CN215638755U - Smelting equipment - Google Patents
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- CN215638755U CN215638755U CN202122207417.3U CN202122207417U CN215638755U CN 215638755 U CN215638755 U CN 215638755U CN 202122207417 U CN202122207417 U CN 202122207417U CN 215638755 U CN215638755 U CN 215638755U
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Abstract
The embodiment of the utility model discloses smelting equipment, which comprises a smelting furnace and a high-energy jet gun, wherein the high-energy jet gun is arranged on the wall of the smelting furnace, and the distance between the installation position of the high-energy jet gun and the bottom of the smelting furnace is not less than a threshold distance. According to the smelting equipment provided by the embodiment of the utility model, the high-energy jet gun is arranged on the wall of the smelting furnace, and the distance between the installation position of the high-energy jet gun and the bottom of the smelting furnace is not less than the threshold distance, so that the air port of the smelting furnace is higher than the melt liquid level in the smelting furnace during smelting, the melt is prevented from flowing backwards or blocking the high-energy jet gun, and the smelting efficiency is improved.
Description
Technical Field
The utility model relates to the technical field of metal smelting, in particular to smelting equipment and a smelting method.
Background
The side-blown smelting technology in the copper smelting technology in the world is favored because of investment saving and low cost, and the tuyere of the existing smelting furnace adopting the side-blown technology is generally low and is positioned below the liquid level of a melt during smelting, so that once the wind pressure is insufficient or the wind is stopped, the melt is easy to flow backwards to block a spray gun, and the spray gun needs to be manually cleaned after being blocked, thereby not only increasing the labor intensity of workers, but also influencing the operation rate.
SUMMERY OF THE UTILITY MODEL
In order to solve or at least partially solve the technical problem, the utility model provides a smelting device and a smelting method.
In a first aspect, the utility model provides a smelting apparatus comprising a smelting furnace and a high-energy jet gun, wherein the high-energy jet gun is arranged on a furnace wall of the smelting furnace, and the distance between the installation position of the high-energy jet gun and the bottom of the smelting furnace is not less than a threshold distance.
Further, when the smelting equipment works, the height of the high-energy jet gun is 500-2000 mm higher than the liquid level of the melt in the smelting furnace.
Further, a plurality of high-energy jet guns are arranged on at least one furnace wall of the smelting furnace.
Further, the muzzle of the high-energy jet gun is inclined obliquely downward and toward the bottom of the smelting furnace.
Furthermore, the jet direction of the high-energy jet gun and the furnace wall of the smelting furnace form an included angle of 30-55 degrees.
Further, the high-energy jet gun is provided with a detachable protective water jacket.
Further, a secondary blast hole is formed in the top of the smelting furnace.
Further, the high-energy jet gun comprises: the main flow channel is arranged in the main body, and the branch flow channel is positioned at the periphery of the main flow channel, wherein the main flow channel has a Laval structure.
Further, the branch channel also adopts a Laval structure.
Further, the high-energy jet gun is arranged at a height of 1200mm from the upper part of the melt level.
Further, the high-energy jet gun comprises: the main flow channel is arranged in the main body, and the branch flow channel is positioned at the periphery of the main flow channel, wherein the main flow channel has a Laval structure.
Further, the branch channel also adopts a Laval structure.
Further, the high-energy jet gun is arranged at a height of 1200mm from the upper part of the slag layer.
In a second aspect, the present invention also provides a smelting process comprising:
mixing materials required by smelting, and adding the mixed materials into a smelting furnace from a charging opening of the smelting furnace;
mounting a high-energy jet gun on the height of a furnace wall, wherein the distance between the interior of a smelting furnace and the bottom of the smelting furnace is not less than a threshold distance;
oxygen-enriched air is blown in through a high-energy jet gun, so that the material reacts with oxygen in the material to generate a target metal melt.
Further, the installation of the high-energy jet gun on the height of the furnace wall, wherein the distance between the interior of the smelting furnace and the bottom of the smelting furnace is not less than a threshold distance, specifically comprises:
calculating the maximum height of the melt liquid level after the material is smelted through the capacity according to the amount of the material added into the smelting furnace;
and installing the high-energy jet gun on the furnace wall with the maximum height 500-2000 mm higher than the melt liquid level according to the maximum height of the melt liquid level.
Further, the smelting method further comprises the following steps:
air or oxygen-enriched air is blown from a secondary tuyere at the top of the furnace.
According to the smelting equipment and the smelting method provided by the embodiment of the utility model, the high-energy jet gun is arranged on the wall of the smelting furnace, and the distance between the installation position of the high-energy jet gun and the bottom of the smelting furnace is not less than the threshold distance, so that the air port of the smelting furnace is higher than the liquid level of the melt in the smelting furnace during copper smelting, the melt is prevented from flowing backwards or blocking the high-energy jet gun, and the working efficiency of metal smelting is improved.
Drawings
In order to more clearly illustrate the embodiments of the present invention, a brief description of the relevant drawings will be given below. It is to be understood that the drawings in the following description are only intended to illustrate some embodiments of the utility model, and that a person skilled in the art may also derive from these drawings many other technical features and connections etc. not mentioned herein.
FIG. 1 is a schematic cross-sectional view of a smelting plant according to a first embodiment of the present invention;
FIG. 2 is a schematic cross-sectional view of a smelting apparatus in operation according to a first embodiment of the present invention;
FIG. 3 is a schematic view in partial cross-section of a smelting plant according to a first embodiment of the present invention;
FIG. 4 is a process flow diagram of a smelting process according to a second embodiment of the present invention;
FIG. 5 is a further process flow diagram of a smelting process according to a second embodiment of the present invention;
FIG. 6 is a further process flow diagram of a smelting process according to a second embodiment of the present invention.
Description of reference numerals:
10. a smelting furnace; 20. a high energy jet gun; 110. a furnace wall; 120. the bottom of the furnace; 30. a matte layer; 40. a slag layer; 50. a protective water jacket; 210. a muzzle; 130. the top of the furnace; 1301. a secondary tuyere; 1302. a feed inlet; 140. a slag discharge chamber; 150. a slag discharge port; 160. a water-cooled partition wall; 170. a flue; 180. a matte discharge port; 190. and connecting the chute.
Detailed Description
The present application will be described in detail below with reference to the accompanying drawings.
Referring to fig. 1, a schematic cross-sectional view of a smelting apparatus according to a first embodiment of the present invention includes a smelting furnace 10 and a high-energy jet lance 20, the high-energy jet lance 20 is disposed on a furnace wall 110 of the smelting furnace 10, and a distance L between an installation position of the high-energy jet lance 20 and a furnace bottom 120 of the smelting furnace 10 is not less than a threshold distance.
In particular, the shape of the melting furnace 10 is not limited thereto, and may be a shape structure that is relatively common in the art, including the furnace bottom 120 and the furnace wall 110 that is enclosed above the outer periphery of the furnace bottom 120. In the conventional smelting furnace that adopts the side-blown technique, the mounting height of high energy jet gun 20 is generally lower, and when carrying out the copper metallurgy, the fuse-element liquid level can submerge the muzzle of high energy jet gun 20, must rely on the blast air that powerful wind pressure lasts this moment, just can avoid the fuse-element to flow backward and block up the spray gun, in case the wind pressure is not enough or stop the blast air, the fuse-element in the smelting furnace 10 becomes flow backward extremely in the high energy jet gun 20, leads to blockking up the spray gun. In the embodiment of the present invention, although the high-energy jet lance 20 is also disposed on the furnace wall 110, the distance L between the installation position of the high-energy jet lance 20 and the bottom 120 of the smelting furnace 10 is not less than a threshold distance, that is, the installation height of the high-energy jet lance 20 is high, and when the smelting furnace 10 is in operation, the height of the melt level in the smelting furnace 10 is below the muzzle of the high-energy jet lance 20, so that the melt can be effectively prevented from flowing backwards or blocking the spray gun of the high-energy jet lance, the trouble caused by manual cleaning can be reduced, and the working efficiency of smelting can be improved.
It is to be noted here that the distance L between the installation position of the high energy jet lance 20 and the bottom 120 of the smelting furnace 10 is not less than the threshold distance, i.e. the distance L is greater than or equal to the threshold distance, and the size of the threshold distance may be any value of 800 to 2800 mm. Here, the threshold distance may be suitably varied according to the specific specifications of the smelting furnace 10, including but not limited to the volume, the bottom area of the smelting furnace 10, the conversion rate of the material within the smelting furnace 10, and the like.
Additionally, in an embodiment of the present invention, the high-energy jet gun 20 may include: the main flow channel is arranged in the main body, and the branch flow channel is positioned at the periphery of the main flow channel, wherein the main flow channel has a Laval structure. Still further, the branch passages may also adopt a laval structure. The laval structure refers to a structure in which the aperture of the duct gradually decreases from the rear end to the front end, then remains unchanged, and finally gradually increases. The Laval structure can change the speed of the airflow due to the change of the area of the channel, so that the airflow is accelerated from subsonic speed to sonic speed to supersonic speed. The high energy jet lance 20 has a longer jet length, more concentrated jet, and much lower momentum decay than conventional supersonic jets, relative to conventional supersonic gas flow. The jet flow of the high-energy jet flow gun 20 is injected into the melt in a laser beam-like mode, so that the splashing is small, the penetrating capability is strong, and the oxygen utilization rate is higher.
Further, please refer to fig. 2, which is a schematic sectional structure diagram of a melting apparatus provided in a first embodiment of the present invention during operation, wherein when the melting apparatus operates, the height of the high energy jet lance 20 is 500 to 2000mm higher than the liquid level of the melt in the melting furnace 10.
Specifically, when the smelting equipment works, materials put into the smelting furnace 10 are melted into liquids, and the liquids are layered under the action of gravity, taking copper-containing materials as an example, the copper-containing materials mainly comprise a matte layer 30 located at the bottom layer and a slag layer 40 located at the upper layer, wherein the slag layer 40 floats above the matte layer 30, the surface of the slag layer 40 is the melt liquid level, that is, the installation height of the high-energy jet gun 20 is 500-2000 mm higher than the surface of the slag layer 40. When the smelting furnace 10 works, if reaction or boiling occurs, objects in the slag layer 40 can not enter the mouth of the high-energy jet gun 20 due to the height difference of 500-2000 mm, and the spray gun is prevented from being blocked.
More closely, the high-energy jet lance 20 is arranged at a height of 1200mm above the melt level. That is, the high-energy jet gun 20 sets up the position and is in on the slag layer 40, specifically for being higher than the surface 1200mm department of slag layer 40, so the design can guarantee that the object in the slag layer 40 can not get into in the muzzle of high-energy jet gun 20 when receiving the air current impact and probably taking place to splash, avoids blockking up the spray gun.
In addition, in other preferred embodiments of the present invention, a plurality of the high energy jet guns 20 are provided on at least one wall of the melting furnace 10.
Specifically, in order to improve the smelting efficiency of the copper smelting equipment and promote rapid reaction of the materials in the smelting furnace 10, a plurality of high-energy jet guns 20 are simultaneously arranged on the furnace wall 10 of the smelting furnace 10, the high-energy jet guns 20 are arranged at intervals and simultaneously blast the slag layer 40 in the smelting furnace 10, and jet gas ejected from the high-energy jet guns 20 can penetrate into the slag layer 40. It is further noted here that the smelting furnace 10 may be provided with the high-energy jet guns 20 on one or both furnace walls, i.e. the high-energy jet guns 20 are provided on at least one wall of the smelting furnace 10.
Further, the muzzle 210 of the high energy jet lance 20 is inclined obliquely downward and towards the bottom 120 of the smelting furnace 10.
Specifically, referring to fig. 3, which is a schematic partial sectional view of a smelting plant according to a first embodiment of the present invention, the high-energy jet lance 20 penetrates through the furnace wall 110, the lance opening 210 is formed in the furnace wall 110, and the lance opening 210 is inclined obliquely downward and faces the bottom 120 of the smelting furnace 10, so that air or oxygen-enriched air blown out from the lance opening 210 can directly face the slag layer 40 material in the smelting furnace 10 to increase the reaction speed thereof.
Furthermore, the jet direction of the high-energy jet gun 20 forms an included angle of 30-55 degrees with the furnace wall 110 of the smelting furnace 10.
Specifically, the muzzle 210 of the high-energy jet gun 20 is inclined obliquely downward, so that an included angle is formed between the muzzle 210 and the furnace wall 110, which is referred to as an included angle α, and the included angle α is an included angle between the jet direction of the high-energy jet gun 20 and the furnace wall 110 of the smelting furnace 10. As the height of the high-energy jet flow gun 20 is 500-2000 mm higher than the liquid level of the melt in the smelting furnace 10, air or oxygen-enriched air blown out from the muzzle 210 of the high-energy jet flow gun 20 can be properly blown to the material of the slag layer 40 in the smelting furnace 10 to improve the smelting efficiency, and the included angle alpha is 30-55 degrees.
In addition, in order to protect the high-energy jet gun 20 from the damage of splashed molten metal, the high-energy jet gun 20 is provided with a detachable protective water jacket 50, wherein the protective water jacket 50 can effectively protect the high-energy jet gun 20, and meanwhile, the protective water jacket 50 is detachably connected to the muzzle 210 on the furnace wall 110 of the smelting furnace 10, so that the installation, the detachment and the replacement of the muzzle are convenient.
In addition, in other preferred embodiments of the present invention, the height of the high-energy jet lance 20 on the furnace wall 110 is adjustable, that is, a plurality of muzzles 210 are arranged along the height direction of the furnace wall 110, and in practical use, the muzzles 210 with different heights can be selected according to the amount of the material put into the smelting furnace 10 to arrange the high-energy jet lance 20, because the melt level height below the material put into the smelting furnace 10 is different, and further, by arranging the high-energy jet lance 20 at a proper height, the melt level in the smelting furnace 10 is ensured to be below the muzzle of the high-energy jet lance 20, so that the melt can be effectively prevented from flowing backwards or blocking the lance of the high-energy jet lance, the trouble caused by manual cleaning is reduced, and the working efficiency of smelting is improved.
Further, a secondary tuyere 1301 is provided in the roof portion 130 of the melting furnace 10.
In particular, a plurality of secondary tuyeres 1301 are provided on the furnace roof 130, which communicate with the high energy jet lances 20 or are connected to separate blast devices for blowing air or oxygen enriched air into the smelting furnace 10. By the design, the blast efficiency of the smelting furnace 10 can be increased, the reaction speed of copper smelting materials in the smelting furnace 10 is increased, the smelting efficiency is increased, meanwhile, top secondary blast can react with harmful combustible gas generated by oxygen-enriched air and the materials in the smelting furnace 10 during reaction, and the gas emission of the smelting furnace 10 is safer while the heat is efficiently utilized.
In addition, the smelting furnace 10 further comprises a slag discharging chamber 140 arranged at one end of the furnace body, the furnace top 130 above the slag discharging chamber 140 is provided with a slag discharging port 150, the slag discharging chamber 140 is separated from the other end of the furnace body through a water-cooling partition wall 160, the water-cooling partition wall 160 is internally cooled by a copper water jacket, the outside is covered by a refractory material for heat insulation, and the water-cooling partition wall 16 has a distance with the furnace bottom 120 of the furnace body, namely, the slag discharging chamber 140 and the furnace body at the other end of the smelting furnace 10 are mutually communicated at the lower part of the furnace body and are on the same horizontal plane, so that the accommodating volume of the smelting furnace 10 can be increased, and the structural design is more reasonable.
In use, slag generated after reaction of the smelting material in the smelting furnace 10 floats at the uppermost end and is discharged through the slag discharge port 150, and fumes generated during the reaction of the smelting material are discharged to the outside of the smelting furnace 10 through a flue 170 provided on the roof 130 of the furnace body of the smelting furnace 10.
In addition, a plurality of feed openings 1302 are provided in the furnace roof 130, through which feed openings 1302 the copper-bearing solid matter can be fed into the smelting furnace 10. In addition, in order to improve the uniformity of the copper-containing solid material charged into the smelting furnace 10, the plurality of feed openings 1302 are generally uniformly distributed on the top 130 of the furnace, and the plurality of feed openings 1302 may be selected to be charged separately during charging.
Furthermore, the copper-containing solid materials include copper concentrate, quartz flux, lump coal and other materials, and partial unreacted elemental sulfur and CO generated by incomplete combustion of the lump coal in the smelting furnace 10 escape from the melt and are completely reacted to generate SO2 and CO2 flue gas after contacting with air blown from a secondary tuyere and are discharged from the flue 170.
The number N of the smelting high-energy jet guns is determined according to the oxygen consumption required by the reaction, and the specific calculation formula is as follows:
the method comprises the following steps of N ═ Kx (QCu + QFe + QS + QF)/(qxeta), wherein K is a correction coefficient, the value of the correction coefficient K is within the range of 0.9-1.1, QCu is the theoretical oxygen consumption required by the oxidation reaction of copper elements in furnace slag, QFe is the theoretical oxygen consumption required by the slagging reaction of iron elements in copper matte, QS is the theoretical oxygen consumption required by the reaction of sulfur elements in flue gas, QF is the theoretical oxygen consumption required by the combustion reaction of fuel, q is the air supply quantity of a single nozzle, eta is the oxygen-enriched concentration, and the oxygen-enriched concentration is 60-90%.
The proper number of high-energy jet guns can be arranged to ensure that the materials and the oxygen fully react to generate the high-grade matte.
Furthermore, the energy of the high-energy jet gun is more concentrated and can be injected into the melt, so that the oxygen utilization rate is improved, and meanwhile, the splashing is reduced. On the basis, the spray gun can be far away from the liquid level of the molten pool, the spray gun is prevented from being blocked by the melt, the operation rate is improved, and high-grade copper matte is produced.
In addition, a matte discharging port 180 and a connecting chute 190 are further arranged at the other end of the smelting furnace 10 opposite to the deslagging chamber 140, specifically, the matte discharging port 180 is arranged at the furnace bottom 120, one end of the matte discharging port 180 is communicated with the matte layer 30 in the smelting furnace 10, the other end of the matte discharging port is communicated with the connecting chute 190, the connecting chute 190 is higher than the furnace bottom 120, the other end of the connecting chute 190 is connected with a pipeline of a next process of the copper smelting equipment, the copper smelting materials react in the smelting furnace 10 to generate the corresponding matte layer 30, and the matte at the lower part of the smelting furnace 10 is discharged to the next process of the copper smelting equipment through the matte discharging port 180 and the connecting chute 190 in a siphoning manner.
Example 2
Referring to fig. 4, a flow chart of a smelting method according to a second embodiment of the present invention is shown, the smelting method including:
step S100, mixing materials required for smelting, and adding the mixed materials into a smelting furnace from a charging hole of the smelting furnace;
step S200, mounting the high-energy jet gun on the height of a furnace wall, wherein the distance between the interior of the smelting furnace and the bottom of the smelting furnace is not less than a threshold distance;
and step S300, blowing oxygen-enriched air through the high-energy jet gun so as to enable the material to react with oxygen in the material to generate a target metal melt.
Specifically, in the embodiment of the present invention, a copper-containing material is added, and a copper smelting method is taken as an example, in step S100, a material containing copper concentrate, a quartz agent and lump coal is mixed and then added into a smelting furnace body from a charging port of the smelting furnace, wherein the usage amount of quartz sand is in a range from 2: 1 the addition is controlled to meet the material reaction conditions.
The step S100 is carried out, in the step S200, the high-energy jet gun is installed on the height of the furnace wall, wherein the distance between the interior of the smelting furnace and the bottom of the smelting furnace is not less than the threshold distance, namely the high-energy jet gun is installed on the furnace wall of the smelting furnace, wherein the distance between the installation position of the high-energy jet gun and the bottom of the smelting furnace is greater than or equal to the threshold distance, namely the installation height of the high-energy jet gun is higher, when the smelting furnace works, the height of the melt liquid level in the smelting furnace is below the muzzle of the high-energy jet gun, the situation that the melt flows backwards or blocks the spray gun of the high-energy jet gun can be effectively avoided, the trouble caused by manual cleaning is reduced, and the working efficiency of copper smelting is improved.
Specifically, referring to fig. 5, in a flowchart of another method of a content material smelting method according to a second embodiment of the present invention, step S200 is to install a high-energy jet gun on a furnace wall height at which a distance between a smelting furnace and a bottom of the smelting furnace is not less than a threshold distance, and specifically includes:
step S210, calculating the maximum height of the melt liquid level after the material is smelted through the productivity according to the amount of the material added into the smelting furnace;
and S220, mounting the high-energy jet gun on the furnace wall with the maximum height 500-2000 mm higher than the melt liquid level according to the maximum height of the melt liquid level.
Firstly, calculating the thickness required by the matte and the slag layer after reaction by a productivity calculation formula according to the amount of materials added into the smelting furnace, thereby determining the maximum height of the liquid level of the melt; then, install the high-energy jet gun on the lateral wall of smelting furnace, the installation angle of high-energy jet gun is: forming an included angle of 30-55 degrees with the furnace wall and facing the direction of the bottom of the smelting furnace; the mounting height of the high-energy jet gun is as follows: 500-2000 mm above the maximum height from the melt level.
After the high-energy jet gun is installed on the side wall of the smelting furnace in the step S200, oxygen-enriched air or air containing 60-85% of oxygen is blown into the smelting furnace through the high-energy jet gun in the step S300, the oxygen-enriched air is jetted into a melt, the material and the oxygen react rapidly to generate copper matte containing 70-75% of copper and sink to the lower part of the smelting furnace body, and the copper matte at the lower part of the smelting furnace body is discharged to the next procedure through a connecting chute in a siphoning mode.
Further, please refer to fig. 6, which is a flowchart of a smelting method according to a second embodiment of the present invention, wherein the smelting method further includes:
and S400, blowing air or oxygen-enriched air from a secondary tuyere at the top of the smelting furnace.
Specifically, after the high-energy jet gun is mounted on the side wall of the smelting furnace or when oxygen-enriched air or air is blown in through the high-energy jet gun, air or oxygen-enriched air is blown in through a secondary air port arranged at the top of the smelting furnace, so that the blowing efficiency of the smelting furnace can be increased, the reaction speed of copper smelting materials in the smelting furnace is increased, the smelting efficiency is improved, meanwhile, oxygen can be made to react with harmful gas generated by the materials in the smelting furnace during reaction, and the gas emission of the smelting furnace is safer.
Wherein the smelting temperature is 1200-1250 ℃, and the blowing rates of the high-energy jet gun and the secondary tuyere can be respectively 450-550m/s and 20-60 m/s.
The matte and the smelting slag generated after the smelting reaction can be naturally layered due to different specific gravities, the specific gravity of the slag slightly floats above the melt, enters a slag chamber through a water-cooling partition wall, and then is continuously overflowed and discharged through a slag discharge port. The matte has high specific gravity, is deposited at the bottom of the smelting furnace body and is continuously discharged to the next working procedure through a matte discharge port in a siphoning mode.
The smelting method provided by the embodiment of the utility model is illustrated by a plurality of specific application examples.
Example 3
The following materials are put into a smelting furnace: 92.4% of mixed copper concentrate, 3.33% of slag concentrate, 0.6% of converting slag, 0.36% of smoke dust, 2.86% of quartz sand, 0.3% of lump coal and 0.15% of other return materials. Wherein the mixed copper concentrate contains 21 percent of copper, 27 percent of sulfur and 27 percent of iron, and enters a smelting furnace through a charging hole at the top of the smelting furnace after being transported by a rubber belt, and the total feeding amount is 200 t/h.
The total thickness of the matte layer and the slag layer is 1500mm, the high-energy jet gun is arranged at a height 1200mm away from the upper part of the slag layer, the angle between the high-energy jet gun and the furnace wall is 45 degrees, and oxygen-enriched air containing 80 percent of oxygen is blown in through the high-energy jet gun.
The sulfur and iron in the material and oxygen have strong oxidation reaction, and the reaction temperature is 1200 ℃. A large amount of chemical reaction heat is released in the chemical reaction to maintain heat balance, when the heat is insufficient, the heat is supplemented by the combustion heat of the lump coal, part of unreacted elemental sulfur and CO generated by incomplete combustion of the lump coal escape out of the melt, and the unreacted elemental sulfur and the CO completely react with air blown in from the secondary air port to generate SO2 and CO2 which enter the flue gas. The high-grade matte containing 75% of copper is produced after the reaction, the product ferrous oxide of the reaction of iron and oxygen reacts with quartz sand to generate smelting slag, the copper content of the smelting slag is 2.5%, and the iron-silicon ratio in the slag is 2.0. The matte and the smelting slag generated after the smelting reaction can be naturally layered due to different specific gravities, the specific gravity of the slag slightly floats above the melt, and the slag enters a slag chamber through a water-cooling partition wall for discharging.
The high-grade matte has high specific gravity, is deposited at the bottom of the furnace body, is continuously discharged through a matte discharge port in a siphon mode and enters the next working procedure.
Example 4
The following materials are put into a smelting furnace: 90% of mixed copper concentrate, 3.5% of slag concentrate, 0.5% of converting slag, 0.4% of smoke dust, 2.9% of quartz sand, 0.3% of lump coal and 0.15% of other return materials. Wherein the mixed copper concentrate contains 20.5 percent of copper, 26 percent of sulfur and 27 percent of iron, and enters the smelting furnace through a charging hole at the top of the smelting furnace after being transported by a rubber belt, and the total feeding amount is 150 t/h.
The total thickness of the matte layer and the slag layer is 1200mm, the high-energy jet gun is arranged at the height of 1000mm away from the upper part of the slag layer, the angle between the high-energy jet gun and the furnace wall is 35 degrees, and oxygen-enriched air containing 75 percent of oxygen is blown in through the high-energy jet gun.
Under the smelting reaction temperature of 1220 ℃, sulfur and iron in the materials and oxygen undergo a strong oxidation reaction, and high-grade matte containing 70% of copper is produced after the reaction.
The high-grade matte has high specific gravity, sinks at the bottom of the furnace body, is continuously discharged through a matte discharge port in a siphoning mode, and enters the next procedure
Example 5
The following materials are put into a smelting furnace: 85% of mixed copper concentrate, 3.5% of slag concentrate, 0.43% of converting slag, 0.4% of smoke dust, 2.9% of quartz sand, 0.3% of lump coal and 0.15% of other return materials. Wherein the mixed copper concentrate contains 20% of copper, 25% of sulfur and 26% of iron, and enters the smelting furnace through a charging hole at the top of the smelting furnace after being transported by a rubber belt, and the total feeding amount is 200 t/h.
The total thickness of the matte layer and the slag layer is 1600mm, the high-energy jet gun is arranged at the height of 1000mm away from the upper part of the slag layer, the high-energy jet gun and the furnace wall form an angle of 55 degrees, and oxygen-enriched air containing 85 percent of oxygen is blown in through the high-energy jet gun.
At the reaction temperature of 1250 ℃, sulfur and iron in the materials and oxygen undergo continuous and strong oxidation reaction, and high-grade matte containing 75 percent of copper is produced after the reaction.
The high-grade matte has high specific gravity, is deposited at the bottom of the furnace body, is continuously discharged through a matte discharge port in a siphon mode and enters the next working procedure.
The copper-containing material can be copper concentrate, and can also be copper-containing waste residues and waste materials; although the examples of the present application are described with reference to copper-containing materials. It will be appreciated by those skilled in the art that the teachings of the present application are equally applicable to the processing and production of other metal-containing materials. That is, in addition to being suitable for copper-containing materials, other metal-containing materials, such as lead-containing, tin-containing, noble metal-containing, and the like, may also be used.
Finally, it should be noted that those skilled in the art will appreciate that embodiments of the present application present many technical details for the purpose of enabling the reader to better understand the present application. However, the technical solutions claimed in the claims of the present application can be basically implemented without these technical details and various changes and modifications based on the above-described embodiments. Accordingly, in actual practice, various changes in form and detail may be made to the above-described embodiments without departing from the spirit and scope of the present application.
Claims (10)
1. The smelting equipment is characterized by comprising a smelting furnace and a high-energy jet gun, wherein the high-energy jet gun is arranged on the wall of the smelting furnace, and the distance between the installation position of the high-energy jet gun and the bottom of the smelting furnace is not less than a threshold distance.
2. The smelting plant according to claim 1, wherein the high energy jet lance is positioned 500 to 2000mm above the melt level in the smelting furnace when the smelting plant is in operation.
3. Smelting apparatus according to claim 2, wherein said high energy jet lances are positioned 1200mm above the melt level in said smelting furnace when the smelting apparatus is in operation.
4. Smelting plant according to claim 1, characterized in that a plurality of said high energy jet lances are provided on at least one furnace wall of the smelting furnace.
5. Smelting plant according to claim 1, characterized in that the muzzle of the high energy jet lance is inclined obliquely downwards and towards the bottom of the smelting furnace.
6. The smelting apparatus according to claim 5, wherein the high energy jet lance has a jet direction that is at an angle of 30 to 55 degrees to the wall of the smelting furnace.
7. Smelting plant according to claim 5, characterized in that the high-energy jet lance is provided with a detachable protective water jacket.
8. The smelting plant according to claim 1, characterized in that the roof of the smelting furnace is provided with secondary tuyeres.
9. Smelting apparatus as claimed in any one of claims 1 to 8, wherein said high energy jet lance comprises: the main flow channel is arranged in the main body, and the branch flow channel is positioned at the periphery of the main flow channel, wherein the main flow channel has a Laval structure.
10. Smelting plant according to claim 9, wherein said branch passages are also of laval construction.
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CN202122207417.3U CN215638755U (en) | 2021-09-13 | 2021-09-13 | Smelting equipment |
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CN202122207417.3U CN215638755U (en) | 2021-09-13 | 2021-09-13 | Smelting equipment |
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