CN216445405U - Direct steelmaking device of iron-containing powder in reducing atmosphere - Google Patents
Direct steelmaking device of iron-containing powder in reducing atmosphere Download PDFInfo
- Publication number
- CN216445405U CN216445405U CN202121859822.7U CN202121859822U CN216445405U CN 216445405 U CN216445405 U CN 216445405U CN 202121859822 U CN202121859822 U CN 202121859822U CN 216445405 U CN216445405 U CN 216445405U
- Authority
- CN
- China
- Prior art keywords
- steelmaking
- iron
- area
- pool
- gas
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Images
Landscapes
- Furnace Details (AREA)
- Carbon Steel Or Casting Steel Manufacturing (AREA)
Abstract
The embodiment of the utility model discloses a direct steelmaking device of iron-containing powder in a reducing atmosphere, belonging to the technical field of metallurgy. The device comprises a steel making pool, wherein the steel making pool is arranged at the bottommost part of the device and comprises a slagging flux pile, a molten steel layer is arranged at the bottom of the steel making pool, a liquid slag layer is arranged on the molten steel layer, a quick reduction area is arranged above the steel making pool, a gas making tower is arranged beside the lower part of the quick reduction area, a mineral aggregate feeding area is arranged above the quick reduction area, the central part of the top of the mineral aggregate feeding area is provided with a tail gas discharge port, the outer side of the tail gas discharge port is provided with a slagging flux feeding port along the circumference, the side surface of the tail gas discharge port is uniformly provided with a cold gas port and a mineral powder feeding port, a slagging flux bin and a slagging flux feeding mechanism are arranged inside the tail gas discharge port, and the direct steel making device is provided with a control system and is electrically connected with the device through a sensor and a control component.
Description
Technical Field
The utility model belongs to the technical field of metallurgy, and relates to a direct steelmaking device of iron-containing powder in a reducing atmosphere.
Background
The process integrates four process links of sintering (or pelletizing), coking, blast furnace iron making and converter oxidation steel making, and has the defects of long production process, high energy consumption, serious environment pollution caused by dependence on coke resources and the like. When the current global environmental pollution and resource and energy shortage problem is getting more serious, the implementation of energy conservation and emission reduction and the implementation of clean production become the necessary routes for the continuous development of the global steel industry.
The traditional steelmaking process adopts an oxygen converter and an electric furnace steelmaking process. The oxygen converter adopts blast furnace molten iron as a raw material to carry out converting to obtain qualified molten steel, and has the advantages of multiple production units, large scale and long production period. The blast furnace molten iron adopted by the oxygen converter has high carbon content (usually 2.5-4.3%), contains more impurities such as silicon, manganese, phosphorus, sulfur and the like, not only needs a slagging flux, but also needs high-purity oxygen blowing, and the heat is lost during the transportation of the molten iron. The electric furnace steelmaking mainly adopts recycled scrap steel, and the process for obtaining qualified molten steel by smelting in the electric furnace by using electric energy as a heat source has the advantages of simple process flow and few production links and periods. Because scrap steel needs to be melted, a large amount of electric energy needs to be consumed, and both the scrap steel and the scrap steel need to build independent steelmaking equipment, so that the investment cost is huge.
Aiming at the problems of high pollution and high energy consumption of the traditional blast furnace ironmaking process, the smelting reduction ironmaking technology is developed in recent years because the dependency on high-pollution and high-energy-consumption processes such as agglomeration, sintering, coking and the like can be reduced, and becomes an important technical approach for realizing energy conservation, emission reduction and clean production in the steel industry, such as COREX, FINEX, HIsmelt and the like. The COREX process uses an upper pre-reduction shaft furnace to pre-reduce iron ore to obtain metallized pellets (DRI) with a metallization rate of 70-90%, and then the DRI is fed into a lower melter-gasifier for final reduction. The process still depends on lump ore, pellet ore, sintered ore and part of coke to maintain smooth operation of the furnace condition. The FINEX process uses fine ore as raw material, adopts a multi-stage fluidized state reactor to complete iron ore pre-reduction, obtains reduced iron powder with the metallization rate of about 90%, and the reduced iron powder and the fine coal are added into a melting gasification furnace as furnace charge after being subjected to hot briquetting for melting final reduction. The HIsmelt process uses fine ore as a main raw material, a cyclone melting furnace is adopted to carry out flash smelting on the fine ore, a fusing agent and coal powder are blown into the cyclone melting furnace along the tangential direction of a furnace body by taking oxygen as a carrier, the fine ore is reduced and melted in the moving process, and then the fine ore flows and drips into the melting reduction furnace along the furnace wall for final reduction.
The processes obviously carry out reduction iron making and melting final reduction steel making through different devices, wherein, iron-containing powder is reduced firstly and then briquetted, and then the reduction steel making is carried out, obviously, the processes are complex, and the utilization rate of the devices is low. Although the flash smelting efficiency is high, the cyclone melting furnace and the smelting reduction furnace are different in device structure, the requirement on the blowing performance of the cyclone melting furnace blown along the tangential direction of the furnace body is very high, the corrosion of refractory materials is serious, the service life of a furnace lining is short, and the industrial large-scale production and popularization cannot be carried out.
The flash iron-making technologies disclosed in patents CN106086280A, CN102690919A, CN103993115A, etc. integrate the processes of reduction, melting, slag-making, etc. into one body, and have the advantages of simplified equipment and easy mass production, but the product molten iron has high carbon content (> 2.0%), and impurities such as Si, Mn, P, S, etc. cannot be effectively removed, and crude steel cannot be directly produced. Other patents CN101906501A and CN108374067A propose a process for direct steelmaking using fine ore and coal oxygen, in which iron ore powder is pre-reduced and then sprayed into a steelmaking furnace together with coal powder and oxygen to make steel. In particular, the device for direct steel making by rapid reduction in CN108374067A includes an iron ore powder pretreatment system, a rapid reduction furnace system and a steel making furnace system, and obviously, reduction iron making and melting final reduction steel making are also performed by different devices.
To sum up, the current-stage smelting reduction iron-making/direct steel-making method can solve the problems of long steel production flow, high energy consumption and serious pollution to a certain extent, but the process still adopts the two-step process of traditional reduction iron-making and oxidation steel-making; the reduction process and the oxidation process are implemented in different devices or containers, so that the defects of high equipment investment and high fault of connecting equipment exist.
SUMMERY OF THE UTILITY MODEL
The utility model solves the technical problems that the traditional blast furnace iron making and converter steel making have large energy consumption and serious environmental pollution and need two steps; although the smelting reduction iron-making technology exists, reduction iron-making and oxidation steel-making are carried out by different devices, the production flow is long, the energy consumption is high, the pollution is serious, the occupied area of different equipment is large, and the synergy rate is low.
In order to solve the technical problems, the utility model provides the following technical scheme:
a direct steelmaking device of iron-containing powder in a reducing atmosphere comprises a steelmaking pool, a gas making tower, a rapid reduction area, an ore feeding area and a control system;
wherein: the device comprises a steelmaking pool, a gas making tower, a control system and a device, wherein the steelmaking pool is arranged at the bottommost part of the device and comprises a slagging flux pile, a molten steel layer is arranged at the bottom of the slagging flux pile, a liquid slag layer is arranged on the molten steel layer, a rapid reduction area is arranged above the slagging flux pile, a gas making tower is arranged beside the lower part of the rapid reduction area, an ore material feeding area is arranged above the rapid reduction area, and the control system is arranged beside the steelmaking pool, the gas making tower, the rapid reduction area or the ore material feeding area and is electrically connected with the device through a sensor and a control part;
the slagging flux pile is a solid slagging flux material pile, and an air making gun and a reducing gas flow channel are arranged in the gas making tower.
Furthermore, the steelmaking pool is a cylinder or a polygonal prism cylinder, the upper part of the steelmaking pool is directly connected with the rapid reduction zone, one side of a molten steel layer of the steelmaking pool, which is close to the bottom, is provided with a steel tapping hole, and the other side of a liquid slag layer, which is close to the molten steel layer, is provided with a slag tapping hole.
Further, the solid slagging flux material pile is in a conical pile shape and is formed by mixing one or more of granular or blocky limestone with the grain diameter of 5-50mm, quick lime, semi-coke, fluorite, dolomite and lump coal and then naturally falling.
Further, the gas making tower is in a shape of a cone frustum or a pyramid frustum; the outside of the gas making gun is connected with an oxygen supply device and a gas making raw material supply device; and the outlet of a reducing gas flow passage of the gas making tower is connected with the lower part of the rapid reduction area.
Furthermore, the reducing gas flow channel is in a bell mouth shape, and the downward inclination angle of the reducing gas flow channel and the horizontal plane is 30-60 degrees; the inclination angle with the centripetal axis is 1-16 degrees for right inclination in the northern hemisphere and 1-16 degrees for left inclination in the southern hemisphere.
Further, the structure of the rapid reduction area is in a variable cross-section cylindrical shape or polygonal cylindrical shape with a thin middle part and thick upper and lower ends; the lower part of the rapid reduction zone is provided with at least 3 gas making towers along the circumference, and the upper part of the rapid reduction zone is provided with at least 2 cooling gas ports.
Furthermore, the mineral aggregate feeding area is of a frustum shape with a large lower part and a small upper part, and a tail gas discharge port is formed in the central part of the top of the mineral aggregate feeding area; the outside in mineral aggregate input area evenly is provided with 2 at least powdered ore input openings, the inside in mineral aggregate input area is provided with slagging flux storage storehouse and slagging flux input mechanism.
Further, the control system consists of a hardware system and control software and is electrically connected with the device through a sensor and a control component.
Further, the surface of the slagging flux pile is an inwards concave cambered surface.
Further, the control system is electrically connected with the gas making tower, the cold air port, the mineral powder feeding port and the slagging flux feeding port.
The technical scheme provided by the embodiment of the utility model at least has the following beneficial effects:
in the scheme, the iron-containing powder is directly used as a steelmaking device in a reducing atmosphere, a traditional process device for coking, sintering and pelletizing of a blast furnace and a device for flash smelting are abandoned, one device is directly used for directly and efficiently producing the crude steel, coke resources are not relied on, and the process with high energy consumption is reduced; a large amount of steel making devices are not needed, the occupied area of a factory is small, and a large amount of capital investment is saved.
The iron-containing powder is directly used in a steelmaking device in a reducing atmosphere, gas-making raw materials are sprayed with high-temperature reducing gas through a gas-making gun arranged beside a slagging flux pile in the device, the high-temperature reducing gas directly acts on the slagging flux pile to provide heat for the slagging flux pile, the lime is favorably melted, the stagnation period is shortened, the slagging process is accelerated, and the heat loss is less; then the high-temperature reducing gas rises through the gas making tower and the rapid reduction area, and meets with the falling iron-containing powder in a countercurrent way in the rapid reduction area, and then the heat transfer and mass transfer reactions are carried out simultaneously, so that the contact reaction is sufficient, and the reaction efficiency is high.
The iron-containing powder is directly steelmaking in a reducing atmosphere, a steelmaking pool is arranged at the bottom of a furnace body, iron and iron ore soft melts falling after reduction reaction fall on the surface of a slagging flux pile together, the unreduced part of the iron-containing powder in a rapid reduction area can be further reduced with high-temperature reducing gas, the final reduced steel slag mixture is subjected to impurity removal reactions such as dephosphorization and desulfurization with the slagging flux to generate final slag, then slag and steel are separated, direct steelmaking can be realized in one device, a large amount of independent investment of steelmaking equipment is not needed, and the fund and the area of a site are greatly saved.
Therefore, the utility model carries out the unique design on the structure of the direct steelmaking equipment based on the integrated reduction of the iron-containing powder in the rapid reduction area and the slagging flux pile, creates a flow field and a temperature field which are beneficial to heat transfer and mass transfer in the device, and achieves the aim of integrated direct steelmaking based on the slagging flux pile in the device under the reducing atmosphere.
Drawings
In order to more clearly illustrate the technical solutions in the embodiments of the present invention, the drawings needed to be used in the description of the embodiments will be briefly introduced below, and it is obvious that the drawings in the following description are only some embodiments of the present invention, and it is obvious for those skilled in the art to obtain other drawings based on these drawings without creative efforts.
FIG. 1 is a schematic structural view of a direct steelmaking apparatus in a reducing atmosphere containing iron powder according to the present invention.
The reference numerals are explained below:
1. a steel-making pool; 11. slagging flux pile; 12. a molten steel layer; 121. a steel tapping hole; 13. a liquid slag layer; 131. a slag outlet;
2. a gas making tower; 21. an air gun; 22. a reducing gas flow channel;
3. a fast reduction zone;
4. a mineral aggregate feeding area; 41. a cold air port; 42. a mineral powder feeding port; 43. a slagging flux storage bin; 44. a slagging flux feeding port; 45. a tail gas discharge port; 46. a slagging flux feeding mechanism;
5. and (4) controlling the system.
Detailed Description
In order to make the technical problems, technical solutions and advantages of the present invention more apparent, the following detailed description is given with reference to the accompanying drawings and specific embodiments.
As shown in fig. 1, an embodiment of the present invention provides a direct steelmaking device of iron-containing powder in a reducing atmosphere, the device includes a steelmaking pool 1, a gas making tower 2, a rapid reduction area 3, an ore material feeding area 4 and a control system 5, the steelmaking pool 1 is disposed at the bottommost portion of the device, the steelmaking pool 1 includes a slagging flux stack 11 disposed at the center, a molten steel layer 12 is disposed at the bottom of the slagging flux stack 11, a liquid slag layer 13 is disposed on the upper layer of the molten steel layer 12, the rapid reduction area 3 is disposed above the slagging flux stack 11, the gas making tower 2 is disposed beside the lower portion of the rapid reduction area 3, the ore material feeding area 4 is disposed above the rapid reduction area 3, and the control system 5 controls measurement and control units distributed at different portions through electrical connection.
The slagging flux pile 11 is a solid slagging flux material pile, and an air making gun 21 and a reducing gas flow passage 22 are arranged in the gas making tower 2.
Preferably, the steelmaking pool 1 is a cylinder or a polygonal prism cylinder, the upper part of the steelmaking pool 1 is directly connected with the rapid reduction zone 3, one side of the molten steel layer 12 of the steelmaking pool 1 close to the bottom is provided with a steel outlet 121, and the other side of the liquid slag layer 13 close to the molten steel layer 12 is provided with a slag outlet 131.
Preferably, the solid slagging flux material pile is in a conical pile shape and is formed by mixing one or more of granular or blocky limestone with the grain diameter of 5-50mm, quick lime, semi-coke, fluorite, dolomite and lump coal and then naturally falling.
Preferably, the gas making tower 2 is a cone frustum or a pyramid frustum; the exterior of the gas making gun 21 is connected with an oxygen supply device and a gas making raw material supply device; the reducing gas flow passage outlet 22 of the gas making tower 2 is connected with the lower part of the rapid reduction area 3.
Preferably, the reducing gas flow channel 22 is in a bell mouth shape, and the downward inclination angle with the horizontal plane is 30-60 degrees; the inclination angle with the centripetal axis is 1-16 degrees for right inclination in the northern hemisphere and 1-16 degrees for left inclination in the southern hemisphere.
The rapid reduction zone 3 is an area for reducing iron-containing powder, and is structurally in the shape of a variable cross section cylinder with a thin middle part and thick upper and lower ends, and the shape of the variable cross section is used for controlling a flow field to operate according to set parameters; 3-36 gas making towers are uniformly arranged at the lower part of the rapid reduction zone 3 along the circumference.
The mineral aggregate feeding area 4 is of a frustum shape with a large lower part and a small upper part, and a tail gas discharge port 45 is formed in the central part of the top of the mineral aggregate feeding area 4; the outer side of the tail gas discharge port is circumferentially provided with 1-3 slagging flux feeding ports 44, the outer side of the mineral aggregate feeding area 4 is uniformly provided with 2-16 mineral powder feeding ports 42, the outer side of the mineral aggregate feeding area 4 is uniformly provided with 2-18 cold air ports 41 for introducing cooling gas and controlling the temperature of tail gas within a set range, and the inner part of the mineral aggregate feeding area 4 is provided with a slagging flux storage bin 43 and a slagging flux feeding mechanism 46.
Preferably, the control system 5 is composed of a hardware system and control software, and is electrically connected with the device through a sensor and a control component.
Preferably, the surface of the slagging flux pile 11 is concave arc surface.
In order to explain the position and connection relation of the device structure more specifically, the detailed explanation is given in conjunction with the method of using the device.
The use method of the device comprises the following steps:
step one, opening a slagging flux feeding port 44 through a control system 5, mixing slagging flux materials, then feeding the mixed materials into a slagging flux storage bin 43, and controlling a slagging flux feeding mechanism 46 to enable the slagging flux materials to enter a steel-making pool 1 from the slagging flux storage bin 43 to form a slagging flux pile 11 with the height of 1-3m at the bottom;
step two, drying the gas making raw material with the average grain diameter of less than 0.1mm until the moisture content is less than or equal to 1 wt%, and then filling the gas making raw material into a gas making raw material supply device;
step three, starting the gas making gun 21 through an ignition device of the gas making gun 21, and adjusting an oxygen supply device and a gas making raw material supply device to enable CO + H in the components of the gas made2>90% of temperature>1800℃；
Step four, drying the iron-containing powder until the moisture content is less than or equal to 1 wt.%, starting a mineral powder feeding port 42 for feeding, wherein the particle size of the iron-containing powder is less than 1mm, the average particle size is 0.074mm, and the TFe content of total iron is 50-70 wt.%;
fifthly, during the falling of the iron-containing powder in the device, the iron-containing powder and the reducing gas generated by the ascending gas making gun 21 are subjected to heat transfer and mass transfer reaction in the rapid reduction area 3 and then fall onto the surface of the slagging flux pile 11 in the steelmaking pool 1, and the unreduced part of the iron-containing powder in the rapid reduction area 3 is further reduced on the surface of the slagging flux pile 11 and the reducing gas generated by the gas making gun 21;
step six, finishing final reduction of the molten iron and the reducing gas, finishing impurity removal reaction with a slagging flux pile 11 to generate final slag, and then separating slag and steel;
and seventhly, discharging the molten steel and the slag liquid from the steel outlet 121 and the slag outlet 131 periodically, timely discharging the generated tail gas through a tail gas discharge port 45, and introducing cold gas into the tail gas through a cold gas port 41 to adjust the temperature of the tail gas.
Preferably, the surface of the slagging flux pile 11 in the first step is an inwards concave arc surface, and the reflowing steel slag mixture slowly flows from the top of the pile to the bottom of the pile along the arc surface under the action of gravity and reversely convects with the high-temperature reducing gas to carry out heat and mass exchange; when the steel slag flows downwards, the steel slag reacts with the slagging flux on the surface of the slagging flux pile 11 to remove impurities such as sulfur, phosphorus and the like in the molten steel and generate high-alkalinity final slag.
Preferably, the molten steel in the step seven is C: <0.5 wt.%, S: <0.02 wt.%, P: <0.02 wt.% of a crude steel; the binary alkalinity of the slag liquid is 1.3-2.0.
While the main reactions in the fast reduction zone are:
[FeO]+H2(g)＝[Fe]+H2O(g)
[FeO]+CO(g)＝[Fe]+CO2(g)
the main reactions in the slagging flux pile area are:
(SiO2)+2(CaO)＝(2CaO·SiO2)
[FeS]+(CaO)＝(CaS)+[FeO]
(P2O5)+4(CaO)＝(4CaO·P2O5)。
the smelting process of the utility model is carried out around the slag-forming flux pile in the steelmaking pool, and the slag-forming flux is sufficient and excessive in the whole smelting process; the impurities such as sulfur, phosphorus and the like and the acidic oxides which need to be removed complete various chemical reactions on the surface of the excessive slagging flux (alkaline oxide) pile to generate low-melting-point final slag, and the low-melting-point final slag is discharged out of the steel-making pool.
In the scheme, the iron-containing powder is directly used for steelmaking in a reducing atmosphere, the traditional process flow of coking, sintering and pelletizing of a blast furnace and a flash smelting method are abandoned, the iron-containing powder is directly used as a raw material and is subjected to partial reduction reaction with reducing gas in a rapid reduction zone, the rest is completed in a slagging flux pile, and impurity removal reactions such as desulfurization, dephosphorization and the like are completed at the same time, so that crude steel can be directly produced in a device with high efficiency, coke resources are not relied on, and the process of high energy consumption is reduced; does not need a large number of steel-making devices, occupies less land in factories and saves a large amount of capital investment.
The iron-containing powder is directly used for steelmaking in a reducing atmosphere, a gas making raw material needs to inject high-temperature reducing gas through a gas making gun, the high-temperature reducing gas directly acts on a slagging flux pile to provide heat for the slagging flux pile, lime melting is facilitated, the stagnation period is shortened, the slagging process is accelerated, and heat loss is low; then the high-temperature reducing gas rises through the rapid reducing region, and meets the falling iron-containing powder in a countercurrent way in the rapid reducing region, and simultaneously, the heat transfer and mass transfer reactions are carried out, the contact reaction is sufficient, and the reaction efficiency is high.
The iron-containing powder is directly steelmaking in a reducing atmosphere, a steelmaking pool is arranged at the bottom of a furnace body, molten iron and iron ore soft melts falling after reduction reaction fall on the surface of a slagging flux pile together, the unreduced part of the iron-containing powder in a rapid reduction area can be further reduced with high-temperature reducing gas to generate molten iron, finally, all iron oxides and the high-temperature reducing gas can be subjected to final reduction, and are subjected to impurity removal reactions such as dephosphorization and desulfurization with the slagging flux to generate final slag, so that slag and steel are separated, direct steelmaking can be realized in one device, a large amount of independent investment of steelmaking equipment is not needed, and the fund and the area of a site are greatly saved.
The utility model is based on the iron-containing powder integrated reduction in the rapid reduction area and the slagging flux pile, and the structure and the process of the direct steelmaking equipment are specially designed, so that a flow field and a temperature field which are beneficial to heat transfer and mass transfer in the device are created, and the aim of integrated direct steelmaking is fulfilled based on the slagging flux pile in the device under the reducing atmosphere.
While the foregoing is directed to the preferred embodiment of the present invention, it will be understood by those skilled in the art that various changes and modifications may be made without departing from the spirit and scope of the utility model as defined in the appended claims.
Claims (8)
1. A direct steelmaking device of iron-containing powder in reducing atmosphere is characterized by comprising a steelmaking pool, a gas making tower, a rapid reduction area, an ore feeding area and a control system;
wherein: the device comprises a steelmaking pool, a gas making tower, a control system and a device, wherein the steelmaking pool is arranged at the bottommost part of the device and comprises a slagging flux pile, a molten steel layer is arranged at the bottom of the slagging flux pile, a liquid slag layer is arranged on the molten steel layer, a rapid reduction area is arranged above the steelmaking pool, a gas making tower is arranged beside the lower part of the rapid reduction area, an ore material feeding area is arranged above the rapid reduction area, and the control system is arranged beside the steelmaking pool, the gas making tower, the rapid reduction area or the ore material feeding area and is electrically connected with the device through a sensor and a control part;
the slagging flux pile is a solid slagging flux material pile, and an air making gun and a reducing gas flow channel are arranged in the gas making tower.
2. The direct steelmaking device of iron-containing powder in a reducing atmosphere of claim 1, wherein the steelmaking pool is a cylinder or a polygonal prismatic cylinder, the upper part of the steelmaking pool is directly connected with the rapid reduction zone, one side of the molten steel layer of the steelmaking pool near the bottom is provided with a tap hole, and the other side of the liquid slag layer near the molten steel layer is provided with a tap hole.
3. Apparatus for the direct steelmaking in a reducing atmosphere of iron-containing powder as claimed in claim 1 in which the solid slagging flux heap is conical.
4. The direct steelmaking device of iron-containing powder in a reducing atmosphere as recited in claim 1, wherein said gas-generating tower is in the shape of a truncated cone or a truncated pyramid; the exterior of the gas making gun is connected with an oxygen supply device and a gas making raw material supply device; and the outlet of a reducing gas flow passage of the gas making tower is connected with the lower part of the rapid reduction area.
5. The apparatus for direct steelmaking in a reducing atmosphere containing iron fines as claimed in claim 4 wherein the reducing gas flow channel is flared with a downward inclination from the horizontal of 30 ° -60 °; the inclination angle with the centripetal axis is 1-16 degrees for right inclination in the northern hemisphere and 1-16 degrees for left inclination in the southern hemisphere.
6. The direct steelmaking device of iron-containing powder in a reducing atmosphere as recited in claim 1, wherein said rapid reduction zone structure is a variable cross-section cylinder or polygonal cylinder with a thin middle and thick upper and lower ends; the lower part of the rapid reduction zone is provided with at least 3 gas making towers along the circumference, and the upper part of the rapid reduction zone is provided with at least 2 cooling gas ports.
7. The direct steelmaking device of iron-containing powder in a reducing atmosphere according to claim 1, wherein the ore charging area is of a frustum shape with a large bottom and a small top, and a tail gas discharge port is formed in the central part of the top of the ore charging area; the outside in mineral aggregate input area evenly is provided with 2 at least powdered ore input openings, the inside in mineral aggregate input area is provided with slagging flux storage storehouse and slagging flux input mechanism.
8. The apparatus of claim 1 for direct steelmaking from iron-containing powder in a reducing atmosphere, wherein the slagging flux stack surface is concave.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121859822.7U CN216445405U (en) | 2021-08-10 | 2021-08-10 | Direct steelmaking device of iron-containing powder in reducing atmosphere |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202121859822.7U CN216445405U (en) | 2021-08-10 | 2021-08-10 | Direct steelmaking device of iron-containing powder in reducing atmosphere |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN216445405U true CN216445405U (en) | 2022-05-06 |
Family
ID=81346952
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202121859822.7U Active CN216445405U (en) | 2021-08-10 | 2021-08-10 | Direct steelmaking device of iron-containing powder in reducing atmosphere |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN216445405U (en) |
-
2021
- 2021-08-10 CN CN202121859822.7U patent/CN216445405U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN110423854B (en) | Electric energy full-hydrogen flash reduction direct steelmaking system and process | |
| CN110438277B (en) | Cyclone flash reduction direct steelmaking system and process | |
| CN108374067B (en) | A kind of device and method of reduction direct steelmaking at full speed | |
| CN102337369B (en) | High-wind-temperature rotational flow injection disturbance melting reduction and prereduction combination device and method | |
| CN112410494B (en) | Iron-making device and method capable of applying suspension melting reduction of fine-grained fine ores | |
| WO2010072043A1 (en) | Smelting vessel, steel making plant and steel production method | |
| CN210215430U (en) | Zero-carbon-emission steelmaking equipment | |
| CN101260448A (en) | Fusion reduction iron-smelting method for directly using concentrate powder | |
| CN111705225A (en) | Method and device for preparing nickel matte | |
| CN101696460B (en) | Process and device for dual continuous steel making with iron-containing material rotary hearth furnace | |
| CN106086281B (en) | A kind of flash ironmaking and the integrated apparatus and method of coal gas | |
| CN201351168Y (en) | Iron-contained material continuous steelmaking device | |
| CN101956038B (en) | Process method and device for performing lower-carbon ironmaking and steelmaking through melting reduction of iron ore | |
| CN1073630C (en) | Coal oxygen fused reduction iron-smelting method and apparatus | |
| CN101956035B (en) | Iron-containing material slag bath smelting reduction steelmaking technical method and device | |
| CN112391507B (en) | Improved flash smelting reduction iron-making device and method | |
| CN102127610B (en) | Ironmaking equipment and process for direct smelting reduction of iron ore | |
| CN216445405U (en) | Direct steelmaking device of iron-containing powder in reducing atmosphere | |
| CN109207664A (en) | Coal, gas integral flash iron-smelting furnace and its technique | |
| CN217459482U (en) | Flash is smelted and is used improved blast furnace | |
| CN113789420B (en) | Direct steelmaking device for iron-containing powder in reducing atmosphere and using method | |
| CN102181776A (en) | Technique and device for producing high-grade nickel and stainless steel by reduction pelletization | |
| CN202063976U (en) | Equipment for producing high manganese-silicon by low-grade ferromanganese ore | |
| CN109536662B (en) | Rotary kiln gas-based reduction-total oxygen molten pool smelting iron-making device | |
| CN113355487A (en) | Magnesium-free mineral phase reconstruction agent, preparation method thereof and converter steelmaking slagging method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |