CN110484716A - A kind of method and device enhancing heat exchange between air and sinter bed - Google Patents

A kind of method and device enhancing heat exchange between air and sinter bed Download PDF

Info

Publication number
CN110484716A
CN110484716A CN201910881821.3A CN201910881821A CN110484716A CN 110484716 A CN110484716 A CN 110484716A CN 201910881821 A CN201910881821 A CN 201910881821A CN 110484716 A CN110484716 A CN 110484716A
Authority
CN
China
Prior art keywords
sintering
heat exchange
air
sintering feed
steam
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.)
Pending
Application number
CN201910881821.3A
Other languages
Chinese (zh)
Inventor
陈波
肖鹏
冷祥全
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.)
Dazhou Iron and Steel Group Co Ltd
Original Assignee
Dazhou Iron and Steel Group 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 Dazhou Iron and Steel Group Co Ltd filed Critical Dazhou Iron and Steel Group Co Ltd
Priority to CN201910881821.3A priority Critical patent/CN110484716A/en
Publication of CN110484716A publication Critical patent/CN110484716A/en
Pending legal-status Critical Current

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 methods of heat exchange between enhancing air and sinter bed, comprising: the air above control sintering feed is flowed along the direction of motion of sintering feed;Steam is sprayed in the upper surface of sintering feed.Compared with the prior art, since the specific heat ratio air of steam wants high, can improve the air themperature entered in sintering feed, avoid sinter liquid from being cooled air impact and cause crystallographic texture extremely, destruction sinter strength the phenomenon that;In addition, the water in steam encounters the carbon-coating of high-temp combustion, H can be cracked into2And O2, H2For good gaseous fuel, O2It is strong combustion adjuvant for another kind, the completion of follow-up sintering process can be accelerated;And since steam cracking is H2And O2, additional fuel and O can be generated2Sintering process is added, can suitably reduce the fuel consumption of sintering, save material.The invention also discloses a kind of devices for implementing the method for heat exchange between above-mentioned enhancing air and sinter bed.

Description

A kind of method and device enhancing heat exchange between air and sinter bed
Technical field
The present invention relates to sintering technology fields, hand over more specifically to heat between a kind of enhancing air and sinter bed The method changed.Moreover, it relates to a kind of dress for implementing the method for heat exchange between above-mentioned enhancing air and sinter bed It sets.
Background technique
The characteristics of from bed of material heat exchange: air is preheated when by being sintered ore bed by red-hot sinter cake, and will Heat takes burning zone to, and when burning generates higher temperature.It is considered that storage heater of the sintering ore bed just as a heating air, With auto accumulation heat effect.Due to this auto accumulation heat effect be with sintering ore bed thicken with the raising of burning zone temperature and Reinforce, thus burning zone elapses more down, the temperature that the air for participating in burning is preheated is higher, and the physical thermal for bringing this layer is cured More, the temperature levels of burning zone are just higher.
In the prior art, carry out sintering process naturally, the time used is longer, and sintering machine running speed is slow, equipment benefit Declined with rate;In addition, if the heat exchange between air and sinter is inadequate, sinter can be made to be cooled air impact, caused Crystallographic texture is abnormal, destroys sinter strength.
It is current this field in conclusion how to provide a kind of method for enhancing heat exchange between sinter bed and air Technical staff's urgent problem to be solved.
Summary of the invention
In view of this, the object of the present invention is to provide a kind of method of heat exchange between enhancing sinter bed and air, it can To accelerate the progress of sintering reaction, sinter is avoided to be influenced by cold air, improves sintering quality.
It is a further object of the present invention to provide heat exchanges between a kind of enhancing sinter bed and air for implementing the above method Device.
To achieve the goals above, the invention provides the following technical scheme:
A method of heat exchange between enhancing air and sinter bed, comprising:
The air above sintering feed is controlled to flow along the direction of motion of the sintering feed;
Steam is sprayed in the upper surface of the sintering feed.
Preferably, steam is sprayed in the upper surface in the sintering feed, comprising:
The eject position of the steam is the upper surface of the sintering feed within the scope of temperature inflection point, and the temperature turns Point range is the range that the sintering feed rate of rise in temperature is greater than or equal to 150 DEG C/min.
Preferably, the temperature inflection point range is 220 DEG C to 390 DEG C.
A kind of device enhancing heat exchange between air and sinter bed, comprising:
Sintering pallet, for driving sintering feed to move;
Exhausting system, for moving air along the direction of motion of the sintering feed in the upper surface of the sintering feed;
Jet chimney, for spraying steam to the upper surface of the sintering feed;
The exhausting system is set to the top of the sintering pallet.
Preferably, the jet chimney includes main pipeline, at least two branch pipe(tube)s being connected to the main pipeline and sets It is placed in the injection pipe of the branch pipe(tube);
The length direction of the main pipeline is parallel with the direction of motion of the sintering feed, the length direction of the branch pipe(tube) with The width direction of the sintering pallet is parallel, and the injection pipe is down-set perpendicular to the branch pipe(tube).
Preferably, the branch pipe(tube) is arranged along the equal spacing in length direction of the main pipeline.
Preferably, any branch pipe(tube) is provided with the switch for controlling its opening and closing.
Preferably, the injection pipe on the different branch pipe(tube)s is staggered along the width direction of the sintering pallet.
Preferably, further include temperature sensor for measuring the sintering feed material temperature and for controlling the steam pipe The control system that the opening and closing in road, the sintering pallet and the exhausting system act;
The temperature sensor, the jet chimney, the sintering pallet and the exhausting system with the control System connection.
A kind of method of heat exchange between enhancing air and sinter bed provided by the invention, comprising: on control sintering feed The air of side is flowed along the direction of motion of sintering feed;Steam is sprayed in the upper surface of sintering feed.
Compared with the prior art, since the specific heat ratio air of steam wants high, the air themperature entered in sintering feed can be improved, It avoids sinter liquid from being cooled air impact and causes that crystallographic texture is abnormal, destroys the phenomenon that sinter strength;In addition, steam In water encounter the carbon-coating of high-temp combustion, H can be cracked into2And O2, H2Good gaseous fuel, O2It is strong combustion-supporting for another kind Agent can accelerate the completion of follow-up sintering process;And since steam cracking is H2And O2, additional fuel and O can be generated2It is added Sintering process can suitably reduce the fuel consumption of sintering, save material.
The present invention also provides a kind of devices for implementing the method for heat exchange between above-mentioned enhancing air and sinter bed.
Detailed description of the invention
In order to more clearly explain the embodiment of the invention or the technical proposal in the existing technology, to embodiment or will show below There is attached drawing needed in technical description to be briefly described, it should be apparent that, the accompanying drawings in the following description is only this The embodiment of invention for those of ordinary skill in the art without creative efforts, can also basis The attached drawing of offer obtains other attached drawings.
Fig. 1 is the stream of the method specific embodiment one of heat exchange between enhancing air and sinter bed provided by the present invention Journey schematic diagram;
Fig. 2 is the specific embodiment one of the device of heat exchange between enhancing air and sinter bed provided by the present invention Front section view;
Fig. 3 is the side sectional view for enhancing the device of heat exchange between air and sinter bed;
Fig. 4 is the side view for enhancing the device of heat exchange between air and sinter bed.
In Fig. 1-4:
1 it is branch pipe(tube), 2 be sintering pallet, 3 be main pipeline, 4 is injection pipe.
Specific embodiment
Following will be combined with the drawings in the embodiments of the present invention, and technical solution in the embodiment of the present invention carries out clear, complete Site preparation description, it is clear that described embodiments are only a part of the embodiments of the present invention, instead of all the embodiments.It is based on Embodiment in the present invention, it is obtained by those of ordinary skill in the art without making creative efforts every other Embodiment shall fall within the protection scope of the present invention.
Core of the invention is to provide a kind of method for enhancing heat exchange between air and sinter bed, and air can be improved Heat exchange between sinter layer improves the temperature of the air entered in sintering feed, accelerates sintering reaction rate.Of the invention is another One core is to provide a kind of device for implementing the method for heat exchange between above-mentioned enhancing air and sinter bed.
Fig. 1-4 is please referred to, Fig. 1 is that the method for heat exchange between enhancing air and sinter bed provided by the present invention is specific The flow diagram of embodiment one;Fig. 2 is the device of heat exchange between enhancing air and sinter bed provided by the present invention The front section view of specific embodiment one;Fig. 3 is the side sectional view for enhancing the device of heat exchange between air and sinter bed; Fig. 4 is the side view for enhancing the device of heat exchange between air and sinter bed.
A kind of method of heat exchange between the enhancing air and sinter bed that this specific embodiment provides, comprising:
Step S1 controls the air above sintering feed and flows along the direction of motion of sintering feed.
In above-mentioned steps S1, heat exchange has the characteristics that obvious and rule in sinter bed, red-hot more than burning zone Sinter by heat be transmitted to by air, make air preheat, sinter cools off;In burning zone, hot-air be heated to The solid fuel of ignition point acts on, and combustion reaction occurs, and releases a large amount of heat, this layer of temperature is made to reach 1300-1500 DEG C;Burning When being moved downwardly to preliminary heating zone and drying layer heat exchange occurs between sintering feed for the high-temp waste gas of generation, to make to burn at this Ramming material temperature quickly rises to the ignition temperature close to fuel and evaporates the moisture in sintering feed sharply and dry.
Step S2 sprays steam in the upper surface of sintering feed.
Compared with the prior art, due to 1.8 times that the specific heat of steam is dry air specific heat, so can be by sintering feed Layer surface sprays steam to improve the specific heat of air, will form more in this way, the air of equivalent amount enters the bed of material just plus steam Strong heat-exchange capacity, the exhaust gas that sintering process generates contain Boydii reaction and the imperfect combustion CO generated jointly of coke cutting, by In the reinforcing of sintering process, fuel combustion chemical process is more complete, and gas phase vapor composition promotes CO and CO2Reaction, add Fast the atmosphere variation of sintering process, reaction rate avoid sinter liquid from being cooled air impact and cause crystallographic texture different Often, the phenomenon that destroying sinter strength;In addition, the water in steam encounters the carbon-coating of high-temp combustion, H can be cracked into2And O2, H2 Good gaseous fuel, O2It is strong combustion adjuvant for another kind, the completion of follow-up sintering process can be accelerated;And due to steam cracking For H2And O2, additional fuel and O can be generated2Sintering process is added, can suitably reduce the fuel consumption of sintering, saves former Material.
On the basis of the above embodiments, in order to make the steam being added preferably play a role, the injection of steam can be made Position is located at the upper surface of the sintering feed within the scope of temperature inflection point, and temperature inflection point range is the model that sintering feed temperature steeply rises It encloses, can be the range that sintering feed rate of rise in temperature is greater than or equal to 150 DEG C/min, certainly, temperature inflection point range needs root Determine that there may be differences for different sintering processes according to actual conditions.
It needs to be illustrated, if steam directly sprays after sintering feed goes out ignition furnace, due to just going out ignition furnace, burn Junction temperature is lower, and the water in steam enters after sintering feed, the temperature of sintering feed can be made to reduce, or even cause sintering process cannot It is normally carried out;When carrying out steam injection at the middle part of sintering machine, since the water in steam resolves into H2And O2It is raw later that baked is fired again At water electrode easily cause the lower part mixture moisture in sintering feed excessive, formed excessive moistening layer, influence the gas permeability of the bed of material, influence to burn Tie the quality of mine;If the position of injection steam is rearward, sintering process all terminates, cannot play dependent interaction;Therefore it selects It selects and sprays steam in temperature inflection point, specific heat capacity increases after admitting air into sintering feed, and increase the temperature of sintering feed, and this When sintering feed temperature increase speed comparatively fast, not will form excessive moistening layer.
Certainly, since sintering machine crude fuel structure difference, the difference of size, the difference of Process configuration etc. will cause The variation of temperature inflection point range, therefore, in actual production process, the range of temperature inflection point needs determines according to actual conditions, In This is not repeated them here.
Preferably, temperature inflection point range is 220 DEG C to 390 DEG C.
It include above-mentioned reality the present invention also provides one kind in addition to the method for heat exchange between above-mentioned enhancing air and sinter bed The device of the method for heat exchange between the disclosed enhancing air of example and sinter bed is applied, it is hot between the enhancing air and sinter bed The device of exchange includes:
Sintering pallet 2, for driving sintering feed to move;
Exhausting system, for moving air along the direction of motion of sintering feed in the upper surface of sintering feed;
Jet chimney, for spraying steam to the upper surface of sintering feed;
Exhausting system is set to the top of sintering pallet 2.
During use, sintering feed is located on sintering pallet 2, and is driven and moved by sintering pallet 2, sintering feed During movement, exhausting system carries out exhausting, moves air along the direction of motion of sintering feed in the upper surface of sintering feed, steams Steam pipe road is used to spray steam to the upper surface of sintering feed, and temperature when admitting air into sintering feed increases.
On the basis of the above embodiments, can make jet chimney includes that main pipeline 3, at least two is connected to main pipeline 3 Branch pipe(tube) 1 and be set to the injection pipe 4 of branch pipe(tube) 1;
The length direction of main pipeline 3 and the direction of motion of sintering feed are parallel, the length direction and sintering pallet of branch pipe(tube) 1 2 width direction is parallel, and injection pipe 4 is down-set perpendicular to branch pipe(tube) 1.
As shown in Figure 2,3, main pipeline 3 is set to the bottom of sintering pallet 2, and along the direction of motion of sintering pallet 2 Setting, branch pipe(tube) 1 is connected to main pipeline 3, it is preferred that and it can may be that the position of temperature inflection point range is respectively provided with branch pipe(tube) 1, And any branch pipe(tube) 1 has individual switch to be controlled, to be suitable for the different situation of temperature inflection point range.
Injection pipe 4 can be straight down perpendicular to branch pipe(tube) 1, be also possible to obliquely, with specific reference to actual conditions It determines.
Preferably, branch pipe(tube) 1 is arranged along the equal spacing in length direction of main pipeline 3, so that sintering feed uniformly connects with steam Touching.
In order to make each position of sintering feed that can uniformly contact steam, the injection on different branch pipe(tube)s 1 can be made Pipeline 4 is staggered along the width direction of sintering pallet 2.
Preferably, 4 spaced set of injection pipe on same branch pipe(tube) 1.
It is staggered, refers to that injection pipe 4 is located at the position difference of 2 width direction of sintering pallet.
On the basis of the above embodiments, for the accurate control of production efficiency and sintering process, use can also be set Temperature sensor in measurement sintering feed material temperature and opening and closing, sintering pallet 2 and exhausting system for controlling jet chimney The control system of movement;
Temperature sensor, jet chimney, sintering pallet 2 and exhausting system are connect with control system.
During use, it is provided with temperature sensor below each bellows of sintering pallet 2, for detecting The temperature of corresponding sintering feed, and the sintering feed temperature data that will test sends control system to, when temperature is located at temperature When within the scope of inflection point, control system controls the jet chimney injection steam on this position top.
In the actual production process, jet chimney temperature inflection point spray steam after, make sintering machine running speed from 2.2 ± 0.1m/min originally is increased to 2.3 ± 0.1m/min in test, improves usage factor 3-5%.This shows hectic fever Heat transfer between air and sinter bed is strengthened, so that bed permeability is improved well, bed of material air penetrates into Speed raising promotes vertical sintering speed to improve.Implement front and back Parameters variation and index situation is as follows:
The air of sintering process is sucked under high-temperature steam effect, the air themperature into sinter bed is increased, reduces Heat needed for sintering process itself, along with sintering process strengthened usage factor is risen, yield raising, make coke Powder consumption reduces 4%.
Each embodiment in this specification is described in a progressive manner, the highlights of each of the examples are with other The difference of embodiment, the same or similar parts in each embodiment may refer to each other.All realities provided by the present invention Any combination mode of example is applied in the protection scope of the invention, this will not be repeated here.
The method and device of heat exchange between enhancing air provided by the present invention and sinter bed has been carried out in detail above It is thin to introduce.Used herein a specific example illustrates the principle and implementation of the invention, and above embodiments are said It is bright to be merely used to help understand method and its core concept of the invention.It should be pointed out that for the ordinary skill of the art , without departing from the principle of the present invention, can be with several improvements and modifications are made to the present invention for personnel, these improvement It is also fallen within the protection scope of the claims of the present invention with modification.

Claims (9)

1. a kind of method of heat exchange between enhancing air and sinter bed characterized by comprising
The air above sintering feed is controlled to flow along the direction of motion of the sintering feed;
Steam is sprayed in the upper surface of the sintering feed.
2. it is according to claim 1 enhancing air and sinter bed between heat exchange method, which is characterized in that it is described Spray steam in the upper surface of the sintering feed, comprising:
The eject position of the steam is the upper surface of the sintering feed within the scope of temperature inflection point, the temperature inflection point model Enclose the range for being greater than or equal to 150 DEG C/min for the sintering feed rate of rise in temperature.
3. the method for heat exchange between enhancing air according to claim 2 and sinter bed, which is characterized in that the temperature Spending inflection point range is 220 DEG C to 390 DEG C.
4. the device of heat exchange between a kind of enhancing air and sinter bed characterized by comprising
Sintering pallet (2), for driving sintering feed to move;
Exhausting system, for moving air along the direction of motion of the sintering feed in the upper surface of the sintering feed;
Jet chimney, for spraying steam to the upper surface of the sintering feed;
The exhausting system is set to the top of the sintering pallet (2).
5. the device of heat exchange between enhancing air according to claim 4 and sinter bed, which is characterized in that the steaming Steam pipe road includes main pipeline (3), at least two branch pipe(tube)s (1) being connected to the main pipeline (3) and is set to the branch pipe The injection pipe (4) in road (1);
The length direction of the main pipeline (3) is parallel with the direction of motion of the sintering feed, the length direction of the branch pipe(tube) (1) Parallel with the width direction of the sintering pallet (2), the injection pipe (4) is down-set perpendicular to the branch pipe(tube) (1).
6. the device of heat exchange between enhancing air according to claim 5 and sinter bed, which is characterized in that the branch Pipeline (1) is arranged along the equal spacing in length direction of the main pipeline (3).
7. the device of heat exchange between enhancing air according to claim 6 and sinter bed, which is characterized in that Ren Yisuo Branch pipe(tube) (1) is stated to be provided with for controlling its switch being opened and closed.
8. according to the device of heat exchange between the described in any item enhancing air of claim 5-7 and sinter bed, feature exists In the injection pipe (4) on the different branch pipe(tube)s (1) is staggered along the width direction of the sintering pallet (2).
9. the device of heat exchange between enhancing air according to claim 8 and sinter bed, which is characterized in that further include For measuring the temperature sensor of the sintering feed material temperature and the opening and closing for controlling the jet chimney, the sintering board The control system of vehicle (2) and exhausting system movement;
The temperature sensor, the jet chimney, the sintering pallet (2) and the exhausting system are with the control System connection.
CN201910881821.3A 2019-09-18 2019-09-18 A kind of method and device enhancing heat exchange between air and sinter bed Pending CN110484716A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201910881821.3A CN110484716A (en) 2019-09-18 2019-09-18 A kind of method and device enhancing heat exchange between air and sinter bed

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201910881821.3A CN110484716A (en) 2019-09-18 2019-09-18 A kind of method and device enhancing heat exchange between air and sinter bed

Publications (1)

Publication Number Publication Date
CN110484716A true CN110484716A (en) 2019-11-22

Family

ID=68558311

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201910881821.3A Pending CN110484716A (en) 2019-09-18 2019-09-18 A kind of method and device enhancing heat exchange between air and sinter bed

Country Status (1)

Country Link
CN (1) CN110484716A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111455167A (en) * 2020-05-23 2020-07-28 山东泰山钢铁集团有限公司 Sintering method for promoting combustion by water spraying for sintering machine
CN112797796A (en) * 2021-01-06 2021-05-14 中冶长天国际工程有限责任公司 Device for spraying water vapor on sintering material surface and control method thereof
CN113106250A (en) * 2020-01-09 2021-07-13 中南大学 Low-energy-consumption low-emission sintering method for multi-component gas medium composite injection

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101104882A (en) * 2007-07-23 2008-01-16 鞍钢股份有限公司 Preheating method and device for sintering mixture
CN103320605A (en) * 2013-06-25 2013-09-25 攀钢集团攀枝花钢钒有限公司 Sintering method and sintering equipment of iron ore
CN103924065A (en) * 2014-04-25 2014-07-16 四川省达州钢铁集团有限责任公司 Sintering method and sintering device of metal compound powder
CN204574798U (en) * 2015-04-02 2015-08-19 伍宏杰 A kind of updraft type sintering machine
CN106521144A (en) * 2016-11-08 2017-03-22 首钢总公司 Method and system for reducing content of CO and nitric oxide in sintering waste gas
CN106595327A (en) * 2017-01-10 2017-04-26 中钢集团鞍山热能研究院有限公司 Linkage type sintered ore waste heat recovery and comprehensive utilization process and system
CN108458593A (en) * 2018-02-11 2018-08-28 山东钢铁股份有限公司 A kind of continuous pallettype sintering machine bed of material jet humidifier and air-humidification method

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101104882A (en) * 2007-07-23 2008-01-16 鞍钢股份有限公司 Preheating method and device for sintering mixture
CN103320605A (en) * 2013-06-25 2013-09-25 攀钢集团攀枝花钢钒有限公司 Sintering method and sintering equipment of iron ore
CN103924065A (en) * 2014-04-25 2014-07-16 四川省达州钢铁集团有限责任公司 Sintering method and sintering device of metal compound powder
CN204574798U (en) * 2015-04-02 2015-08-19 伍宏杰 A kind of updraft type sintering machine
CN106521144A (en) * 2016-11-08 2017-03-22 首钢总公司 Method and system for reducing content of CO and nitric oxide in sintering waste gas
CN106595327A (en) * 2017-01-10 2017-04-26 中钢集团鞍山热能研究院有限公司 Linkage type sintered ore waste heat recovery and comprehensive utilization process and system
CN108458593A (en) * 2018-02-11 2018-08-28 山东钢铁股份有限公司 A kind of continuous pallettype sintering machine bed of material jet humidifier and air-humidification method

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
姜涛: "《烧结球团生产技术手册》", 30 June 2014, 北京:冶金工业出版社 *
龙红明编: "《冶金过程数学模型与人工智能应用》", 30 June 2010, 北京:冶金工业出版社 *

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113106250A (en) * 2020-01-09 2021-07-13 中南大学 Low-energy-consumption low-emission sintering method for multi-component gas medium composite injection
CN113106250B (en) * 2020-01-09 2022-05-17 中南大学 Low-energy-consumption low-emission sintering method for multi-component gas medium composite injection
CN111455167A (en) * 2020-05-23 2020-07-28 山东泰山钢铁集团有限公司 Sintering method for promoting combustion by water spraying for sintering machine
CN112797796A (en) * 2021-01-06 2021-05-14 中冶长天国际工程有限责任公司 Device for spraying water vapor on sintering material surface and control method thereof

Similar Documents

Publication Publication Date Title
CN110484716A (en) A kind of method and device enhancing heat exchange between air and sinter bed
CN106595327B (en) A kind of coordinated type sinter waste heat recycling comprehensive utilization process and system
KR101685735B1 (en) Method for reducing nitrogen oxides from the exhaust gas of a coke oven
EP0019425B1 (en) Process for baking carbon electrodes
CN102225749B (en) Start-up method of fluidized bed roaster
CN101353579A (en) 7.63m coke oven negative pressure in-furnace furnace drying method
CN203432299U (en) Tunnel kiln for ceramic product
JPS63180340A (en) Method for regenerating molding sand
CN103382520A (en) Manufacturing method of copper rods and copper plate preheating furnace thereof
CN201621952U (en) Tunnel-type fluosolid roaster
CN206973530U (en) A kind of fire air nozzle arrangement form of high-alkali coal face-fired boiler
CN208059594U (en) A kind of petroleum coke calciners that calcination efficiency is high
CN1271022A (en) Homogeneous agglomerate sintering method and equipment
CN209622785U (en) A kind of nozzle
US2563683A (en) Gas burner for soaking pit furnaces and the like
CN103333978B (en) Top-burning hot-blast stove with cone-column composite vault structure
CN204630380U (en) Sintering ignition furnace furnace system
CN204612446U (en) The roasting shaft kiln of integral type bulk material
CN208791706U (en) A kind of aluminium volume annealing furnace
CN215572213U (en) Heat-preservation energy-saving sintering ignition furnace
CN206527143U (en) A kind of pyrolysis furnace
US2367093A (en) Manufacture of insulating products
CN209623352U (en) A kind of fireproofing prefabricated member or precast concrete roasting kiln
CN206695133U (en) Small yield is interrupted type of production natural gas cupola
CN206721248U (en) Combustion furnace

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20191122