CN207175997U - A kind of horizontal continuity charging preheating device - Google Patents
A kind of horizontal continuity charging preheating device Download PDFInfo
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- CN207175997U CN207175997U CN201721224728.8U CN201721224728U CN207175997U CN 207175997 U CN207175997 U CN 207175997U CN 201721224728 U CN201721224728 U CN 201721224728U CN 207175997 U CN207175997 U CN 207175997U
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- preheating
- dust removal
- flue gas
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- horizontal continuity
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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Abstract
The utility model belongs to metallurgical technology field, disclose a kind of horizontal continuity charging preheating device, scheme is included in two dust removal ports of front and rear setting on horizontal continuity charging preheating duct, and horizontal continuity charging preheating duct is divided into strengthening preheating area and smoke pre-heating area by two dust removal ports of front and rear setting；Strengthening preheating area is equipped with burner, and two dust removal ports connect distributor with flue gas tune by flue respectively and coupled；The dedusting negative pressure of the dust removal port of Jetstream fluid kinetic pressure balancing second of multiple rows of burner in strengthening preheating area；Pass through pressure sensor, the tiny structure requirement of the first dust removal port is controlled, so as to reduce the mixed volume of the first dust removal port cold air, by controlling mixed flue gas flow and mixed flue gas temperature, the pre- thermal efficiency of burner and electric arc kiln gas to steel scrap is improved, and make it that production is more environmentally friendly.
Description
Technical field
The utility model belongs to metallurgical technology field, and in particular to a kind of horizontal continuity charging preheating device.
Background technology
Energy-saving in electric-arc furnace steelmaking, environmentally friendly, automation is one of core of EAF steelmaking technology development all the time.
Scrap steel preheating type electric arc furnaces is a kind of energy-saving electric arc furnaces, the electric arc furnaces steel scrap cigarette risen from the end of the eighties in last century
Gas preheating technology is typical power-saving technology, representative art such as CONSTEEL (US5400358).CONSTEEL technologies experience is near
The development of 30 years, more ripe, its flat molten bath, which smelts, reduces power network impact, has the advantages of reducing electric furnace ontology maintenance,
And there is certain energy-saving effect in actual production.But CONSTEEL is not so good as shaft furnace also showing power savings using process
The shortcomings of.With the decline of the bottom such as U.S.'s shale gas revolution, petroleum gas carbon geochemistry energy price, introduced on CONSTEEL outer
Portion's chemical energy becomes an economic method.By adding chemical energy on the conveyor belt, so as to improve the useless of existing CONSTEEL
The pre- thermal efficiency of steel, similar thinking CONSTEEL improve the patent applications such as CN103003453B, CN104583700A body
It is existing.Nozzle or burner are housed on traditional CONSTEEL flues, also embodied on US5400358, but traditional CONSTEEL
Because preheating duct is also simultaneously total exhaust gases passes, the area of passage is big, and height is high so that burner combustion gas and the heat friendship of steel scrap
Change insufficient, the thermal efficiency is not high.
The content of the invention
In view of this, the purpose of this utility model is to provide a kind of horizontal continuity charging preheating device, traditional
Chemical energy is added on the basis of CONSTEEL, is moved towards by shunting flue gas flow and optimization flue gas, reduces cold air mixed volume, so as to
Obtain the higher chemical energy thermal efficiency.
To reach above-mentioned purpose, the utility model provides following technical scheme：A kind of horizontal continuity charging preheating device, bag
Horizontal continuity charging preheating duct and electric arc furnaces are included, is set on the horizontal continuity charging preheating duct along material conveying direction interval
After thering is the first dust removal port and the second dust removal port, first dust removal port to be located at the feeding seal mouth of horizontal continuity charging preheating duct
Side and close feeding seal mouth, second dust removal port are located at the back segment of horizontal continuity charging preheating duct and entered close to electric arc furnaces
Material mouth, the horizontal continuity charging preheating duct between two dust removal ports form the first preheating zone, the second dust removal port and electric arc furnaces feeding mouth
Between horizontal continuity charging preheating duct formed the second preheating zone；Also horizontal continuity charging is inclined at including several intervals
Preheat the burner I at the first preheating zone of duct, horizontal component and the material conveying direction phase of the combustion-gas flow of each burner I
Instead.
Further, the duct of the first preheating zone is highly less than the second preheating zone in the horizontal continuity charging preheating duct
Duct height.
Further, interval is provided tiltedly with several burners at the second preheating zone of the horizontal continuity charging preheating duct
II, the horizontal component of the combustion-gas flow of each burner II is opposite with material conveying direction.
Further, mixed flue gas pipeline is connected with first dust removal port, hot cigarette is connected with second dust removal port
Feed channel；The mixed flue gas pipeline and heat smoke pipeline are connected with expansion chamber.
Further, the mixed flue gas pipeline and heat smoke pipeline adjust distributor and flue and expansion chamber phase by flue gas
Even.
Further, it is equipped with regulating valve on the mixed flue gas pipeline and heat smoke pipeline；The mixed flue gas pipeline and
Heat smoke pipeline is connected by flue with expansion chamber.
Further, in addition to expansion chamber the rapid cooling device for fume being connected.
Further, in addition to steel scrap charging magnetic disc suspending, steel scrap charging magnetic disc suspending or by vibrating charging device by thing
Material is delivered at the material feeding section of horizontal continuity charging preheating duct.
A kind of strengthening preheating method based on above-mentioned horizontal continuity charging preheating device, including herein below：From electric arc furnaces
Total flue gas of middle discharge preheats to the material of the second preheating zone；Spaced first dust removal port will be total with the second dust removal port
Flue gas shunting shunts flue gas and the second tunnel shunting flue gas into the first via, and first via shunting flue gas is extracted out by the second dust removal port, the
Two roads shunt the material during flue gas preheats the first preheating zone during by the first preheating zone；First preheating zone is provided with to the
The burner I of spray combustion gas in one preheating zone, it is material bed that the flame jet of burner I drives the second tunnel shunting flue gas to penetrate jointly
Gap；First dust removal port extracts cold air, burning gases and two tunnels the shunting flue gas entered at feeding seal mouth out.
Further, distributor or regulating valve are adjusted by adjusting flue gas, respectively the blended flue of convection current and heat smoke
The flue gas allocation proportion of pipeline is adjusted, and control first via shunting flue gas, the second road shunt flue gas flow and enter mixing
The mixed flue gas temperature of flue.
The beneficial effects of the utility model are：
1st, due to shunting and guide effect of the double dust collection mouth to electric arc kiln gas, traditional CONSTEEL flue gas stream is changed
To be taken away to duct structure, most of flue gas by the second dust removal port close to electric arc furnaces, the exhaust gas volumn in strengthening preheating area reduces,
The height of duct can be designed according to the requirement that the mixed flue gas and hydrodynamic of burner combustion gas and electric arc furnaces balance,
And allow steel scrap layer of the flame jet directly in shock peening preheating zone of burner, while flame jet drives shunting flue gas
Steel scrap gap is permeated, both improves the heat transfer effect of shunting flue gas, the combustion thermal efficiency of burner also obtains larger raising.
2nd, traditional CONSTEEL only has one dust removal port of afterbody, and duct will provide the passage of big exhaust gas volumn, can not accomplish most
It is good, duct burner preheating scrap it is less efficient.Relative to traditional CONSTEEL, flue gas shunting technology of the present utility model is excellent
CONSTEEL duct height is changed so that original burner can directly heat steel scrap in strengthening preheating area, improve outside
The efficiency of chemical energy, enhancing outside chemical can pre- heat effect.
3rd, in the utility model, the first dust removal port has cut off the passage that cold air enters strengthening preheating area, in strengthening preheating
The burner in area can directly heat steel scrap, and strengthening preheating area is filled with high-temperature flue gas, and the thermal efficiency sent of its burner is big
It is big to improve.
4th, burner I is tilted to the first dust removal port and reverse second dust removal port of combustion-gas flow, the water jets of multiple rows of burner I are divided equally
Amount forms jet pump effect with narrow steel scrap duct, and the combustion gas drive for flowing to the first dust removal port is produced in the first preheating zone duct
Dynamic dynamic pressure, two flue gas ash removal mouths adjust distributor with flue gas by flue respectively and coupled, flue gas regulation distributor difference
The first dust removal port, the flue gas allocation proportion of the second dedusting are adjusted, it is significant.
5th, the control to flue-gas temperature after mixing can be achieved, asked to suppress the discharge of scrap steel preheating Guo journey Zhong bioxin
Topic.
Brief description of the drawings
In order that the purpose of this utility model, technical scheme and beneficial effect are clearer, the utility model provides as follows
Accompanying drawing illustrates：
Fig. 1 is system schematic of the present utility model；
Fig. 2 is the schematic diagram of Fig. 1 distressed structures；
Reference：
Horizontal continuity charging preheating duct 1, electric arc furnaces 2, the first dust removal port 3, the second dust removal port 4, feeding seal mouth 5, burning
Mouth I 6, burner II 7, mixed flue gas pipeline 8, heat smoke pipeline 9, expansion chamber 10, flue gas regulation distributor 11, flue 12, flue gas
Pressure sensor 13, regulating valve 14, rapid cooling device for fume 15, steel scrap charging magnetic disc suspending 16；
F0：Total flue gas of electric arc furnaces discharge；
F1：Flow to the first via shunting flue gas of the second dust removal port；
F2：Flow to the second tunnel shunting flue gas of the first dust removal port；
F3：Enter the cold air of the first preheating zone at feeding seal mouth；
F4：The burning gases that burner I sprays；
FF：The mixed gas of F1, F2, F3 and F4；
P0：Fluid driving pressure caused by first preheating zone duct；
P1：Negative pressure at first dust removal port；
P2：Negative pressure at second dust removal port.
Embodiment
Below in conjunction with accompanying drawing, preferred embodiment of the present utility model is described in detail.
As illustrated, the horizontal continuity charging preheating device in the utility model, including horizontal continuity charging preheating duct 1
And electric arc furnaces 2, the horizontal continuity charging preheats is interval with the first dust removal port 3 and second on duct 1 along material conveying direction
Dust removal port 4, first dust removal port 3 is located at the rear of feeding seal mouth 5 of horizontal continuity charging preheating duct 1 and close charging is close
Sealing 5, second dust removal port 4 are located at the back segment of horizontal continuity charging preheating duct 1 and close to the feeding mouths of electric arc furnaces 2, and two remove
Horizontal continuity charging preheating duct between dirt mouth forms the first preheating zone I, the level between the second dust removal port 4 and electric arc furnaces feeding mouth
Continuous charging preheating duct forms the second preheating zone II；Also horizontal continuity charging preheating is inclined at including several intervals to contain
Burner I 6 at the preheating zone of road 1 first, the horizontal component of the combustion-gas flow of each burner I 6 are opposite with material conveying direction.
In the utility model, due to double dust collection mouth flue gas F0 total to electric arc furnaces shunting action, tradition is changed
CONSTEEL flue gas flow direction.First via shunting flue gas F1 (most electric arc kiln gas) is by close to the of electric arc furnaces feeding mouth
Two dust removal ports 4 are taken away, and material is mainly by smoke pre-heating in the region, so region is also referred to as smoke pre-heating area；Second tunnel
Shunting flue gas F2 (remainder electric arc kiln gas) flows through the first preheating zone I and carries out smoke pre-heating to material in this region, should
The burner I 6 of the tilted setting in region is to material jet flames, to this area together with the second tunnel shunting flue gas F2 for flowing through this region
Material is preheated in domain, so region is also referred to as strengthening preheating area.The jet horizontal component direction of burner I 6 being obliquely installed
The first dust removal port is pointed to backwards to the second dust removal port (i.e. the reverse material conveying direction in jet horizontal component direction), may be such that burner I 6
The direct shock peening preheating zone of flame jet in steel scrap layer；Meanwhile flame jet drives shunting flue permeating steel scrap gap,
Also the heat transfer effect of shunting flue gas can be improved, the combustion thermal efficiency of burner I 6 is also obtained larger raising.In addition, it is arranged on charging
The passage that cold air enters strengthening preheating area can be cut off in first dust removal port 3 at the rear of seal 5, and the burner in strengthening preheating area can
Steel scrap is directly heated, and strengthening preheating area is filled with high-temperature flue gas, further increases the thermal efficiency of burner I 6.
In the utility model, the duct of first preheating zone I is highly less than second in the horizontal continuity charging preheating duct 1
The duct height of preheating zone II.Due to double dust collection mouth flue gas F0 total to electric arc furnaces shunting action so that the cigarette in strengthening preheating area
Tolerance reduces, and duct height can be put down according to mixed flue gas (the second roads of burner combustion gas F4+ shunt flue gas F2) and hydrodynamic
The requirement of weighing apparatus is redesigned.That is, the utility model for employing flue gas shunting technology can be by reducing the first preheating
The duct height in area I, makes the burner I 6 in strengthening preheating area directly heat steel scrap, to improve its outside chemical energy efficiency, strengthens
Outside chemical can pre- heat effect.
In the utility model, if interval is provided tiltedly with the second preheating zone II of horizontal continuity charging preheating duct 1
Dry burner II 7, the horizontal component of the combustion-gas flow of each burner II 7 are opposite with material conveying direction.By setting up burner
II 7, the pre-heat effect of the material of the second preheating zone II can be further improved in limited preheating time.
In the utility model, mixed flue gas pipeline 8 is connected with first dust removal port 3, is connected in second dust removal port 4
It is connected to heat smoke pipeline 9；The mixed flue gas pipeline 8 and heat smoke pipeline 9 are connected with expansion chamber 10.
Specifically, being equipped with flue gas pressures sensor 13 at the first dust removal port 3 and the second dust removal port 4 in the present embodiment, mix
Close flue 8 and heat smoke pipeline 9 distributor 11 adjusted by flue gas and be connected on flue 12, flue 12 again with expansion chamber
10 are connected.Ensureing the dust removing effects of whole electric arc furnaces 2, it is necessary to assure the second dust removal port 4 has enough rates of air sucked in required (negative pressure), if
Without the first dust removal port 3 to the cut-off in strengthening preheating area, have after a large amount of cold airs are introduced into strengthening preheating area and go successively to second
Dust removal port 4 so that burner I 6 because must heat this part cold air and caused by its thermal efficiency reduction.Burner I 6 is to the first dedusting
Mouth is tilted, and its reverse material conveying direction of jet horizontal component that burns, multiple rows of jet of burner I 6 is formed with narrow preheating duct
Jet pump effect, the combustion gas in strengthening preheating area can produce the driving force for flowing to the first dust removal port, that is, generate circulation dynamic pressure,
The circulation dynamic pressure can balance the dedusting negative pressure at the second dust removal port 4, so as to realize the tiny structure of the first dust removal port.With reference to flue gas
Adjust distributor 11 and adjust the first dust removal port 3, the flue gas allocation proportion of the second dust removal port 4, can cause in feeding seal mouth
Cold air influx minimizes, or even close to 0, so that the thermal efficiency of whole horizontal charging pre-heating system obtains overall carry
It is high.In addition, the second tunnel shunting flue gas F2 into strengthening preheating area feeds preheating duct 1 because of cooling supplemented with horizontal continuity
The heat of loss, and then the combustion gas thermal efficiency of the scrap steel preheating in strengthening preheating area can be improved.It is pointed out that the utility model
In flue gas regulation distributor 11 can be threeway flap valve or other flue gas tunable arrangements.
As the alternative of above-described embodiment, can use smoke elimination controlled atmosphere section distributor 11, directly in mixed flue gas pipeline 8 and
Regulating valve 14 is correspondingly arranged on heat smoke pipeline 9；Then mixed flue gas pipeline 8 and heat smoke pipeline 9 are directly connected with flue,
Mixed flue gas pipeline 8 and the resistance on heat smoke pipeline 9 are adjusted by regulating valve 14.
Also include the rapid cooling device for fume 15 being connected with expansion chamber 10 in the utility model, to realize that the cooling to flue gas is cold
But.
Also include steel scrap charging magnetic disc suspending 16 in the utility model, the steel scrap charging magnetic disc suspending 16, which launches steel scrap, arrives water
The material feeding section of flat continuous charging preheating duct 1.Certainly, it can also add and shake in front of the material feeding section of horizontal continuity charging preheating duct
Charging device is moved, steel scrap charging magnetic disc suspending 16 launches steel scrap into vibration charging device, and vibration charging device, which is used as, keeps in material
Case, can be uninterruptedly to feed at the material feeding section of horizontal continuity charging preheating duct.
As mentioned earlier, to ensure the dust removing effects to electric arc furnaces 2, the second dust removal port 4 is used as main dust removal port not only
Extract first via shunting flue gas F1 out, also to ensure certain negative pressure P2 at the second dust removal port 4 be present.Second tunnel shunting flue gas F2
Into in the first preheating zone I duct；Multiple rows of burner I 6 diagonally downward, each water jets of burner I 6 are housed at first preheating zone I
The amount of dividing equally forms pump injection effect (multiple rows of multistage jet pump of burner I 6) with this section of duct, so as to strengthen the first preheating zone I ducts
Caused fluid driving pressure P0 (circulation dynamic pressure), fluid driving pressure P0 can balance (P0=P2) or partial equilibrium (P0
<) or overbalance (P0 P2>P2) the negative pressure P2 at the second dust removal port 4.Certainly, certain bear can be also provided at the first dust removal port 3
P1 is pressed, to separate cold air F3, it is not entered strengthening preheating area；Cold air F3, the burning gases F4 and second of burner injection
Road shunting flue gas F2 is extracted out in the first dust removal port 4, and F1, F2 tolerance point is controlled by the pressure sensor 13 at two dust removal ports
Match somebody with somebody, and then the resistance on adjustment mixed flue gas pipeline 8, heat smoke pipeline 9 causes the flue gas in horizontal continuity charging preheating duct 1
Reach optimum balance.
Analytic explanation will be carried out to several operating modes existing for the system warm-up process below：
Operating mode 1：If P0=P2, i.e., the negative pressure value of fuel gas injection driving force and the second dust removal port 4 in the first preheating zone I connects
Closely, then negative pressure P1 ≈ 0 of the first dust removal port, the second tunnel shunting flue gas F2=0 in the first preheating zone I can be now realized, only
It is that the burning gases F4 that a small amount of cold air F3 sprays with burner enters the first dust removal port 3, but it is more difficult in the control of this working condition system
Realize.
Operating mode 2：If P0>P2, i.e., the second tunnel shunting flue gas F2, the burning gases F4 of burner injection in the first preheating zone I
Actively enter the first dust removal port 3, now P1 should be in micro-vacuum state, and the entrance that otherwise feeds can emerge flue gas.Because P1 is micro- negative
Pressure, then the cold air F3 through feeding seal mouth 5 is less, and the second tunnel shunting flue gas F2 is more, and steel scrap can obtain the second road point
Flow flue gas F2 and the burning gases F4 of burner injection preheating.
Operating mode 3：If P0<P2, P1>P2-P0, P1 now, one can be mixed into the first preheating zone I in certain negative pressure state
Quantitative cold air F3, but few, total exhaust gas volumn F2+F3+ that the first dust removal port extracts when mixed cold air amount F3 is more than P0≤0
F4 is smaller, and steel scrap can obtain the second tunnel shunting flue gas F2 and burning gases F4 preheating.
Operating mode 2, operating mode 3 are the basic working modes of the system, and both operating modes can pass through the pressure at two dust removal ports
Sensor 13 adjusts PLC, controls flue gas to adjust by PLC and connects distributor 11 and burner I 6, burner II 7, it is final realize to F1,
The regulation of F2 tolerance distribution.
Also need to emphasize is：The fluidic tilt direction of burner I 6 is particularly important in first preheating zone I, and it determines P0 pairs
P2 plays balanced action or booster action.In the utility model, if P0 is excessive to there is P0>P2, now the first dust removal port 3 can
Second tunnel shunting flue gas F2 is taken away, and what flue gas tune connect distributor 11 is substantially the pressure distribution for regulating and controlling P1, P2 so that it is
System is issued to " gas power-dedusting static(al) " optimization balance in PLC controls, realizes the dynamic sealing of system, improves the first preheating
The area I thermal efficiency, this is significance existing for the first dust removal port 3.Steel scrap feeds in preheating duct 1 in horizontal continuity, first wears
Cross reinforcing preheating zone, after enter back into smoke pre-heating area, can be further pre- because the flue-gas temperature at electric arc furnaces feeding mouth is higher
Hot steel scrap.
It can be seen that by described above：The system, which has to greatly reduce in horizontal continuity charging preheating duct 1, is mixed into cold air
The characteristic of F3 amounts.
It should be noted that, flue gas flow direction and steel scrap flow direction of material in the first preheating zone I are gone relatively, burner I 6 in addition
Chemical energy strengthening preheating steel scrap, the efficiency for being advantageous to heat exchange improve.Cold air F3 mixed volume is reduced, contributes to input chemistry
The thermal efficiency of energy improves.
Assuming that it is mixed into the cold air F3=5000m of the first preheating zone3/ h (traditional consteel 75tEAF, into preheating cigarette
The gas flow in road is in 4~60,000 m3/ h, take 1/10), temperature is 40 DEG C；
The burning gases F4=12500m of first preheating zone burner injection3/ h (uses equivalent to 75tEAF in the first preheating zone
Air-breathing consumption natural gas 10Nm3/ t), ignition temperature is controlled at 1200 DEG C or so；
For convenience of assessment, set that the specific heat of each gas is identical, the thermal efficiency of equipment itself is constant；
So the first mixed temperature of preheating zone hot and cold gas is about 868 DEG C；
The mixed flue gas temperature discharged after first preheating zone preheating scrap is about 600 DEG C；
Heat equivalent：(868-600) × (5000+12500)=4690000 (J)；
If it is mixed into the cold air F3=1000m of the first preheating zone3/h；40 DEG C of temperature；
The second tunnel shunting flue gas F2=5000m in first preheating zone3/h；Temperature is 1100 DEG C；
1110 DEG C of temperature at first dust removal port after gas mixing, the temperature in strengthening preheating area after gas mixing are about
1171℃；
Heat equivalent (with the first dust removal port temperature computation)：(1110-600) × (1000+12500+5000)=9435000
(J)；
Strengthening preheating area thermal efficiency improves：(9435000-4690000)/4690000=100%.
The reason for thermal efficiency improves essentially consists in：1) reduce the heat that cold air is taken away, the 2) heat exchange of shunting heat smoke
It is improved.
Above-mentioned is only an analysis examples, illustrates to be mixed into the great of the pre- thermal efficiency of heat that cold air is taken away to cold air
Influence.This and pure oxygen burning reduce the heat that the nitrogen in air is taken away, and are to improve the operation principle of ignition temperature and the thermal efficiency
Similar.In actual use, the fuel of burner can be reduced by adjusting burner I 6, when meeting operating mode preheating requirement
Consumption.
The design of this steel scrap continuous charging pre-heating device and flue gas flow field, can preferably improve outside chemical can strengthen
The efficiency of combustion of preheating zone 21, it can also improve the thermal efficiency of whole system.
If there is the requirement for suppressing preheating bioxin during scrap steel preheating, also flue gas can be set in the position that system needs
Temperature detection, typically require that the first dust removal port 3, the flue-gas temperature of the second dust removal port 4 are above 800 DEG C (such as 850~950 DEG C),
Now, the heat that mixed cold air is taken away is higher (the heated temperature of cold air is higher), now to the heat of burner I 6
Efficiency influences bigger.
A kind of strengthening preheating method based on above-mentioned horizontal continuity charging preheating device, including herein below：From electric arc furnaces 2
Total flue gas F0 of middle discharge preheats to the material of the second preheating zone II；The spaced dedusting of first dust removal port 3 and second
Total flue gas F0 is split into mouth 4 into first via shunting flue gas F1 and the second tunnel shunting flue gas F2, F1 are extracted out by the second dust removal port 4,
F2 preheat the first preheating zone during by the first preheating zone I in material；First preheating zone is provided with to the first preheating zone
Interior spray combustion gas F4 burner I 6, the flame jet of burner I 6 drive F2 to penetrate material bed gap jointly；First dust removal port 3
The cold air F3, the burner combustion gas F4 that enter at feeding seal mouth 5 and the second tunnel shunting flue gas F2 are extracted out.
Specifically, the first dust removal port 3 is the burning gases F4 of burner injection main bleeding point, the second dust removal port 4 is first
Road shunting flue gas F1 main bleeding point；The flame jet of burner I 6 drives the second tunnel shunting flue gas F2 of shunting to penetrate steel scrap jointly
Lamellar spacing；The jet horizontal component of the multiple rows of burner I 6 in strengthening preheating area points to the first dust removal port, constitutes strengthening preheating area duct
Interior driving pressure P0, to balance the dedusting negative pressure P2 of the second dust removal port；By flue gas pressures sensor 13, the first dedusting is controlled
The tiny structure requirement of mouth, so as to reduce the mixed cold air F3 of the first dust removal port, cut-out cold air F3 enters strengthening preheating area.Enter
Enter the steel scrap in smoke pre-heating area, shunted by the first via after flue gas F1 and burner II 7 preheat jointly again and enter electric arc furnaces 2, it is overall
Step improves the pre- thermal efficiency of burner I, II and electric arc kiln gas, realizes the strengthening preheating of steel scrap.
Further, distributor 11 can be adjusted by flue gas or regulating valve 14 distinguishes the blended flue 8 of convection current and heat
The flue gas allocation proportion of flue 9 is adjusted, so as to control F1, F2 flow and enter the mixing of mixed flue gas pipeline 8
Flue gas (F2+F3+F4) temperature, realizes more environmentally friendly production.
Finally illustrate, preferred embodiment above is only unrestricted to illustrate the technical solution of the utility model, to the greatest extent
The utility model has been described in detail by above preferred embodiment for pipe, but those skilled in the art should manage
Solution, can make various changes, without departing from the utility model claims book institute to it in the form and details
The scope of restriction.
Claims (8)
- The preheating device 1. a kind of horizontal continuity feeds, including horizontal continuity charging preheating duct and electric arc furnaces, it is characterised in that：Institute State and be interval with the first dust removal port and the second dust removal port along material conveying direction on horizontal continuity charging preheating duct, described first Dust removal port is located at the feeding seal mouth rear of horizontal continuity charging preheating duct and close to feeding seal mouth, second dust removal port Feed the back segment for preheating duct and the horizontal continuity charging preheating between electric arc furnaces feeding mouth, two dust removal ports positioned at horizontal continuity Duct forms the first preheating zone, and it is pre- that the horizontal continuity charging preheating duct between the second dust removal port and electric arc furnaces feeding mouth forms second Hot-zone；Also include the burner I that several intervals are inclined at the first preheating zone of horizontal continuity charging preheating duct, each institute The horizontal component for stating the combustion-gas flow of burner I is opposite with material conveying direction.
- The preheating device 2. horizontal continuity according to claim 1 feeds, it is characterised in that：The horizontal continuity charging preheating The duct of the first preheating zone is highly less than the duct height of the second preheating zone in duct.
- The preheating device 3. horizontal continuity according to claim 1 feeds, it is characterised in that：The horizontal continuity charging preheating Interval is provided tiltedly with several burners II at second preheating zone of duct, the horizontal component of the combustion-gas flow of each burner II with Material conveying direction is opposite.
- 4. the horizontal continuity charging preheating device according to claim any one of 1-3, it is characterised in that：First dedusting Mixed flue gas pipeline is connected with mouthful, heat smoke pipeline is connected with second dust removal port；The mixed flue gas pipeline and heat Flue is connected with expansion chamber.
- The preheating device 5. horizontal continuity according to claim 4 feeds, it is characterised in that：The mixed flue gas pipeline and heat Flue adjusts distributor by flue gas and flue is connected with expansion chamber.
- The preheating device 6. horizontal continuity according to claim 4 feeds, it is characterised in that：The mixed flue gas pipeline and heat Regulating valve is equipped with flue；The mixed flue gas pipeline and heat smoke pipeline are connected by flue with expansion chamber.
- 7. the horizontal continuity charging preheating device according to any one of claim 5 or 6, it is characterised in that：Also include with sinking The connected rapid cooling device for fume in room drops.
- The preheating device 8. horizontal continuity according to claim 1 feeds, it is characterised in that：Also include steel scrap charging disk Hang, steel scrap charging magnetic disc suspending or the material feeding that horizontal continuity charging preheating duct is delivered to by vibrating charging device by material At section.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
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| CN201721224728.8U CN207175997U (en) | 2017-09-22 | 2017-09-22 | A kind of horizontal continuity charging preheating device |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201721224728.8U CN207175997U (en) | 2017-09-22 | 2017-09-22 | A kind of horizontal continuity charging preheating device |
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| CN207175997U true CN207175997U (en) | 2018-04-03 |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107460274A (en) * | 2017-09-22 | 2017-12-12 | 中冶赛迪工程技术股份有限公司 | A kind of horizontal continuity charging preheating device and its strengthening preheating method |
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2017
- 2017-09-22 CN CN201721224728.8U patent/CN207175997U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107460274A (en) * | 2017-09-22 | 2017-12-12 | 中冶赛迪工程技术股份有限公司 | A kind of horizontal continuity charging preheating device and its strengthening preheating method |
| WO2019056930A1 (en) * | 2017-09-22 | 2019-03-28 | 中冶赛迪工程技术股份有限公司 | Continuous horizontal-feeding preheating device and preheating enhancement method thereof |
| CN107460274B (en) * | 2017-09-22 | 2023-09-12 | 中冶赛迪工程技术股份有限公司 | Horizontal continuous feeding preheating device and reinforced preheating method thereof |
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