and the reinforcing pipe are firmly fixed on the settling chamber; the upright post 5 is arranged corresponding to the conveying pipeline and used for supporting the conveying pipeline; the denitration agent enters a circulating pipeline in the kiln body through a conveying pipeline in the settling chamber, and is sprayed out through nozzles arranged on the distribution pipe through the pressure and flow uniform distribution effect of the distribution disc, so that the denitration agent is fully mixed with the flue gas, and the nitrogen oxides in the flue gas are removed.
The utility model discloses when using: the denitration agent enters the settling chamber through the conveying pipeline 1, then enters an SNCR reaction temperature area in the rotary kiln through the circulating pipeline 2, enters the 6 distribution pipes through the pressure and flow uniform distribution effect of the distribution disc 3, and then is fully mixed with high-temperature flue gas through the atomization effect of the spray head 7 to remove partial nitrogen oxides.

Claims (2)

1. An ammonia injection grid for SNCR denitration of a zinc oxide rotary kiln is characterized in that: the ammonia injection grid is provided with a conveying pipeline arranged in the settling chamber; the ammonia injection grid is also provided with a flow pipeline in the kiln body; the circulating pipeline is arranged along the length direction of the kiln body; one end of the circulating pipeline extends out of the kiln body and is communicated with a conveying pipeline positioned in the settling chamber, the other end of the circulating pipeline extends into a reaction area of the kiln body, and a distribution disc is arranged at the end head of the circulating pipeline; a plurality of distribution pipes communicated with the distribution disc are arranged on the circumference of the distribution disc; the distribution pipes are arranged in a star shape, each distribution pipe is provided with a plurality of spray heads, and the mounting directions of two adjacent spray heads are opposite; a plurality of inclined struts for supporting the circulation pipeline are arranged corresponding to the circulation pipeline; the inclined strut is fixed on the blanking pipe, and the blanking pipe is fixed on the settling chamber through the reinforcing pipe.
2. The ammonia injection grid for SNCR denitration of a zinc oxide rotary kiln as recited in claim 1, wherein: the diameter of the flow conduit is smaller than the diameter of the delivery conduit.
CN201920633639.1U 2019-05-06 2019-05-06 Ammonia spraying grid for SNCR denitration of zinc oxide rotary kiln Active CN210021685U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201920633639.1U CN210021685U (en) 2019-05-06 2019-05-06 Ammonia spraying grid for SNCR denitration of zinc oxide rotary kiln

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201920633639.1U CN210021685U (en) 2019-05-06 2019-05-06 Ammonia spraying grid for SNCR denitration of zinc oxide rotary kiln

Publications (1)

Publication Number Publication Date
CN210021685U true CN210021685U (en) 2020-02-07

Family

ID=69363477

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201920633639.1U Active CN210021685U (en) 2019-05-06 2019-05-06 Ammonia spraying grid for SNCR denitration of zinc oxide rotary kiln

Country Status (1)

Country Link
CN (1) CN210021685U (en)

Similar Documents

Publication Publication Date Title
CN103657385A (en) Double-atomization spray gun for SNCR (selective non-catalytic reduction) denitration system
CN202921159U (en) Double-atomization spray gun for SNCR (selective non-catalytic reduction) denitration system
CN204724006U (en) For the ozone injection apparatus of ozone denitration
CN211328967U (en) Venturi mixing device with embedded throat pipe
CN206152600U (en) Flue gas system distribution apparatus of high -efficient denitration of ozone in low temperature section absorption tower
CN204933244U (en) NOx removal device in coal-burning power plant's coal-powder boiler flue gas
CN210021685U (en) Ammonia spraying grid for SNCR denitration of zinc oxide rotary kiln
CN202315691U (en) SNCR-SCR (Selective Non-Catalytic Reduction-Selective Catalytic Reduction) combined smoke denitration device
CN211462689U (en) Ammonia spraying device for flue gas denitration and flue gas denitration system
CN203173834U (en) Reverse-flow urea-pyrolysis ammonia preparing device
CN204952626U (en) Gas cleaning equipment of gas -phase oxidation system and this system of application
CN207805381U (en) A kind of low-temperature denitration device
CN102350216A (en) Tripod nozzle device of thermal power station ammonia-injection and denitration system
CN104607032B (en) Desulphurization plant
CN206823552U (en) A kind of ammonia-spraying grid device
CN206837860U (en) A kind of carbon ammonium is that reducing agent decomposes ammonia SCR denitration system processed
CN215326964U (en) Skid-mounted horizontal urea pyrolysis furnace
CN206168206U (en) Drying grate rotary kiln deNOx systems
CN101905120A (en) Ammonia spray nozzle mixer for SCR denitrating device
CN106731810A (en) A kind of SCR denitration eddy flow chip static mixer
CN210495940U (en) Urea pyrolysis ammonia production device with uniform flow field
CN207042259U (en) A kind of ammonia-spraying grid
CN203355594U (en) Denitration urea ejector
CN207628203U (en) A kind of molecular sieve exhaust gas denitration dust-extraction unit
CN206355836U (en) One kind spray ammonia structure

Legal Events

Date Code Title Description
GR01 Patent grant
CP01 Change in the name or title of a patent holder
CP01 Change in the name or title of a patent holder

Address after: 471000 1-10-1006, Runsheng building, intersection of Heluo road and Sanshan Road, high tech Zone, Luoyang area, China (Henan) pilot Free Trade Zone, Luoyang City, Henan Province

Patentee after: Luoyang Hollysys Environmental Protection Engineering Co., Ltd

Address before: 471000 1-10-1006, Runsheng building, intersection of Heluo road and Sanshan Road, high tech Zone, Luoyang area, China (Henan) pilot Free Trade Zone, Luoyang City, Henan Province

Patentee before: Luoyang Helishi Environmental Protection Technology Co.,Ltd.