The method that high carbon steel is produced in the high catch carbon tapping of a kind of double slag process
Technical field
The invention belongs to converter smelting high carbon steel technical field, particularly relate to the method that high carbon steel is produced in the high catch carbon tapping of a kind of double slag process.
Background technology
Converter smelting high carbon steel has dual mode according to the difference of when tapping carbon content of molten steel: a kind of is high catch carbon method, and a kind of is low catch carbon method.High catch carbon method tapping duration of blast is short, and the oxygen depletion amount is few, and the damage of blowing of iron is lacked, and recovery rate of iron is high; The tapping carbon content is high, and the slag all iron content is low, can alleviate slag lining erosion is improved furnace life; Carbon content is high during tapping, and the molten steel oxygen activity is low, can improve yield of alloy; The consumption of high catch carbon tapping can minimizing carburelant had both been practiced thrift cost, had reduced in the carburelant nitrogen impurity again to the influence of steel cleanliness factor.But tap under the high catch carbon condition, the liquid steel dephosphorization problem is the technological difficulties that will solve.
Japan just proposes producing high carbon steel by high-catching carbon method as far back as nineteen seventies.System iron in Kobe adopts " height draws the method for re-blowing " to produce high-carbon cord steel (Ironmaking and Steelmaking, 1977, No.1 p29~38), bessemerizes oxygen supply intensity at 1.1~2.5Nm
3Between/the min/t, " the soft blow method " of this low oxygen supply intensity is beneficial to dephosphorization, realized tapping 0.67~0.68%C; 0.012~0.013%P, the time of bessemerizing, this method duration of blast was longer at 17.5~19 minutes; Production efficiency is low, the efficient converter production of incompatible modernization.
Domestic steel mill adopts the high catch carbon tapping of double slag process to produce high carbon steel 82B (Liu Yue, Liu Liu, Tong Puqiao; Deng. the high catch carbon dephosphorizing process control in early stage of high-quality high carbon steel [J]. steel-making, 2006,22 (2): 27~29); Early stage, duration of blast was greater than 8 minutes, had influenced rhythm of production; The siliceous amount mark of molten iron will be had relatively high expectations to blast-melted below 0.55%.Test is for the not research of important parameters such as control of rifle position and oxygen supply intensity in the whole smelting process and later stage technology controlling and process measure.
The method of a kind of producing high carbon steel by high-catching carbon method of Chinese patent document (CN101333578A), converter is with 3.1~3.4Nm
3The oxygen supply system of constant current amount, change rifle position is adopted in the blowing of/min/t oxygen supply intensity, is slag former with quickened lime and ore; The higher rifle of blowing whole process using position; Open to blow to and finish to adopt the rifle position system of falling rifle piecemeal, the converter smelting endpoint deslagging of falling the stove, sampling detects composition, temperature; The tapping carbon content can reach 0.46~0.65%, phosphorus content 0.013~0.014%.The constant oxygen supply intensity of this method blowing whole process using; Do not consider the favourable condition of soft blow operation to low temperature dephosphorization in early stage; Do not have big flow bottom blowing and stir, after the blowing deslagging of falling the stove in latter stage, still have a large amount of rich phosphorus slags to stay in the stove, so tapping process can produce serious rephosphorization.
Summary of the invention
The method that the object of the present invention is to provide the tapping of the high catch carbon of a kind of double slag process to produce high carbon steel has overcome above-mentioned tapping process and has produced deficiencies such as serious rephosphorization, production efficiency be low.The present invention adopts double slag process smelting in early stage, regulates oxygen supply intensity, is the high catch carbon tapping of converter smelting high carbon steel of slag making material with lime and ore.
The present invention is container with the converter, is guaranteeing that smelting endpoint tapping temperature, molten steel phosphorus content all reach the high carbon steel smelting requirements under the carbon content higher level.High carbon steel that the present invention produces is carbon content 0.60~1.20% by weight percentage, phosphorus content≤0.018%, and all the other compositions add according to the steel grade needs.
The technical parameter of process step of the present invention and control is following:
(1) according to the tapping temperature requirement, according to certain hot metal ratio (weight of molten iron be total Intake Quantity 85%~90%) in converter, pack into molten iron and steel scrap;
(2) (0~6min) with 2.8Nm the converter smelting fs
3The oxygen supply intensity blowing of/min/t adds quickened lime, ore slag former in converter, adopt big bottom blowing flow to stir; Bottom blown gas adopts nitrogen, and the bottom blowing flow is 0.1Nm
3/ min/t;
(3) converter oxygen gun adopts the bit manipulation of constant current quantitative change rifle, and according to the standard rifle position system of bessemerizing, converter standard rifle position is opened and blown, and improves the rifle position behind the 2min gradually;
(4) grate is outwelled the part slag, and the deslagging amount is no less than the 40%-60% of slag gross weight;
(5) bessemerize subordinate phase with 3.3Nm
3The oxygen supply intensity blowing of/min/t adds quickened lime, ore slag former in converter, adopt less bottom blowing flow; Bottom blown gas adopts argon gas, and the bottom blowing flow is 0.05Nm
3/ min/t;
(6) later stage adopts higher rifle position to open to blow, fall the rifle position system of rifle piecemeal;
(7) total blowing oxygen consumption 80%~90% in, many batches of a small amount of ore and fluorites of adding; The ore add-on is at 2.5~5 kilograms of/ton steel, and the fluorite consumption is at 1~2.5 kilogram of/ton steel;
(8) bessemerize end, the deslagging of converter grate, thermometric, sampling;
(9) converter tapping, converter terminal control carbon content is 0.4~0.85%, phosphorus content≤0.015%.
Go into converter molten iron requirement phosphorus content≤0.12%, molten iron silicon content≤0.60%, molten iron temperature≤1380 ℃.Adopting quickened lime and ore is main slag making mode.
It is main slag making mode that quickened lime and ore are adopted in converter, and active ash requires effective CaO content >=85%.
In step (2), lime and ore join in the converter bessemerizing in 2 minutes, and head batch lime adds 10~30 kilograms of/ton steel according to molten iron silicon content, adds 3~10 kilograms of/ton steel of ore according to the molten iron temperature situation;
The smelting process bottom blown gas adopts nitrogen, and the bottom blowing flow is 0.1Nm
3/ min/t.
In step (3); Converter oxygen gun adopts the bit manipulation of constant current quantitative change rifle, and according to the standard rifle position system of bessemerizing, converter standard rifle position is opened and blown; Improve the rifle position behind the 2min; Process rifle position is higher 0.2~0.4 meter than normal, adopts the rifle position system that rises rifle piecemeal, and early stage, the rifle position was higher 0.2~0.4 meter than normal blowing during finishing blowing.
In step (5), the smelting process bottom blown gas adopts argon gas, and the bottom blowing flow is 0.05Nm
3/ min/t; According to molten iron silicon content and smelt the deslagging amount early stage and add 15~30 kilograms of/ton steel of lime, add 7~20 kilograms of/ton steel of ore according to the molten iron temperature situation.
In step (6); Converter oxygen gun adopts the bit manipulation of constant current quantitative change rifle, and according to the standard rifle position system of bessemerizing, converter opens that to blow the rifle position higher 0.2~0.4 meter than normally with process rifle position; Adopt the rifle position system of falling rifle piecemeal, it is higher 0.2 meter than normal blowing to carry rifle rifle position during finishing blowing.
In step (7), the ore add-on is at 2.5~5 kilograms of/ton steel, and the fluorite consumption is at 1~2.5 kilogram of/ton steel.
The invention has the advantages that: the big oxygen flow of the oxygen rifle soft blow technology of fs and subordinate phase combines, and has not only improved dephosphorization rate but also improved smelting efficient; Adopt early stage the soft blow operation can make slag active, improve the slag dephosphorizing capacity; Adopt bigger bottom blowing flow that slag is fully contacted, for dephosphorization provides good dynamic conditions; The smelting process deslagging can reduce the rich phosphorus slag quantity of slag, has reduced later stage rephosphorization amount; Later stage is reduced the bottom blowing flow, has effectively avoided the erosion of high-temperature molten steel to furnace bottom, can improve furnace life; Present method dephosphorization effect is stable, and molten steel is to the requirement of phosphorus content in the time of can satisfying high catch carbon tapping.
Embodiment
For smelting main points of the present invention and implementation result thereof clearly are described, the embodiment and the implementation result of 210 tons of converter smeltings is provided.
Embodiment 1:
The method that high carbon steel is produced in high catch carbon tapping according to double slag process of the present invention adds 185 tons of molten iron in 210 tons of converters, 23.5 tons of steel scraps, and the molten iron condition is: 4.13%C, 0.37%Si, 0.23%Mn, 0.10%P, 0.038%S, 1357 ℃; Fs is adopted 2.8Nm
3The blowing of the oxygen supply intensity of/min/t is opened and is blown 2.5 meters of rifle positions, 2.7~2.1 meters of process rifle positions, and 1.9 meters of catch carbon rifle positions are opened and are blown the back and in 1 minute, in converter, add 5 tons of lime (25 kilograms of/ton steel), 1.5 tons of ores (7 kilograms of/ton steel), the bottom blowing nitrogen flow is for being 0.1Nm
3/ min/t, the fs finishes hot metal composition and temperature is: 3.53%C, 0.002%Si, 0.09%Mn, 0.021%P, 0.041%S, 1387 ℃; Subordinate phase adopts 3.3Nm
3The oxygen supply intensity blowing of/min/t is opened and is blown 2.3 meters of rifle positions, 2.6~2.1 meters of process rifle positions, and 1.9 meters of blow off rifle positions are opened and are blown back adding 6 tons of lime (28 kilograms of/ton steel) in converter, 3.1 tons of ores (15 kilograms of/ton steel), the bottom blowing nitrogen flow is for being 0.05Nm
3/ min/t adds totally 700 kilograms and 200 kilograms in ore and fluorite in two batches in 80~90% of blowing oxygen consumption; Total duration of blast 14 minutes, finishing blowing, deslagging, thermometric, sampling; Tapping.Through above-mentioned smelting process, realized tapping C=0.55%, P=0.008%, tapping temperature=1595 ℃.
Embodiment 2:
The method that high carbon steel is produced in high catch carbon tapping according to double slag process of the present invention adds 183 tons of molten iron in 210 tons of converters, 25 tons of steel scraps, and the molten iron condition is: 4.03%C, 0.58%Si, 0.21%Mn, 0.097%P, 0.034%S, 1377 ℃; Fs is adopted 2.8Nm
3The oxygen supply intensity blowing of/min/t is opened and is blown 2.4 meters of rifle positions, 2.6~2.1 meters of process rifle positions; 1.8 meters of catch carbon rifle positions; Open and blow the back 4.5 tons of lime (23 kilograms of/ton steel) that in 1 minute, in converter, add, 1.5 tons of ores (7 kilograms of/ton steel), the bottom blowing nitrogen flow is for being 0.1Nm
3/ min/t, the fs finishes hot metal composition and temperature is: 3.68%C, 0.002%Si, 0.08%Mn, 0.023%P, 0.035%S, 1369 ℃; Subordinate phase adopts 3.3Nm
3The oxygen supply intensity blowing of/min/t is opened and is blown 2.3 meters of rifle positions, 2.7~2.0 meters of process rifle positions, and 1.9 meters of blow off rifle positions are opened and are blown back adding 5 tons of lime (24 kilograms of/ton steel) in converter, 3.4 tons of ores (16 kilograms of/ton steel), the bottom blowing nitrogen flow is for being 0.05Nm
3/ min/t adds totally 550 kilograms and 200 kilograms in ore and fluorite in two batches in 80~90% of blowing oxygen consumption; Total duration of blast 14.4 minutes, finishing blowing, deslagging, thermometric, sampling; Tapping.Through above-mentioned smelting process, realized tapping C=0.62%, P=0.012%, tapping temperature=1599 ℃.
Can find out that through above embodiment the method that adopts the high catch carbon tapping of double slag process of the present invention to produce high carbon steel can satisfy the dephosphorization effect under the high catch carbon condition of molten steel, realizes high catch carbon tapping.