CN105543471B - A kind of NOx control methods based on suppression Ore Sintering Process fuel bound nitrogen conversion - Google Patents

A kind of NOx control methods based on suppression Ore Sintering Process fuel bound nitrogen conversion Download PDF

Info

Publication number
CN105543471B
CN105543471B CN201610071111.0A CN201610071111A CN105543471B CN 105543471 B CN105543471 B CN 105543471B CN 201610071111 A CN201610071111 A CN 201610071111A CN 105543471 B CN105543471 B CN 105543471B
Authority
CN
China
Prior art keywords
sintering
fine
nox
ore
fuel
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
CN201610071111.0A
Other languages
Chinese (zh)
Other versions
CN105543471A (en
Inventor
范晓慧
甘敏
吕薇
陈许玲
姜涛
李光辉
季志云
周阳
余志元
何向宁
袁礼顺
郭宇峰
杨永斌
黄柱成
李骞
张元波
朱忠平
李强
汪国靖
田野
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.)
Central South University
Original Assignee
Central South University
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 Central South University filed Critical Central South University
Priority to CN201610071111.0A priority Critical patent/CN105543471B/en
Publication of CN105543471A publication Critical patent/CN105543471A/en
Application granted granted Critical
Publication of CN105543471B publication Critical patent/CN105543471B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B1/00Preliminary treatment of ores or scrap
    • C22B1/14Agglomerating; Briquetting; Binding; Granulating
    • C22B1/16Sintering; Agglomerating

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Geochemistry & Mineralogy (AREA)
  • Geology (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Manufacture And Refinement Of Metals (AREA)

Abstract

The invention discloses a kind of based on the NOx control methods for suppressing the conversion of Ore Sintering Process fuel bound nitrogen, first the particle screening for being less than 1mm in sinter return fine is come out, then by 1mm sinter return fine, Fine Hematite Ore, quick lime, sintering fuel and with cementation hydrocarbon dispensing after, prefabricated grain is carried out in trommel mixer, gained compound is pelletized with remaining iron-bearing material, flux, sinter return fine;Then by its cloth, igniting, sintering.The present invention for the conversion of volatile matter nitrogen and coke nitrogen to NOx has separately designed discharge-reducing method, by suppressing fuel N oxidation reaction and promoting NOx reduction reaction two methodses, realizes the discharge of the control NOx in sintering process, with strong points, emission reduction effect is good.

Description

A kind of NOx control methods based on suppression Ore Sintering Process fuel bound nitrogen conversion
Technical field
The invention belongs to field of steel metallurgy, more particularly to it is a kind of based on suppressing the conversion of Ore Sintering Process fuel bound nitrogen NOx control methods.
Background technology
NOx (nitrogen oxides) is one of main reason of photochemical fog and acid rain, and pollution problem caused by it is discharged is tight Ghost image rings ecological environment and is detrimental to health.The most important NOx emission of industry comes from fossil fuel (coal, oil, day at present Right gas etc.) burning, iron and steel enterprise is one of important sources of NOx emission, accounts for more than the 10% of national NOx discharge.And In sintering circuit, substantial amounts of coke powder, anthracite etc. are consumed, its NOx discharge accounts for the 48% of iron and steel enterprise's total release.2015 On January 1, in comes into effect《Steel sintering, pelletizing industrial air pollution thing discharge standard》Middle regulation NOx emission new standard is 300mg/m3, and NOx concentration is typically in 400~600mg/m in current domestic iron and steel enterprises sintering flue gas3, realize in sintering process NOx emission reduction is extremely urgent.
NOx is mainly fuel type NOx in sintering process, is typically derived from the burning of coke powder or anthracite etc..Common Under ignition temperature, NO accounts for 90% or so, NO in NOx caused by solid fuel ignition2Account for 5%~10%, N2O accounts for 1% or so.Together When, if there is reducing atmosphere and appropriate catalyst action, NOx is also possible to be reduced into N2Or the NOx of low price.Fuel type NOx formation mechanism is more complicated, with the close phase such as distribution, ignition temperature and oxygen concentration of the nitrogen in volatile matter and coke Close.Abundant experimental results show, heat initial stage, and volatile matter nitrogen discharges that nitrogen-containing group ratio is higher, with temperature rise and The extension in reaction time, the nitrogen-containing group in coke nitrogen start a large amount of to participate in reaction.
At present, substantial amounts of research has been expanded for NOx abatement and removal methods domestic and foreign scholars, mainly had following The technology of three types:1. low NOx combusting technology, by using oxygen concentration, reduction ignition temperature, reduction around reduction fuel Fuel is in the high-temperature region residence time, the means such as addition reducing agent promote NOx to decompose or be reduced to N in stove2;2. selectivity is urged Change reduction gas denitrifying technology, under conditions of certain temperature and with catalyst, utilize CH4、CO、H2、NH3Etc. reproducibility thing NOx is reduced into N by matter2;3. SNCR gas denitrifying technology, it is to spray ammonia or urea etc. into flue gas to contain amino Reducing agent, in the case of high temperature (850~1100 DEG C) and without catalyst, pass through caused ammonia free radical in flue gas stream Reacted with NOx, NOx is reduced into N2And H2O.NOx emission reduction technically can be achieved above, but it is multiple cost height, technique to be present The problems such as miscellaneous, and it is primarily adapted for use in coal-burning power plant.Because steel sintering smoke yields are big, flue-gas temperature is low, urged using selectivity Changing the technique of the end treatments such as denitration needs supporting fume treatment auxiliary to put into big, cost height.And for low NOx combustion skill Art, because sintering process is related to the course of reaction of Various Complex, change burning condition may produce considerable influence to sintering process, Still hardly possible is applied to sintering process for it.Foreign countries have scholar to utilize microwave heating treatment upper strata sintering feed before sintering ignition, it is believed that can To reduce NOx discharge to a certain extent, but O2Concentration need to be controlled below 18%.Domestic Wang Zhi et al. is fired using decoupling Burn and return to denitrating technique altogether with flue gas, added into the flue gas for be recycled back to pallet and contain H2, CO and NH3, HCN pyrolysis gas With the NOx of reduction generation so that NOx obtains a certain degree of degraded;Wuhan University Of Technology's Bi Xue works et al. are to sinter mixture Generation NH can be decomposed under middle addition hot conditions3Ammonia additive, under the catalytic action of iron ore, NH3Burning can be reduced The NOx generated during knot.Studies have shown that above technology can not only influence Sintering Operation Index index, and emission reduction efficiency is simultaneously Undesirable, the use of a large amount of additives also increases cost.Therefore, a kind of easy and effective, inexpensive sintering NOx abatement is developed Technology, pollutant emission is reduced to steel sintering factory, the environmentally friendly cost of reduction has great importance.
The content of the invention
The technical problem to be solved in the present invention is overcome the deficiencies in the prior art, there is provided one kind is fired based on sintering process is suppressed Expect nitrogen conversion NOx control methods, the technical process is simple, low for equipment requirements, cost is cheap, do not increase sintering production into This, do not reduce the emission reduction that NOx can be effectively realized on the basis of Sintering Operation Index.
In order to solve the above technical problems, technical scheme proposed by the present invention is:
A kind of NOx control methods based on suppression Ore Sintering Process fuel bound nitrogen conversion, first will be less than 1mm in sinter return fine Particle screening come out, then by -1mm sinter return fine, Fine Hematite Ore, quick lime, sintering fuel and there is cementation Hydrocarbon dispensing after, carry out prefabricated grain in trommel mixer, gained compound and remaining iron-bearing material, flux, burning Knot, which is returned mine, carries out conventional granulation;Then by its cloth, igniting, sintering;Wherein described sintering fuel is coke powder or anthracite.
Above-mentioned method, it is preferred that during the prefabricated grain, the dosage of -1mm sinter return fines is sintering fuel quality 1.5~3.0 times.
Above-mentioned method, it is preferred that SiO in the Fine Hematite Ore2Mass content be 4~6%;The red iron of particulate Ore deposit is more than 70% hematite concentrates for -0.074mm mass contents, or -0.5mm mass contents are more than 50% hematite ore fines, or Both mixtures.
Above-mentioned method, it is preferred that the addition of the Fine Hematite Ore is the 20~40% of sintering iron ore gross mass.
Above-mentioned method, it is preferred that the hydrocarbon is in sucrose, starch, carboxymethyl cellulose, pendant benefit One or several kinds, its addition be sintering fuel, -1mm sinter return fine, Fine Hematite Ore quality sum 0.1%~ 0.3%.
Above-mentioned method, it is preferred that Fine Hematite Ore and the compound basicity of quick lime composition are adjusted by quick lime (CaO and SiO2Mass ratio) be 2.0~2.4.
The present invention passes through sintering fuel and Fine Hematite Ore, particulate sinter return fine, quick lime and with cementation Bead is made in hydrocarbon, its object is to:1. volatile matter nitrogen just starts to discharge initial stage in burning, now sintering fuel periphery Hydrocarbon the groups such as CH, CO, H, OH can be decomposited when ignition temperature is relatively low, these groups not only can be with volatile matter In nitrogen-containing compound response inhabitation NOx generations, additionally it is possible to the NOx that has generated of reduction;2. with the raising of ignition temperature, coke Nitrogen takes place oxidation reaction, and the now sinter return fine of -1mm in bead, due to itself containing the catalysis NOx drops such as calcium ferrite The material of solution, and specific surface area is larger, NOx can be promoted to be reduced to N2, simultaneously as fine-graded sinter return fine is in lower temperature Under can form liquid phase, can promote the reaction between Fine Hematite Ore and quick lime, and due to the control of material basicity 2.0~ Between 2.4, be advantageous to fuel periphery and form more calcium ferrite systems material, so as to further promote NOx deoxidization, degradation.
Compared with prior art, the advantage of the invention is that:
(1) present invention has separately designed discharge-reducing method for the conversion of volatile matter nitrogen and coke nitrogen to NOx, by suppressing to fire Expect N oxidation reaction and promote NOx reduction reaction two methodses, realize the discharge that NOx is controlled in sintering process, for Property is strong, emission reduction effect is good.
(2) present invention by sintering fuel and Fine Hematite Ore, particulate sinter return fine, quick lime and has cementation Hydrocarbon bead is made, given full play to the effect of hydrocarbon, its adhesive property is advantageous to pelletize, while is firing The volatile generation of hydrocarbon is beneficial to suppress the groups such as CH, CO, H, OH of NO generations under the conditions of burning, and self-produced using sintering Sinter return fine contains the characteristic of catalyst calcium ferrite, and effectively facilitates sintering process fast-growing fast at low temperature by reasonable dispensing Into calcium ferrite, combustion process NOx deoxidization, degradation is effectively increased, realizes and NOx emission is controlled in sintering process, without follow-up Fume treatment, and do not change conventional sintering process system, do not increase production cost, Sintering Operation Index will not be reduced.
Embodiment
For the ease of understanding the present invention, present invention work more comprehensively, is meticulously described below in conjunction with preferred embodiment, But protection scope of the present invention is not limited to embodiment in detail below.
Unless otherwise defined, the implication that all technical terms used hereinafter are generally understood that with those skilled in the art It is identical.Technical term used herein is intended merely to describe the purpose of specific embodiment, is not intended to the limitation present invention Protection domain.
Except there is a special instruction, the various reagents used in the present invention, raw material be can be commercially commodity or Person can pass through product made from known method.
Embodiment 1:
It is a kind of of the invention based on the NOx control methods for suppressing the conversion of Ore Sintering Process fuel bound nitrogen, comprise the following steps:
(1) -1mm sinter return fines are sifted out first;
(2) coke powder is weighed, -1mm sinter return fines (the quality of -1mm sinter return fines that step (1) is sifted out is added in coke powder For 1.5 times of coke powder quality);According still further to sintered iron ore gross mass 20% addition hematite concentrates (in hematite concentrates- 0.074mm concentrate mass content accounts for 75%, SiO in hematite concentrates2Content is 4%) to mix;It is red to add quick lime regulation particulate Iron ore is 2.4 with the compound basicity that quick lime is formed;Finally adding sucrose, (addition of sucrose is coke powder, -1mm sintering returns Ore deposit and hematite concentrates quality sum 0.3%), prefabricated grain is carried out after above proportioning materials in trommel mixer, is obtained prefabricated Grain compound;
(3) it is the compound that step (2) obtains and the conventional granulation of remaining iron-bearing material, sinter return fine and flux progress is laggard Row cloth, igniting, sintering.
Test sintering index and NOx abatement amount are as shown in table 1, Sintering Operation Index and benchmark the sintering index phase of this technique Closely, and NOx discharge is from 349mg/Nm3It is reduced to 302mg/Nm3
Embodiment 2:
It is a kind of of the invention based on the NOx control methods for suppressing the conversion of Ore Sintering Process fuel bound nitrogen, comprise the following steps:
(1) -1mm sinter return fines are sifted out first;
(2) coke powder is weighed, -1mm sinter return fines (the quality of -1mm sinter return fines that step (1) is sifted out is added in coke powder For 3.0 times of coke powder quality);According still further to 40% addition hematite ore fines (- 0.5mm in hematite ore fines of sintered iron ore gross mass Fine ore mass content account for 60%, SiO in hematite ore fines2Content is 6.0%) to mix;Add quick lime regulation Fine Hematite Ore It is 2.0 with the compound basicity that quick lime is formed;Finally add starch (addition of starch be coke powder, -1mm sinter return fines and Hematite ore fines quality sum 0.2%), prefabricated grain is carried out after above proportioning materials in trommel mixer, prefabricated grain is obtained and mixes Close material;
(3) it is the compound that step (2) obtains and the conventional granulation of remaining iron-bearing material, sinter return fine and flux progress is laggard Row cloth, igniting, sintering.
Test sintering index and NOx abatement amount are as shown in table 1, Sintering Operation Index and benchmark the sintering index phase of this technique Closely, and NOx discharge is from 349mg/Nm3It is reduced to 281mg/Nm3
Embodiment 3:
It is a kind of of the invention based on the NOx control methods for suppressing the conversion of sintering process fuel bound nitrogen, comprise the following steps:
(1) -1mm sinter return fines are sifted out first;
(2) coke powder is weighed, -1mm sinter return fines (the quality of -1mm sinter return fines that step (1) is sifted out is added in coke powder For 2.5 times of coke powder quality);According still further to 30% addition hematite ore fines (- 0.5mm in hematite ore fines of sintered iron ore gross mass Fine ore mass content account for 55%, SiO in hematite ore fines2Content is 5.0%) to mix;Add quick lime regulation Fine Hematite Ore It is 2.2 with the compound basicity that quick lime is formed;Finally adding pendant benefit, (addition of pendant benefit is coke powder, -1mm sintering returns Ore deposit and hematite ore fines quality sum 0.1%), prefabricated grain is carried out after above proportioning materials in trommel mixer, is obtained prefabricated Grain compound;
(3) it is the compound that step (2) obtains and the conventional granulation of remaining iron-bearing material, sinter return fine and flux progress is laggard Row cloth, igniting, sintering.
Test sintering index and NOx abatement amount are as shown in table 1, Sintering Operation Index and benchmark the sintering index phase of this technique Closely, and NOx discharge is from 349mg/Nm3It is reduced to 292mg/Nm3
Embodiment 4:
It is a kind of of the invention based on the NOx control methods for suppressing the conversion of sintering process fuel bound nitrogen, comprise the following steps:
(1) -1mm sinter return fines are sifted out first;
(2) coke powder is weighed, -1mm sinter return fines (the quality of -1mm sinter return fines that step (1) is sifted out is added in coke powder For 2.2 times of coke powder quality);According still further to sintered iron ore gross mass 25% addition hematite concentrates (in hematite concentrates- 0.074mm concentrate mass content accounts for 90%, SiO in hematite concentrates2Content is 5.2%) to mix;Add quick lime regulation particulate Bloodstone is 2.1 with the compound basicity that quick lime is formed;Finally adding CMC, (CMC addition is coke powder, -1mm sintering returns Ore deposit and hematite concentrates quality sum 0.2%), prefabricated grain is carried out after above proportioning materials in trommel mixer, is obtained prefabricated Grain compound;
(3) it is the compound that step (2) obtains and the conventional granulation of remaining iron-bearing material, sinter return fine and flux progress is laggard Row cloth, igniting, sintering.
Test sintering index and NOx abatement amount are as shown in table 1, Sintering Operation Index and benchmark the sintering index phase of this technique Closely, and NOx discharge is from 349mg/Nm3It is reduced to 299mg/Nm3
1 different embodiments of table sinter index and NOx abatement amount
It is of the invention based on the NOx control methods for suppressing the conversion of sintering process fuel bound nitrogen it was found from above-mentioned analysis, do not changing Become conventional sintering process system, do not increase production cost, on the premise of not reducing Sintering Operation Index, realize NOx emission reduction, Pollutant emission is reduced to steel sintering factory, the environmentally friendly cost of reduction has great importance.

Claims (3)

  1. It is 1. a kind of based on the NOx control methods for suppressing the conversion of Ore Sintering Process fuel bound nitrogen, it is characterised in that first by sinter return fine In come out less than 1mm particle screening, then by -1mm sinter return fine, Fine Hematite Ore, quick lime, sintering fuel and have After the hydrocarbon dispensing of cementation, prefabricated grain is carried out in trommel mixer, gained compound and remaining iron-bearing material, Flux, sinter return fine are pelletized;Then by its cloth, igniting, sintering;Wherein described sintering fuel is coke powder or smokeless Coal;
    During the prefabricated grain, the dosage of -1mm sinter return fines is 1.5~3.0 times of sintering fuel quality;
    SiO in the Fine Hematite Ore2Mass content be 4~6%;The Fine Hematite Ore is that -0.074mm mass contents are big In 70% hematite concentrates, or -0.5mm mass contents are more than 50% hematite ore fines, or both mixture;
    The addition of the Fine Hematite Ore is the 20%~40% of sintering iron ore gross mass;The addition of the hydrocarbon For sintering fuel, -1mm sinter return fine, Fine Hematite Ore quality sum 0.1%~0.3%.
  2. 2. the method as described in claim 1, it is characterised in that the hydrocarbon is selected from sucrose, starch, carboxymethyl cellulose One or several kinds in element, pendant benefit.
  3. 3. the method as described in claim 1, it is characterised in that adjust what Fine Hematite Ore was formed with quick lime by quick lime Compound basicity is 2.0~2.4.
CN201610071111.0A 2016-02-01 2016-02-01 A kind of NOx control methods based on suppression Ore Sintering Process fuel bound nitrogen conversion Active CN105543471B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610071111.0A CN105543471B (en) 2016-02-01 2016-02-01 A kind of NOx control methods based on suppression Ore Sintering Process fuel bound nitrogen conversion

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610071111.0A CN105543471B (en) 2016-02-01 2016-02-01 A kind of NOx control methods based on suppression Ore Sintering Process fuel bound nitrogen conversion

Publications (2)

Publication Number Publication Date
CN105543471A CN105543471A (en) 2016-05-04
CN105543471B true CN105543471B (en) 2017-11-21

Family

ID=55823027

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610071111.0A Active CN105543471B (en) 2016-02-01 2016-02-01 A kind of NOx control methods based on suppression Ore Sintering Process fuel bound nitrogen conversion

Country Status (1)

Country Link
CN (1) CN105543471B (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106521143A (en) * 2016-11-08 2017-03-22 攀钢集团攀枝花钢铁研究院有限公司 Method for reducing NOx emission in sintering process
CN108267023B (en) * 2016-12-30 2020-03-17 中冶长天国际工程有限责任公司 Nitrogen oxide emission control method and device
CN108823401A (en) * 2018-05-28 2018-11-16 安徽工业大学 A kind of method that Ore Sintering Process shunts granulation emission reduction NOX
CN108823402A (en) * 2018-05-28 2018-11-16 安徽工业大学 One kind is for emission reduction NO in sintering processXMethod for mixing
CN109248673B (en) * 2018-09-21 2020-05-22 中南大学 Method for realizing emission reduction of iron ore sintering NOx and dioxin by resource utilization of waste activated carbon
CN109251779B (en) * 2018-09-30 2021-09-17 柳州钢铁股份有限公司 NOx emission reduction method based on modified fuel iron ore sintering process
CN109365490B (en) * 2018-12-07 2020-08-25 中南大学 Method for preparing sintering NOx inhibitor by utilizing metallurgy and municipal solid wastes
CN110607436B (en) * 2019-09-18 2021-01-26 攀钢集团攀枝花钢铁研究院有限公司 Method for improving sinter yield
CN112226613B (en) * 2020-09-17 2022-04-26 马鞍山钢铁股份有限公司 Multi-pollutant collaborative emission reduction method in sintering process

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0437407B1 (en) * 1990-01-11 1995-03-29 Sumitomo Metal Industries, Ltd. Method for sintering fine iron ore using dual ignition system
CN1286314A (en) * 1999-08-31 2001-03-07 中国钢铁股份有限公司 In-line denitration method for sinter process
CN101148695A (en) * 2007-11-13 2008-03-26 中国科学院过程工程研究所 Method for reducing NOx discharge in sintering process by using additive modified coke
CN105087906A (en) * 2015-08-27 2015-11-25 中南大学 Method for reducing NOx emission in iron ore sintering process

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0437407B1 (en) * 1990-01-11 1995-03-29 Sumitomo Metal Industries, Ltd. Method for sintering fine iron ore using dual ignition system
CN1286314A (en) * 1999-08-31 2001-03-07 中国钢铁股份有限公司 In-line denitration method for sinter process
CN101148695A (en) * 2007-11-13 2008-03-26 中国科学院过程工程研究所 Method for reducing NOx discharge in sintering process by using additive modified coke
CN105087906A (en) * 2015-08-27 2015-11-25 中南大学 Method for reducing NOx emission in iron ore sintering process

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
"焦粉改性降低烧结过程NOx排放的模拟";陈彦广等;《钢铁研究学报》;20090531;第21卷(第5期);第8页第2栏,第11页第1栏 *

Also Published As

Publication number Publication date
CN105543471A (en) 2016-05-04

Similar Documents

Publication Publication Date Title
CN105543471B (en) A kind of NOx control methods based on suppression Ore Sintering Process fuel bound nitrogen conversion
CN105087906B (en) A kind of Ore Sintering Process NOXThe method of emission reduction
CN106282542A (en) A kind of collaborative discharge-reducing method of sintering process multiple pollutant
CN109248673A (en) A kind of method that resource utilization discards active carbon realization agglomeration for iron mine NOx and dioxin emission reducing
CN107287414A (en) A kind of raw material for reducing agglomeration for iron mine NOx emission is prepared and sintering method
CN104403697A (en) Flue gas emission pollutant control process device for coal-fired boiler in power plant and control method
CN102936526B (en) Combustion improver for blast furnace coal powder injection and use method thereof
CN104449943A (en) Fire coal combustion-supporting desulfurization powder for flue gas desulfurization and preparation method thereof
CN108823401A (en) A kind of method that Ore Sintering Process shunts granulation emission reduction NOX
CN109487077B (en) Method for reducing emission of NOx in iron ore sintering process based on coking wastewater modified fuel
CN103160358B (en) Denitration coal water slurry
CN102086485B (en) Comprehensive utilization method for vanadium extraction and power generation by using stone coal burned by circulating fluidized bed boiler
CN109181808B (en) Emission reduction method for nitrogen oxides in iron ore sintering process
CN111910073B (en) Method for producing low-dust particle emission granules based on high-proportion micro-fine particle materials
CN206570278U (en) ERD+ fire coal saturated vapor catalysis combustion denitration devices
CN114061321B (en) Pellet flue gas treatment system based on rotary kiln primary circulation air inlet and flue gas treatment process thereof
CN114061320B (en) Grate-rotary kiln-circular cooler pellet smoke circulation coupling treatment system and smoke treatment process thereof
CN109251779B (en) NOx emission reduction method based on modified fuel iron ore sintering process
CN103830997B (en) The apparatus and method that a kind of smoke comprehensive is administered
CN102585968A (en) Nanometer composite coal-economizing agent for power plant boiler
CN113877409A (en) High-temperature flue gas treatment system and method for grate-kiln oxidized pellets
CN104962732A (en) Cooperative emission reduction method and system for SO2 and dioxin produced in sintering
CN110343851B (en) Ore blending method for effectively reducing NOx emission in sintering process
Zhang et al. Sulfur migration behavior in sintering and pelletizing processes: A review
CN109631608B (en) Sintering method for controlling emission concentration of nitrogen oxides in sintering process

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant