CN212713622U - System for smelting scrap steel by utilizing once-combustion heat energy - Google Patents
System for smelting scrap steel by utilizing once-combustion heat energy Download PDFInfo
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- CN212713622U CN212713622U CN202020919976.XU CN202020919976U CN212713622U CN 212713622 U CN212713622 U CN 212713622U CN 202020919976 U CN202020919976 U CN 202020919976U CN 212713622 U CN212713622 U CN 212713622U
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Abstract
A system for smelting scrap steel by utilizing once combustion heat energy belongs to the field of metallurgy and comprises a feeding system, a furnace body, a pipeline reactor, a dust remover, an air inlet pipe, a variable-frequency draught fan, a chimney, a liftable heat-preservation cover, a storage bin, a fine-adjustment tundish and a steel ladle. The utility model utilizes the heat energy of one-time combustion to melt and preheat the scrap steel and heat the molten steel, and provides heat energy for the whole smelting continuous casting link, thereby improving the heat efficiency of scrap steel steelmaking and reducing the emission of carbon dioxide; pollutants such as sulfur, nitrate, dioxin, heavy metals and the like are removed by an activated carbon adsorption technology, so that the once-combustion heat energy scrap steel smelting process becomes an energy-saving and environment-friendly green smelting process; the utility model has the advantages of less smoke and less heat taken away when the steelmaking furnace is in the total oxygen combustionThe quantity is small, the energy utilization rate is high, the energy-saving and emission-reducing effects are obvious, and the energy consumption in the smelting link is only about 30 percent of that of the traditional electric furnace smelting; CO 22The emission is less than one third of the emission of electric arc furnace smelting and less than 10% of the emission of long-process smelting, and the emission reduction effect is obvious.
Description
Technical Field
The utility model belongs to the metallurgical field, in particular to utilize one shot burning heat energy to smelt steel scrap system.
Background
At present, two main methods for steel smelting are available: one is a long process, which comprises the working procedures of mining, ore dressing, sintering, blast furnace ironmaking, converter steelmaking, refining, continuous casting and the like; the other is a short process, which comprises the procedures of melting, refining, continuous casting and the like in an electric arc furnace or an intermediate frequency furnace. Influenced by the factors of increasing discharge pressure and steel scrap resources, the short process is favored by the industry.
The scrap steel making process is an industry with the largest heat energy consumption, the short-flow process favored at present has huge electricity consumption every year, and with the continuous popularization of the process, the capacity of electric furnace steel in China can reach 2 hundred million tons at the end of the next year, although the short-flow process is continuously improved, the electricity consumption for smelting the whole scrap steel is over 400 degrees per ton of steel, if auxiliary energy is added, the total energy consumption is over 600 degrees per ton of steel, namely the electricity consumption of the industry is over 800 hundred million degrees. According to the current power generation level and smelting equipment level of China, the energy utilization rate of short-process smelting pure steel scrap is not more than 30%, the short-process smelting process wastes a large amount of electric energy and consumes a large amount of graphite electrodes with high energy consumption, the average consumption level of the current pure steel scrap smelting electrodes is about 4 kilograms per ton of steel, the consumption increases the steel-making cost by about 200-300 yuan and almost exceeds the electricity consumption cost, if the energy consumption is converted into capital, the power consumption is equivalent to 800 hundred million DEG C, and if the energy consumption is considered in the energy conversion rate of steel-making, the energy utilization rate of the short-process smelting steel scrap is not more than 15%. Therefore, the short-process steel scrap smelting process has the problems of high energy consumption, high cost and low conversion rate, and is an unreasonable energy utilization mode.
SUMMERY OF THE UTILITY MODEL
In order to solve the problems of high energy consumption and low conversion rate of short-process scrap steel smelting, the utility model provides a scrap steel smelting system by utilizing one-time combustion heat energy, which utilizes one-time combustion heat energy to melt and preheat scrap steel and heat molten steel, provides heat energy for the whole smelting continuous casting link, improves the heat efficiency of scrap steel smelting, and reduces the emission of carbon dioxide; and pollutants such as sulfur, nitrate, dioxin, heavy metals and the like are removed through an activated carbon adsorption technology, so that the once-combustion heat energy scrap steel smelting process becomes an energy-saving and environment-friendly green smelting system, and the specific technical scheme is as follows:
a system for smelting scrap steel by utilizing primary combustion heat energy comprises a feeding system 1, a shaft furnace 2, a pipeline reactor 3, a dust remover 4, an air inlet pipe 5, a variable-frequency draught fan 6, a chimney 7, a liftable heat preservation cover 8, a stock bin 9, a fine-adjustment tundish 10 and a steel ladle 11;
a steel tapping hole 12 is formed in the side wall of the bottom of the shaft furnace 2, a molten steel heating oxygen combustion burner 13 is arranged at the lower part of a melting section of the shaft furnace 2, a main oxygen burner 14 is arranged at the upper part of the melting section of the shaft furnace 2, an oxygen supplementing and blowing pipe 15 is arranged at the middle section of the shaft furnace 2, a cooling spray system 16 is arranged at the upper section of the shaft furnace 2, and a closed charging system 17 is arranged at the top of the shaft furnace 2;
the liftable heat preservation cover 8 is provided with an auxiliary material feeding port 18, a smoke return port 19, a temperature measurement sampling port 20 and an oxygen combustion gun 21;
a steel flowing port 22 is formed in the lower part of the side wall of the fine adjustment tundish 10; the bottom of the fine adjustment tundish 10 is provided with an air blowing air brick I23; the bottom of the steel ladle 11 is provided with a blowing air brick II 25;
the feeding end of the feeding system 1 is connected with a closed feeding system 17 at the top of the shaft furnace 2, a smoke outlet at the upper part of the shaft furnace 2 is connected with a smoke inlet of the pipeline reactor 3 through a pipeline, the smoke outlet of the pipeline reactor 3 is connected with an air inlet of the dust remover 4 through a pipeline, an air outlet of the dust remover 4 is connected with an induced air port of the variable-frequency induced draft fan 6 through a pipeline, an air inlet pipe 5 is arranged on a connecting pipeline of the dust remover 4 and the variable-frequency induced draft fan 6, and an air outlet of the variable-frequency induced draft fan 6 is connected with a chimney 7 through a pipeline;
a steel tapping hole 12 of the shaft furnace 2 is connected with a fine adjustment tundish 10 through a pipeline, a liftable heat preservation cover 8 is covered on the fine adjustment tundish 10, an auxiliary material feeding hole 18 on the liftable heat preservation cover 8 is connected with a bottom discharge hole of a storage bin 9 through a pipeline, and a smoke return hole 19 on the liftable heat preservation cover 8 is connected with an air inlet of the shaft furnace 2 through a smoke return pipeline 24; a steel ladle 11 is arranged below a steel flowing port 22 of the fine adjustment tundish 10 and is used for receiving molten steel;
a valve is arranged at the air outlet of the dust remover 4;
the air inlet pipe 5 is provided with a valve;
valves are arranged at the smoke return pipeline 24 and the air inlet of the shaft furnace 2;
a blocking stopper rod is arranged at a steel tapping hole 12 of the shaft furnace 2;
a stopper rod is arranged outside the steel flowing port 22 of the fine tuning tundish 10;
a valve is arranged at an auxiliary material feeding port 18 of the liftable heat preservation cover 8;
the cooling spraying system 16 is externally connected with a water source;
the number of the molten steel heating oxygen combustion burner nozzles 13, the number of the main oxygen combustion nozzles 14 and the number of the supplemental oxygen blowing oxygen pipes 15 are determined according to the specific scale of the shaft furnace 2;
the molten steel heating oxygen combustion burner 13 is replaced by an oxygen combustion gun; the primary oxygen burner 14 is replaced with an oxygen burner;
the fine tuning tundish 10 can be replaced by a ladle 11;
when the ladle 11 is subsequently connected with smelting and refining equipment, the auxiliary material charging port 18, the temperature measurement sampling port 20 and the oxygen combustion gun 21 on the liftable heat preservation cover 8 can be individually omitted or completely omitted;
a preheating chamber is additionally arranged in the stock bin 9;
the steelmaking method of the system for smelting the steel scrap by utilizing the once-combustion heat energy comprises the following steps:
step 1, feeding:
when a furnace is built or overhauled, 2-4 layers of square timbers are laid at the bottom of the furnace, the thickness of the square timbers is 200-500 mm, then 1-2 m of coke is laid on the square timbers, relatively long medium-sized waste steel is placed on the coke, a combustion area is reserved, the diameter of the middle-sized waste steel is larger than the inner diameter of a preheating section furnace, the crushed waste steel is not added during the furnace drying period, the medium-sized waste steel is completely used, and the crushed waste steel is added during normal smelting;
step 2, preheating and melting:
starting a variable-frequency draught fan 6 for cold debugging, igniting the oil-impregnated wood block after normal operation, starting a main oxygen burner 14, increasing the peroxide coefficient by 2-3 at the early stage, and burning part of coke to heat the whole system; the carbon ratio of molten steel melted in the early stage is high, the molten steel is cast into iron blocks, a small amount of molten steel can be gradually doped for carbon regulation during normal smelting, and the peroxide coefficient is regulated to be below 1 after the furnace temperature is normal; the main oxygen burner 14 of the shaft furnace 2 provides the main heat energy for preheating the scrap steel in the furnace, and the combustion temperature is above 1800 ℃; the scrap steel at the bottom of the shaft furnace 2 is preheated to be close to the melting temperature and can be rapidly melted after encountering high-temperature flame;
at the moment, the scrap steel above the flame is softened, the air permeability is poor, high-temperature flue gas can flow from the flame perforation place to the peripheral space without the scrap steel and then go upwards to the transition section of the shaft furnace 2, the scrap steel at the transition section is not softened, the flue gas can penetrate, the flow area of the flue gas is reduced along with the gradual reduction of the diameter upwards, the flue gas can accelerate to diffuse into the scrap steel material column, and finally the flue gas completely penetrates through the scrap steel material column; the high-temperature flue gas is used for heating the scrap steel, the heat efficiency of the shaft furnace 2 is very high, the temperature of the flue gas can be adjusted by adjusting the height of a material column, and the temperature of the flue gas is controlled to be below 150 ℃; the surface layer scrap steel of the scrap steel material column is heated more, part of the scrap steel is melted and bonded, the material column is not scattered, and the lower part of the shaft furnace 2 is provided with a gas ascending space, so that a space is provided for the flue gas of the shaft furnace 2 to move forward; molten steel molten at the lower part flows to the runner along a brick joint on the upper part of the runner lined with enamel, and the molten steel heating oxygen-combustion burner nozzle 13 arranged at the lower part carries out secondary heating on the molten steel so as to improve the fluidity of the molten steel;
opening a plugging stopper of a steel tapping hole 12, enabling molten steel to flow into a fine adjustment tundish 10, starting an oxygen combustion gun 21 to heat the molten steel in the fine adjustment tundish 10 to more than 1600 ℃, opening an auxiliary material feeding hole 18 according to the components of the molten steel before tapping, adding alloy auxiliary materials in a storage bin 9 into the fine adjustment tundish 10, and performing alloying component fine adjustment, recarburization and diffusion deoxidation on the molten steel;
when the components of the molten steel are fine-adjusted, the bottom-blowing air brick 23 blows argon gas and is stirred, so that the temperature and the components of the molten steel are uniform, the alloy yield is high due to diffusion deoxidation, and less aluminum deoxidizers can be added, so that the molten steel has few inclusions;
during the tapping process and the component fine adjustment, the oxygen combustion gun 21 is always in a working state, the air supply intensity can be adjusted according to the heating requirement, the oxygen combustion ratio is controlled to be 1-1.01, the valve of the smoke return pipeline 24 is controlled by a pressure sensor in the fine adjustment tundish 10, the micro negative pressure is always kept to be-20-30 Pa, and not only is the situation that smoke can not overflow out ensured, but also too much air can not be sucked in; the burnt high-temperature flue gas is completely returned to the shaft furnace 2 through the smoke return pipeline 24 to preheat the scrap steel, so that the heat loss is reduced;
and 4, replacement and maintenance:
in the normal smelting process, the steel tapping hole 12 of the shaft furnace 2 is always in a steel tapping state, when the fine adjustment tundish 10 is replaced, the molten steel heating oxygen combustion burner nozzle 13 and the main oxygen combustion nozzle 14 of the shaft furnace 2 are stopped from working, the molten steel in the shaft furnace 2 and the molten steel in the fine adjustment tundish 10 are exhausted, and after the new fine adjustment tundish 10 is replaced, the molten steel heating oxygen combustion burner nozzle 13 and the main oxygen combustion nozzle 14 are continuously opened for smelting;
when the steel outlet 12 of the shaft furnace 2 is corroded greatly, stopping the operation of heating the oxygen combustion burner 13 and the main oxygen burner 14 by the molten steel of the shaft furnace 2, discharging the molten steel in the shaft furnace 2 completely, plugging the steel outlet 12 by using refractory stemming, and then continuing to operate after re-opening by using a drill bit with a proper diameter;
step 5, tapping:
after the temperature and the composition of the molten steel are finely adjusted in the fine adjustment tundish 10, when tapping is needed, the stopper rod of the tapping hole 22 is pulled by a machine, the molten steel automatically flows into the ladle 11, the stopper rod of the tapping hole 22 is automatically blocked by a manipulator after tapping, the ladle 11 is transferred to an LF furnace for station refining, and final fine adjustment and waiting are carried out.
In the step 3, the ladle 11 can be used for replacing the fine adjustment tundish 10 for receiving molten steel and fine adjustment, when the ladle 11 is replaced, intermittent tapping is needed, the tapping hole 12 is blocked by refractory mortar, tapping is carried out by opening a tapping machine during each tapping, and steel slag is mixed out during tapping;
the utility model relates to an utilize one-time combustion heat energy to smelt steel scrap system, compared with the prior art, beneficial effect is:
the melting section and the preheating section of the shaft furnace are arranged to be ultra-thick for heat preservation, the exhaust gas temperature can be adjusted by adding waste steel and the height is controlled below 150 ℃, so that the thermal efficiency is very high, the energy utilization rate can reach about 80% in the smelting and melting process and is 2-3 times of that of an electric furnace, and if the energy consumption factors of graphite electrodes are considered together, the energy conversion rate of the electric arc furnace is more than 4-5 times.
Secondly, a pipeline reactor is arranged between the shaft furnace and the induced draft fan, a dust remover is arranged behind the pipeline reactor, and no matter gas or carbon powder is directly combusted, the gas or the carbon powder isIn the presence of sulfur, SO is formed during combustion2And SO3The utility model discloses a set up the pipeline reactor on the flue, to the active carbon powder of jetting in the pipeline reactor, use the sulfur in the active carbon powder absorption flue gas, nitre, dioxin, heavy metal, set up the dust remover behind the pipeline reactor and retrieve adsorbent and dirt, the flue gas after the processing is up to standard and discharges; because the scrap steel in the furnace is completely melted before stopping the furnace each time, the temperature of the flue gas is very high, in order to protect the equipment at the furnace top, the flue at the rear part and the dedusting filter materials, the spray cooling device is arranged at the furnace top, the spray amount is controlled by the temperature of the rear part dedusting system, the rear part equipment cannot be damaged by overheating, the temperature of the flue gas is not lower than the dew point, and the blockage of the filtering materials by pasting is avoided. The process solves the problem that the emission of harmful gases exceeds the standard in the prior scrap steel preheating smelting process; in order to prevent CO emission from exceeding the standard, air or oxygen blowing holes are arranged in the upper furnace temperature range of 600-800 ℃ of the shaft furnace for secondary combustion.
Thirdly, when the steelmaking system of the utility model is in full-oxygen combustion, the smoke gas quantity is less, the quantity of heat taken away is less, and the energy utilization rate is high; the energy source flow is reasonable, the energy-saving and emission-reducing effects are obvious, and the energy consumption in the smelting link is only about 30 percent of that of the traditional electric furnace smelting; CO 22The emission is less than one third of the emission of electric arc furnace smelting and less than 10% of that of long-process smelting, and the emission reduction effect is obvious;
fourthly, because the oxygen-fuel ratio of the oxygen-fuel burner or the oxygen-fuel gun can be less than 1, the high-temperature zone at the lower part of the shaft furnace is in reducing atmosphere, the oxidation of scrap steel can be greatly reduced, the metal yield can be greatly improved, the oxygen content of molten steel can be greatly reduced, the cost of the deoxidizer can be reduced, and the refining cost can be reduced.
Fifthly, because the energy source flows reasonably, the smelting process is optimized, and the whole manufacturing cost is reduced by 180-260 yuan per ton of steel compared with an electric arc furnace; the equipment investment is far less than the electric arc furnace process investment, and the equipment depreciation cost is far lower than the electric arc furnace process.
To sum up, the utility model discloses a full scrap steel smelting system is energy-conserving, low carbon, environmental protection, low cost in the green smelting system of an organic whole.
Drawings
FIG. 1 is a schematic structural view of a system for smelting steel scrap by using primary combustion heat energy in embodiment 1 of the present invention;
FIG. 2 is an enlarged view of a portion of the schematic view of FIG. 1;
FIG. 3 is a schematic structural view of a ladle of a system for smelting steel scrap by using primary combustion heat energy according to embodiment 1 of the present invention;
in the figure: 1-a feeding system, 2-a shaft furnace, 3-a pipeline reactor, 4-a dust remover, 5-an air inlet pipe, 6-a variable frequency draught fan, 7-a chimney, 8-a liftable heat preservation cover, 9-a storage bin, 10-a fine adjustment tundish, 11-a steel ladle, 12-a steel outlet, 13-a molten steel heating oxygen burner, 14-a main oxygen burner, 15-an after-blowing oxygen pipe, 16-a cooling spray system, 17-a closed feeding system, 18-an auxiliary material feeding port, 19-a smoke return port, 20-a temperature measurement sampling port, 21-an oxygen burner, 22-a steel flowing port, 23-a blowing air brick I, 24-a smoke return pipe and 25-a blowing air brick II.
Detailed Description
The present invention will be further described with reference to the following embodiments and accompanying fig. 1-3, but the present invention is not limited to these embodiments.
Example 1
As shown in fig. 1-3, a system for smelting scrap steel by using primary combustion heat energy comprises a feeding system 1, a shaft furnace 2, a pipeline reactor 3, a dust remover 4, an air inlet pipe 5, a variable-frequency induced draft fan 6, a chimney 7, a liftable heat-insulating cover 8, a stock bin 9, a fine-tuning tundish 10 and a steel ladle 11;
a steel tapping hole 12 is formed in the side wall of the bottom of the shaft furnace 2, a molten steel heating oxygen combustion burner 13 is arranged at the lower part of a melting section of the shaft furnace 2, a main oxygen burner 14 is arranged at the upper part of the melting section of the shaft furnace 2, an oxygen supplementing and blowing pipe 15 is arranged at the middle section of the shaft furnace 2, a cooling spray system 16 is arranged at the upper section of the shaft furnace 2, and a closed charging system 17 is arranged at the top of the shaft furnace 2;
the liftable heat preservation cover 8 is provided with an auxiliary material feeding port 18, a smoke return port 19, a temperature measurement sampling port 20 and an oxygen combustion gun 21;
a steel flowing port 22 is formed in the lower part of the side wall of the fine adjustment tundish 10; the bottom of the fine adjustment tundish 10 is provided with an air blowing air brick I23; the bottom of the steel ladle 11 is provided with a blowing air brick II 25;
the feeding end of the feeding system 1 is connected with a closed feeding system 17 at the top of the shaft furnace 2, a smoke outlet at the upper part of the shaft furnace 2 is connected with a smoke inlet of the pipeline reactor 3 through a pipeline, the smoke outlet of the pipeline reactor 3 is connected with an air inlet of the dust remover 4 through a pipeline, an air outlet of the dust remover 4 is connected with an induced air port of the variable-frequency induced draft fan 6 through a pipeline, an air inlet pipe 5 is arranged on a connecting pipeline of the dust remover 4 and the variable-frequency induced draft fan 6, and an air outlet of the variable-frequency induced draft fan 6 is connected with a chimney 7 through a pipeline;
a steel tapping hole 12 of the shaft furnace 2 is connected with a fine adjustment tundish 10 through a pipeline, a liftable heat preservation cover 8 is covered on the fine adjustment tundish 10, an auxiliary material feeding hole 18 on the liftable heat preservation cover 8 is connected with a bottom discharge hole of a storage bin 9 through a pipeline, and a smoke return hole 19 on the liftable heat preservation cover 8 is connected with an air inlet of the shaft furnace 2 through a smoke return pipeline 24; a steel ladle 11 is arranged below a steel flowing port 22 of the fine adjustment tundish 10 and is used for receiving molten steel;
a valve is arranged at the air outlet of the dust remover 4;
the air inlet pipe 5 is provided with a valve;
valves are arranged at the smoke return pipeline 24 and the air inlet of the shaft furnace 2;
a blocking stopper rod is arranged at a steel tapping hole 12 of the shaft furnace 2;
a stopper rod is arranged outside the steel flowing port 22 of the fine tuning tundish 10;
a valve is arranged at an auxiliary material feeding port 18 of the liftable heat preservation cover 8;
the cooling spraying system 16 is externally connected with a water source;
the number of the molten steel heating oxygen combustion burner nozzles 13, the number of the main oxygen combustion nozzles 14 and the number of the supplemental oxygen blowing oxygen pipes 15 are determined according to the specific scale of the shaft furnace 2;
the molten steel heating oxygen combustion burner 13 is replaced by an oxygen combustion gun; the primary oxygen burner 14 is replaced with an oxygen burner;
the fine tuning tundish 10 can be replaced by a ladle 11;
when the ladle 11 is subsequently connected with smelting and refining equipment, the auxiliary material charging port 18, the temperature measurement sampling port 20 and the oxygen combustion gun 21 on the liftable heat preservation cover 8 can be individually omitted or completely omitted;
the silo 9 is additionally provided with a preheating chamber.
In the embodiment, a system for smelting scrap steel by utilizing once combustion heat energy is newly built in a certain iron and steel enterprise, the inner diameter of an upper preheating zone of a shaft furnace 2 is 2.4 meters, the height of the upper preheating zone is 15 meters, the inner diameter of a lower combustion zone is 3.5 meters, the height of the combustion zone is 3 meters, the transition height from the combustion zone to an upper thin section is 2 meters, the total height of the shaft furnace 2 is 20 meters, a scrap steel supporting platform is arranged at the bottom, the diameter of the platform is 2.8 meters, a steel flowing channel is arranged at the periphery of the platform, the steel flowing channel is inclined, the steel tapping hole is lowest, the steel tapping hole is shallowest, the steel flowing channel at the shallowest position is 300mm and 500mm in the deepest position, molten steel liquid flows to the steel tapping hole 12; the 800mm position on the scrap steel supporting platform is provided with 6 main oxygen combustion nozzles 14 which are uniformly distributed on the periphery of the furnace, the muzzle is arranged obliquely downwards, the flame lower limit reaches the center of the scrap steel supporting platform, the main oxygen combustion nozzles are mainly used for melting and preheating the scrap steel and are the main energy provider of the shaft furnace 2; 4 molten steel heating oxygen combustion burners 13 are arranged at the position of 200mm on the scrap steel supporting table, the molten steel heating oxygen combustion burners are arranged obliquely downwards in a tangent line, the flame points to the molten steel flow channel, the impact direction is consistent with the flow direction of the molten steel, the molten steel heating oxygen combustion burners 13 are mainly used for heating the molten steel after melting and cleaning the scrap steel falling to the molten steel flow channel, and the molten steel heating oxygen combustion burners 13 can also be used for adjusting and improving the productivity; in order to prevent the unmelted scrap from falling into the runner, the runner is covered by refractory bricks, the molten steel flows down through the brick joints, and the molten steel flows to the steel outlet 12 through the inclined runner and flows out of the shaft furnace 2;
the gas is gas of a gas generator, the heat value is 1350 kilocalories/cubic meter, and the combustion-supporting gas is full oxygen;
8 oxygen supplementing and blowing pipes 15 are arranged in the middle of the preheating section for secondary combustion, so that the emission of the CO in the exhaust flue gas is ensured to reach the standard;
a pipeline reactor 3 is arranged behind a smoke outlet at the top of the shaft furnace 2, activated carbon powder is sprayed to adsorb SO2, SO3, NOx, dioxin and heavy metals in smoke, a dust remover 4 is arranged behind the pipeline reactor 3, in order to prevent accidental overhigh smoke temperature from influencing the service life of dust removing filter materials and damaging furnace top facilities, a cooling spray system 16 is arranged at the top of the shaft furnace 2, the spray amount is controlled by a furnace top temperature sensor to ensure that the smoke temperature is lower than the highest temperature borne by the filter materials, and the spray amount is controlled to ensure that the smoke temperature is higher than the dew point, SO that the blockage of the filter materials is avoided;
a variable-frequency draught fan 6 is arranged behind the dust remover 4, the motor is a frequency modulation motor, the frequency modulation motor is controlled by the pressure of a combustion area, and the combustion area keeps micro negative pressure.
The steelmaking method of the system for smelting the steel scrap by utilizing the once-combustion heat energy comprises the following steps:
step 1, feeding:
when a furnace is built or overhauled, 2-4 layers of square timbers are laid at the bottom of the furnace, the thickness of the square timbers is 200-500 mm, then 1-2 m of coke is laid on the square timbers, relatively long medium-sized waste steel is placed on the coke, a combustion area is reserved, the diameter of the middle-sized waste steel is larger than the inner diameter of a preheating section furnace, the crushed waste steel is not added during the furnace drying period, the medium-sized waste steel is completely used, and the crushed waste steel is added during normal smelting;
step 2, preheating and melting:
starting a variable-frequency draught fan 6 for cold debugging, igniting the oil-impregnated wood block after normal operation, starting a main oxygen burner 14, increasing the peroxide coefficient by 2-3 at the early stage, and burning part of coke to heat the whole system; the carbon ratio of molten steel melted in the early stage is high, the molten steel is cast into iron blocks, a small amount of molten steel can be gradually doped for carbon regulation during normal smelting, and the peroxide coefficient is regulated to be below 1 after the furnace temperature is normal; the main oxygen burner 14 of the shaft furnace 2 provides the main heat energy for preheating the scrap steel in the furnace, and the combustion temperature is above 1800 ℃; the scrap steel at the bottom of the shaft furnace 2 is preheated to be close to the melting temperature and can be rapidly melted after encountering high-temperature flame; at the moment, the scrap steel above the flame is softened, the air permeability is poor, high-temperature flue gas can flow from the flame perforation place to the peripheral space without the scrap steel and then go upwards to the transition section of the shaft furnace 2, the scrap steel at the transition section is not softened, the flue gas can penetrate, the flow area of the flue gas is reduced along with the gradual reduction of the diameter upwards, the flue gas can accelerate to diffuse into the scrap steel material column, and finally the flue gas completely penetrates through the scrap steel material column; the high-temperature flue gas is used for heating the scrap steel, the heat efficiency of the shaft furnace 2 is very high, the temperature of the flue gas can be adjusted by adjusting the height of a material column, and the temperature of the flue gas is controlled to be below 150 ℃; the surface layer scrap steel of the scrap steel material column is heated more, part of the scrap steel is melted and bonded, the material column is not scattered, and the lower part of the shaft furnace 2 is provided with a gas ascending space, so that a space is provided for the flue gas of the shaft furnace 2 to move forward; molten steel molten at the lower part flows to the runner along a brick joint on the upper part of the runner lined with enamel, and the molten steel heating oxygen-combustion burner nozzle 13 arranged at the lower part carries out secondary heating on the molten steel so as to improve the fluidity of the molten steel;
opening a plugging stopper of a steel tapping hole 12, enabling molten steel to flow into a fine adjustment tundish 10, starting an oxygen combustion gun 21 to heat the molten steel in the fine adjustment tundish 10 to more than 1600 ℃, opening an auxiliary material feeding hole 18 according to the components of the molten steel before tapping, adding alloy auxiliary materials in a storage bin 9 into the fine adjustment tundish 10, and performing alloying component fine adjustment, recarburization and diffusion deoxidation on the molten steel;
when the components of the molten steel are fine-adjusted, the bottom blowing air-permeable brick I23 blows argon gas and is stirred, so that the temperature and the components of the molten steel are uniform, the alloy yield is high due to diffusion deoxidation, and less aluminum deoxidizers can be added, so that the molten steel has few inclusions;
during the tapping process and the component fine adjustment, the oxygen combustion gun 21 is always in a working state, the air supply intensity can be adjusted according to the heating requirement, the oxygen combustion ratio is controlled to be 1-1.01, the valve of the smoke return pipeline 24 is controlled by a pressure sensor in the fine adjustment tundish 10, the micro negative pressure is always kept to be-20-30 Pa, and not only is the situation that smoke can not overflow out ensured, but also too much air can not be sucked in; the burnt high-temperature flue gas is completely returned to the shaft furnace 2 through the smoke return pipeline 24 to preheat the scrap steel, so that the heat loss is reduced; the oxygen combustion gun 21 heats the molten steel to the greatest extent so that the temperature of the molten steel meets the rear refining requirement, the subsequent heating step in the LF furnace is saved, and the heating cost is reduced; a preheating chamber can be additionally arranged on the storage bin 9, alloy auxiliary materials to be put into the fine adjustment tundish are firstly sent into the preheating chamber, high-temperature flue gas in the fine adjustment tundish 10 is introduced into the preheating chamber, and the alloy auxiliary materials are preheated and then put into the fine adjustment tundish 10, so that the temperature drop caused by the alloy auxiliary materials can be reduced, the hydrogen increase of molten steel is also reduced, the refining pressure of the LF furnace can be greatly reduced, the refining cost is greatly reduced, and the smelting efficiency can be improved;
and 4, replacement and maintenance:
in the normal smelting process, the steel tapping hole 12 of the shaft furnace 2 is always in a steel tapping state, when the fine adjustment tundish 10 is replaced, the molten steel heating oxygen combustion burner nozzle 13 and the main oxygen combustion nozzle 14 of the shaft furnace 2 are stopped from working, the molten steel in the shaft furnace 2 and the molten steel in the fine adjustment tundish 10 are exhausted, and after the new fine adjustment tundish 10 is replaced, the molten steel heating oxygen combustion burner nozzle 13 and the main oxygen combustion nozzle 14 are continuously opened for smelting;
when the steel outlet 12 of the shaft furnace 2 is corroded greatly, stopping the operation of heating the oxygen combustion burner 13 and the main oxygen burner 14 by the molten steel of the shaft furnace 2, discharging the molten steel in the shaft furnace 2 completely, plugging the steel outlet 12 by using refractory stemming, and then continuing to operate after re-opening by using a drill bit with a proper diameter;
step 5, tapping:
after the temperature and the composition of the molten steel are finely adjusted in the fine adjustment tundish 10, when tapping is needed, the stopper rod of the tapping hole 22 is pulled by a machine, the molten steel automatically flows into the ladle 11, the stopper rod of the tapping hole 22 is automatically blocked by a manipulator after tapping, the ladle 11 is transferred to an LF furnace for station refining, and final fine adjustment and waiting are carried out.
According to the system and the method for smelting the steel scrap by utilizing the once-combustion heat energy, 3 ladles of molten steel are discharged in 2 hours on average during normal smelting, 60 tons of molten steel are discharged in each ladle, the molten steel is just matched with rear continuous casting, and the operation is stable for 3 months.
Claims (8)
1. A system for smelting scrap steel by utilizing primary combustion heat energy is characterized by comprising a feeding system (1), a shaft furnace (2), a pipeline reactor (3), a dust remover (4), an air inlet pipe (5), a variable-frequency draught fan (6), a chimney (7), a liftable heat-insulating cover (8), a storage bin (9), a fine-adjustment tundish (10) and a steel ladle (11);
a steel tapping hole (12) is formed in the side wall of the bottom of the shaft furnace (2), a molten steel heating oxy-combustion burner (13) is arranged at the lower part of a melting section of the shaft furnace (2), a main oxygen burner (14) is arranged at the upper part of the melting section of the shaft furnace (2), an oxygen supplementing and blowing pipe (15) is arranged at the middle section of the shaft furnace (2), a cooling spray system (16) is arranged at the upper section of the shaft furnace (2), and a closed charging system (17) is arranged at the top of the shaft furnace (2);
the liftable heat preservation cover (8) is provided with an auxiliary material feeding port (18), a smoke return port (19), a temperature measurement sampling port (20) and an oxygen combustion gun (21);
a steel flowing port (22) is formed in the lower portion of the side wall of the fine adjustment tundish (10); the bottom of the fine adjustment tundish (10) is provided with an air blowing air brick I (23); the bottom of the ladle (11) is provided with a blowing air brick II (25);
the feeding end of the feeding system (1) is connected with a closed feeding system (17) at the top of the shaft furnace (2), a smoke outlet at the upper part of the shaft furnace (2) is connected with a smoke inlet of the pipeline reactor (3) through a pipeline, the smoke outlet of the pipeline reactor (3) is connected with an air inlet of the dust remover (4) through a pipeline, an air outlet of the dust remover (4) is connected with an induced air port of the variable-frequency induced draft fan (6) through a pipeline, an air inlet pipe (5) is arranged on a connecting pipeline of the dust remover (4) and the variable-frequency induced draft fan (6), and an air outlet of the variable-frequency induced draft fan (6) is connected with a chimney (7) through a pipeline;
a tapping hole (12) of the shaft furnace (2) is connected with a fine adjustment tundish (10) through a pipeline, a liftable heat preservation cover (8) is covered on the fine adjustment tundish (10), an auxiliary material feeding hole (18) on the liftable heat preservation cover (8) is connected with a bottom discharge hole of a storage bin (9) through a pipeline, and a smoke return hole (19) on the liftable heat preservation cover (8) is connected with an air inlet of the shaft furnace (2) through a smoke return pipeline (24); a steel ladle (11) is arranged below a steel flowing port (22) of the fine adjustment tundish (10) and is used for receiving molten steel.
2. A system for smelting steel scrap by utilizing primary combustion heat energy according to claim 1, wherein a valve is arranged at the air outlet of the dust remover (4); the air inlet pipe (5) is provided with a valve; valves are arranged at the air inlets of the smoke return pipeline (24) and the shaft furnace (2); a blocking stopper rod is arranged at a steel tapping hole (12) of the shaft furnace (2); a stopper rod is arranged outside a steel flowing port (22) of the fine adjustment tundish (10); and a valve is arranged at an auxiliary material feeding port (18) of the liftable heat-insulating cover (8).
3. The system for smelting steel scraps by using primary combustion heat energy as claimed in claim 1, wherein the cooling spray system (16) is externally connected with a water source.
4. A system for smelting steel scrap using primary combustion heat energy according to claim 1, wherein the number of the molten steel heating oxy-fuel burner (13), the number of the main oxygen burner (14) and the number of the oxygen supplementing blowing pipes (15) are determined according to the specific size of the shaft furnace (2).
5. The system for smelting steel scrap by using primary combustion heat energy as claimed in claim 1, wherein the molten steel heating oxygen combustion burner (13) is replaced by an oxygen combustion gun; the primary oxygen burner (14) is replaced by an oxygen lance.
6. A system for smelting steel scrap using primary combustion heat energy according to claim 1, wherein the fine-tuning tundish (10) is replaced with a ladle (11).
7. The system for smelting steel scraps by using primary combustion heat energy as claimed in claim 1 or 5, wherein the auxiliary material charging port (18), the temperature measuring sampling port (20) and the oxygen combustion lance (21) on the liftable heat insulating cover (8) can be omitted individually or entirely when the ladle (11) is subsequently connected with smelting and refining equipment.
8. The system for smelting steel scraps by using heat energy generated by one-time combustion as set forth in claim 1, wherein the bunker (9) is additionally provided with a preheating chamber.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020919976.XU CN212713622U (en) | 2020-05-27 | 2020-05-27 | System for smelting scrap steel by utilizing once-combustion heat energy |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020919976.XU CN212713622U (en) | 2020-05-27 | 2020-05-27 | System for smelting scrap steel by utilizing once-combustion heat energy |
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| CN212713622U true CN212713622U (en) | 2021-03-16 |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111518986A (en) * | 2020-05-27 | 2020-08-11 | 沈阳东大山汇环境科技有限公司 | System for smelting scrap steel by utilizing primary combustion heat energy and steelmaking method thereof |
| CN114504944A (en) * | 2022-01-26 | 2022-05-17 | 大冶有色金属有限责任公司 | Composite desulfurizer for low-concentration sulfur dioxide flue gas desulfurization and application thereof |
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2020
- 2020-05-27 CN CN202020919976.XU patent/CN212713622U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111518986A (en) * | 2020-05-27 | 2020-08-11 | 沈阳东大山汇环境科技有限公司 | System for smelting scrap steel by utilizing primary combustion heat energy and steelmaking method thereof |
| CN114504944A (en) * | 2022-01-26 | 2022-05-17 | 大冶有色金属有限责任公司 | Composite desulfurizer for low-concentration sulfur dioxide flue gas desulfurization and application thereof |
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