WO2021073015A1 - 转炉 co2-o2 混合喷吹冶炼方法和火点区温度动态控制方法 - Google Patents

转炉 co2-o2 混合喷吹冶炼方法和火点区温度动态控制方法 Download PDF

Info

Publication number
WO2021073015A1
WO2021073015A1 PCT/CN2020/073500 CN2020073500W WO2021073015A1 WO 2021073015 A1 WO2021073015 A1 WO 2021073015A1 CN 2020073500 W CN2020073500 W CN 2020073500W WO 2021073015 A1 WO2021073015 A1 WO 2021073015A1
Authority
WO
WIPO (PCT)
Prior art keywords
temperature
smelting
converter
stage
mixing ratio
Prior art date
Application number
PCT/CN2020/073500
Other languages
English (en)
French (fr)
Inventor
朱荣
冯超
魏光升
韩宝臣
董凯
王雪亮
武文合
胡绍岩
李伟峰
姜娟娟
董建锋
Original Assignee
北京科技大学
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 北京科技大学 filed Critical 北京科技大学
Priority to US17/049,449 priority Critical patent/US11788160B2/en
Priority to AU2020257077A priority patent/AU2020257077A1/en
Publication of WO2021073015A1 publication Critical patent/WO2021073015A1/zh

Links

Images

Classifications

    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/28—Manufacture of steel in the converter
    • C21C5/30—Regulating or controlling the blowing
    • C21C5/32—Blowing from above
    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/28—Manufacture of steel in the converter
    • C21C5/42—Constructional features of converters
    • C21C5/46—Details or accessories
    • C21C5/4606—Lances or injectors
    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/28—Manufacture of steel in the converter
    • C21C5/42—Constructional features of converters
    • C21C5/46—Details or accessories
    • C21C5/4673—Measuring and sampling devices
    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
    • C21C5/28—Manufacture of steel in the converter
    • C21C5/42—Constructional features of converters
    • C21C5/46—Details or accessories
    • C21C5/4606—Lances or injectors
    • C21C2005/4626—Means for cooling, e.g. by gases, fluids or liquids
    • C—CHEMISTRY; METALLURGY
    • C21—METALLURGY OF IRON
    • C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C2300/00—Process aspects
    • C21C2300/06—Modeling of the process, e.g. for control purposes; CII
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00—Technologies related to metal processing
    • Y02P10/20—Recycling

Definitions

  • the present disclosure relates to the technical field of iron and steel metallurgy, in particular to a converter CO 2 -O 2 mixed injection smelting method and a method for dynamically controlling the temperature of the fire point area.
  • CO 2 emissions is the main reason a lot of the greenhouse effect, emissions per ton of steel production of about 2 tons CO 2, CO 2 efficient use is important for reducing greenhouse gas emissions, so the development of new technologies, explore new ways to achieve Steel The reduction or elimination of CO 2 emissions in the industry is urgent.
  • the high-speed oxygen jet is in contact with the molten pool to form a high-temperature fire point area where iron evaporates, which generates a large amount of smoke and dust, which causes environmental pollution.
  • the heat loss of the converter increases and the metal recovery rate decreases. Therefore, how to dynamically adjust and control the fire point
  • the zone temperature is of great significance for reducing the generation of steel-making smoke and dust, improving the metal recovery rate and the utilization of heat energy.
  • the reaction between CO 2 and [C] is an endothermic reaction (mainly limited by the concentration and temperature of [C]), which generates 1.2-2 times of CO bubbles, which can not only reduce the temperature of the fire zone and realize the conversion of mass and energy, but also enhance the molten pool Stirring, CO 2 is the cleanest coolant. How to dynamically adjust the mixing ratio of CO 2 to achieve precise and effective control of the temperature in the fire zone is important for reducing converter smelting costs, increasing metal yields, and enhancing smelting process flexibility. significance.
  • the embodiments of the present disclosure provide a converter CO 2 -O 2 mixed injection smelting method and a converter CO 2 -O 2 mixed injection smelting fire point temperature dynamic control method, which can dynamically adjust the converter smelting fire point temperature and molten pool
  • the heating rate is used to realize the efficient use of CO 2 and the energy of the molten pool, and reduce the amount of steelmaking fumes.
  • an infrared thermometer is installed inside the oxygen lance, the infrared thermometer is connected to the data processing system, the data processing system is connected to the secondary smelting system, and the secondary smelting system is connected to the CO 2 flow regulating valve and O 2 flow. Regulating valve and oxygen lance control system, the oxygen lance is connected to the thermometer protection system and the oxygen lance cooling system.
  • the embodiments of the present disclosure provide a converter CO 2 -O 2 mixed injection smelting method, wherein the converter CO 2 -O 2 mixed injection smelting process includes a smelting start stage, a heating slagging stage, a high-efficiency dephosphorization stage, and a rapid The decarbonization stage and the end-point control stage; the converter CO 2 -O 2 mixed injection smelting method includes:
  • the temperature of the fire point is measured in the beginning stage of smelting, the temperature rising slagging stage, the early high-efficiency dephosphorization stage, the rapid decarburization stage and the end-point regulation stage to control the temperature of the fire point and dynamically adjust the CO 2 mixing ratio.
  • the temperature of the fire point area measured at the beginning of smelting is T 1
  • the temperature of the fire point area is required to be controlled to be less than T 2
  • the CO 2 mixing ratio is dynamically adjusted based on the difference ⁇ T between T1 and T2;
  • T1 and T2 ⁇ T The thermal balance dynamically adjusts the CO 2 mixing ratio in real time, and the CO 2 mixing ratio is adjusted correspondingly by 0.5-2.0% every time the ⁇ T value changes by 10°C; and/or
  • T1 and T2 ⁇ T The thermal balance dynamically adjusts the CO 2 mixing ratio in real time, and the CO 2 mixing ratio is adjusted correspondingly by 0.3-1.6% when the ⁇ T value changes by 10°C; and/or
  • T1 and T2 ⁇ T The thermal balance dynamically adjusts the CO 2 mixing ratio in real time.
  • the CO 2 mixing ratio is adjusted correspondingly by 0.35-2.0%.
  • the converter CO 2 -O 2 mixed injection smelting process further includes a preparation stage; the converter CO 2 -O 2 mixed injection smelting method includes:
  • the oxygen lance is lowered to the specified height below the furnace mouth and then CO 2 and O 2 are introduced to control the flow of CO 2 and O 2 to measure the temperature of the fire zone.
  • the converter CO 2 -O 2 mixed injection smelting process further includes an end stage;
  • the converter CO 2 -O 2 mixed injection smelting method includes:
  • the converter CO 2 -O 2 mixed injection smelting method includes: after analyzing the composition of molten steel and the temperature is qualified, tapping the converter by shaking the converter.
  • the converter CO 2 -O 2 mixed injection smelting method includes installing an infrared thermometer inside the oxygen lance to measure the temperature of the fire area.
  • the converter CO 2 -O 2 mixed injection smelting method further includes: the infrared thermometer (2-1) is connected to the data processing system (2-2), and the data processing system (2-2) is connected to the second smelting system.
  • the CO 2 flow regulating valve (4-3), O 2 flow regulating valve (4-4) and the oxygen lance control system (5) to the secondary smelting system (3), and the oxygen lance (1) Thermometer protection system (6) and oxygen lance cooling system (7).
  • the metal material conditions in the preparation stage include the weight and temperature of molten iron and scrap steel.
  • the air supply flow rate of the oxygen lance (1) is 6000-100000Nm 3 /h, wherein the O 2 concentration is greater than 97%, the mixing ratio is 50-100%, the CO 2 concentration is greater than 90%, and the mixing ratio It is 0-50%, and the water flow of the oxygen lance cooling system (7) is 60-600m 3 /h.
  • the infrared thermometer (2-1) transmits 4-20mA electrical signals, the infrared spectrum is 4-30um, single laser or dual laser sighting form, the outer diameter of the meter is 5-40mm, and the infrared axis is in line with The included angle of the nozzle axis of the oxygen lance nozzle is 0-70°.
  • the protection system (6) of the thermometer ensures that the temperature of the infrared thermometer (2-1) is 0-70°C, and the protective gas medium is any one or two of N 2 , Ar, and CO 2
  • the shielding gas flow rate is 500-10000Nm 3 /h, and the inner diameter of the shielding gas pipeline is 5-200mm.
  • the data processing system (2-2) converts the 4-20 mA electrical signal into a digital signal.
  • the method is suitable for 30-400t converter CO 2 -O 2 mixed injection smelting.
  • the present embodiment provides a converter CO 2 -O 2 mixture injection point Pyrometallurgy dynamic zone temperature control method disclosed, wherein the converter CO 2 -O 2 mixture injection process includes smelting the beginning of smelting, the slagging stage heating, pre-efficient Dephosphorization stage, rapid decarburization stage and end-point regulation stage;
  • the dynamic control method for the temperature of the fire point of the converter CO 2 -O 2 mixed injection smelting includes: measuring the temperature of the fire point in the initial stage of smelting, the temperature rising slagging stage, the early high-efficiency dephosphorization stage, the rapid decarburization stage and the end control stage. In order to control the temperature of the fire zone and dynamically adjust the CO 2 mixing ratio.
  • the method installs an infrared thermometer (2-1) inside the oxygen lance (1), the infrared thermometer (2-1) is connected to the data processing system (2-2), and the data processing system (2) -2) Connect the secondary smelting system (3), and connect the secondary smelting system (3) to the CO 2 flow regulating valve (4-3), O 2 flow regulating valve (4-4) and the oxygen lance control system (5),
  • the method for connecting the oxygen lance (1) to the temperature measuring instrument protection system (6) and the oxygen lance cooling system (7) includes one or more of the following steps:
  • the temperature of the fire spot area measured by the infrared thermometer (2-1) is T 1
  • the temperature of the fire spot area is required to be controlled to be less than T 2
  • the difference ⁇ T between T 1 and T 2 is transmitted to the secondary smelting system (3)
  • Secondary smelting system (3) Dynamic adjustment of CO 2 mixing ratio; and/or
  • 0-3min is the heating and slagging stage.
  • the range is 10-30°C/min.
  • the smelting secondary system (3) dynamically adjusts the CO 2 mixing ratio in real time according to the difference ⁇ T between T1 and T2 and the heat balance.
  • the ⁇ T value changes by 10°C, and the CO 2 mixing ratio is adjusted correspondingly by 0.5- 2.0%; and/or
  • 3-5min is the early stage of high-efficiency dephosphorization. It is required to control the temperature of the fire point to be lower than 2700°C, and control the heating rate of the molten pool in the range of 5-18°C/min.
  • the secondary smelting system (3) is based on the difference between T1 and T2.
  • the value ⁇ T and the thermal balance dynamically adjust the CO 2 mixing ratio in real time, and the CO 2 mixing ratio is adjusted by 0.35-1.8% for every 10°C change in the ⁇ T value; and/or
  • the smelting secondary system (3) dynamically adjusts the CO 2 mixing ratio in real time according to the difference ⁇ T between T1 and T2 and the heat balance. When the ⁇ T value changes by 10°C, the CO 2 mixing ratio is adjusted correspondingly by 0.3- 1.6%; and/or
  • the method for dynamically controlling the temperature of the fire point zone of the converter CO 2 -O 2 mixed injection smelting further includes:
  • the secondary smelting system (3) calculates the amount of slagging agent and coolant added through the static model of material balance and heat balance and formulates the addition system according to the conditions of the metal material entering the furnace, the condition of the slagging agent, the condition of the coolant, and the steel tapping target requirements; and /or
  • the smelting secondary system (3) controls the oxygen lance control system (5) to lift the oxygen lance to the bottom of the furnace mouth, and close the CO 2 flow regulating valve (4-3), O 2 flow regulating valve (4-4), Infrared thermometer (2-1), continue to lift the oxygen lance to the top of the furnace mouth, close the thermometer protection system (6), and close the oxygen lance cooling system (7) after the oxygen lance is raised to the original standby position, and wait for the next Furnace operation; and/or
  • the steel After analyzing the composition and temperature of the molten steel, the steel is tapped by shaking the converter.
  • the metal material conditions in the preparation stage include the weight and temperature of molten iron and scrap steel.
  • the air supply flow rate of the oxygen lance (1) is 6000-100000Nm 3 /h, wherein the O 2 concentration is greater than 97%, the mixing ratio is 50-100%, the CO 2 concentration is greater than 90%, and the mixing ratio It is 0-50%, and the water flow of the oxygen lance cooling system (7) is 60-600m 3 /h.
  • the infrared thermometer (2-1) transmits 4-20mA electrical signals, the infrared spectrum is 4-30um, single laser or dual laser sighting form, the outer diameter of the meter is 5-40mm, and the infrared axis is in line with The included angle of the nozzle axis of the oxygen lance nozzle is 0-70°.
  • the protection system (6) of the thermometer ensures that the temperature of the infrared thermometer (2-1) is 0-70°C, and the protective gas medium is any one or two of N 2 , Ar, and CO 2
  • the shielding gas flow rate is 500-10000Nm 3 /h, and the inner diameter of the shielding gas pipeline is 5-200mm.
  • the data processing system (2-2) converts the 4-20 mA electrical signal into a digital signal.
  • Fig. 1 is a schematic diagram of the system structure of the disclosed CO 2 -O 2 mixed injection smelting fire point temperature dynamic control method
  • Figure 2 is a schematic diagram of the assembly of the non-contact infrared thermometer of the present disclosure
  • Figure 3 is a cross-sectional view along the line A in Figure 2;
  • Fig. 4 is a curve of oxygen lance position and CO 2 flow rate change during the smelting process in the embodiment of the disclosure.
  • 1 oxygen lance
  • 2-1 infrared thermometer
  • 2-2 data processing system
  • 3 smelting secondary system
  • 4-1 CO 2 gas storage tank
  • 4-2 O 2 gas storage tank
  • 4-3 CO 2 flow regulating valve
  • 4-4 O 2 flow regulating valve
  • 4-5 CO 2 -O 2 gas mixing device
  • 5 Oxygen lance control system
  • 6 Thermometer protection system
  • 7 Oxygen lance cooling system.
  • the embodiments of the present disclosure provide a method for dynamically controlling the temperature of the fire point area of the converter CO 2 -O 2 mixed injection smelting.
  • the method uses an infrared thermometer installed inside the oxygen lance to measure the temperature of the fire point area, and according to the temperature of the fire point area Dynamically adjust the CO 2 flow and O 2 flow in the changing situation, realize the dynamic adjustment of the temperature of the fire point and the heating rate of the molten pool, realize the efficient use of the energy in the converter smelting process, reduce the consumption of steel materials, and reduce the amount of steelmaking smoke and dust emissions and slag generation .
  • an infrared thermometer 2-1 is installed inside the oxygen lance 1, and the infrared thermometer 2-1 is connected to the data processing system 2-2 ,
  • Data processing system 2-2 is connected to smelting secondary system 3
  • smelting secondary system 3 is connected to CO 2 flow regulating valve 4-3, O 2 flow regulating valve 4-4 and oxygen lance control system 5, oxygen lance 1 is connected to temperature measurement Instrument protection system 6 and oxygen lance cooling system 7;
  • CO 2 flow regulating valve 4-3 is connected to CO 2 gas storage tank 4-1, O 2 flow regulating valve 4-4 is connected to O 2 gas storage tank 4-2, CO 2 flow
  • the pipes after the regulating valve 4-3 and the O 2 flow regulating valve 4-4 are merged into the CO 2 -O 2 gas mixing device 4-5 for gas mixing.
  • the infrared thermometer installed inside the oxygen lance is used to measure the temperature of the fire point, and the electrical signal is transmitted to the data processing system, and then the processed digital signal is transmitted to
  • the secondary smelting system dynamically adjusts the CO 2 flow regulating valve, O 2 flow regulating valve and the oxygen lance control system according to the temperature change of the fire spot area, realizing dynamic adjustment of the temperature of the fire spot area and the heating rate of the molten pool, and realizing the efficient use of the converter smelting process Reduce the consumption of steel materials, reduce the emissions of steelmaking fumes and the amount of slag produced.
  • a converter CO 2 -O 2 mixed injection smelting method wherein the converter CO 2 -O 2 mixed injection smelting process includes the initial stage of smelting, the heating up slagging stage, the early stage of high-efficiency dephosphorization, and the rapid Decarbonization stage and end-point regulation stage.
  • the converter CO 2 -O 2 mixed injection smelting method includes:
  • the temperature of the fire point is measured in the beginning stage of smelting, the temperature rising slagging stage, the early high-efficiency dephosphorization stage, the rapid decarburization stage and the end-point regulation stage to control the temperature of the fire point and dynamically adjust the CO 2 mixing ratio.
  • the temperature of the fire point area is measured by the infrared thermometer 2-1 at the beginning of smelting to control the temperature of the fire point area, thereby dynamically adjusting the CO 2 mixing ratio.
  • the temperature of the fire spot area is measured as T 1 by the infrared thermometer 2-1, and the temperature of the fire spot area is required to be controlled to be less than T 2.
  • the CO 2 mixing ratio is dynamically adjusted based on the difference ⁇ T between T 1 and T 2, For example , the difference ⁇ T between T 1 and T 2 is transmitted to the smelting secondary system 3, and the smelting secondary system 3 dynamically adjusts the CO 2 mixing ratio.
  • the infrared thermometer 2-11 is used to measure the temperature of the fire point area in order to control the temperature of the fire point area, thereby dynamically adjusting the CO 2 mixing ratio.
  • T 1 temperature in the fire spot area
  • T 2 2800°C
  • the CO 2 mixing ratio is dynamically adjusted in real time
  • the CO 2 mixing ratio is adjusted by 0.5-2.0% for every 10°C change in the ⁇ T value.
  • infrared thermometers 2-11 are used to measure the temperature of the fire point in order to control the temperature of the molten pool, the rate of temperature increase in the molten pool, and dynamically adjust the CO 2 mixing ratio.
  • it is required to control the temperature of the fire point to be lower than 2700°C, and control the temperature rise rate of the molten pool from 5-18°C/min.
  • the smelting secondary system 3 dynamically real-time according to the difference ⁇ T and heat balance between T1 and T2
  • the CO 2 mixing ratio is adjusted, and the ⁇ T value changes by 10° C., the CO 2 mixing ratio is adjusted correspondingly by 0.35-1.8%.
  • infrared thermometers 2-11 are used to measure the temperature of the fire point in order to control the temperature of the molten pool, the rate of temperature increase in the molten pool, and dynamically adjust the CO 2 mixing ratio.
  • the smelting secondary system 3 dynamically adjusts the CO 2 mixing ratio in real time according to the difference ⁇ T between T1 and T2 and the heat balance.
  • the ⁇ T value changes by 10° C.
  • the CO 2 mixing ratio is adjusted correspondingly by 0.3-1.6%.
  • the infrared thermometer 2-11 is used to measure the temperature of the fire point in order to control the temperature of the molten pool, the rate of temperature rise of the molten pool, and dynamically adjust the CO 2 mixing ratio.
  • the smelting secondary system 3 dynamically adjusts the CO 2 mixing ratio in real time according to the difference ⁇ T between T1 and T2 and the heat balance. When the ⁇ T value changes by 10° C., the CO 2 mixing ratio is adjusted correspondingly by 0.35-2.0%.
  • the converter CO 2 -O 2 mixed injection smelting process may also include a preparation phase and an end phase.
  • the preparation stage may include the smelting secondary system 3 according to the furnace metal material conditions, slagging agent conditions, coolant conditions, and steel tapping target requirements, and calculate the slagging agent and coolant through the static model of material balance and thermal balance. Join the amount and formulate the joining system.
  • the preparation phase may also include after the converter is ironed, the converter mouth is turned to the vertical position, the smelting secondary system 3 turns on the oxygen lance cooling system 7, and then controls the oxygen lance control system 5 to lower the oxygen lance to the furnace mouth After a certain height above, open the thermometer protection system 6, continue to descend to the specified height below the furnace mouth, open the CO 2 flow control valve 4-3, O 2 flow control valve 4-4 and the infrared thermometer 2-1, use The infrared thermometer 2-1 measures the temperature of the fire spot area.
  • the end stage may include: the end of the smelting process, the smelting secondary system 3 controls the oxygen lance control system 5 to raise the oxygen lance to a certain height below the furnace mouth, and then closes the CO 2 flow regulating valve 4-3 and the O 2 flow Regulating valve 4-4, infrared thermometer 2-1, continue to raise the oxygen lance to a certain height above the furnace mouth, close the thermometer protection system 6, and close the oxygen lance cooling system 7 after the oxygen lance is raised to the original standby position, and wait Next furnace operation.
  • the converter CO 2 -O 2 mixed injection smelting process can also include analyzing the composition of molten steel and the temperature is qualified, and then shaking the converter to tap steel.
  • the embodiment of the present disclosure also provides a method for dynamically controlling the temperature in the fire point area of the converter CO 2 -O 2 mixed injection smelting.
  • the method may include at least part of the following steps.
  • the CO 2 -O 2 mixed injection smelting process in the converter includes the initial stage of smelting, the heating slagging stage, the early efficient dephosphorization stage, the rapid decarburization stage and the end-point control stage.
  • the converter CO 2 -O 2 mixed injection smelting fire point area The temperature dynamic control method includes measuring the temperature of the fire point at the beginning of smelting, heating and slagging stage, early high-efficiency dephosphorization stage, rapid decarburization stage, and end-point control stage to control the temperature of the fire point and change the information of the temperature of the fire point.
  • the secondary smelting system 3 dynamically adjusts the CO 2 mixing ratio. The method is specifically described below.
  • the smelting secondary system 3 calculates the amount of slagging agent and coolant added through the static model of material balance and thermal balance and formulates the addition system according to the conditions of the metal material entering the furnace, the slagging agent condition, the coolant condition and the steel tapping target requirements;
  • the temperature of the fire spot area measured by the infrared thermometer 2-1 is T 1
  • the temperature of the fire spot area is required to be controlled to be less than T 2
  • the difference ⁇ T between T 1 and T 2 is transmitted to the secondary smelting system 3 ,
  • the smelting secondary system 3 dynamically adjusts the CO 2 mixing ratio
  • S5: 3-5min in the early stage of smelting is the early stage of high-efficiency dephosphorization. It is required to control the temperature of the fire point to be lower than 2700°C, and control the heating rate of the molten pool in the range of 5-18°C/min.
  • the secondary smelting system 3 is based on the difference between T1 and T2. ⁇ T and thermal balance dynamically adjust the CO 2 mixing ratio in real time, and each time the ⁇ T value changes by 10° C., the CO 2 mixing ratio is adjusted correspondingly by 0.35-1.8%;
  • S6: 5-10min in the middle stage of smelting is the rapid decarburization stage.
  • S7: 10-16min in the later stage of smelting is the end-point control stage.
  • the ⁇ T value changes by 10°C
  • the CO 2 mixing ratio is adjusted correspondingly by 0.35-2.0%;
  • the smelting secondary system 3 controls the oxygen lance control system 5 after raising the oxygen lance to a certain height below the furnace mouth, close the CO 2 flow regulating valve 4-3, O 2 flow regulating valve 4-4, and infrared temperature measurement Meter 2-1, continue to raise the oxygen lance to a certain height above the furnace mouth and close the temperature measuring instrument protection system 6, after the oxygen lance is raised to the original standby position, close the oxygen lance cooling system 7, and wait for the next furnace operation;
  • the method is applied to 260t converter steelmaking, an oxygen lance with an outer tube diameter of 402mm is selected, the top blowing gas is a mixture of O 2 and CO 2 and the total gas flow is 57000Nm 3 /h, infrared
  • the outer diameter of the thermometer is 15mm, the diameter of the nozzle center hole is 30mm, the protective gas medium is N2 and Ar, N2 is switched to Ar in the later stage of smelting, and the protective gas flow rate is 2500Nm 3 /h;
  • the smelting secondary system calculates the addition of slagging agent and cooling agent through the static model of material balance and thermal balance according to the conditions of the entering metal material (weight and temperature of molten iron and scrap steel), slagging agent conditions, coolant conditions and steel tapping target requirements. Quantify and develop a joining system.
  • the weight of molten iron is 249t
  • the weight of scrap steel is 39t
  • the amount of lime added is 35kg/t
  • the light burnt dolomite is 14.8kg/t.
  • the parameters of molten iron, scrap steel and slagging agent are shown in Table 1 and Table 2.
  • the smelting secondary system opens the oxygen lance cooling system, and when the water flow is greater than 400m 3 /h and the pressure is stable, control the oxygen lance control system to lower the oxygen lance to In the movable fume hood above the furnace mouth, open the protection system of the thermometer, inject N 2 with a flow rate of 800Nm 3 /h, continue to lower the oxygen lance to 500mm below the furnace mouth, open the O 2 flow regulating valve and infrared thermometer , The flow of O 2 is 57000Nm 3 /h, the flow of protective gas N 2 of the thermometer is adjusted to 2500Nm 3 /h, continue to lower the height of the oxygen lance to 2.3m at the opening position, and add 50% slagging agent.
  • the early stage of smelting (0-3min) is the stage of heating up and slagging.
  • Point area control temperature (2800°C) 180°C smelting secondary system calculates the CO 2 mixing amount based on heat balance, opens the CO 2 flow regulating valve, dynamically adjusts the CO 2 mixing ratio to 9.4%, and ⁇ T changes every 10 °C during the continuous monitoring process , The proportion of CO 2 is adjusted accordingly by 0.52%.
  • the smelting secondary system calculated the CO 2 mixing amount according to the heat balance and dynamically adjusted the CO 2 The mixing ratio is 12.3%.
  • the CO 2 ratio will be adjusted accordingly by 0.41% (due to the increase in temperature, the CO 2 utilization rate will increase.), while providing "low temperature” thermodynamic conditions for the early dephosphorization, Realize the reduction of iron oxidation and reduce the amount of smoke and dust produced.
  • the smelting process enters the rapid decarburization stage (5-11min), and the [C] in the molten pool is rapidly oxidized, which not only causes the temperature of the fire point area and the heating rate of the molten pool to increase, but also generates a lot of smoke and dust, but due to the temperature and the molten pool [ C] Higher concentration is beneficial to increase the reaction rate of CO 2.
  • the temperature of the fire point is controlled to be lower than 2700 °C (the amount of CO produced at this stage is large, and a lower temperature of the fire point needs to be controlled to effectively suppress the generation of smoke and dust.), and control the average heating rate of the molten pool 30°C/min.
  • the temperature T 1 in the fire spot area measured by the infrared thermometer is 2690°C, which is 10°C lower than the control temperature of the fire spot area (2700°C).
  • the smelting secondary system calculates the CO 2 mixing amount according to the heat balance and dynamically adjusts the CO 2
  • the mixing ratio is 9.6%, and the CO 2 ratio is adjusted by 0.32% for every 10°C change in ⁇ T during the continuous monitoring process (relative to the melting bath temperature and [C] concentration in the early stage of smelting, it is beneficial to improve the CO 2 reaction rate).
  • the main task is to regulate the composition and temperature of molten steel to meet the requirements of steel tapping.
  • the temperature of the fire point area is controlled to be lower than 2800°C, and the average heating rate of the molten pool is controlled to 22.5°C/min.
  • the temperature T 1 in the fire spot area measured by the infrared thermometer was 2680°C, which was 20°C lower than the control temperature of the fire spot area (2700°C).
  • the smelting secondary system calculated the CO 2 mixing amount according to the heat balance and dynamically adjusted the CO 2 The mixing ratio is 10.8%.
  • the smelting secondary system controls the oxygen lance control system to raise the oxygen lance to 500mm below the furnace mouth, close the CO 2 flow regulating valve, O 2 flow regulating valve, and infrared thermometer, and continue to raise the oxygen lance to the top of the furnace mouth In the cooling fume hood, close the protection system of the thermometer, continue to raise the oxygen lance to the original standby position and then close the cooling system of the oxygen lance.
  • the smoke and dust emission of the converter is reduced by 8.2%
  • the gas recovery volume is increased by 5.9 m 3 /t
  • the steel material consumption is reduced by 2.4 kg/t.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Carbon Steel Or Casting Steel Manufacturing (AREA)

Abstract

一种转炉CO 2-O 2混合喷吹冶炼方法和火点区温度动态控制方法。该方法通过安装于氧枪（1）内部的红外温度传感器实现在线监测，根据冶炼不同时期火点区温度变化及工艺要求，动态调节CO 2与O 2的混合比例和氧枪枪位高度，实现冶炼二级系统联锁动态控制火点区温度和熔池升温速率。

Description

转炉 CO2-O2 混合喷吹冶炼方法和火点区温度动态控制方法 技术领域
本公开涉及钢铁冶金技术领域，特别是转炉CO 2-O 2混合喷吹冶炼方法及其火点区温度动态控制方法。
背景技术
CO 2大量排放是产生温室效应的主要原因，每生产1吨钢将排放约2吨CO 2，CO 2的高效利用对于减少温室气体排放具有重要意义，因此开发新技术、探索新途径，实现钢铁行业CO 2排放的减少或消纳显得刻不容缓。
转炉冶炼过程中高速氧气射流与熔池接触，形成铁蒸发的高温火点区，产生大量烟尘，造成了环境污染，转炉的热损失增大，金属收得率降低，因此如何动态调节控制火点区温度对于减少炼钢烟尘的产生、提高金属收得率和热能利用率具有重要意义，但目前仍没有有效的方法实现火点区温度的连续监测，并根据火点区温度和冶炼要求实现火点区温度动态调节。
CO 2与[C]反应属于吸热反应(主要受[C]浓度和温度限制)，生成1.2-2倍的CO气泡，不仅能降低火点区温度和实现质能转换，而且能增强熔池搅拌，CO 2是一种最洁净的冷却剂，如何通过动态调节CO 2的混合比例，实现精确有效控制火点区温度对于降低转炉冶炼成本，提高金属收得率，增强冶炼工艺灵活度具有重要意义。
发明内容
本公开的实施例提供转炉CO 2-O 2混合喷吹冶炼方法和一种转炉CO 2-O 2混合喷吹冶炼火点区温度动态控制方法，能够动态调节转炉冶炼火点区温度和熔池升温速率，实现CO 2和熔池能量高效利用，减少炼钢烟尘产生量。
本公开的实施例提供的方法在氧枪内部安装红外测温仪，红外测温仪连接数据处理系统，数据处理系统连接冶炼二级系统，冶炼二级系统连接CO 2流量调节阀、O 2流量调节阀和氧枪控制系统，氧枪连接测温仪保护系统和氧枪冷却系统。
本公开的实施例提供一种转炉CO 2-O 2混合喷吹冶炼方法，其中，转炉CO 2-O 2混合喷吹冶炼过程包括冶炼开始阶段、升温造渣阶段、前期高效脱磷阶段、快速脱碳阶段和终点调控阶段；转炉CO 2-O 2混合喷吹冶炼方法包括：
分别在冶炼开始阶段、升温造渣阶段、前期高效脱磷阶段、快速脱碳阶段和终点调控阶段测量火点区温度，以便控制火点区温度和动态调节CO 2混入比例。
在一个实施例中，在冶炼开始阶段测量火点区温度为T 1，火点区温度要求控制小于T 2，基于T1与T2的差值ΔT动态调节CO 2混入比例；和/或
在升温造渣阶段，测得火点区温度T 1，控制火点区温度低于T 2＝2800℃，控制熔池升温速率范围10-30℃/min，根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.5-2.0％；和/或
在前期高效脱磷阶段，测量火点区温度，控制火点区温度低于2700℃，控制熔池升温速率范围5-18℃/min，根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.35-1.8％；和/或
在快速脱碳阶段，测得火点区温度T 1，控制火点区温度低于T 2＝2700℃，控制熔池升温速率范围24-40℃/min，根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.3-1.6％；和/或
在终点调控阶段，测得火点区温度T 1，要求控制火点区温度低于T 2＝2800℃，控制熔池升温速率范围14-30℃/min，根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.35-2.0％。
在一个实施例中，转炉CO 2-O 2混合喷吹冶炼过程还包括准备阶段；转炉CO 2-O 2混合喷吹冶炼方法包括：
根据入炉金属料条件、造渣剂条件、冷却剂条件和出钢目标要求，通过物料平衡和热平衡静态模型计算造渣剂和冷却剂加入量并制定加入制度；和/或
转炉兑铁后，下降氧枪至至炉口下方规定高度后通入CO 2和O 2，控制CO 2 和O 2的流量，测得火点区温度。
在一个实施例中，转炉CO 2-O 2混合喷吹冶炼过程还包括结束阶段；转炉CO 2-O 2混合喷吹冶炼方法包括：
提升氧枪至炉口下方一定高度后，关闭CO 2、O 2，继续提升氧枪至炉口上方一定高度，等待下一炉操作。
在一个实施例中，转炉CO 2-O 2混合喷吹冶炼方法包括：分析钢水成分及温度合格后，摇转转炉出钢。
在一个实施例中，转炉CO 2-O 2混合喷吹冶炼方法包括在氧枪内部安装红外测温仪，测量火点区温度。
在一个实施例中，转炉CO 2-O 2混合喷吹冶炼方法还包括：红外测温仪(2-1)连接数据处理系统(2-2)，数据处理系统(2-2)连接冶炼二级系统(3)，冶炼二级系统(3)连接CO 2流量调节阀(4-3)、O 2流量调节阀(4-4)和氧枪控制系统(5)，氧枪(1)连接测温仪保护系统(6)和氧枪冷却系统(7)。
在一个实施例中，在准备阶段中金属料条件包括铁水和废钢重量、温度。
在一个实施例中，所述氧枪(1)的供气流量为6000-100000Nm 3/h，其中O 2浓度大于97％，混合比例为50-100％，CO 2浓度大于90％，混合比例为0-50％，氧枪冷却系统(7)水流量为60-600m 3/h。
在一个实施例中，所述红外测温仪(2-1)传输4-20mA电信号，红外光谱为4-30um，单激光或双激光瞄准形式，仪表外径为5-40mm，红外线轴线与氧枪喷头喷孔轴线夹角为0-70°。
在一个实施例中，所述测温仪保护系统(6)确保红外测温仪(2-1)温度为0-70℃，保护气介质为N 2、Ar、CO 2任意一种或任意两种以上的混合气体，保护气气体流量为500-10000Nm 3/h，保护气管路内径为5-200mm。
在一个实施例中，所述数据处理系统(2-2)将4-20mA电信号转换为数字信号。
在一个实施例中，该方法适用于30-400t转炉CO 2-O 2混合喷吹冶炼。
本公开的实施例提供一种转炉CO 2-O 2混合喷吹冶炼火点区温度动态控制方法，其中转炉CO 2-O 2混合喷吹冶炼过程包括冶炼开始阶段、升温造渣阶段、前期高效脱磷阶段、快速脱碳阶段和终点调控阶段；
转炉CO 2-O 2混合喷吹冶炼火点区温度动态控制方法包括：分别在冶炼开始阶段、升温造渣阶段、前期高效脱磷阶段、快速脱碳阶段和终点调控阶段测量火点区温度，以便控制火点区温度，动态调节CO 2混入比例。
在一个实施例中，该方法在氧枪(1)内部安装红外测温仪(2-1)，红外测温仪(2-1)连接数据处理系统(2-2)，数据处理系统(2-2)连接冶炼二级系统(3)，冶炼二级系统(3)连接CO 2流量调节阀(4-3)、O 2流量调节阀(4-4)和氧枪控制系统(5)，氧枪(1)连接测温仪保护系统(6)和氧枪冷却系统(7)方法包括如下步骤中的一个或多个：
在冶炼开始阶段，通过红外测温仪(2-1)测得火点区温度为T 1，火点区温度要求控制小于T 2，T 1与T 2的差值ΔT传入冶炼二级系统(3)，冶炼二级系统(3)动态调节CO 2混入比例；和/或
在冶炼前期0-3min为升温造渣阶段，利用红外测温仪(2-1)测得火点区温度T 1，要求控制火点区温度低于T 2＝2800℃，控制熔池升温速率范围10-30℃/min，冶炼二级系统(3)根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.5-2.0％；和/或
在冶炼前期3-5min为前期高效脱磷阶段，要求控制火点区温度低于2700℃，控制熔池升温速率范围5-18℃/min，冶炼二级系统(3)根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.35-1.8％；和/或
在冶炼中期5-10min为快速脱碳阶段，利用红外测温仪(2-1)测得火点区温度T 1，要求控制火点区温度低于T 2＝2700℃，控制熔池升温速率范围24-40℃/min，冶炼二级系统(3)根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.3-1.6％；和/或
在冶炼后期10-16min为终点调控阶段，利用红外测温仪(2-1)测得火点区温度T 1，要求控制火点区温度低于T 2＝2800℃，控制熔池升温速率范围14-30℃/min，冶炼二级系统(3)根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.35-2.0％。
在一个实施例中，转炉CO 2-O 2混合喷吹冶炼火点区温度动态控制方法，还包括：
冶炼二级系统(3)根据入炉金属料条件、造渣剂条件、冷却剂条件和出钢目标要求，通过物料平衡和热平衡静态模型计算造渣剂和冷却剂加入量并制定加入制度；和/或
转炉兑铁后，摇正转炉炉口至垂直位置，冶炼二级系统(3)打开氧枪冷却系统(7)后，控制氧枪控制系统(5)下降氧枪至炉口上方，打开测温仪保护系统(6)，继续下降至炉口下方规定高度后打开CO 2流量调节阀(4-3)、O 2流量调节阀(4-4)和红外测温仪(2-1)，利用红外测温仪(2-1)测取火点区温度；和/或
吹炼结束，冶炼二级系统(3)控制氧枪控制系统(5)提升氧枪至炉口下方，关闭CO 2流量调节阀(4-3)、O 2流量调节阀(4-4)、红外测温仪(2-1)，继续提升氧枪至炉口上方后关闭测温仪保护系统(6)，氧枪提升至原始待用位后关闭氧枪冷却系统(7)，等待下一炉操作；和/或
分析钢水成分及温度合格后，摇转转炉出钢。
在一个实施例中，所述准备阶段中金属料条件包括铁水和废钢重量、温度。
在一个实施例中，所述氧枪(1)的供气流量为6000-100000Nm 3/h，其中O 2浓度大于97％，混合比例为50-100％，CO 2浓度大于90％，混合比例为0-50％，氧枪冷却系统(7)水流量为60-600m 3/h。
在一个实施例中，所述红外测温仪(2-1)传输4-20mA电信号，红外光谱为4-30um，单激光或双激光瞄准形式，仪表外径为5-40mm，红外线轴线与氧枪喷头喷孔轴线夹角为0-70°。
在一个实施例中，所述测温仪保护系统(6)确保红外测温仪(2-1)温度为0-70℃，保护气介质为N 2、Ar、CO 2任意一种或任意两种以上的混合气体，保护气气体流量为500-10000Nm 3/h，保护气管路内径为5-200mm。
在一个实施例中，所述数据处理系统(2-2)将4-20mA电信号转换为数字信号。
附图说明
图1为本公开的转炉CO 2-O 2混合喷吹冶炼火点区温度动态控制方法系统结构示意图；
图2为本公开的非接触式红外测温仪装配示意图；
图3为图2中A向剖视图；
图4为本公开实施例中冶炼过程中氧枪枪位与CO 2流量变化曲线。
其中：1：氧枪；2-1：红外测温仪；2-2：数据处理系统；3：冶炼二级系统；4-1：CO 2储气罐；4-2：O 2储气罐；4-3：CO 2流量调节阀；4-4：O 2流量调节阀；4-5：CO 2-O 2混气装置；5：氧枪控制系统；6：测温仪保护系统；7：氧枪冷却系统。
具体实施方式
为使本公开要解决的技术问题、技术方案和优点更加清楚，下面将结合附图及具体实施例进行详细描述。
本公开的实施例提供一种转炉CO 2-O 2混合喷吹冶炼火点区温度动态控制方法，该方法利用安装在氧枪内部的红外测温仪测量火点区温度，根据火点区温度变化情况动态调节CO 2流量、O 2流量，实现动态调节火点区温度和熔池升温速率，实现高效利用转炉冶炼过程中的能量，降低钢铁料消耗，减少炼钢烟尘排放量和炉渣产生量。
如图1、图2和图3所示，在一个实施例中，在该方法中在氧枪1内部安装红外测温仪2-1，红外测温仪2-1连接数据处理系统2-2，数据处理系统2-2连接冶炼二级系统3，冶炼二级系统3连接CO 2流量调节阀4-3、O 2流量调节阀4-4和氧枪控制系统5，氧枪1连接测温仪保护系统6和氧枪冷却系统7；CO 2流量调节阀4-3连接CO 2储气罐4-1，O 2流量调节阀4-4连接O 2储气罐4-2，CO 2流量调节阀4-3和O 2流量调节阀4-4之后的管道合并到CO 2-O 2混气装置4-5处进行混气。
该方法在CO 2-O 2混合喷吹冶炼过程中，利用安装在氧枪内部的红外测温仪测量火点区温度，将电信号传递给数据处理系统，再将处理后的数字信号传递给冶炼二级系统，根据火点区温度变化情况动态调节CO 2流量调节阀、O 2流量调节阀和氧枪控制系统，实现动态调节火点区温度和熔池升温速率，实现高效 利用转炉冶炼过程中的能量，降低钢铁料消耗，减少炼钢烟尘排放量和炉渣产生量。
在一个实施例中，一种转炉CO 2-O 2混合喷吹冶炼方法，其中，转炉CO 2-O 2混合喷吹冶炼过程包括冶炼开始阶段、升温造渣阶段、前期高效脱磷阶段、快速脱碳阶段和终点调控阶段。转炉CO 2-O 2混合喷吹冶炼方法包括：
分别在冶炼开始阶段、升温造渣阶段、前期高效脱磷阶段、快速脱碳阶段和终点调控阶段测量火点区温度，以便控制火点区温度和动态调节CO 2混入比例。
在一个实施例中，在冶炼开始阶段通过红外测温仪2-1测量火点区温度以便控制火点区温度，从而动态调节CO 2混入比例。例如，在冶炼开始阶段通过红外测温仪2-1测量火点区温度为T 1，火点区温度要求控制小于T 2，基于T 1与T 2的差值ΔT动态调节CO 2混入比例，例如将T 1与T 2的差值ΔT传入冶炼二级系统3，冶炼二级系统3动态调节CO 2混入比例。
在一个实施例中，在升温造渣阶段，利用红外测温仪2-11测量火点区温度以便控制火点区温度，从而动态调节CO 2混入比例。例如，利用红外测温仪2-1测得火点区温度T 1，要求控制火点区温度低于T 2＝2800℃，控制熔池升温速率范围10-30℃/min，冶炼二级系统3根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.5-2.0％。
在一个实施例中，在前期高效脱磷阶段，利用红外测温仪2-11测量火点区温度以便控制熔池温度、熔池升温速率和动态调节CO 2混入比例。例如，在前期高效脱磷阶段，要求控制火点区温度低于2700℃，控制熔池升温速率范围5-18℃/min，冶炼二级系统3根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.35-1.8％。
在一个实施例中，在快速脱碳阶段，利用红外测温仪2-11测量火点区温度以便控制熔池温度、熔池升温速率和动态调节CO 2混入比例。例如，在快速脱碳阶段，利用红外测温仪2-1测得火点区温度T 1，要求控制火点区温度低于T 2＝2700℃，控制熔池升温速率范围24-40℃/min，冶炼二级系统3根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃， CO 2混合比例对应调整0.3-1.6％。
在一个实施例中，在终点调控阶段，利用红外测温仪2-11测量火点区温度以便控制熔池温度、熔池升温速率和动态调节CO 2混入比例。例如，在终点调控阶段，利用红外测温仪2-1测得火点区温度T 1，要求控制火点区温度低于T 2＝2800℃，控制熔池升温速率范围14-30℃/min，冶炼二级系统3根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.35-2.0％。
在一个实施例中，转炉CO 2-O 2混合喷吹冶炼过程还可以包括准备阶段和结束阶段。
在一个实施例中，准备阶段可以包括冶炼二级系统3根据入炉金属料条件、造渣剂条件、冷却剂条件和出钢目标要求，通过物料平衡和热平衡静态模型计算造渣剂和冷却剂加入量并制定加入制度。
在一个实施例中，准备阶段还可以包括转炉兑铁后，摇正转炉炉口至垂直位置，冶炼二级系统3打开氧枪冷却系统7后，控制氧枪控制系统5下降氧枪至炉口上方一定高度后，打开测温仪保护系统6，继续下降至炉口下方规定高度后打开CO 2流量调节阀4-3、O 2流量调节阀4-4和红外测温仪2-1，利用红外测温仪2-1测取火点区温度。
在一个实施例中，结束阶段可以包括：吹炼结束，冶炼二级系统3控制氧枪控制系统5提升氧枪至炉口下方一定高度后，关闭CO 2流量调节阀4-3、O 2流量调节阀4-4、红外测温仪2-1，继续提升氧枪至炉口上方一定高度后关闭测温仪保护系统6，氧枪提升至原始待用位后关闭氧枪冷却系统7，等待下一炉操作。
转炉CO 2-O 2混合喷吹冶炼过程还可以包括分析钢水成分及温度合格后，摇转转炉出钢。
本公开的实施例还提供一种转炉CO 2-O 2混合喷吹冶炼火点区温度动态控制方法。具体地，该方法可以包括如下步骤的至少部分。
在转炉CO 2-O 2混合喷吹冶炼过程包括冶炼开始阶段、升温造渣阶段、前期高效脱磷阶段、快速脱碳阶段和终点调控阶段，转炉CO 2-O 2混合喷吹冶炼火点区温度动态控制方法包括分别在冶炼开始阶段、升温造渣阶段、前期高效脱磷 阶段、快速脱碳阶段和终点调控阶段测量火点区温度，以便控制火点区温度，将火点区温度的信息传入冶炼二级系统3中，冶炼二级系统3动态调节CO 2混入比例。下面具体地描述方法。
S1：冶炼二级系统3根据入炉金属料条件、造渣剂条件、冷却剂条件和出钢目标要求，通过物料平衡和热平衡静态模型计算造渣剂和冷却剂加入量并制定加入制度；
S2：转炉兑铁后，摇正转炉炉口至垂直位置，冶炼二级系统3打开氧枪冷却系统7后，控制氧枪控制系统5下降氧枪至炉口上方一定高度后，打开测温仪保护系统6，继续下降至炉口下方规定高度后打开CO 2流量调节阀4-3、O 2流量调节阀4-4和红外测温仪2-1，利用红外测温仪2-1测取火点区温度；
S3：冶炼开始阶段，通过红外测温仪2-1测得火点区温度为T 1，火点区温度要求控制小于T 2，T 1与T 2的差值ΔT传入冶炼二级系统3，冶炼二级系统3动态调节CO 2混入比例；
S4：冶炼前期0-3min为升温造渣阶段，利用红外测温仪2-1测得火点区温度T 1，要求控制火点区温度低于T 2＝2800℃，控制熔池升温速率范围10-30℃/min，冶炼二级系统3根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.5-2.0％；
S5：冶炼前期3-5min为前期高效脱磷阶段，要求控制火点区温度低于2700℃，控制熔池升温速率范围5-18℃/min，冶炼二级系统3根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.35-1.8％；
S6：冶炼中期5-10min为快速脱碳阶段，利用红外测温仪2-1测得火点区温度T 1，要求控制火点区温度低于T 2＝2700℃，控制熔池升温速率范围24-40℃/min，冶炼二级系统3根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.3-1.6％；
S7：冶炼后期10-16min为终点调控阶段，利用红外测温仪2-1测得火点区温度T 1，要求控制火点区温度低于T 2＝2800℃，控制熔池升温速率范围14-30℃/min，冶炼二级系统3根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.35-2.0％；
S8：吹炼结束，冶炼二级系统3控制氧枪控制系统5提升氧枪至炉口下方一定高度后，关闭CO 2流量调节阀4-3、O 2流量调节阀4-4、红外测温仪2-1，继续提升氧枪至炉口上方一定高度后关闭测温仪保护系统6，氧枪提升至原始待用位后关闭氧枪冷却系统7，等待下一炉操作；
S9：分析钢水成分及温度合格后，摇转转炉出钢。
下面通过一个具体实施例予以说明。在本实施例中，为了理解本公开的技术内容，给出了具体的特定技术参数，然而，应该理解这些参数并不是为了限制本公开的实施例，相反，根据下面公开的实施例本领域技术人员可以得出本公开的其他实施例。
1)在本实施例中，所述方法应用于260t转炉炼钢，选用外管直径402mm的氧枪，顶吹气体为O 2与CO 2的混合气，气体总流量为57000Nm 3/h，红外测温仪外径为15mm，喷头中心孔直径为30mm，保护气介质为N2和Ar，冶炼后期将N2切换为Ar，保护气流量为2500Nm 3/h；
2)冶炼二级系统根据入炉金属料条件(铁水和废钢重量、温度)、造渣剂条件、冷却剂条件和出钢目标要求，通过物料平衡和热平衡静态模型计算造渣剂和冷却剂加入量并制定加入制度。铁水重量为249t，废钢重量为39t，石灰加入量为35kg/t，轻烧白云石14.8kg/t。铁水参数、废钢参数和造渣剂参数如表1和表2所示。
表1 铁水、废钢和钢水参数
名称 C/％ Si/％ Mn/％ P/％ S/％ 温度/℃
铁水 4.2 0.43 0.14 0.07 0.018 1312
废钢 0.10 0.05 0.20 0.015 0.010 25
钢水 0.05 0.003 0.072 0.012 0.010 1670
表2 造渣剂成分
名称 CaO/％ SiO 2/％ MgO/％
石灰 82 4 3
轻烧白云石 50 1 35
转炉装废钢和兑铁后，摇正转炉炉口至垂直位置，冶炼二级系统打开氧枪冷却系统，待水流量大于400m 3/h，且压力稳定后，控制氧枪控制系统下降氧枪至炉口上方的活动烟罩内，打开测温仪保护系统，喷吹N 2，流量为800Nm 3/h， 继续下降氧枪至炉口下方500mm后，打开O 2流量调节阀和红外测温仪，O 2流量为57000Nm 3/h，测温仪保护气N 2流量调节至2500Nm 3/h，继续降低氧枪高度至开吹枪位2.3m，加入50％造渣剂。
冶炼前期(0-3min)为升温造渣阶段，吹炼开始，红外测温仪使用双激光瞄准器，测得电信号经计算机处理系统处理后的火点区温度T 1＝2980℃，超过火点区控制温度(2800℃)180℃，冶炼二级系统依据热平衡计算CO 2的混合量，打开CO 2流量调节阀，动态调节CO 2混合比例为9.4％，连续监测过程中ΔT每变化10℃，CO 2比例相应调节0.52％。(前期温度限制CO 2与[C]的反应率，CO 2利用率较低。)，保持火点区稳定控制在2800℃以下，控制熔池平均升温速率为19℃/min(前期[Si]、[Mn]、[P]和[Fe]元素与O 2反应放热造成熔池的快速升温)。
冶炼前期(3-5min)为前期高效脱磷阶段，控制火点区温度低于2700℃，控制熔池平均升温速率10℃/min。冶炼开始3min，红外测温仪测得火点区温度T 1＝2790℃，超过火点区控制温度(2700℃)90℃，冶炼二级系统依据热平衡计算CO 2的混合量，动态调节CO 2混合比例为12.3％，连续监测过程中ΔT每变化10℃，CO 2比例相应调节0.41％(由于温度升高，CO 2利用率提高。)，为前期脱磷提供“低温”热力学条件的同时，实现减少铁氧化，降低烟尘产生量。
冶炼过程进入快速脱碳阶段(5-11min)，熔池中的[C]快速氧化，不仅造成火点区温度和熔池升温速度加快，而且会产生大量烟尘，但由于温度和熔池中[C]浓度较高，有利于提高CO 2的反应率。为保证出钢温度满足要求，控制火点区温度低于2700℃(此阶段的CO产生量较大，需要控制更低的火点区温度才能有效抑制烟尘产生。)，控制熔池平均升温速率30℃/min。冶炼开始5min，红外测温仪测得火点区温度T 1为2690℃，低于火点区控制温度(2700℃)10℃，冶炼二级系统依据热平衡计算CO 2的混合量，动态调节CO 2混合比例为9.6％，连续监测过程中ΔT每变化10℃，CO 2比例相应调节0.32％(相对冶炼前期熔池温度和[C]浓度较高，有利于提高CO 2的反应率)。
冶炼后期(11-15min)终点调控阶段，主要任务是调控钢水成分和温度，满足出钢要求。为保证出钢温度和成分，控制火点区温度低于2800℃，控制熔池平均升温速率22.5℃/min。冶炼开始11min，红外测温仪测得火点区温度 T 1为2680℃，低于火点区控制温度(2700℃)20℃，冶炼二级系统依据热平衡计算CO 2的混合量，动态调节CO 2混合比例为10.8％，连续监测过程中ΔT每变化10℃，CO 2比例相应调节0.36％((此阶段熔池中的[C]浓度限制CO 2与[C]的反应，CO 2利用率降低，为减少[Fe]氧化和提高金属收得率，需增强熔池搅拌。)。
吹炼结束后，冶炼二级系统控制氧枪控制系统提升氧枪至炉口下方500mm时，关闭CO 2流量调节阀、O 2流量调节阀、红外测温仪，继续提升氧枪至炉口上方冷却烟罩内，关闭测温仪保护系统，继续提升氧枪至原始待用位后关闭氧枪冷却系统。
采用副枪或其他分析方法，分析钢水成分及温度合格后，摇炉出钢。
上述冶炼过程中氧枪枪位与CO 2流量变化曲线如图4所示。
采用本公开所述方法后，转炉烟尘排放量减少8.2％，煤气回收量增加5.9m 3/t，钢铁料消耗降低2.4kg/t。
以上所述是本公开的多个实施方式，应当指出，对于本技术领域的普通技术人员来说，在不脱离本公开所述原理的前提下，还可以做出若干改进和润饰，这些改进和润饰也应视为本公开的保护范围。

Claims (21)

  1. 一种转炉CO 2-O 2混合喷吹冶炼方法，其中，转炉CO 2-O 2混合喷吹冶炼过程包括冶炼开始阶段、升温造渣阶段、前期高效脱磷阶段、快速脱碳阶段和终点调控阶段；转炉CO 2-O 2混合喷吹冶炼方法包括：
    分别在冶炼开始阶段、升温造渣阶段、前期高效脱磷阶段、快速脱碳阶段和终点调控阶段测量火点区温度，以便控制火点区温度和动态调节CO 2混入比例。
  2. 根据权利要求1所述的转炉CO 2-O 2混合喷吹冶炼方法，其中，
    在冶炼开始阶段测量火点区温度为T 1，火点区温度要求控制小于T 2，基于T1与T2的差值ΔT动态调节CO 2混入比例；和/或
    在升温造渣阶段，测得火点区温度T 1，控制火点区温度低于T 2＝2800℃，控制熔池升温速率范围10-30℃/min，根据T1与T2的差值ΔT和热平衡动态实时调节C() 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.5-2.0％；和/或
    在前期高效脱磷阶段，测量火点区温度，控制火点区温度低于2700℃，控制熔池升温速率范围5-18℃/min，根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.35-1.8％；和/或
    在快速脱碳阶段，测得火点区温度T 1，控制火点区温度低于T 2＝2700℃，控制熔池升温速率范围24-40℃/min，根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.3-1.6％；和/或
    在终点调控阶段，测得火点区温度T 1，要求控制火点区温度低于T 2＝2800℃，控制熔池升温速率范围14-30℃/min，根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.35-2.0％。
  3. 根据权利要求1所述的转炉CO 2-O 2混合喷吹冶炼方法，转炉CO 2-O 2混合喷吹冶炼过程还包括准备阶段；转炉CO 2-O 2混合喷吹冶炼方法包括：
    根据入炉金属料条件、造渣剂条件、冷却剂条件和出钢目标要求，通过物 料平衡和热平衡静态模型计算造渣剂和冷却剂加入量并制定加入制度；和/或转炉兑铁后，下降氧枪至至炉口下方规定高度后通入CO 2和O 2，控制CO 2和O 2的流量，测得火点区温度。
  4. 根据权利要求1所述的转炉CO 2-O 2混合喷吹冶炼方法，转炉CO 2-O 2混合喷吹冶炼过程还包括结束阶段；转炉CO 2-O 2混合喷吹冶炼方法包括：
    提升氧枪至炉口下方一定高度后，关闭CO 2、O 2，继续提升氧枪至炉口上方一定高度，等待下一炉操作。
  5. 根据权利要求1所述的转炉CO 2-O 2混合喷吹冶炼方法，包括：分析钢水成分及温度合格后，摇转转炉出钢。
  6. 根据权利要求1所述的转炉CO 2-O 2混合喷吹冶炼方法，包括在氧枪内部安装红外测温仪，测量火点区温度。
  7. 根据权利要求6所述的转炉CO 2-O 2混合喷吹冶炼方法，还包括：红外测温仪(2-1)连接数据处理系统(2-2)，数据处理系统(2-2)连接冶炼二级系统(3)，冶炼二级系统(3)连接C() 2流量调节阀(4-3)、O 2流量调节阀(4-4)和氧枪控制系统(5)，氧枪(1)连接测温仪保护系统(6)和氧枪冷却系统(7)。
  8. 根据权利要求3所述的转炉CO 2-O 2混合喷吹冶炼方法，其中：在准备阶段中金属料条件包括铁水和废钢重量、温度。
  9. 根据权利要求7所述的转炉CO 2-O 2混合喷吹冶炼方法，其中：所述氧枪(1)的供气流量为6000-100000Nm 3/h，其中O 2浓度大于97％，混合比例为50-100％，CO 2浓度大于90％，混合比例为0-50％，氧枪冷却系统(7)水流量为60-600m 3/h。
  10. 根据权利要求7所述的转炉CO 2-O 2混合喷吹冶炼方法，其中：所述红外测温仪(2-1)传输4-20mA电信号，红外光谱为4-30um，单激光或双激光瞄准形式，仪表外径为5-40mm，红外线轴线与氧枪喷头喷孔轴线夹角为0-70°。
  11. 根据权利要求7所述的转炉CO 2-O 2混合喷吹冶炼方法，其中：所述测温仪保护系统(6)确保红外测温仪(2-1)温度为0-70℃，保护气介质为N 2、Ar、CO 2任意一种或任意两种以上的混合气体，保护气气体流量为500-10000Nm 3/h，保护气管路内径为5-200mm。
  12. 根据权利要求7所述的转炉CO 2-O 2混合喷吹冶炼方法，其中：所述数据处理系统(2-2)将4-20mA电信号转换为数字信号。
  13. 根据权利要求1所述的转炉CO 2-O 2混合喷吹冶炼方法，其中：该方法适用于30-400t转炉CO 2-O 2混合喷吹冶炼。
  14. 一种转炉CO 2-O 2混合喷吹冶炼火点区温度动态控制方法，其中转炉CO 2-O 2混合喷吹冶炼过程包括冶炼开始阶段、升温造渣阶段、前期高效脱磷阶段、快速脱碳阶段和终点调控阶段；
    转炉CO 2-O 2混合喷吹冶炼火点区温度动态控制方法包括：分别在冶炼开始阶段、升温造渣阶段、前期高效脱磷阶段、快速脱碳阶段和终点调控阶段测量火点区温度，以便控制火点区温度，动态调节CO 2混入比例。
  15. 根据权利要求14所述的转炉CO 2-O 2混合喷吹冶炼火点区温度动态控制方法，该方法在氧枪(1)内部安装红外测温仪(2-1)，红外测温仪(2-1)连接数据处理系统(2-2)，数据处理系统(2-2)连接冶炼二级系统(3)，冶炼二级系统(3)连接CO 2流量调节阀(4-3)、O 2流量调节阀(4-4)和氧枪控制系统(5)，氧枪(1)连接测温仪保护系统(6)和氧枪冷却系统(7)方法包括如下步骤中的一个或多个：
    在冶炼开始阶段，通过红外测温仪(2-1)测得火点区温度为T 1，火点区温度要求控制小于T 2，T 1与T 2的差值ΔT传入冶炼二级系统(3)，冶炼二级系统(3)动态调节CO 2混入比例；和/或
    在冶炼前期0-3min为升温造渣阶段，利用红外测温仪(2-1)测得火点区温度T 1，要求控制火点区温度低于T 2＝2800℃，控制熔池升温速率范围10-30℃/min，冶炼二级系统(3)根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.5-2.0％；和/或
    在冶炼前期3-5min为前期高效脱磷阶段，要求控制火点区温度低于2700℃，控制熔池升温速率范围5-18℃/min，冶炼二级系统(3)根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.35-1.8％；和/或
    在冶炼中期5-10min为快速脱碳阶段，利用红外测温仪(2-1)测得火点 区温度T 1，要求控制火点区温度低于T 2＝2700℃，控制熔池升温速率范围24-40℃/min，冶炼二级系统(3)根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.3-1.6％；和/或
    在冶炼后期10-16min为终点调控阶段，利用红外测温仪(2-1)测得火点区温度T 1，要求控制火点区温度低于T 2＝2800℃，控制熔池升温速率范围14-30℃/min，冶炼二级系统(3)根据T1与T2的差值ΔT和热平衡动态实时调节CO 2混入比例，所述ΔT值每变化10℃，CO 2混合比例对应调整0.35-2.0％。
  16. 根据权利要求15所述的转炉CO 2-O 2混合喷吹冶炼火点区温度动态控制方法，还包括：
    冶炼二级系统(3)根据入炉金属料条件、造渣剂条件、冷却剂条件和出钢目标要求，通过物料平衡和热平衡静态模型计算造渣剂和冷却剂加入量并制定加入制度；和/或
    转炉兑铁后，摇正转炉炉口至垂直位置，冶炼二级系统(3)打开氧枪冷却系统(7)后，控制氧枪控制系统(5)下降氧枪至炉口上方，打开测温仪保护系统(6)，继续下降至炉口下方规定高度后打开CO 2流量调节阀(4-3)、O 2流量调节阀(4-4)和红外测温仪(2-1)，利用红外测温仪(2-1)测取火点区温度；和/或
    吹炼结束，冶炼二级系统(3)控制氧枪控制系统(5)提升氧枪至炉口下方，关闭CO 2流量调节阀(4-3)、O 2流量调节阀(4-4)、红外测温仪(2-1)，继续提升氧枪至炉口上方后关闭测温仪保护系统(6)，氧枪提升至原始待用位后关闭氧枪冷却系统(7)，等待下一炉操作；和/或
    分析钢水成分及温度合格后，摇转转炉出钢。
  17. 根据权利要求16所述的转炉CO 2-O 2混合喷吹冶炼火点区温度动态控制方法，其中：在准备阶段中金属料条件包括铁水和废钢重量、温度。
  18. 根据权利要求16所述的转炉CO 2-O 2混合喷吹冶炼火点区温度动态控制方法，其中：所述氧枪(1)的供气流量为6000-100000Nm 3/h，其中O 2浓度大于97％，混合比例为50-100％，CO 2浓度大于90％，混合比例为0-50％，氧枪冷却系统(7)水流量为60-600m 3/h。
  19. 根据权利要求16所述的转炉CO 2-O 2混合喷吹冶炼火点区温度动态控制方法，其中：所述红外测温仪(2-1)传输4-20mA电信号，红外光谱为4-30um，单激光或双激光瞄准形式，仪表外径为5-40mm，红外线轴线与氧枪喷头喷孔轴线夹角为0-70°。
  20. 根据权利要求16所述的转炉CO 2-O 2混合喷吹冶炼火点区温度动态控制方法，其中：所述测温仪保护系统(6)确保红外测温仪(2-1)温度为0-70℃，保护气介质为N 2、Ar、CO 2任意一种或任意两种以上的混合气体，保护气气体流量为500-10000Nm 3/h，保护气管路内径为5-200mm。
  21. 根据权利要求16所述的转炉CO 2-O 2混合喷吹冶炼火点区温度动态控制方法，其中：所述数据处理系统(2-2)将4-20mA电信号转换为数字信号。
PCT/CN2020/073500 2019-10-16 2020-01-21 转炉 co2-o2 混合喷吹冶炼方法和火点区温度动态控制方法 WO2021073015A1 (zh)

Priority Applications (2)

Application Number Priority Date Filing Date Title
US17/049,449 US11788160B2 (en) 2019-10-16 2020-01-21 Converter CO2—O2 mixed injection smelting method and method of dynamically controlling fire point area temperature
AU2020257077A AU2020257077A1 (en) 2019-10-16 2020-01-21 Converter CO2-O2 mixed injection smelting method and method of dynamically controlling fire point area temperature

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201910984480.2A CN110804684B (zh) 2019-10-16 2019-10-16 一种转炉co2-o2混合喷吹冶炼火点区温度动态控制方法
CN201910984480.2 2019-10-16

Publications (1)

Publication Number Publication Date
WO2021073015A1 true WO2021073015A1 (zh) 2021-04-22

Family

ID=69488761

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2020/073500 WO2021073015A1 (zh) 2019-10-16 2020-01-21 转炉 co2-o2 混合喷吹冶炼方法和火点区温度动态控制方法

Country Status (4)

Country Link
US (1) US11788160B2 (zh)
CN (1) CN110804684B (zh)
AU (1) AU2020257077A1 (zh)
WO (1) WO2021073015A1 (zh)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114410877A (zh) * 2021-12-30 2022-04-29 钢铁研究总院 一种转炉冶炼过程中顶吹氧枪供氧工艺的自动控制方法
CN114774616A (zh) * 2022-04-26 2022-07-22 山东莱钢永锋钢铁有限公司 一种控制顶吹转炉氧枪枪位降低氧气消耗的方法
CN116240328A (zh) * 2021-12-03 2023-06-09 清华大学 转炉炼钢终点控制方法、系统、装置、设备、介质及产品
CN115595405B (zh) * 2022-09-27 2024-03-15 中国重型机械研究院股份公司 一种rh喷粉工艺的长寿喷吹装置及方法

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111500815B (zh) * 2020-05-28 2021-06-11 北京科技大学 一种底吹O2-CO2-CaO转炉炼钢过程动态控制方法
CN114317879B (zh) * 2022-01-26 2023-04-11 南京钢铁股份有限公司 一种化炉口氧枪控制方法
CN115747404A (zh) * 2022-11-07 2023-03-07 河钢乐亭钢铁有限公司 一种转炉过程冷料加入方法
CN115927784B (zh) * 2022-11-30 2023-07-14 北京科技大学 一种基于co2动态混合喷吹的转炉炼钢终点控制方法
CN115852083A (zh) * 2022-12-08 2023-03-28 北京科技大学 一种转炉高效顶底复吹二氧化碳二次燃烧低碳系统及方法
TWI827485B (zh) * 2023-03-16 2023-12-21 中國鋼鐵股份有限公司 用於預測分鋼槽內鋼液溫度的方法
CN116463469B (zh) * 2023-03-29 2024-03-26 北京科技大学 基于火点区发光检测的转炉炼钢自动控制系统及运行方法
CN116067900B (zh) * 2023-03-29 2023-06-16 北京科技大学 火点区自主发光监测熔池温度和成分数据分析方法及装置
CN117972999A (zh) * 2024-01-10 2024-05-03 北京科技大学 一种基于Fluent-UDF的转炉熔池火点区传热行为模拟方法

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0633127A (ja) * 1992-07-20 1994-02-08 Kawasaki Steel Corp 含クロム溶鉄の脱炭方法
JP2003328021A (ja) * 2002-05-16 2003-11-19 Jfe Steel Kk 低燐溶銑の製造方法
CN101250606A (zh) * 2008-04-16 2008-08-27 北京科技大学 一种利用co2气体减少炼钢烟尘产生的方法
CN101608250A (zh) * 2009-07-20 2009-12-23 北京科技大学 一种喷吹co2气体控制转炉炼钢熔池温度的方法
US20180163280A1 (en) * 2014-03-14 2018-06-14 Berry Metal Company Metal making lance with infrared camera in lance head
CN108165700A (zh) * 2018-03-02 2018-06-15 北京科技大学 一种安装于转炉底部的测温喷枪及使用方法
CN108359766A (zh) * 2018-03-02 2018-08-03 北京科技大学 一种基于钢水连续测温的底吹氧气转炉冶炼过程控制方法
CN108796163A (zh) * 2018-06-13 2018-11-13 北京科技大学 一种利用co2控制转炉氧枪射流冲击区高温火点的方法

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5594421A (en) * 1979-01-13 1980-07-17 Nippon Steel Corp Operating method in top blowing oxygen converter
CN108330242B (zh) * 2018-02-08 2019-03-15 北京科技大学 一种利用co2抑制转炉炼钢火点区吸氮的方法

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0633127A (ja) * 1992-07-20 1994-02-08 Kawasaki Steel Corp 含クロム溶鉄の脱炭方法
JP2003328021A (ja) * 2002-05-16 2003-11-19 Jfe Steel Kk 低燐溶銑の製造方法
CN101250606A (zh) * 2008-04-16 2008-08-27 北京科技大学 一种利用co2气体减少炼钢烟尘产生的方法
CN101608250A (zh) * 2009-07-20 2009-12-23 北京科技大学 一种喷吹co2气体控制转炉炼钢熔池温度的方法
US20180163280A1 (en) * 2014-03-14 2018-06-14 Berry Metal Company Metal making lance with infrared camera in lance head
CN108165700A (zh) * 2018-03-02 2018-06-15 北京科技大学 一种安装于转炉底部的测温喷枪及使用方法
CN108359766A (zh) * 2018-03-02 2018-08-03 北京科技大学 一种基于钢水连续测温的底吹氧气转炉冶炼过程控制方法
CN108796163A (zh) * 2018-06-13 2018-11-13 北京科技大学 一种利用co2控制转炉氧枪射流冲击区高温火点的方法

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN116240328A (zh) * 2021-12-03 2023-06-09 清华大学 转炉炼钢终点控制方法、系统、装置、设备、介质及产品
CN114410877A (zh) * 2021-12-30 2022-04-29 钢铁研究总院 一种转炉冶炼过程中顶吹氧枪供氧工艺的自动控制方法
CN114774616A (zh) * 2022-04-26 2022-07-22 山东莱钢永锋钢铁有限公司 一种控制顶吹转炉氧枪枪位降低氧气消耗的方法
CN115595405B (zh) * 2022-09-27 2024-03-15 中国重型机械研究院股份公司 一种rh喷粉工艺的长寿喷吹装置及方法

Also Published As

Publication number Publication date
US20220340986A1 (en) 2022-10-27
CN110804684A (zh) 2020-02-18
AU2020257077A1 (en) 2021-05-06
US11788160B2 (en) 2023-10-17
CN110804684B (zh) 2020-08-11

Similar Documents

Publication Publication Date Title
WO2021073015A1 (zh) 转炉 co2-o2 混合喷吹冶炼方法和火点区温度动态控制方法
CN106282487B (zh) 一种铁水预脱磷方法
Li et al. Numerical simulation of off-gas formation during top-blown oxygen converter steelmaking
CN112029956B (zh) 一种电弧炉炼钢的供氧方法
CN108165700A (zh) 一种安装于转炉底部的测温喷枪及使用方法
CN102732668B (zh) 一种预热氧气提高射流速度的吹氧炼钢方法
CN108728607B (zh) 一种LF炉动态底吹CO2-Ar精炼方法及装置
CN111575443B (zh) 一种aod炉冶炼低碳合金的供气装置及方法
CN103266195B (zh) 一种提高转炉冶炼脱磷的方法
CN108396102A (zh) 电炉冶炼特钢钢水的方法
CN110628983A (zh) 一种转炉冶炼火点区温度连续监测氧枪系统及监测方法
CN208071732U (zh) 一种安装于转炉底部的测温喷枪
US4405365A (en) Method for the fabrication of special steels in metallurgical vessels
CN103757173B (zh) 低石灰消耗的转炉炼钢方法
CN115927784B (zh) 一种基于co2动态混合喷吹的转炉炼钢终点控制方法
JP2602573B2 (ja) 金属精錬法
CN108977620B (zh) 一种提高转炉废钢比的单流道二次燃烧氧枪及其使用方法
CN107675069A (zh) 采用co2+o2混合气体吹炼实现脱碳保锰冶炼中高锰钢的方法
CN108588324B (zh) 转炉炼钢通过CO2高强度输入控制渣中(FeO)和粉尘产生的方法
CN109423533A (zh) 一种全量铁水转炉冶炼控制方法
CN208517458U (zh) 一种LF炉动态底吹CO2-Ar精炼装置系统
CN109280741A (zh) 一种奥氏体不锈钢精炼方法
CN204138734U (zh) 侧吹铅熔融还原装置
CN102140567A (zh) 一种氩氧精炼低碳铬铁合金方法
CN113862551B (zh) 氩氧精炼炉喷吹不锈钢除尘灰冶炼不锈钢的工艺控制方法

Legal Events

Date Code Title Description
ENP Entry into the national phase

Ref document number: 2020257077

Country of ref document: AU

Date of ref document: 20200121

Kind code of ref document: A

121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 20876058

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 20876058

Country of ref document: EP

Kind code of ref document: A1