CN101575656B - Oxygen top blown converter steel making method - Google Patents
Oxygen top blown converter steel making method Download PDFInfo
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- CN101575656B CN101575656B CN2009101473571A CN200910147357A CN101575656B CN 101575656 B CN101575656 B CN 101575656B CN 2009101473571 A CN2009101473571 A CN 2009101473571A CN 200910147357 A CN200910147357 A CN 200910147357A CN 101575656 B CN101575656 B CN 101575656B
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Abstract
The invention relates to an oxygen top blown converter steel making method, comprising the following steps: the steel material is added to a converter, oxygen is blown into the converter by an oxygen lance and auxiliary materials are added into the furnace by stages in the process of oxygen blowing; wherein the steel material comprises semisteel; lance position of the oxygen lance moves within 1.5-2.2m above molten steel liquid surface in the converter, wherein blowing beginning lance position is 1.95-2.05m, blowing lance position is 1.5-2.2m and catch carbon lance position is 1.7-1.75m; wherein, the auxiliary materials comprise compound slag, lime and high-magnesium lime; in every ton of semisteel, 17-20kg of the compound slag is used, 30-34.5kg of lime is used, 30-34.5kg of high-magnesium lime is used, a total of 43-53 cubic meters of oxygen is blown into the furnace; with the total content of the blown oxygen as a benchmark, the first batch of auxiliary materials are added when the oxygen blowing content is 0.8-2%; with the method of the invention adopted, steelmaking time can be reduced and slag splashing and drying can be effectively avoided in the process of steelmaking.
Description
Technical field
The present invention relates to a kind of method of oxygen top blown converter steel making.
Background technology
Climbing the steel steelworks raw materials used is the molten iron that contains V, Ti, for extracting the useful element vanadium in the molten iron, climb steel and adopt duplex technology, promptly molten iron need carry out vanadium extraction through special converter extracting vanadium, molten iron after the vanadium extraction becomes half steel, and the half steel molten iron is sent into steel-making converter and made steel then.Improve along with climbing steel variety steel output, particularly some high value added products require strict (wishing low as far as possible) to terminal point S, P, O and N content value, and how fast and effectively the low P of production, S steel become the bottleneck of producing high-quality steel.
Compare with common molten iron-steelmaking, climb the steel semi-steel making its singularity is arranged, Si in the half steel, Mn constituent content are very low, so its metallurgical performance is not good, desulfurization, dephosphorizing capacity are low, often rely on oxygen blast to come desulfurization, dephosphorization, thereby cause the quantity of slag to increase, slag charge consumes high, and iron and steel stock consumption is risen, and is limiting the raising of converter lining life and the shortening of smelting cycle.And Pan Gangtieshui is through vanadium extraction, and the C composition also has very big loss in the half steel molten iron, causes the semi-steel making shortage of heat, mainly relies on slag making repeatedly and oxygen blast guaranteeing steel-making terminal point composition and temperature, so FeO content height in the slag, slag oxidation are strong.So climbing steel converter, comprehensive above reason when smelting the steel grade of some high added values, need add a large amount of steelmaking ingredients, yet, strengthen a large amount of steelmaking ingredients and tend to bring operational difficulty to converter steelmaking, wayward splash and return dried (being furnace clinker), the efficient of making steel is very low.
Summary of the invention
The present invention is in order to add a large amount of steelmaking feeds and to make in the steelmaking process wayward splash and returning and do and make steel inefficient defective in the method for making steel that overcomes prior art, provide a kind of and add a large amount of steelmaking ingredients but the method for doing and making steel the high oxygen top blown converter steel making of efficient is not returned in not splash of steelmaking process in steelmaking process.
The invention provides a kind of method of oxygen top blown converter steel making, this method comprises the steel raw material is added in the converter, by oxygen rifle oxygen blast gas in converter, and adds auxiliary material in the oxygen blast process in converter in batches, and wherein, described steel raw material contains half steel; The rifle position of described oxygen rifle in converter liquid steel level above move in the scope of 1.5-2.2 rice, wherein, open that to blow the rifle position be 1.95-2.05 rice, blowing rifle position is a 1.5-2.2 rice, catch carbon rifle position is a 1.7-1.75 rice; Described auxiliary material comprises composite slag, lime and high magnesium lime, and with respect to half steel per ton, the consumption of composite slag is the 17-20 kilogram, and the consumption of lime is the 30-34.5 kilogram, and the consumption of high magnesium lime is the 30-34.5 kilogram, and the total amount that is blown into oxygen is the 43-53 cubic meter; With the total amount that is blown into oxygen is benchmark, when blowing oxygen quantity is 0.8-2%, add first auxiliary material, described first auxiliary material comprises the composite slag of the 78-85 weight % of the high magnesium lime of 58-65 weight % of lime, high magnesium lime total amount of the 57-63 weight % of lime total amount and composite slag total amount, and described composite slag is for being benchmark SiO with its gross weight
2Content be the composite fluxing medium of 40-70 weight %.
In the method for oxygen top blown converter steel making of the present invention, though added a large amount of auxiliary materials, but owing in steelmaking process, pass through the rifle position of control oxygen rifle and the adding moment and the add-on of auxiliary material, thereby avoided the splash in the steelmaking process effectively and returned driedly, and obviously improved the efficient of steel-making.Method for making steel provided by the invention is applicable to that Si, Mn in the various raw materials, C constituent content are very low, causes its metallurgical performance not good, and desulfurization, dephosphorizing capacity are low, and slag making must rely on to add and contain SiO
2Auxiliary slag making materials and the FeO that improves oxygen lance position and increase in the smelting process slag just can impel the lime fusing, and steel-making shortage of heat, mainly rely on slag making repeatedly and oxygen blast to guarantee steel-making terminal point composition and temperature, it is slower that thereby steel-making initial stage temperature slag low, that cover molten steel forms, the steel-making situation that the process slag oxidation is high.
Description of drawings
Fig. 1 represents the rifle position of embodiment of the invention 1-3 and the graph of a relation of blowing oxygen quantity.
Embodiment
In the present invention, described oxygen rifle can be the various rifle shape things that are used for to molten steel or molten iron injection of oxygen, both can be the conventional oxygen rifle that uses in present this area, also can be other the oxygen rifle that can realize above-mentioned functions.For ease of explanation, below be that example illustrates the present invention with the conventional oxygen rifle that uses in this area.Described rifle position is meant before the lower-most point of shower nozzle of oxygen rifle and the oxygen blast distance of liquid steel level in the converter; Described opening blown the rifle position and is meant before the lower-most point of the shower nozzle of oxygen rifle when beginning is blown into oxygen in converter and the oxygen blast distance of liquid steel level in the converter; Described blowing rifle position is meant that oxygen lance blow head was apart from the distance of bath surface when converter was normally blown; Described catch carbon rifle position is meant bessemerizes the latter stage oxygen lance blow head apart from the distance of bath surface.
The method of oxygen top blown converter steel making of the present invention comprises the steel raw material is added in the converter, by oxygen rifle oxygen blast gas in converter, and adds auxiliary material in the oxygen blast process in converter in batches.Described steel raw material comprises half steel, and common described half steel is meant through the half steel that obtains after the vanadium extraction, but also can be that molten iron is carried out the very low steel raw material that is in molten iron and molten steel intermediateness of Si, Mn, C constituent content that obtains after pre-treatment such as desulfurization, the deoxidation.Described half steel can be a benchmark for the total amount with half steel, contains the half steel of the iron of the vanadium of titanium, 0.02-0.06 weight % of sulphur, the 0.01-0.06 weight % of phosphorus, the 0.02-0.035 weight % of manganese, the 0.06-0.08 weight % of silicon, the 0.02-0.07 weight % of carbon, the 0.001-0.02 weight % of 3.2-4.4 weight % and 95.4-96.65 weight %.
The consumption of described auxiliary material and the total amount that is blown into oxygen can be made steel modeling by static state and be calculated.Generally, described auxiliary material comprises composite slag, lime and high magnesium lime, and with respect to half steel per ton, the consumption of composite slag is the 17-20 kilogram, the consumption of lime is the 30-34.5 kilogram, and the consumption of high magnesium lime is the 30-34.5 kilogram, and the total amount that is blown into oxygen is the 43-53 cubic meter.Under the preferable case, with respect to half steel per ton, the consumption of described composite slag is the 17.42-19.7 kilogram, and the consumption of described lime is the 30.3-34.09 kilogram, and the consumption of described high magnesium lime is the 30.3-34.09 kilogram, and the total amount that is blown into oxygen is the 45.5-51.3 cubic meter.Described composite slag is for being benchmark SiO with its gross weight
2Content be the composite fluxing medium of 40-70 weight %, described composite slag for example can be acid composite slag, SiO in described acid composite slag
2Content be generally 45-55 weight %, normally used acid composite slag for example can be quartz sand.Described lime and high magnesium lime are mainly used in sulphur and the phosphorus of sloughing in the stove half steel composition.Described lime mainly contains CaO, and is benchmark with the gross weight of described lime, and the content of CaO is 85-90 weight %.Described high magnesium lime mainly contains MgO and CaO, is benchmark with the gross weight of described high magnesium lime, and the content of MgO is 30-40 weight %, and the content of CaO is 48-55 weight %.
Be blown into to converter in the process of oxygen, the flow of oxygen can adopt and well known to a person skilled in the art parameter, for example 20000-30000 standard cubic meter (Nm
3)/hour.Under the preferable case, in oxygen blown initial stage and mid-term, with the flow control of oxygen be the 25000-30000 standard cubic meter/hour; Be benchmark with the total amount that is blown into oxygen, when blowing oxygen quantity is 89-90%, with the flow control of oxygen be 20000 standard cubic meter/hour to less than 25000 standard cubic meter/hour.Control the flow of oxygen in described preferred mode and can control steel-making terminal point composition and temperature exactly.
In method for making steel of the present invention, the rifle position of described oxygen rifle can be in converter liquid steel level above move in the scope of 1.4-2.2 rice, particularly, will open and blow the rifle position and be controlled to be 1.95-2.05 rice, blowing rifle position is controlled to be 1.5-2.2 rice, and catch carbon rifle position is controlled to be 1.7-1.75 rice; Simultaneously add auxiliary material according to blowing oxygen quantity in batches, particularly, with the total amount that is blown into oxygen is benchmark, when blowing oxygen quantity is 0.8-2%, add first auxiliary material, described first auxiliary material comprises the composite slag of the 78-85 weight % of the high magnesium lime of 58-65 weight % of lime, high magnesium lime total amount of the 57-63 weight % of lime total amount and composite slag total amount.Can prevent the splash in the steelmaking process effectively and return dried phenomenon by adopt aforesaid way to control the rifle position of oxygen rifle and add auxiliary material in batches, and can smelt qualified molten steel fast, thereby improve steel-making efficient effectively according to blowing oxygen quantity.In the preferred case, the lot number that adds auxiliary material in the oxygen blast process in converter is 3-9, and with the total amount that is blown into oxygen is benchmark, when blowing oxygen quantity is 28-32%, add second batch of auxiliary material, described second batch of auxiliary material comprises the composite slag of the 0-15 weight % of the high magnesium lime of 8-30 weight % of lime, high magnesium lime total amount of the 8-30 weight % of lime total amount and composite slag total amount; When blowing oxygen quantity is 44-55%, add the 3rd batch of auxiliary material, described the 3rd batch of auxiliary material comprises the composite slag of the 0-22 weight % of the high magnesium lime of 8-30 weight % of lime, high magnesium lime total amount of the 8-30 weight % of lime total amount and composite slag total amount.Further under the preferable case, the rifle position of described oxygen rifle and the relation of blowing oxygen quantity are controlled to be: with the total amount that is blown into oxygen is benchmark, and when blowing oxygen quantity was 0-5%, the rifle position was a 1.95-2.05 rice; Blowing oxygen quantity is greater than 5% to 28% o'clock, and the rifle position is a 1.5-1.55 rice; Blowing oxygen quantity is greater than 28% to 35% o'clock, and the rifle position is a 2.15-2.2 rice; Blowing oxygen quantity is greater than 35% to 40% o'clock, and the rifle position is a 1.95-2.05 rice; Blowing oxygen quantity is greater than 40% to 50% o'clock, and the rifle position is a 1.75-1.85 rice; Blowing oxygen quantity is greater than 50% to 65% o'clock, and the rifle position is a 1.65-1.75 rice; Blowing oxygen quantity is greater than 65% to 70% o'clock, and the rifle position is a 1.55-1.65 rice; Blowing oxygen quantity is greater than 70% to 80% o'clock, and the rifle position is a 1.85-1.95 rice, and blowing oxygen quantity is greater than 80% to 90% o'clock, and the rifle position is a 1.65-1.75 rice; Blowing oxygen quantity is greater than 90% to 100% o'clock, and the rifle position is a 1.5-1.55 rice.In addition, preferably the lot number that described auxiliary material is added is controlled to be 6, the adition process of described auxiliary material and the relation of blowing oxygen quantity are controlled to be at this moment: with the total amount that is blown into oxygen is benchmark, blowing oxygen quantity adds first auxiliary material during for 0.9-1.1%, and first auxiliary material comprises the composite slag of the 78-85 weight % of the high magnesium lime of 58-65 weight % of lime, high magnesium lime total amount of the 57-63 weight % of lime total amount and composite slag total amount; Blowing oxygen quantity adds second batch of auxiliary material during for 28-32%, and the second batch of auxiliary material comprises the high magnesium lime of the 8-12 weight % of the lime of 8-12 weight % of lime total amount and high magnesium lime total amount; Blowing oxygen quantity adds the 3rd batch of auxiliary material during for 44-48%, and the 3rd batch of auxiliary material comprises the composite slag of the 15-22 weight % of composite slag total amount; Blowing oxygen quantity adds the 4th batch of auxiliary material during for 50-55%, and the 4th batch of auxiliary material comprises the high magnesium lime of the 8-12 weight % of the lime of 8-12 weight % of lime total amount and high magnesium lime total amount; Blowing oxygen quantity adds the 5th batch of auxiliary material during for 60-64%, and the 5th batch of auxiliary material comprises the high magnesium lime of the 8-12 weight % of the lime of 8-12 weight % of lime total amount and high magnesium lime total amount; Blowing oxygen quantity adds the 6th batch of auxiliary material during for 70-73%, and the 6th batch of auxiliary material comprises the high magnesium lime of the 8-12 weight % of the lime of 8-12 weight % of lime total amount and high magnesium lime total amount.Under the most preferred case, can be simultaneously the rifle position of described oxygen rifle and the adition process of described auxiliary material and the relation of blowing oxygen quantity be all controlled according to above-mentioned parameter.The method for making steel that meets above-mentioned preferable case can quicken the generation of slag, thereby shortens the steel-making time.
In the present invention, the plurality of raw materials in each batch auxiliary material can add respectively also and can add after the uniform mixing, can continous way add also and can add by intermittent type.
In order to make full use of steel scrap, thereby make steel scrap obtain recycling and saving cost, in method for making steel of the present invention, the described steel raw material that adds in the converter can also contain steel scrap, and with respect to the described half steel of 100 weight parts, described steel scrap is the 2.5-6.5 weight part.Described steel scrap is meant the iron and steel stock that some are scrapped, mainly the consisting of of steel scrap: C:0.03-0.75 weight %, Si:0.02-0.50 weight %, Mn:0.03-0.75 weight %, P:0.003-0.035 weight %, S:0.003-0.035 weight %, Fe:98.15-99.91 weight %.Adopting steel scrap instead of part half steel is when hot metal supply deficiency or steel scrap resource surplus, the technical measures that steel mill extensively adopts.
In method for making steel of the present invention, the content of carbon is 3.3-3.7 weight % based on the gross weight of described half steel in described half steel, and corresponding to described half steel per ton, and the add-on of described steel scrap is during greater than 50 kilograms, and described raw material also contains temperature raising agent.Described temperature raising agent is selected carbonaceous material usually for use, and for example class graphite and/or carburelant, described class graphite and carburelant can be conventional various types of graphite and the carburelant that uses in this area, and the carbon content of common described class graphite and carburelant is more than 85%.The consumption of described temperature raising agent is the 0.05-0.5 kilogram for heat 1 ℃ with respect to steel raw material per ton.Described temperature raising agent adds during for 1-3% at blowing oxygen quantity, and concrete add-on is decided according to the temperature of the required lifting of steel raw material in the steel melting furnace and the amount of steel raw material.For example, in steel melting furnace, contain 100 tons of steel raw materials, and need make steel raw material per ton promote 10 ℃ the time, then the consumption of temperature raising agent is 100 * 10 * (0.05-0.5)=50-500 kilogram.The calculating of the consumption of following refrigerant similarly.
In semi-steel making method of the present invention, when the content of carbon in the described half steel is more than the 4.2 weight % based on the gross weight of described half steel, and corresponding to described half steel per ton, the add-on of described steel scrap is below 46 kilograms the time, and described raw material also contains refrigerant.Because the content of carbon is more than the 4.2 weight % based on the gross weight of described half steel in the described half steel of steel, and corresponding to described half steel per ton, the add-on of described steel scrap is below 46 kilograms the time, there is heat situation more than needed in the steel-making system, therefore the refrigerant that can prevent that molten steel temperature is too high and can reduce molten steel temperature preferably is provided, described refrigerant for example can be sludge ball, and described sludge ball is the conventional sludge ball that uses in this area.The consumption of described refrigerant is to be the 0.05-0.5 kilogram for 1 ℃ with respect to steel raw material cooling per ton.Described refrigerant adds during for 77-79% at blowing oxygen quantity, and concrete add-on is decided according to the temperature of raw material in the steel melting furnace.
According to method provided by the invention, the process of described oxygen blown process and adding auxiliary material can realize automatic control by computer.
The invention will be further described below in conjunction with embodiment.In following examples, the content of CaO is 88 weight % in the lime; The content of MgO is 30 weight % in the high magnesium lime, and the content of CaO is 52 weight %; Acid composite slag is quartz sand, wherein SiO
2Content be 55 weight %.
Embodiment 1
Present embodiment is used to illustrate the method for oxygen top blown converter steel making provided by the invention.
To smelt in the adding of the half steel after the 132 tons of vanadium extractions converter, wherein the composition of half steel and charging temperature are as shown in table 1 below, then to wherein being blown into oxygen and adding auxiliary material, auxiliary material (the lime that adds, high magnesium lime and acid composite slag) gross weight and to be blown into the total amount of oxygen as shown in table 2, the relation of pairing blowing oxygen quantity is as follows when the adding of auxiliary material and adding auxiliary material: with the total amount that is blown into oxygen is benchmark, blowing oxygen quantity is 1% o'clock, adds the lime of 60 weight % of lime total amount, the acid composite slag of 80 weight % of the high magnesium lime of 60 weight % of high magnesium lime total amount and acid composite slag total amount; Blowing oxygen quantity is 30% o'clock, the high magnesium lime of the lime of 10 weight % of adding lime total amount and 10 weight % of high magnesium lime total amount; Blowing oxygen quantity is 46% o'clock, adds the acid composite slag of 20 weight % of acid composite slag total amount; Blowing oxygen quantity is the lime of 10 weight % of 51% o'clock adding lime total amount; Blowing oxygen quantity is 54% o'clock, adds the high magnesium lime of 10 weight % of high magnesium lime total amount; Blowing oxygen quantity is the high magnesium lime that added 10 weight % of the lime of 10 weight % of lime total amount and high magnesium lime total amount at 61% o'clock; Blowing oxygen quantity is 71% o'clock, the high magnesium lime of the lime of 10 weight % of adding lime total amount and 10% total amount of high magnesium lime total amount.(with the total amount that is blown into oxygen is benchmark, and when blowing oxygen quantity was 0-5%, the rifle position was 2.0 meters as shown in Figure 1 in the rifle position of oxygen rifle; Blowing oxygen quantity is greater than 5% to 28% o'clock, and the rifle position is 1.5 meters; Blowing oxygen quantity is greater than 28% to 35% o'clock, and the rifle position is 2.2 meters; Blowing oxygen quantity is greater than 35% to 40% o'clock, and the rifle position is 2.0; Blowing oxygen quantity is greater than 40% to 50% o'clock, and the rifle position is 1.8 meters; Blowing oxygen quantity is greater than 50% to 65% o'clock, and the rifle position is 1.7 meters; Blowing oxygen quantity is greater than 65% to 70% o'clock, and the rifle position is 1.6 meters; Blowing oxygen quantity is greater than 70% to 80% o'clock, and the rifle position is 1.9 meters; Blowing oxygen quantity is greater than 80% to 90% o'clock, and blowing oxygen quantity is 1.7 meters; Blowing oxygen quantity is greater than 90% to 100% o'clock, and the rifle position is 1.5 meters).From the beginning oxygen blast to blowing oxygen quantity is to be blown into 90% of amount of oxygen, the flow of oxygen be 30000 standard cubic meter/hour; Blowing oxygen quantity is after 90%, the flow of oxygen be 20000 standard cubic meter/hour.Thereby obtain molten steel and tap, wherein, the composition and the tapping temperature of tapping molten steel are as shown in table 3, and the weight of tapping is 126 tons, and the steel of refining is the steel of 34Mn2V steel grade.
Table 1
| C | Si | Mn | P | S | V | Ti | Fe | Charging temperature (℃) | |
| Half steel composition (weight %) | 3.81 | 0.019 | 0.015 | 0.078 | 0.012 | 0.02 | 0.025 | 96.021 | 1330 |
Table 2
| Auxiliary material | Lime (kg) | High magnesium lime (kg) | Acid composite slag (kg) | Be blown into the total amount (m of oxygen 3) |
| Add total amount | 4485 | 3535 | 2804 | 6772 |
Table 3
| C | Si | Mn | P | S | V | Ti | Fe | Tapping temperature (℃) | |
| Tapping molten steel composition (weight %) | 0.081 | 0.018 | 0.02 | 0.005 | 0.01 | 0.02 | 0.02 | 99.826 | 1690 |
The finishing slag basicity that this stove is smelted is 3.452, and full iron is 19.5 weight % in the finishing slag, and oxygen activity is 510ppm.In the present invention, the weight percentage of described full iron is represented the weight percentage of the ferro element that exists with various forms such as ferric oxide, iron protoxide and Z 250 form in the slag.In this stove steelmaking process, splash do not occur and return dried phenomenon, and from described half steel add converter to the used time of tapping be 11 minutes, shorten 1 minute than method time spent of the steel that adopts conventional refining 34Mn2V steel grade.
Embodiment 2
Present embodiment is used to illustrate the method for oxygen top blown converter steel making provided by the invention.
To smelt in the adding of the half steel after the 138.36 tons of vanadium extractions converter, to wherein adding 6.969 tons of steel scraps, wherein the charging temperature of the composition of half steel and steel scrap and half steel is as shown in table 4 below again.According to the wherein carbon content of half steel and the add-on of steel scrap, adopt static steel-making model to go out to need to add temperature raising agent the steel-making system is heated up 15 ℃ by computer calculates.In converter, be blown into oxygen and add auxiliary material, the gross weight of the auxiliary material (lime, high magnesium lime, acid composite slag and class graphite (model is YB/T 044-2007)) that adds and to be blown into the total amount of oxygen as shown in table 5, the relation of the adding of auxiliary material pairing blowing oxygen quantity when adding auxiliary material as: with the total amount that is blown into oxygen is benchmark, and blowing oxygen quantity is the acid composite slag of 78 weight % of the high magnesium lime of 65 weight % of the lime that added 57 weight % of all class graphite (as temperature raising agent), lime total amount at 1% o'clock, high magnesium lime total amount and acid composite slag total amount; Blowing oxygen quantity is the high magnesium lime that added 11 weight % of the lime of 12 weight % of lime total amount and high magnesium lime total amount at 28% o'clock; Blowing oxygen quantity is to add the acid composite slag of 22 weight % of acid composite slag total amount at 44% o'clock; Blowing oxygen quantity is the lime of 12 weight % of 50% o'clock adding lime total amount; Blowing oxygen quantity is the high magnesium lime of 8 weight % of 55% o'clock adding high magnesium lime total amount; Blowing oxygen quantity is the high magnesium lime that added 8 weight % of the lime of 11 weight % of lime total amount and high magnesium lime total amount at 64% o'clock; Blowing oxygen quantity is the high magnesium lime that added 8 weight % of the lime of 8 weight % of lime total amount and high magnesium lime total amount at 73% o'clock.The rifle position of oxygen rifle as shown in Figure 1.From the beginning oxygen blast to blowing oxygen quantity is to be blown into 90% of amount of oxygen, the flow of oxygen be 30000 standard cubic meter/hour; Blowing oxygen quantity is after 90%, the flow of oxygen be 20000 standard cubic meter/hour.Thereby obtain molten steel and tap, wherein, the composition and the tapping temperature of tapping molten steel are as shown in table 6, and the weight of tapping is 132.04 tons, and the steel of refining is the steel of SS310 steel grade.
Table 4
| C | Si | Mn | P | S | V | Ti | Fe | Charging temperature (℃) | |
| Half steel composition (weight %) | 3.65 | 0.022 | 0.04 | 0.07 | 0.004 | 0.021 | 0.015 | 96.178 | 1344 |
| Steel scrap composition (weight %) | 0.34 | 0.30 | 0.45 | 0.005 | 0.004 | 0.2 | 0.002 | 98.699 | 30 |
Table 5
| Auxiliary material | Lime (kg) | High magnesium lime (kg) | Acid composite slag (kg) | Class graphite (kg) | Be blown into the total amount (m of oxygen 3) |
| Add total amount | 4026 | 3901 | 2981 | 370 | 6550 |
Table 6
| C | Si | Mn | P | S | V | Ti | Fe | Tapping temperature (℃) | |
| Tapping molten steel composition (weight %) | 0.06 | 0.02 | 0.036 | 0.007 | 0.007 | 0.02 | 0.02 | 99.83 | 1681 |
The finishing slag basicity that this stove is smelted is 3.44, and full iron is 19.5 weight % in the finishing slag, and oxygen activity is 612ppm.In this stove steelmaking process, splash do not occur and return dried phenomenon, and from described half steel add converter to the used time of tapping be 13 minutes, shorten 1.2 minutes than method time spent of the steel that adopts conventional refining SS310 steel grade.
Embodiment 3
Present embodiment is used to illustrate the method for oxygen top blown converter steel making provided by the invention.
To smelt in the adding of the half steel after the 135.2 tons of vanadium extractions converter, to wherein adding 6.17 tons of steel scraps, wherein the charging temperature of the composition of half steel and steel scrap and half steel is as shown in table 7 below again.According to the wherein carbon content of half steel and the add-on of steel scrap, adopt static steel-making model to go out to need to add refrigerant to 25 ℃ of steel-making system coolings by computer calculates.In converter, be blown into oxygen and add auxiliary material, the auxiliary material that adds (lime, high magnesium lime, acid composite slag and sludge ball (produce by the converter mud of the finely powdered of the metallic iron that contains 45-50 weight %)) gross weight and to be blown into the total amount of oxygen as shown in table 8, the relation of the adding of auxiliary material pairing blowing oxygen quantity when adding auxiliary material as: with the total amount that is blown into oxygen is benchmark, and blowing oxygen quantity is the acid composite slag of 85 weight % of the high magnesium lime of 58 weight % of the lime that added 63 weight % of lime total amount at 1% o'clock, high magnesium lime total amount and acid composite slag total amount; Blowing oxygen quantity is the high magnesium lime that added 8 weight of the lime of 9 weight % of lime total amount and high magnesium lime total amount at 32% o'clock; Blowing oxygen quantity is to add the acid composite slag of 15 weight % of acid composite slag total amount at 48% o'clock; Blowing oxygen quantity is the lime of 8 weight % of 51% o'clock adding lime total amount; Blowing oxygen quantity is the high magnesium lime of 12 weight % of 55% o'clock adding high magnesium lime total amount; Blowing oxygen quantity is the high magnesium lime that added 11 weight % of the lime of 8 weight % of lime total amount and high magnesium lime total amount at 60% o'clock; Blowing oxygen quantity is the high magnesium lime that added 11 weight % of the lime of 12 weight % of lime total amount and high magnesium lime total amount at 70 o'clock; Blowing oxygen quantity is to add all sludge balls (as refrigerant) at 78% o'clock.The rifle position of oxygen rifle as shown in Figure 1.From the beginning oxygen blast to blowing oxygen quantity is to be blown into 90% of amount of oxygen, the flow of oxygen be 30000 standard cubic meter/hour; Blowing oxygen quantity is after 90%, the flow of oxygen be 20000 standard cubic meter/hour.Thereby obtain molten steel and tap, wherein, the composition and the tapping temperature of tapping molten steel are as shown in table 9, and the weight of tapping is 132.2 tons, and the steel of refining is the steel of LA60 steel grade.
Table 7
| C | Si | Mn | P | S | V | Ti | Fe | Charging temperature (℃) | |
| Half steel composition (weight %) | 4.29 | 0.022 | 0.022 | 0.072 | 0.007 | 0.015 | 0.02 | 95.552 | 1350 |
| Steel scrap composition (weight %) | 0.65 | 0.29 | 0.28 | 0.003 | 0.003 | 0.022 | 0.04 | 98.712 | 30 |
Table 8
| Auxiliary material | Lime (kg) | High magnesium lime (kg) | Acid composite slag (kg) | Sludge ball (kg) | Be blown into the total amount (m of oxygen 3) |
| Add total amount | 4076 | 3702 | 2950 | 590 | 6152 |
Table 9
| C | Si | Mn | P | S | V | Ti | Fe | Tapping temperature (℃) | |
| Tapping molten steel composition (weight %) | 0.09 | 0.02 | 0.021 | 0.005 | 0.007 | 0.011 | 0.019 | 99.827 | 1680 |
The finishing slag basicity that this stove is smelted is 3.66, and full iron is 21 weight % in the finishing slag, and oxygen activity is 720ppm.In this stove steelmaking process, splash do not occur and return dried phenomenon, and from described half steel add converter to the used time of tapping be 12.5 minutes, shorten 0.65 minute than method time spent of the steel that adopts conventional refining SS310 steel grade.
This shows, adopt the method for oxygen top blown converter steel making provided by the invention, can shorten the steel-making time, and in steelmaking process, effectively avoided splash and returned the generation of doing phenomenon.
Claims (15)
1. the method for an oxygen top blown converter steel making, this method comprise the steel raw material are added in the converter, by oxygen rifle oxygen blast gas in converter, and add auxiliary material in the oxygen blast process in converter in batches, it is characterized in that described steel raw material contains half steel;
Wherein, described half steel contains the carbon of 3.2-4.4 weight %, the silicon of 0.001-0.02 weight %, the manganese of 0.02-0.07 weight %, the phosphorus of 0.06-0.08 weight %, the sulphur of 0.02-0.035 weight %, the titanium of 0.01-0.06 weight %, the vanadium of 0.02-0.06 weight % and the iron of 95.4-96.65 weight %;
The rifle position of described oxygen rifle in converter liquid steel level above move in the scope of 1.5-2.2 rice, wherein, open that to blow the rifle position be 1.95-2.05 rice, blowing rifle position is a 1.5-2.2 rice, catch carbon rifle position is a 1.7-1.75 rice; Described auxiliary material comprises composite slag, lime and high magnesium lime, and with respect to half steel per ton, the consumption of composite slag is the 17-20 kilogram, and the consumption of lime is the 30-34.5 kilogram, and the consumption of high magnesium lime is the 30-34.5 kilogram, and the total amount that is blown into oxygen is the 43-53 cubic meter; With the total amount that is blown into oxygen is benchmark, when blowing oxygen quantity is 0.8-2%, add first auxiliary material, described first auxiliary material comprises the composite slag of the 78-85 weight % of the high magnesium lime of 58-65 weight % of lime, high magnesium lime total amount of the 57-63 weight % of lime total amount and composite slag total amount, and described composite slag is for being benchmark SiO with its gross weight
2Content be the composite fluxing medium of 40-70 weight %.
2. method according to claim 1, wherein, with respect to half steel per ton, the consumption of described composite slag is the 17.42-19.7 kilogram, the consumption of described lime is the 30.3-34.09 kilogram, and the consumption of described high magnesium lime is the 30.3-34.09 kilogram, and the total amount that is blown into oxygen is the 45.5-51.3 cubic meter.
3. method according to claim 1, wherein, the rifle position of described oxygen rifle and the pass of blowing oxygen quantity are: with the total amount that is blown into oxygen is benchmark, when blowing oxygen quantity was 0-5%, the rifle position was a 1.95-2.05 rice; Blowing oxygen quantity is greater than 5% to 28% o'clock, and the rifle position is a 1.5-1.55 rice; Blowing oxygen quantity is greater than 28% to 35% o'clock, and the rifle position is a 2.15-2.2 rice; Blowing oxygen quantity is greater than 35% to 40% o'clock, and the rifle position is a 1.95-2.05 rice; Blowing oxygen quantity is greater than 40% to 50% o'clock, and the rifle position is a 1.75-1.85 rice; Blowing oxygen quantity is greater than 50% to 65% o'clock, and the rifle position is a 1.65-1.75 rice; Blowing oxygen quantity is greater than 65% to 70% o'clock, and the rifle position is a 1.55-1.65 rice; Blowing oxygen quantity is greater than 70% to 80% o'clock, and the rifle position is a 1.85-1.95 rice, and blowing oxygen quantity is greater than 80% to 90% o'clock, and the rifle position is a 1.65-1.75 rice; Blowing oxygen quantity is greater than 90% to 100% o'clock, and the rifle position is a 1.5-1.55 rice.
4. method according to claim 1, wherein, the lot number that adds auxiliary material in the oxygen blast process in converter is 3-9, and with the total amount that is blown into oxygen is benchmark, when blowing oxygen quantity is 28-32%, add second batch of auxiliary material, described second batch of auxiliary material comprises the composite slag of the 0-15 weight % of the high magnesium lime of 8-30 weight % of lime, high magnesium lime total amount of the 8-30 weight % of lime total amount and composite slag total amount; When blowing oxygen quantity is 44-55%, add the 3rd batch of auxiliary material, described the 3rd batch of auxiliary material comprises the composite slag of the 0-22 weight % of the high magnesium lime of 8-30 weight % of lime, high magnesium lime total amount of the 8-30 weight % of lime total amount and composite slag total amount.
5. method according to claim 4, wherein, the lot number that adds auxiliary material in the oxygen blast process in converter is 6, and the adition process of described auxiliary material and the pass of blowing oxygen quantity are: with the total amount that is blown into oxygen is benchmark, blowing oxygen quantity adds first auxiliary material during for 0.9-1.1%, and first auxiliary material comprises the composite slag of the 78-85 weight % of the high magnesium lime of 58-65 weight % of lime, high magnesium lime total amount of the 57-63 weight % of lime total amount and composite slag total amount; Blowing oxygen quantity adds second batch of auxiliary material during for 28-32%, and the second batch of auxiliary material comprises the high magnesium lime of the 8-12 weight % of the lime of 8-12 weight % of lime total amount and high magnesium lime total amount; Blowing oxygen quantity adds the 3rd batch of auxiliary material during for 44-48%, and the 3rd batch of auxiliary material comprises the composite slag of the 15-22 weight % of composite slag total amount; Blowing oxygen quantity adds the 4th batch of auxiliary material during for 50-55%, and the 4th batch of auxiliary material comprises the high magnesium lime of the 8-12 weight % of the lime of 8-12 weight % of lime total amount and high magnesium lime total amount; Blowing oxygen quantity adds the 5th batch of auxiliary material during for 60-64%, and the 5th batch of auxiliary material comprises the high magnesium lime of the 8-12 weight % of the lime of 8-12 weight % of lime total amount and high magnesium lime total amount; Blowing oxygen quantity adds the 6th batch of auxiliary material during for 70-73%, and the 6th batch of auxiliary material comprises the high magnesium lime of the 8-12 weight % of the lime of 8-12 weight % of lime total amount and high magnesium lime total amount.
6. according to any described method among the claim 1-5, wherein, described steel raw material also contains steel scrap, and with respect to the half steel of 100 weight parts, the add-on of described steel scrap is the 2.5-6.5 weight part.
7. method according to claim 6, wherein, the content of carbon is 3.3-3.7 weight % based on the gross weight of described half steel in described half steel, and described half steel corresponding to 100 weight parts, when the add-on of described steel scrap was the 5-6.5 weight part, this method also was included in and adds temperature raising agent in the oxygen blast process in converter.
8. method according to claim 7, wherein, described temperature raising agent adds during for 0.9-1.1% at blowing oxygen quantity.
9. method according to claim 7, wherein, the consumption of described temperature raising agent is the 0.05-0.5 kilogram for heat 1 ℃ with respect to steel raw material per ton.
10. according to any described method among the claim 7-9, wherein, described temperature raising agent is a carburelant.
11. according to any described method among the claim 7-9, wherein, described temperature raising agent is a class graphite.
12. method according to claim 6, wherein, when the content of carbon in the described half steel is more than the 4.2 weight % based on the gross weight of described half steel, and corresponding to the described half steel of 100 weight parts, when the add-on of described steel scrap was the 2.5-4.6 weight part, this method also was included in and adds refrigerant in the oxygen blast process in converter.
13. method according to claim 12, wherein, described refrigerant adds during for 77-79% at blowing oxygen quantity.
14. method according to claim 12, wherein, described refrigerant is a sludge ball.
15. according to any described method among the claim 12-14, wherein, the consumption of described refrigerant is to be the 0.05-0.5 kilogram for 1 ℃ with respect to steel raw material cooling per ton.
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| CN102312036B (en) * | 2010-07-06 | 2013-04-10 | 攀钢集团钢铁钒钛股份有限公司 | Steelmaking and slagging method |
| CN103060511B (en) * | 2013-01-14 | 2014-07-09 | 攀钢集团攀枝花钢铁研究院有限公司 | Oxygen supply method for preventing dedusting explosion venting of semisteel steel converter and semisteel smelting method |
| CN103849704B (en) * | 2014-03-11 | 2016-01-20 | 攀钢集团西昌钢钒有限公司 | The method of semisteel converter steelmaking |
| CN104032067B (en) * | 2014-06-19 | 2016-06-08 | 攀钢集团攀枝花钢铁研究院有限公司 | The method of a kind of low silicon vanadium-bearing hot metal blowing |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
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| US3511490A (en) * | 1967-02-24 | 1970-05-12 | Brown Fintube Co | Apparatus for introducing addition agent into molten steel |
| CN1048563A (en) * | 1990-07-23 | 1991-01-16 | 冶金工业部攀枝花钢铁公司 | The compound blow-double flow duct oxygen lance semisteel making technology and oxygen lance |
| CN1850999A (en) * | 2006-05-10 | 2006-10-25 | 徐建明 | Method for direct making steel by converter using waste iron and steel furnace burden |
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2009
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Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3511490A (en) * | 1967-02-24 | 1970-05-12 | Brown Fintube Co | Apparatus for introducing addition agent into molten steel |
| CN1048563A (en) * | 1990-07-23 | 1991-01-16 | 冶金工业部攀枝花钢铁公司 | The compound blow-double flow duct oxygen lance semisteel making technology and oxygen lance |
| CN1850999A (en) * | 2006-05-10 | 2006-10-25 | 徐建明 | Method for direct making steel by converter using waste iron and steel furnace burden |
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