CN209541411U - A kind of Two-cuff Technique roller hearth type heating furnace - Google Patents

A kind of Two-cuff Technique roller hearth type heating furnace Download PDF

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Publication number
CN209541411U
CN209541411U CN201822146050.7U CN201822146050U CN209541411U CN 209541411 U CN209541411 U CN 209541411U CN 201822146050 U CN201822146050 U CN 201822146050U CN 209541411 U CN209541411 U CN 209541411U
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China
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air
gas
storage tank
heat storage
heat
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Withdrawn - After Issue
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CN201822146050.7U
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Chinese (zh)
Inventor
丁国伟
王禹尧
杨森
刘洪�
马中杰
栗建辉
刘曙光
胥强
白阳
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Tangshan Iron and Steel Group Co Ltd
HBIS Co Ltd Tangshan Branch
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Tangshan Iron and Steel Group Co Ltd
HBIS Co Ltd Tangshan Branch
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Priority to CN201822146050.7U priority Critical patent/CN209541411U/en
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Publication of CN209541411U publication Critical patent/CN209541411U/en
Withdrawn - After Issue legal-status Critical Current
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Abstract

The utility model relates to a kind of Two-cuff Technique roller hearth type heating furnaces, belong to metallurgy industry heater for rolling steel technical field.Technical solution is: the side A and the side B of roller bottom furnace body (1) are respectively equipped with multiple heat-accumulating burners being evenly arranged, the heat-accumulating burner includes an air heat storage tank (17) and a coal gas heat storage tank (11), one burner partition (14) is set between air heat storage tank (17) and coal gas heat storage tank (11), in one end of air heat storage tank (17) and coal gas heat storage tank (11), burner block (21) are set, burner turns to be equipped with premix chamber in (21), coal gas ignition spout (12) and air ignition spout (15) and gas-fired spout (13) and air burning spout (16) are respectively set in the premix chamber of burner block (21);The beneficial effects of the utility model are: can waste heat in whole recovered flue gas, the exhaust temperature of final flue gas is at 150 DEG C hereinafter, improving the thermal efficiency of heating furnace.

Description

A kind of Two-cuff Technique roller hearth type heating furnace
Technical field
The utility model relates to a kind of Two-cuff Technique roller hearth type heating furnaces, belong to metallurgy industry heater for rolling steel technical field.
Background technique
Thin slab continuous casting and rolling production technology is a kind of short route broad hot strip production technology, has been widely used in heat Rolling strip production field, equipment composition includes thin-slab caster, roller hearth type heating furnace and thick, finishing mill, coiling machine etc., Between continuous casting and milling train, main function is heating slab and is mill roll, processing accident etc. middle roller hearth type heating furnace Certain buffer time is provided when abnormal conditions.Therefore, the structure and production technology of this roller bottom furnace are different from normal reheating furnace: Roller bottom furnace length is about 200-300 meters, and 2 meters of inner width or so, fire box temperature is controlled at 1170~1250 DEG C, and continuous casting billet is poured from continuous casting After the completion of note, just immediately enters and heated in the furnace of roller bottom, and according to the condition of production of milling train, it at any time can be by the slab after heating It is sent to mill milling, residence time of the slab in the furnace of roller bottom and continuous casting and the production kind of milling train, rhythm of production are closely related, Generally between 10~50 minutes, to adapt to the production of continuous casting with milling train difference rhythm, qualified board briquette and enough slow Rush one of the necessary condition that the time is sheet billet continuous casting and rolling production line steady production.
In sheet billet production technology, the length of slab is generally at 25~35 meters, but in half production without a head, slab length It can reach 220 meters or more.For the stabilization for stablizing milling train production and finished strip performance, when carrying out Rolling production, steel rolling process It is required that entering the slab temperature difference≤10 DEG C of mill milling, in the same temperature controlled section, furnace each section of temperature difference in roller bottom also requires to control Within 10 DEG C, based on the special technique requirement of such roller bottom furnace, it is exactly to protect other than bringing-up section that roller bottom furnace, which does not set preheating section, Temperature section, the high-temperature flue gas for generation of burning are directly discharged to flue after diluting air cooling, although passing through preheated air and coal Gas can recycle the heat of part of smoke, but the thermal efficiency of roller bottom furnace is also only 15~20%, be far below normal reheating furnace 50% thermal efficiency.
Patent 201010110775.6 describes a kind of regenerative combustion technology of roller bottom furnace, which adopts on the furnace of roller bottom With the regenerative combustion technology of air single regenerative, common burner is substituted with heat-accumulating burner, part high-temperature flue gas is recycled It utilizes, meets requirement of the steel rolling process to board briquette harshness, while can also solve that existing roller bottom furnace efficiency of combustion is low to ask Topic, smog discharge temperature are lower than 150 DEG C, and energy-saving effect is significant.But the patent only to air carry out accumulation of heat, coal gas not accumulation of heat, It burns in the high-temperature flue gas generated, still some flue gas can directly drain, and the sensible heat in flue gas is not returned adequately It receives and utilizes, in addition fuel still uses the mixed gas of high heating value, for the enterprise of coke-stove gas resource anxiety, the technology Using having difficulties.
Currently, heater for rolling steel generallys use regenerative combustion technology in smelter, which can be used metallurgical enterprise The blast furnace gas or coal gas of converter of the low heat value of industry recycling do fuel, to reduce production cost, which is produced using burning Raw high-temp waste gas directly heats heat storage, then reheats air with heat storage or coal gas, which can be by air or coals Gas is directly preheated to 1000 DEG C, and the exhaust gas temperature of flue gas be then reduced to 150 DEG C hereinafter, to improve the thermal efficiency of heating furnace, Usual heat storage type combustion is carried out between the heat-accumulating burner or two groups of heat-accumulating burners of two same performances, is burnt when one Mouth burn when, another burner is then discharged fume, two ways alternately, since the regenerator temperature of air or coal gas is attained by 1000 DEG C, to reduce the security risk in use, in heat-accumulation combustion, all use outer mixed combustion system, i.e. air and coal gas point Accumulation of heat is not carried out by different heat storage tanks, is then sprayed into heating furnace by respective air and coal gas spray orifice, in heating furnace It is inside mixed, and completes combustion process, since the mixing of coal gas and air is a physical diffusion phenomenon, when needing certain Between could complete, this process is more many slowly than combustion reaction process, and therefore, heat storage type combustion speed is slow, and the length of flame is partially long, right For less than 2 meters roller bottom furnaces of inner width, common heat storage type combustion mode can be such that flame is directly sprayed on the burner of smoke evacuation, not The coal gas of completely burned can be directly entered in the heat storage tank of the heat-accumulating burner of smoke evacuation, influence the normal accumulation of heat of heat-accumulating burner Journey causes gas utilization rate to decline, or even safety accident occurs.
Heat accumulating type roller bottom furnace transmits steel billet using furnace roller, and furnace roller needs to regularly replace maintenance, and roll change tool is C-shaped hook, mesh Preceding existing heat-accumulating burner is bulky, and other than burner body, three-way diverter valve, there are also air, coal gas, empty cigarette and coal smokes A variety of medium pipelines such as pipeline will affect replacing furnace roller if directly arranging a large amount of heat-accumulating burner in roller bottom furnace two sides.
Utility model content
The utility model aim is to provide a kind of Two-cuff Technique roller hearth type heating furnace, can waste heat in whole recovered flue gas, The thermal efficiency of heating furnace is improved, and is meeting the maintenance that will not influence roller bottom furnace while slab heating temperature requirement, is solved The problem of background technique.
The technical solution of the utility model is:
A kind of Two-cuff Technique roller hearth type heating furnace includes roller bottom furnace body, air pipeline, air three-way valve, empty pipe, coal Feed channel, empty cigarette air-introduced machine, air-blaster, coal gas heat storage tank, coal gas ignition spout, gas-fired spout, burner partition, sky Gas igniting spout, air burning spout, air heat storage tank, gas three-way valve, soot pipe, coal smoke air-introduced machine and burner block, roller Bottom furnace body includes bringing-up section and soaking zone, and the side of roller bottom furnace body is the side A, and the other side of roller bottom furnace body is the side B, roller bottom The side A and the side B of furnace body are respectively equipped with multiple heat-accumulating burners being evenly arranged, the heat-accumulating burner and B of the roller bottom side furnace body A The heat-accumulating burner interlaced arrangement of side;The heat-accumulating burner includes an air heat storage tank and a coal gas heat storage tank, in sky One burner partition is set between gas heat storage tank and coal gas heat storage tank, is arranged in one end of air heat storage tank and coal gas heat storage tank and burns Mouth brick, the burner block are arranged in furnace wall, and premix chamber is equipped in burner block, coal gas point is respectively set in the premix chamber of burner block Fire-fighting mouth and air ignition spout and gas-fired spout and air burning spout;The air heat storage tank passes through air threeway Valve is connect with air pipeline and air-blaster and empty pipe and empty cigarette air-introduced machine respectively, air pipeline, air three-way valve, Empty pipe, empty cigarette air-introduced machine, air-blaster and air heat storage tank form air hold over system;The coal gas heat storage tank passes through Gas three-way valve is connect with gas piping and soot pipe and coal smoke air-introduced machine respectively, gas piping, gas three-way valve, coal smoke Pipeline, coal smoke air-introduced machine and coal gas heat storage tank form coal gas hold over system.
The gas three-way valve in air three-way valve and coal gas hold over system in the air hold over system is divided into control roller The air three-way valve and gas three-way valve and the control side roller bottom furnace body B heat-accumulating burner of the bottom side furnace body A heat-accumulating burner Air three-way valve and gas three-way valve, control the side roller bottom furnace body A heat-accumulating burner air three-way valve and gas three-way valve And the air three-way valve and gas three-way valve of the control side roller bottom furnace body B heat-accumulating burner are arranged in the B of roller bottom furnace body Side.
The side A of roller bottom furnace body is changing side, and the side B of roller bottom furnace body is non-changing side.
Air three-way valve in the air hold over system is identical with the structure of the gas three-way valve in coal gas hold over system, Air or gas inlet valve plate and flue gas valve plate are respectively equipped in air three-way valve and gas three-way valve.
Premix chamber in the burner block is taper, and the opening angle of taper is γ.
Between the center line of coal gas ignition spout in the premix chamber of the burner block and the center line of air ignition spout Arranged crosswise, the angle between the center line of coal gas ignition spout and the center line of air ignition spout is α;Gas-fired spout Center line and air burning spout center line between arranged crosswise, the center line and air burning spout of gas-fired spout Center line between angle be β.
The heat-accumulating burner of the roller bottom side furnace body A and the side B is divided into two groups, every group of three heat-accumulating burners, and one group It is arranged in bringing-up section, another group is arranged in soaking zone.
Burner partition between the air heat storage tank and coal gas heat storage tank is made of heat-resisting steel sheet and plate S304, steel plate two sides point Other pouring fireproof material.
Fuel in the utility model uses the blast furnace gas or coal gas of converter of low heat value, and bringing-up section mainly completes slab Heating, fire box temperature is usually between 1200~1250 DEG C, and soaking zone is then that board briquette is remained to certain temperature, Fire box temperature is between 1160~1180 DEG C.Bringing-up section and soaking zone all use Two-cuff Technique combustion system.Pass through heat storage type point Not by the temperature accumulation of heat of coal gas and air to 1000 DEG C or so, and after-combustion is mixed in burner block, heat-accumulating burner when burning Accumulation of heat, smoke evacuation alternately, finally realize heating of the roller bottom furnace to steel billet.
The beneficial effects of the utility model are: fuel uses the blast furnace gas or coal gas of converter of low heat value, combustion system is Air and coal gas Two-cuff Technique, can waste heat in whole recovered flue gas, the exhaust temperature of final flue gas is at 150 DEG C hereinafter, improving The thermal efficiency of heating furnace.And the heating efficiency of roller bottom furnace and the heating quality of slab can be guaranteed, and will not influence existing There is the maintenance etc. of roller bottom furnace.
Detailed description of the invention
Fig. 1 is the utility model structure top view;
Fig. 2 is the utility model cross-section diagram;
Fig. 3 is Two-cuff Technique nozzle structure schematic diagram;
Fig. 4 is triple valve structural schematic diagram;
Fig. 5 is triple valve F-F sectional view;
In figure: roller bottom furnace body 1, roll change C-shaped hook 2, furnace roller 3, slab 4, air pipeline 5, air three-way valve 6, empty smoke pipe Road 7, gas piping 8, empty cigarette air-introduced machine 9, air-blaster 10, coal gas heat storage tank 11, coal gas ignition spout 12, gas-fired spray Mouth 13, burner partition 14, air ignition spout 15, air burning spout 16, air heat storage tank 17, gas three-way valve 18, coal smoke Pipeline 19, coal smoke air-introduced machine 20, burner block 21, air or gas inlet valve plate 22, flue gas valve plate 23.
Specific embodiment
Below in conjunction with attached drawing, by example, the utility model is described in further detail.
Referring to attached drawing 1 ~ 5, a kind of Two-cuff Technique roller hearth type heating furnace includes roller bottom furnace body 1, air pipeline 5, air threeway Valve 6, empty pipe 7, gas piping 8, empty cigarette air-introduced machine 9, air-blaster 10, coal gas heat storage tank 11, coal gas ignition spout 12, Gas-fired spout 13, burner partition 14, air ignition spout 15, air burning spout 16, air heat storage tank 17, gas three-way Valve 18, soot pipe 19, coal smoke air-introduced machine 20 and burner block 21, roller bottom furnace body 1 include bringing-up section and soaking zone, roller bottom furnace furnace The side of body 1 is the side A, and the other side of roller bottom furnace body 1 is the side B, and the side A and the side B of roller bottom furnace body 1 are respectively equipped with multiple uniform The heat-accumulating burner of arrangement, the heat-accumulating burner of the roller bottom side furnace body 1A and the heat-accumulating burner interlaced arrangement of the side B;The accumulation of heat Formula burner includes an air heat storage tank 17 and a coal gas heat storage tank 11, between air heat storage tank 17 and coal gas heat storage tank 11 One burner partition 14 is set, burner block 21, the burner block are set in one end of air heat storage tank 17 and coal gas heat storage tank 11 21 are arranged in furnace wall, and premix chamber is equipped in burner block 21, coal gas ignition spout 12 is respectively set in the premix chamber of burner block 21 With air ignition spout 15 and gas-fired spout 13 and air burning spout 16;The air heat storage tank 17 passes through air three Port valve 6 is connect with air pipeline 5 and air-blaster 10 and empty pipe 7 and empty cigarette air-introduced machine 9 respectively, air pipeline 5, sky Gas triple valve 6, empty pipe 7, empty cigarette air-introduced machine 9, air-blaster 10 and air heat storage tank 17 form air hold over system;Institute It states coal gas heat storage tank 11 and is connected respectively with gas piping 8 and soot pipe 19 and coal smoke air-introduced machine 20 by gas three-way valve 18 It connects, gas piping 8, gas three-way valve 18, soot pipe 19, coal smoke air-introduced machine 20 and coal gas heat storage tank 11 form coal gas accumulation of heat system System.
In the present embodiment, referring to attached drawing 1, roller bottom furnace includes bringing-up section C and soaking zone D, and the side A of roller bottom furnace body 1 is Changing side, the side B are non-changing side, and the heat-accumulating burner of the roller bottom side furnace body 1A and the side B is divided into two groups, every group of three heat accumulating types Burner, one group is arranged in bringing-up section, and another group is arranged in soaking zone.The ability of the heat-accumulating burner of bringing-up section C and soaking zone D is not Together, the power of bringing-up section C and the single heat-accumulating burner of soaking zone D is respectively 442KW and 151KW, and fuel uses 5024KJ/Nm3 Coal gas of converter, the coal gas and air mass flow, coal gas and air heat storage that can calculate bringing-up section and soaking zone burner accordingly uses Amount, and the critical technical parameters such as volume for designing coal gas heat storage tank 11 and air heat storage tank 17 accordingly.
Roller bottom furnace is made of roller bottom furnace body 1, furnace roller 3 and air hold over system and coal gas hold over system, and slab 4 is in roller Run on the furnace roller 3 of bottom furnace, bringing-up section mainly completes the heating of slab, fire box temperature usually between 1200~1250 DEG C, and Soaking zone is then that board briquette is remained to certain temperature, and fire box temperature is between 1160~1180 DEG C.
Referring to attached drawing 1,2, air-blaster 10, air pipeline 5, air three-way valve 6, empty pipe 7, air heat storage tank 17 With the equal composition air hold over system of empty cigarette air-introduced machine 9, gas piping 8, gas three-way valve 18, soot pipe 19, coal smoke air-introduced machine 20 and coal gas heat storage tank 11 form coal gas hold over system.
Referring to attached drawing 3, heat-accumulating burner includes 11 groups of an air regenerative burner case 17 and coal gas heat-accumulating burner case, One partition 14 is set between air heat storage tank 17 and coal gas heat storage tank 11, and partition 14 is made of heat resisting steel S304, steel plate two sides Pouring fireproof material respectively prevents air and coal gas in heat storage tank internal short-circuit, it is existing that burning occurs for separating two heat storage tanks As.
In the front end of air heat storage tank 17 and coal gas heat storage tank 11, burner block 21 is set, burner block 21 is arranged in furnace wall, And air heat storage tank 17 and coal gas heat storage tank 11 are designed to external pulling type, are arranged into outside furnace wall, and premix chamber is set in burner block 21, premix Chamber is cone, and opening angle γ is related with calorific value of gas, and the more low then opening angle γ of calorific value is smaller;The premix of burner block 21 It is intracavitary that coal gas ignition spout 12 and air ignition spout 15 and gas-fired spout 13 and air burning spout 16 is respectively set, Arranged crosswise between the center line of coal gas ignition spout 12 in premix chamber and the center line of air ignition spout 15, angle are α;Arranged crosswise between the center line of gas-fired spout 13 and the center line of air burning spout 16, angle β.Work as coal gas When being sprayed respectively from coal gas ignition spout 12 and air ignition spout 15 with air, with angle of cut α in the premix chamber of burner block 21 Mixing, and starts to burn, in this, as incendiary source, by the coal gas sprayed in gas-fired spout 13 and air burning spout 16 and Air is lighted, and the coal gas and the air angle of cut sprayed from gas-fired spout 13 and air burning spout 16 is β, reasonable by designing β angle control the length of flame, prevent flame from directly washing away opposite furnace wall or be directly sprayed onto the burner that opposite is being discharged fume The inside, the principle that β is set up at angle are to guarantee that combustion air and coal gas are mixed and burned at furnace wide 1/2.
Air and coal gas are fired from coal gas ignition spout 12 and air ignition spout 15 and gas-fired spout 13 and air 16 high speed ejection of spout is burnt, spouting velocity reaches 15~20m/s, for the 2 times or more of conventional burner spouting velocity, it is therefore an objective to right Air and coal gas strengthen mixing, guarantee combustion efficiency, while can be realized flame flow under high-velocity combustion to the volume of combustion product It inhales, plays the role of dilute combustion region oxygen concentration, reduces NOx in combustion product.
Heat storage type combustion is that air or coal gas are carried out accumulation of heat, is carried out between two groups of pairs of heat-accumulating burners, when the side A When heat-accumulating burner burns, then the side B heat-accumulating burner is discharged fume accumulation of heat, after a cycle (40~50 seconds), two sides heat-accumulating burner State exchange, the side A heat-accumulating burner smoke evacuation, and the side B heat-accumulating burner burn.
The regenerative burner burning state of 1 side roll change A of roller bottom furnace body and the side non-roll change B is by air three-way valve 6 and coal gas Triple valve 18 controls respectively.Air three-way valve 6 and gas three-way valve 18 are divided into a, b two parts, are arranged in the side non-roll change B, and three Port valve a controls the accumulation of heat and combustion process of the side roll change A heat-accumulating burner, and triple valve b then controls the side non-roll change B heat-accumulating burner Accumulation of heat and combustion process.
Referring to attached drawing 4,5, air three-way valve 6 is identical with the structure of gas three-way valve 18, arrow P and arrow Y difference in figure The airintake direction of air or coal gas and the emission direction of flue gas or exhaust gas are represented, is respectively equipped with air or gas inlet in triple valve Valve plate 22 and flue gas valve plate 23.
Combustion process is as follows: when the side roll change A is in combustion state, triple valve a(includes air three-way valve and gas three-way Valve) air or gas inlet valve plate 22 open, smoke evacuation valve plate 23 is closed, and air and coal gas enter burning in the furnace of roller bottom, rather than The side roll change B is then in smoke evacuation state, and triple valve b(includes air three-way valve and gas three-way valve) air or gas inlet valve plate 22 close, and smoke evacuation valve plate 23 is opened.The burning of next cycle two sides heat-accumulating burner and heat storage state exchange, the side roll change A row Cigarette triple valve a(includes air three-way valve and gas three-way valve) air or gas inlet valve plate 22 close, smoke evacuation valve plate 23 beat It opens, burning waste gas enters accumulation of heat in burner, rather than the side roll change B then starts to burn, and triple valve b(includes air three-way valve and coal gas Triple valve) air or gas inlet valve plate 22 open, smoke evacuation valve plate 23 close.The opening and closing of two sides heat-accumulating burner is synchronous to be carried out, Combustion process is all controlled by computer.
Referring to attached drawing 1,2, heat-accumulating burner and necessary air pipeline 5 and gas piping 8 are only arranged in the side roll change A, and The triple valve of the control side roll change A heat-accumulating burner is arranged into the side non-roll change B, merges with the triple valve of the side non-roll change B, this When sample carries out sending 3 operation of furnace roller using roll change C-shaped hook 2, it is only necessary to avoid coal gas heat storage tank 11 or air heat storage tank 17, and The side non-roll change B in addition to arrangement air regenerative burner 17 and gas regenerative burner 11, air pipeline 5 and gas piping 8 other than, Air three-way valve 6 and gas three-way valve 18 are also arranged, but this arrangement will not influence the roller replacing operation of roller bottom furnace.
The double heat storage type roller hearth furnace does fuel with the blast furnace gas or coal gas of converter of low heat value, meets steel rolling process It is required that reducing the energy consumption of roller bottom furnace, and reduce the NOx in combustion product.

Claims (8)

1. a kind of Two-cuff Technique roller hearth type heating furnace, it is characterised in that: include roller bottom furnace body (1), air pipeline (5), air three Port valve (6), empty pipe (7), gas piping (8), empty cigarette air-introduced machine (9), air-blaster (10), coal gas heat storage tank (11), Coal gas ignition spout (12), gas-fired spout (13), burner partition (14), air ignition spout (15), air burning spout (16), air heat storage tank (17), gas three-way valve (18), soot pipe (19), coal smoke air-introduced machine (20) and burner block (21), roller Bottom furnace body (1) includes bringing-up section and soaking zone, and the side of roller bottom furnace body (1) is the side A, the other side of roller bottom furnace body (1) For the side B, the side A and the side B of roller bottom furnace body (1) are respectively equipped with multiple heat-accumulating burners being evenly arranged, roller bottom furnace body (1) A The heat-accumulating burner of side and the heat-accumulating burner interlaced arrangement of the side B;The heat-accumulating burner includes an air heat storage tank (17) With a coal gas heat storage tank (11), a burner partition is set between air heat storage tank (17) and coal gas heat storage tank (11) (14), burner block (21) are set in one end of air heat storage tank (17) and coal gas heat storage tank (11), burner block (21) arrangement In furnace wall, it is equipped with premix chamber in burner block (21), coal gas ignition spout (12) are respectively set in the premix chamber of burner block (21) With air ignition spout (15) and gas-fired spout (13) and air burning spout (16);The air heat storage tank (17) is logical Cross air three-way valve (6) respectively with air pipeline (5) and air-blaster (10) and empty pipe (7) and empty cigarette air-introduced machine (9) connect, air pipeline (5), air three-way valve (6), empty pipe (7), empty cigarette air-introduced machine (9), air-blaster (10) and Air heat storage tank (17) forms air hold over system;The coal gas heat storage tank (11) by gas three-way valve (18) respectively with coal gas Pipeline (8) and soot pipe (19) and coal smoke air-introduced machine (20) connection, gas piping (8), gas three-way valve (18), coal smoke pipe Road (19), coal smoke air-introduced machine (20) and coal gas heat storage tank (11) form coal gas hold over system.
2. a kind of Two-cuff Technique roller hearth type heating furnace according to claim 1, it is characterised in that: in the air hold over system Air three-way valve (6) and coal gas hold over system in gas three-way valve (18) include control roller bottom furnace body (1) side A heat accumulating type The air three-way valve and gas three-way valve of burner and control roller bottom furnace body (1) side B heat-accumulating burner air three-way valve and Gas three-way valve, the air three-way valve and gas three-way valve of control roller bottom furnace body (1) side A heat-accumulating burner and control roller bottom The air three-way valve and gas three-way valve of furnace body (1) side B heat-accumulating burner are arranged in the side B of roller bottom furnace body (1).
3. a kind of Two-cuff Technique roller hearth type heating furnace according to claim 1 or 2, it is characterised in that: roller bottom furnace body (1) the side A is changing side, and the side B of roller bottom furnace body (1) is non-changing side.
4. a kind of Two-cuff Technique roller hearth type heating furnace according to claim 1 or 2, it is characterised in that: air accumulation of heat system Air three-way valve (6) in system is identical with the structure of gas three-way valve (18) in coal gas hold over system, air three-way valve (6) and Air or gas inlet valve plate (22) and flue gas valve plate (23) are respectively equipped in gas three-way valve (18).
5. a kind of Two-cuff Technique roller hearth type heating furnace according to claim 1, it is characterised in that: in the burner block (21) Premix chamber is taper, and the opening angle of taper is γ.
6. a kind of Two-cuff Technique roller hearth type heating furnace according to claim 1 or 5, it is characterised in that: described, burner block (21) Premix chamber in the center line of coal gas ignition spout (12) and the center line of air ignition spout (15) between arranged crosswise, coal The angle that gas is lighted a fire between the center line of spout (12) and the center line of air ignition spout (15) is α;Gas-fired spout (13) arranged crosswise between the center line of center line and air burning spout (16), the center line of gas-fired spout (13) and Angle between the center line of air burning spout (16) is β.
7. a kind of Two-cuff Technique roller hearth type heating furnace according to claim 1, it is characterised in that: the roller bottom furnace body (1) A The heat-accumulating burner of side and the side B is divided into two groups, and every group of three heat-accumulating burners, one group is arranged in bringing-up section, another group of arrangement In soaking zone.
8. a kind of Two-cuff Technique roller hearth type heating furnace according to claim 1, it is characterised in that: the air heat storage tank (17) Burner partition (14) between coal gas heat storage tank (11) is made of heat-resisting steel sheet and plate S304, and steel plate two sides are poured fire proofed wood respectively Material.
CN201822146050.7U 2018-12-20 2018-12-20 A kind of Two-cuff Technique roller hearth type heating furnace Withdrawn - After Issue CN209541411U (en)

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Application Number Priority Date Filing Date Title
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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109631574A (en) * 2018-12-20 2019-04-16 唐山钢铁集团有限责任公司 A kind of Two-cuff Technique roller hearth type heating furnace

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109631574A (en) * 2018-12-20 2019-04-16 唐山钢铁集团有限责任公司 A kind of Two-cuff Technique roller hearth type heating furnace
CN109631574B (en) * 2018-12-20 2024-01-16 唐山钢铁集团有限责任公司 Double heat accumulating roller bottom type heating furnace

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