CA1153560A - Production of carbon steel and low-alloy steel with bottom blowing basic oxygen furnace - Google Patents
Production of carbon steel and low-alloy steel with bottom blowing basic oxygen furnaceInfo
- Publication number
- CA1153560A CA1153560A CA000352347A CA352347A CA1153560A CA 1153560 A CA1153560 A CA 1153560A CA 000352347 A CA000352347 A CA 000352347A CA 352347 A CA352347 A CA 352347A CA 1153560 A CA1153560 A CA 1153560A
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- Prior art keywords
- blowing
- gas
- oxygen
- steel
- furnace
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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
- C21C5/35—Blowing from above and through the bath
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- 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)
- Treatment Of Steel In Its Molten State (AREA)
Abstract
ABSTRACT OF THE DISCLOSURE
A method of producing carbon steel and low-alloy steel in a basic oxygen furnace is disclosed, in which a blow of the bottom-blowing gas predominantly comprised of carbon dioxide is introduced into a molten metal through at least one nozzle provided in the bottom or side wall of said basic oxygen furnace at least partly during the period of time from the beginning of blowing to the tapping of the melt, and the flow rate of the bottom-blowing gas is 1/200 - 9/200 the rate of oxygen impinged upon the melt through a lance. A steel making apparatus adapted to carry out the above-mentioned novel method of producing steel is also disclosed, which comprises, in combination, a furnace permitting both top-blowing of pure oxygen and bottom-blowing of a gas mainly composed of carbon dioxide, means for collecting the waste gas generated from the furnace, means for mixing the waste gas with oxygen and/or steam, means for burning the mixture thereof, and means for injecting the resulting combustion gas into the molten metal within said furnace.
A method of producing carbon steel and low-alloy steel in a basic oxygen furnace is disclosed, in which a blow of the bottom-blowing gas predominantly comprised of carbon dioxide is introduced into a molten metal through at least one nozzle provided in the bottom or side wall of said basic oxygen furnace at least partly during the period of time from the beginning of blowing to the tapping of the melt, and the flow rate of the bottom-blowing gas is 1/200 - 9/200 the rate of oxygen impinged upon the melt through a lance. A steel making apparatus adapted to carry out the above-mentioned novel method of producing steel is also disclosed, which comprises, in combination, a furnace permitting both top-blowing of pure oxygen and bottom-blowing of a gas mainly composed of carbon dioxide, means for collecting the waste gas generated from the furnace, means for mixing the waste gas with oxygen and/or steam, means for burning the mixture thereof, and means for injecting the resulting combustion gas into the molten metal within said furnace.
Description
56~
PRODUCTION OF CARBON ~TEEL AND LOW-ALLOY ST~EL
~ITH BOTTOM BLOWING BASIC OXYGEN FURNACE
This invention rela~es to the production o~` carbon steels and low-alloy steels with a bo-ttom blowing basic oxygen furnace ~hereinafter sometimes referred to as "bot-tom blowing BOF"~. More particularly9 this in~ention relates to a steel making process in which a blow of gas is injected into a melt so as to promote the agitation of the melt during top-blowing of pure oxygen through a lance.
In the oxygen top-blowing steel making process9 molten iron, scrap and other starting materials are charged into a converter and then refining of steel is carried out while blowing pure oxygen onto the charge melt through an oxygen lance. In the early or intermediate stage of the blowing, the oxygen vigorously reacts to the melt still containing a sub-stantial level of carbon so that the generation of carbon monoxide is sufficien-t to bring about thorough agitation of the melt.
However, since the amount of carbon in the melt decreases at the end stage of the blowing, the generation of carbon monoxide rapidly diminishes and the reaction between the molten steel and slag rapidly goes down. Due to such decrease in decarburizing efficiency of oxygen9 i.e. decrease in the proportion of oxygen which has been used to effect decarburization to the total amount of oxygen blown into the melt, the presence of excess oxygen is unavoidable resulting in oxidation of iron far beyond the equilibrium level. In addition, due to insufficient agitation of the ,~
56~
molten s-teel and slag, there will be a temperature di~ference be-tween them9 resulting in a dephosphorizing reaction proceed-ing in an adverse direction. This is caused by less agitation of the molten metal. Therefore, it has been proposed to provide an oxygen converter with an electromagnetic agitator.
It has also been proposed to add scrap iron to the melt at the last stage of blowing to generate a turbulence of the melt due to a temperature difference between the scrap and melt.
However, these proposals have never been practiced because they require a high construction cost and their effect is supposed not so large as expected.
Furthermore, it has been proposed to rotate or swing the oxygen blowing lance to provide additional agitation of molten metal and slag. But this promotes the agitation of slag, not of the molten steel.
In order to eliminate these prior art disadvantages, it has also been proposed to inject a blow of gas into a molten metal through the bottom while pure oxygen is blown onto the melt through a lance. Examples of the gases to be injected into the melt are limited to an inert gas such as argon and a neutral gas such as ni-trogen. However, since argon is very expensive, and a relatively large amount must be blown into the melt in the bottom blowing so as to thorough-ly agitate the melt, a sharp increase in cost is unavoidable.
The introduction of pure ni-trogen or a gas predominantly comprised of nitrogen, such as a compressed air will increase the nitrogen content of the melt. Thus, the blowing of nitrogen is not practical) either.
~15~560 French Patent 1,151,05~ and U.S. Patent 3,~54,9~2 disclose the bottom blowing of various kinds of gases, includ-ing argon, steam, air, carbon oxide, etc. However, U.S.
Patent 3,854,g32, for example, is directed to the production of stainless steel, so that the main purpose is to suppress the oxidation of chromium. Thus, it is necessary to carry out the process of this invention under subatmospheric conditions. In addition, it treats these gases as being equivalent. Furthermore, since the French patent teaches the bottom blowing of a relatively large amount of gas into the melt, the process disclosed therein is less economical.
In addition, the oxygen is blown through the convention-al lance into the steel melt as a supersonic oxygen jet.
Therefore, the temperature at the impinging surface between the oxygen and molten steel, goes up to 2,000C or more.
Therefore, iron loss due to evaporation (hereinafter referred to as "fume-loss") is significant. Furthermore, the problems of spitting of fine iron particles after firing and the slGp-ping of slag and molten steel still remain unsolved. There-fore, even in this combined blowing process, a remarkableincrease in tapping yield cannot be expected. This is because, according to the conventional oxygen steel process, the Lavel-type nozzle is used as a lance and the oxygen jet is injected at a supersonic rate of Mach 2 - 2.5 so that the disadvantages mentioned above are inevitable. In order to avoid such disadvantages controlling the decarburization rate and the slag conditions during blowing has been tried. However, it is difficult to control these factors during operation and9 56~) in fact, such improved results as expected could not be obtained.
A recent development in this field is the "Q-Bop"
process, in which instead of top-blowing of pure oxygen, the oxygen is blown into the molten metal through nozzles provided at the bottom of the converter. Since the "Q-Bop" process employs the pure oxygen gas for bottom-blowing instead of for top~blowing, it is necessary to blow another gas such as propane for protecting the nozzles. Consequently, in this case,, too, a relatively large amount of blowing gas must be injected into the molten metal. The "uniform mixing time"
hereinafter described in detail is about 10 seconds.
The primary object of this invention is to provide a method of producing carbon steel and low-alloy steel with a basic oxygen furnace.
Another object of this invention is to provide an economical method of thoroughly agitating a melt in an oxygen steel converter.
Still another object of this invention is to provide a method of producing carbon steel and low-alloy steel with a basic oxygen furnace, in which a waste gas discharged from the furnace is circulated and used as the only source of the gas to be blown through the bottom of the furnace.
Still another object of this invention is to provide a method of producing carbon steel and low-alloy steel with improved tapping yield.
This invention resides in a method of producing carbon steels and low-alloy steels in a basic oxygen furnace, characterized in that a blow of gas predominantly comprised of carbon dioxide is introduced into the molten metal through at least one nozzle provided in the bottom or side wall of said basic oxygen furnace at least partly during the period of time from the beginning of blowing to the tapping of the melt) the flow rate of the bottom blowing gas being 1/200 -9/100 the rate of oxygen impinged upon the melt through a lance.
The blowing gas predominantly comprised of carbon dioxide may comprise more than 50% by volume of carbon dioxide, including the exhaust gas from a metal refining furnace such as a steel converter and a purified or concentrated gas derived from a combustion gas of a heating furnace. Other components of the blowing gas may be nitrogen, oxygen, etc. The more nitrogen there is in the blowing gas, the greater the nitrogen content of the melt. In case of producing the usual rimmed steels, nitrogen in an amount of less than 50% by volume may be present in -the blowing gas without bringing in any troubles.
But it is preferable to use a gas containing less than 20%
by volume of nitrogen if it is intended to produce a low-nitrogen steel. It is to be noted, however, that if a rela-tively large amount of nitrogen is blown into the melt, the nitrogen will be almost completely removed until the carbon content reduces to 0.5%. This is because the denitrifying reaction takes place vigorously when the carbon content is more than 0.5%. Thus, nitrogen gas may be blown into the melt instead of carbon dioxide gas until the carbon content reduces to 0.5%. After the carbon content reduces to Q.5%
s~
~ 6 --or less, the bottom blowing should be carried out in accordance with this invention.
In addition, mushroom deposition about 5 - 15 cm thick will sometimes be formed at the tip of the nozzle in practicing the method of this invention because of the temperature dif-ference found between the nozzle cooled with the blown gas and the melt surrounding it. It is supposed that the deposi-tion is formed at the beginning of operation and is mainly comprised of slag. The formation of such a deposition at the tip of a nozzle makes difficult the blowing of gas in a pre-determined amount. In order to avoid such a difficulty, it is advisable to increase the pressure or flow rate of the blowing gas to such a level that the deposition is made porous due to the passing of the gas through the nozzle. It is also advisable to incorporate a small amount of oxygen in the blow-ing gas so as to utilize its generation of heat in accordance with the equationo 2C0 + 2 = 2C2 According to thls invention, the bottom blowing i5 applied at least partly during the period of time from the beginning of the blowing of oxygen through a lance to the ta~ping of the refined molten steel. The bottom blowing rate may be varied during the process, e.g. depending on the proceed-ing of -the steel making reaction in the converter. For example, it is preferable to increase the blowing rate at a final stage of the top-blowing so as to compensa-te for the decrease in agitation due to the going down of the decarburizing reaction.
Therefore, an effective refining reaction can be con-tinued ~l3 S~5 successfully to the end, resulting in a remarkable reduction in the amount of gas used.
The blowing of carbon dioxide is preferably carried out by way of at least one nozzle provided in the bottom or in the side wall of the oxygen steel converter.
The advantages obtained by using carbon dioxide as a blowing gas is not only that it is less expensive than an inert gas such as argon, but also that carbon dioxide increases twice in volume when it is added to the melt in accordance with the equation~ C + C02 = 2CO, bringing about violent agitation of the melt. In other words, less gas is required to achieve the same effect of agitation in comparison with argon or nitrogen. This reduction in amount of gas used means that it is possible to simplify the equipment includ-ing piping required to blow gas into the molten steel inaccordance with this invention. This is very advantageous from a practical viewpoint.
According to this invention the flow rate of the bottom blowing gas is limited to less than 9/100, preferably less than 5/100 the rate of oxygen impinged upon the melt through a lance. This means that a relatively small amount of gas is injected into the melt through the bottom blowing. If the bottom blowing gas is injected into the melt in an amount of more than 9/100 the rate of oxygen blown through a lance, the agitation takes place so vigorously that reduction in tapping yield is substantial due to much slopping of the melt. On the other hand, if the amount of the bottom blowing gas is less than 1/200 the top-blowing gas, the necessary 35~) agitation of the melt canno-t be obtained.
In addition, the amount of the bottom-blowing gas may preferably be res-tricted on the basis of the amount of molten metal to be treated, independently from the blowing rate of pure oxygen through a lance. According to this embodiment, the amount of gas to be injected into the melt is precisely regulated or adjusted such that the uniform mixing time is 20 seconds or more.
The uniform mixing time means the time which is required to uniformly mix the molten steel and molten slag ~nly by the bottom-blowing. The uniform mixing time is a factor introduced by K. Nakanishi et al ("Ironmaking and Steelmaking" (1975) 3, 193) and is defined as follows.
Uniform Mixing Time T = 800 x ~ 0 4 (sec.) ~ - 28.5 WQ x T x log (1 + z/148) (Watt/ton) wherein Q = gas flow rate (Nm3/min) Wg - amount of molten steel (ton~
T = bath temperature (~) Z = depth of the bath (cm) In a preferred embodiment9 the uniform mixing time is more than 30 seconds. If the amount of gas falls within the limitation defined above, then thorough agitation will be obtained. If the uniform mixing time is less than 20 seconds, the agitation between molten steel and molten slag occurs so vigorously that the reduction of iron oxide in the molten slag proceeds excessively, reducing the content of the iron oxide, whic~ is effective for dephosphorization of the molten steel.
~5~5~
g Furthermore, if the uniform mixing time is less than 15 seconds, there is much leakage of the molten steel from the nozzles~ resulting in less -tapping ~ield of steel.
If the uniform mixing time is longer than 70 seconds, i.e. the amount of the bot-tom blowing gas is much reduced, no agitation is expected, and the blowing process is substan-tially the same as the conventional oxygen steel making process with top-blowing. This results in a remarkable increase in the total amount of iron in the molten slag, and a decrease in the tapping yield. Thus, it is desirable to adjust the uniform mixing time to 20 - 70 seconds.
It can be said on the basis of experiments that, for example 9 when the bath depth is 250 cm the uniform mixing time of 20 seconds corresponds to bottom blowing at a rate of 0.5 Nm3/min per ton of molten steel, and uniform mixing -time of 70 seconds to 0.02 Nm3/min per ton of molten metal.
Noting the fact that oxygen gas is discharged primarily as carbon monoxide gas after the decarburizing operation in such oxygen top-blowing refining furnace, this in~ention, in one aspect, provides a steel refining process that utilizes said waste gas as the only source of the gas to be blown from below the melt bath to stir it. In so doing, the process supplies i-ts own gas for stirring the molten steel.
This invention, therefore, also resides in a process for making steel in a basic oxygen furnace by the top-blowing of pure oxygen and the bottom-blowing of a gas mainly composed of carbon dioxide, characterized in that a waste gas discharged and collected from said furnace is combined with additional oxygen and/or steam9 the mixture thereof is burned, and the resulting combustion gas mainly composed of carbon dioxide is used as at least a part of the bottom-blowing gas.
Since the combustion gas sometimes contains a rela-tively large amount of nitrogen gas, it i9 preferable toremove the nitrogen gas, or to collect carbon dioxide from the combustion gas and then the gas rich in carbon dioxide is used as the bottom-blowing gas. The removal of nitrogen gas from the combustion gas is preferably carried out when low-nitrogen steel is intended to produce.
For carrying out the process above9 a steel making apparatus having a gas circulation system, has been provided, which comprises, in combination, a basic oxygen furnace permit-ting both top-blowing of oxygen and bottom-blowing of carbon dioxide-rich gas, a device for collecting the waste gas generated from the furnace, a device for burning said gas with oxygen and/or steaml an optional device for separating the combustion gas into carbon dioxide and nitrogen, and a piping system for supplying the molten steel in the furnace with carbon dioxide generated from said burner and separator.
This invention also resides in a method characterized in that the top-blowing oxygen is injected through a lance onto the molten metal at an outlet velocity of Mach 0.8
PRODUCTION OF CARBON ~TEEL AND LOW-ALLOY ST~EL
~ITH BOTTOM BLOWING BASIC OXYGEN FURNACE
This invention rela~es to the production o~` carbon steels and low-alloy steels with a bo-ttom blowing basic oxygen furnace ~hereinafter sometimes referred to as "bot-tom blowing BOF"~. More particularly9 this in~ention relates to a steel making process in which a blow of gas is injected into a melt so as to promote the agitation of the melt during top-blowing of pure oxygen through a lance.
In the oxygen top-blowing steel making process9 molten iron, scrap and other starting materials are charged into a converter and then refining of steel is carried out while blowing pure oxygen onto the charge melt through an oxygen lance. In the early or intermediate stage of the blowing, the oxygen vigorously reacts to the melt still containing a sub-stantial level of carbon so that the generation of carbon monoxide is sufficien-t to bring about thorough agitation of the melt.
However, since the amount of carbon in the melt decreases at the end stage of the blowing, the generation of carbon monoxide rapidly diminishes and the reaction between the molten steel and slag rapidly goes down. Due to such decrease in decarburizing efficiency of oxygen9 i.e. decrease in the proportion of oxygen which has been used to effect decarburization to the total amount of oxygen blown into the melt, the presence of excess oxygen is unavoidable resulting in oxidation of iron far beyond the equilibrium level. In addition, due to insufficient agitation of the ,~
56~
molten s-teel and slag, there will be a temperature di~ference be-tween them9 resulting in a dephosphorizing reaction proceed-ing in an adverse direction. This is caused by less agitation of the molten metal. Therefore, it has been proposed to provide an oxygen converter with an electromagnetic agitator.
It has also been proposed to add scrap iron to the melt at the last stage of blowing to generate a turbulence of the melt due to a temperature difference between the scrap and melt.
However, these proposals have never been practiced because they require a high construction cost and their effect is supposed not so large as expected.
Furthermore, it has been proposed to rotate or swing the oxygen blowing lance to provide additional agitation of molten metal and slag. But this promotes the agitation of slag, not of the molten steel.
In order to eliminate these prior art disadvantages, it has also been proposed to inject a blow of gas into a molten metal through the bottom while pure oxygen is blown onto the melt through a lance. Examples of the gases to be injected into the melt are limited to an inert gas such as argon and a neutral gas such as ni-trogen. However, since argon is very expensive, and a relatively large amount must be blown into the melt in the bottom blowing so as to thorough-ly agitate the melt, a sharp increase in cost is unavoidable.
The introduction of pure ni-trogen or a gas predominantly comprised of nitrogen, such as a compressed air will increase the nitrogen content of the melt. Thus, the blowing of nitrogen is not practical) either.
~15~560 French Patent 1,151,05~ and U.S. Patent 3,~54,9~2 disclose the bottom blowing of various kinds of gases, includ-ing argon, steam, air, carbon oxide, etc. However, U.S.
Patent 3,854,g32, for example, is directed to the production of stainless steel, so that the main purpose is to suppress the oxidation of chromium. Thus, it is necessary to carry out the process of this invention under subatmospheric conditions. In addition, it treats these gases as being equivalent. Furthermore, since the French patent teaches the bottom blowing of a relatively large amount of gas into the melt, the process disclosed therein is less economical.
In addition, the oxygen is blown through the convention-al lance into the steel melt as a supersonic oxygen jet.
Therefore, the temperature at the impinging surface between the oxygen and molten steel, goes up to 2,000C or more.
Therefore, iron loss due to evaporation (hereinafter referred to as "fume-loss") is significant. Furthermore, the problems of spitting of fine iron particles after firing and the slGp-ping of slag and molten steel still remain unsolved. There-fore, even in this combined blowing process, a remarkableincrease in tapping yield cannot be expected. This is because, according to the conventional oxygen steel process, the Lavel-type nozzle is used as a lance and the oxygen jet is injected at a supersonic rate of Mach 2 - 2.5 so that the disadvantages mentioned above are inevitable. In order to avoid such disadvantages controlling the decarburization rate and the slag conditions during blowing has been tried. However, it is difficult to control these factors during operation and9 56~) in fact, such improved results as expected could not be obtained.
A recent development in this field is the "Q-Bop"
process, in which instead of top-blowing of pure oxygen, the oxygen is blown into the molten metal through nozzles provided at the bottom of the converter. Since the "Q-Bop" process employs the pure oxygen gas for bottom-blowing instead of for top~blowing, it is necessary to blow another gas such as propane for protecting the nozzles. Consequently, in this case,, too, a relatively large amount of blowing gas must be injected into the molten metal. The "uniform mixing time"
hereinafter described in detail is about 10 seconds.
The primary object of this invention is to provide a method of producing carbon steel and low-alloy steel with a basic oxygen furnace.
Another object of this invention is to provide an economical method of thoroughly agitating a melt in an oxygen steel converter.
Still another object of this invention is to provide a method of producing carbon steel and low-alloy steel with a basic oxygen furnace, in which a waste gas discharged from the furnace is circulated and used as the only source of the gas to be blown through the bottom of the furnace.
Still another object of this invention is to provide a method of producing carbon steel and low-alloy steel with improved tapping yield.
This invention resides in a method of producing carbon steels and low-alloy steels in a basic oxygen furnace, characterized in that a blow of gas predominantly comprised of carbon dioxide is introduced into the molten metal through at least one nozzle provided in the bottom or side wall of said basic oxygen furnace at least partly during the period of time from the beginning of blowing to the tapping of the melt) the flow rate of the bottom blowing gas being 1/200 -9/100 the rate of oxygen impinged upon the melt through a lance.
The blowing gas predominantly comprised of carbon dioxide may comprise more than 50% by volume of carbon dioxide, including the exhaust gas from a metal refining furnace such as a steel converter and a purified or concentrated gas derived from a combustion gas of a heating furnace. Other components of the blowing gas may be nitrogen, oxygen, etc. The more nitrogen there is in the blowing gas, the greater the nitrogen content of the melt. In case of producing the usual rimmed steels, nitrogen in an amount of less than 50% by volume may be present in -the blowing gas without bringing in any troubles.
But it is preferable to use a gas containing less than 20%
by volume of nitrogen if it is intended to produce a low-nitrogen steel. It is to be noted, however, that if a rela-tively large amount of nitrogen is blown into the melt, the nitrogen will be almost completely removed until the carbon content reduces to 0.5%. This is because the denitrifying reaction takes place vigorously when the carbon content is more than 0.5%. Thus, nitrogen gas may be blown into the melt instead of carbon dioxide gas until the carbon content reduces to 0.5%. After the carbon content reduces to Q.5%
s~
~ 6 --or less, the bottom blowing should be carried out in accordance with this invention.
In addition, mushroom deposition about 5 - 15 cm thick will sometimes be formed at the tip of the nozzle in practicing the method of this invention because of the temperature dif-ference found between the nozzle cooled with the blown gas and the melt surrounding it. It is supposed that the deposi-tion is formed at the beginning of operation and is mainly comprised of slag. The formation of such a deposition at the tip of a nozzle makes difficult the blowing of gas in a pre-determined amount. In order to avoid such a difficulty, it is advisable to increase the pressure or flow rate of the blowing gas to such a level that the deposition is made porous due to the passing of the gas through the nozzle. It is also advisable to incorporate a small amount of oxygen in the blow-ing gas so as to utilize its generation of heat in accordance with the equationo 2C0 + 2 = 2C2 According to thls invention, the bottom blowing i5 applied at least partly during the period of time from the beginning of the blowing of oxygen through a lance to the ta~ping of the refined molten steel. The bottom blowing rate may be varied during the process, e.g. depending on the proceed-ing of -the steel making reaction in the converter. For example, it is preferable to increase the blowing rate at a final stage of the top-blowing so as to compensa-te for the decrease in agitation due to the going down of the decarburizing reaction.
Therefore, an effective refining reaction can be con-tinued ~l3 S~5 successfully to the end, resulting in a remarkable reduction in the amount of gas used.
The blowing of carbon dioxide is preferably carried out by way of at least one nozzle provided in the bottom or in the side wall of the oxygen steel converter.
The advantages obtained by using carbon dioxide as a blowing gas is not only that it is less expensive than an inert gas such as argon, but also that carbon dioxide increases twice in volume when it is added to the melt in accordance with the equation~ C + C02 = 2CO, bringing about violent agitation of the melt. In other words, less gas is required to achieve the same effect of agitation in comparison with argon or nitrogen. This reduction in amount of gas used means that it is possible to simplify the equipment includ-ing piping required to blow gas into the molten steel inaccordance with this invention. This is very advantageous from a practical viewpoint.
According to this invention the flow rate of the bottom blowing gas is limited to less than 9/100, preferably less than 5/100 the rate of oxygen impinged upon the melt through a lance. This means that a relatively small amount of gas is injected into the melt through the bottom blowing. If the bottom blowing gas is injected into the melt in an amount of more than 9/100 the rate of oxygen blown through a lance, the agitation takes place so vigorously that reduction in tapping yield is substantial due to much slopping of the melt. On the other hand, if the amount of the bottom blowing gas is less than 1/200 the top-blowing gas, the necessary 35~) agitation of the melt canno-t be obtained.
In addition, the amount of the bottom-blowing gas may preferably be res-tricted on the basis of the amount of molten metal to be treated, independently from the blowing rate of pure oxygen through a lance. According to this embodiment, the amount of gas to be injected into the melt is precisely regulated or adjusted such that the uniform mixing time is 20 seconds or more.
The uniform mixing time means the time which is required to uniformly mix the molten steel and molten slag ~nly by the bottom-blowing. The uniform mixing time is a factor introduced by K. Nakanishi et al ("Ironmaking and Steelmaking" (1975) 3, 193) and is defined as follows.
Uniform Mixing Time T = 800 x ~ 0 4 (sec.) ~ - 28.5 WQ x T x log (1 + z/148) (Watt/ton) wherein Q = gas flow rate (Nm3/min) Wg - amount of molten steel (ton~
T = bath temperature (~) Z = depth of the bath (cm) In a preferred embodiment9 the uniform mixing time is more than 30 seconds. If the amount of gas falls within the limitation defined above, then thorough agitation will be obtained. If the uniform mixing time is less than 20 seconds, the agitation between molten steel and molten slag occurs so vigorously that the reduction of iron oxide in the molten slag proceeds excessively, reducing the content of the iron oxide, whic~ is effective for dephosphorization of the molten steel.
~5~5~
g Furthermore, if the uniform mixing time is less than 15 seconds, there is much leakage of the molten steel from the nozzles~ resulting in less -tapping ~ield of steel.
If the uniform mixing time is longer than 70 seconds, i.e. the amount of the bot-tom blowing gas is much reduced, no agitation is expected, and the blowing process is substan-tially the same as the conventional oxygen steel making process with top-blowing. This results in a remarkable increase in the total amount of iron in the molten slag, and a decrease in the tapping yield. Thus, it is desirable to adjust the uniform mixing time to 20 - 70 seconds.
It can be said on the basis of experiments that, for example 9 when the bath depth is 250 cm the uniform mixing time of 20 seconds corresponds to bottom blowing at a rate of 0.5 Nm3/min per ton of molten steel, and uniform mixing -time of 70 seconds to 0.02 Nm3/min per ton of molten metal.
Noting the fact that oxygen gas is discharged primarily as carbon monoxide gas after the decarburizing operation in such oxygen top-blowing refining furnace, this in~ention, in one aspect, provides a steel refining process that utilizes said waste gas as the only source of the gas to be blown from below the melt bath to stir it. In so doing, the process supplies i-ts own gas for stirring the molten steel.
This invention, therefore, also resides in a process for making steel in a basic oxygen furnace by the top-blowing of pure oxygen and the bottom-blowing of a gas mainly composed of carbon dioxide, characterized in that a waste gas discharged and collected from said furnace is combined with additional oxygen and/or steam9 the mixture thereof is burned, and the resulting combustion gas mainly composed of carbon dioxide is used as at least a part of the bottom-blowing gas.
Since the combustion gas sometimes contains a rela-tively large amount of nitrogen gas, it i9 preferable toremove the nitrogen gas, or to collect carbon dioxide from the combustion gas and then the gas rich in carbon dioxide is used as the bottom-blowing gas. The removal of nitrogen gas from the combustion gas is preferably carried out when low-nitrogen steel is intended to produce.
For carrying out the process above9 a steel making apparatus having a gas circulation system, has been provided, which comprises, in combination, a basic oxygen furnace permit-ting both top-blowing of oxygen and bottom-blowing of carbon dioxide-rich gas, a device for collecting the waste gas generated from the furnace, a device for burning said gas with oxygen and/or steaml an optional device for separating the combustion gas into carbon dioxide and nitrogen, and a piping system for supplying the molten steel in the furnace with carbon dioxide generated from said burner and separator.
This invention also resides in a method characterized in that the top-blowing oxygen is injected through a lance onto the molten metal at an outlet velocity of Mach 0.8
2.0, preferably Mach 0.8 - 1.5.
The oxygen top-blowing steelmaking process of this invention, in another aspect, resides in a method characterized in that a powder of a slag-forming agent (flux) comprising quick lime, limestone, fluorite, dolomite, iron ore or mixtures thereof is supplied together with a top-blowing oxygen jet, and at the same time, carbon dioxide is blo~
from below the molten steel throughout the period of oxygen top-blowing or even up -to the time of the start of tapping, i.e. at least partly during the period of time fro~ the beginning of blowing to the tapping of the melt.
In the case of using the conventional oxygen top-blowing converter, the oxygen jet may be supplied wit~ a powder from a conventional oxygen top-blowing lance. However, the supply of a powder into a high-pressure oxygen piping inevitably results in a high equipment cost. Therefore, a separate path is provided for directing the powder on a car~
rier gas up to the tip of the oxygen blowing lance and for mixing the powder with an oxygen jet being delivered from the nozzle of the lance. By so doing, the defects mentioned above of the LD-AC process can be eliminated without abrasion of the Lavel-type oxygen blowing nozzle. More specifically, a three-sheathed lance (four coaxial tubes) used in one embodi-ment of this invention (see Figs. 6 and 7 referred to herein-after) is one example of such method. The carrier gas forthe flux powder is not specified, and a suitable gas can be selected depending upon the composition and particle size of the flux, the inside diameter of the piping, the type and flow rate of the carrier gas or the type of the furnace used.
But it is desired that the total amount of a given flux powder be supplied within about three quarters of the blowing period.
This is in order to dissolve the flux within the period of refining operation and rapidly form a reactive slag for 5~
effective refining operation.
According to -the process of this inven-tion9 a gas is blown from below the molten steel together with -the supply of a flux through a lance, and the bottom blowing gas is prefer~
ably blown at a rate of 0.02 to 0.50 Nm3/min per ton of the molten steel in case the bath dep-th is 250 cm. Within this range, less oxidation of iron and manganese takes place as the gas flow rate increases. Therefore, by choosing a suit-able pattern for blowing the flux and for blowing the gas from below the melt bath depending upon the type of the steel to be produced, a steel of a desired final composition can be produced with high accuracy, in high yield and with great ease.
The features of this invention have been described hereinbefore in detail.
This invention is particularly applicable -to produce carbon steel9 such as rimmed steel, killed steel etc.9 and low-alloy steel. More particularly, this invention provides a satisfac-tory method of producing low-carbon steel, such as carbon steel con-taining less -than 0.3D/D C.
Comparing the col~ven-tional process with this inven-tion method, the following advan-tages of this inven-tlon are no-tedO
Since -the oxidation of iron, manganese etc. is signifi-cantly inhibited, the yield of iron is markedly improved and the amount of ferro-alloys used may be decreasedO In addi-tion, since the temperature difference between the molten steei and the slag diminishes, the dephosphorizing is promoted.
Another advantage of this inven-tion is that the blowing gas, i.e. carbon dioxide9 is ab~dan-t in a s-teel making plant and is available at low cost. This is an economicaL aspect o~
this invention. Thus, this invention has also a practical value in the light of the present day demand for saving energy and preventing the discharge of pollutants into the environment.
As hereinbefore mentioned9 the method of this l~vention can easily be practiced in the usual steel making process by installing at least one nozzle in the conventional basic oxygen furnace. Of course, the application of this invention is not limited to the existing oxygen converters. As far as the combination of the top-blowing and the bottom-blowing is possible, this inven-tion is applicable to any type of metal refining furnace.
Fig. 1 is an elevational side view diagrammatically showing the bottom-blowing BOF utilized in this invention, Fig. 2 is a graph showing -the blowing patterns of this invention, Fig. 3 is a schematic diagram illustrating -the arrange-ment of the steel making apparatus according to -this invention, Figs. 4 and 5 are graphs showing the effect of this invention, Fig. 6 is a bot-tom view of the three~sheathed lance -to be used in one embodiment of this inven-tion, and Fig~ 7 is a longi-tudinal cross section of said lance taken on -the line a-a of Fig. 6.
According -to this invention, molten iron, iron scrap and other starting materials are charged into a bottom-~5356~) blowing BOF, i.e. converter 1, as shown in Fig. 1. Two to ten concentric nozzles 2 are provided at the bottom of this oxygen converter. During operation of the converter pure oxygen is impinged onto the surface or into the molten metal
The oxygen top-blowing steelmaking process of this invention, in another aspect, resides in a method characterized in that a powder of a slag-forming agent (flux) comprising quick lime, limestone, fluorite, dolomite, iron ore or mixtures thereof is supplied together with a top-blowing oxygen jet, and at the same time, carbon dioxide is blo~
from below the molten steel throughout the period of oxygen top-blowing or even up -to the time of the start of tapping, i.e. at least partly during the period of time fro~ the beginning of blowing to the tapping of the melt.
In the case of using the conventional oxygen top-blowing converter, the oxygen jet may be supplied wit~ a powder from a conventional oxygen top-blowing lance. However, the supply of a powder into a high-pressure oxygen piping inevitably results in a high equipment cost. Therefore, a separate path is provided for directing the powder on a car~
rier gas up to the tip of the oxygen blowing lance and for mixing the powder with an oxygen jet being delivered from the nozzle of the lance. By so doing, the defects mentioned above of the LD-AC process can be eliminated without abrasion of the Lavel-type oxygen blowing nozzle. More specifically, a three-sheathed lance (four coaxial tubes) used in one embodi-ment of this invention (see Figs. 6 and 7 referred to herein-after) is one example of such method. The carrier gas forthe flux powder is not specified, and a suitable gas can be selected depending upon the composition and particle size of the flux, the inside diameter of the piping, the type and flow rate of the carrier gas or the type of the furnace used.
But it is desired that the total amount of a given flux powder be supplied within about three quarters of the blowing period.
This is in order to dissolve the flux within the period of refining operation and rapidly form a reactive slag for 5~
effective refining operation.
According to -the process of this inven-tion9 a gas is blown from below the molten steel together with -the supply of a flux through a lance, and the bottom blowing gas is prefer~
ably blown at a rate of 0.02 to 0.50 Nm3/min per ton of the molten steel in case the bath dep-th is 250 cm. Within this range, less oxidation of iron and manganese takes place as the gas flow rate increases. Therefore, by choosing a suit-able pattern for blowing the flux and for blowing the gas from below the melt bath depending upon the type of the steel to be produced, a steel of a desired final composition can be produced with high accuracy, in high yield and with great ease.
The features of this invention have been described hereinbefore in detail.
This invention is particularly applicable -to produce carbon steel9 such as rimmed steel, killed steel etc.9 and low-alloy steel. More particularly, this invention provides a satisfac-tory method of producing low-carbon steel, such as carbon steel con-taining less -than 0.3D/D C.
Comparing the col~ven-tional process with this inven-tion method, the following advan-tages of this inven-tlon are no-tedO
Since -the oxidation of iron, manganese etc. is signifi-cantly inhibited, the yield of iron is markedly improved and the amount of ferro-alloys used may be decreasedO In addi-tion, since the temperature difference between the molten steei and the slag diminishes, the dephosphorizing is promoted.
Another advantage of this inven-tion is that the blowing gas, i.e. carbon dioxide9 is ab~dan-t in a s-teel making plant and is available at low cost. This is an economicaL aspect o~
this invention. Thus, this invention has also a practical value in the light of the present day demand for saving energy and preventing the discharge of pollutants into the environment.
As hereinbefore mentioned9 the method of this l~vention can easily be practiced in the usual steel making process by installing at least one nozzle in the conventional basic oxygen furnace. Of course, the application of this invention is not limited to the existing oxygen converters. As far as the combination of the top-blowing and the bottom-blowing is possible, this inven-tion is applicable to any type of metal refining furnace.
Fig. 1 is an elevational side view diagrammatically showing the bottom-blowing BOF utilized in this invention, Fig. 2 is a graph showing -the blowing patterns of this invention, Fig. 3 is a schematic diagram illustrating -the arrange-ment of the steel making apparatus according to -this invention, Figs. 4 and 5 are graphs showing the effect of this invention, Fig. 6 is a bot-tom view of the three~sheathed lance -to be used in one embodiment of this inven-tion, and Fig~ 7 is a longi-tudinal cross section of said lance taken on -the line a-a of Fig. 6.
According -to this invention, molten iron, iron scrap and other starting materials are charged into a bottom-~5356~) blowing BOF, i.e. converter 1, as shown in Fig. 1. Two to ten concentric nozzles 2 are provided at the bottom of this oxygen converter. During operation of the converter pure oxygen is impinged onto the surface or into the molten metal
3 through a lance 4 while the bottom-blowing gas pr~dominantly comprised of carbon dioxide is blown into the molten metal by way of the nozzles 2. The nozzles are arranged in two rows in this example. It is to be noted, however, that the structure, arrangement and number of the nozzle are not limited to particular ones.
In a preferred embodiment of this invention, a blow of gas predominantly comprised of carbon dioxide and supplied by way of conduits 5 is introduced into the molten metal 3 through concentric nozzles Z provided in the bottom of said basic oxygen furnace at least partly during the period of time from the beginning of blowing to the tapping of the melt and the M ow rate of the bottom blowing gas is less than 9/100 the rate of oxygen blown onto the melt through lance 4.
In one embodiment of this invention, the uniform mixing time is adjusted to 20 seconds or more.
Another embodiment of this invention is now described by reference to Fig. 3, an oxygen steel furnace 31 has an oxygen top-blowing lance 32 and a series of gas bottom-blowing nozzles 33. Oxygen gas is blown from the top-blowing lance 32 into the furnace 31 to perform decarburization and is discharged primarily as carbon monoxide gas. A gas primarily consisting of carbon dioxide is jetted from the bottom-blowing nozzles 33 into the furnace 31 where it is decomposed .535~i~
following the course C + C02 ~ 2C0 and discharged from -the furrlace. These two supplies of carbon monoxide gas are caught in a hood 34 on top of the furnace 31. They contain less than 20 vol% of nitrogen gas since they entail a-tmosphere as they are being caught in the hood.
The gas caught in the hood 34 is first freed of dust through a dust collector 35 and transferred to a gas holder 36 where it is stored temporarily before proceeding to sub sequent treatments. The gas in the holders 36 is mixed with oxygen and/or steam prior to entering into a burner 37. The gas in the holder 36 may be burnt with oxygen coming from an oxygen holder 41 for supplying oxygen to the oxygen top-blowing lance 329 and is optionally dehumidified before i~
is transferred to a carbon dioxide holder 399 or after the burning, the gas may be denitrified in a C02/N2 separator 38 to increase the C02 content before it is transferred to the carbon dioxide holder 39.
The carbon dioxide transferred to its holder 39 is supplied to the gas bottom-blowing nozzle 33 through the flow regulator 40. Alternatively, it may be combined with untreated gas from the gas holder 36 before it is supplied to the nozzle 33.
The gas Jetted from the bottom-blowing nozzle 33 into the bath is again caught in the hood 34 together with the carbon monoxide resulting from decarburization. Thus, each supply of carbon monoxide gas and carbon dioxide gas keeps recycling through the path described above.
Another embodiment of this invention is now described ~ 16 -by reference to Figs. 6 and 7. A 2~ton pure oxygen -top-blow ing converter is provided wi-th -two bo-ttom nozzles (I~D~ 8rnm) -through which a gas is -to be blown f`rom below the rnelr bath.
The oxygen top-blowing lance used is a three-sheathed lance (four coaxial tubes) 61 as shown in the bottom view and longitudinal cross section of Fi~s. 6 and 79 wherein -the center of the disc 63 of i-ts tip 62 is provided with a single nozzle opening 659 10 mm in diameter serving as a passage 64 for the supply of a flux powder and said opening is surrounded by -three nozzle openings 67 each 4.2 mm in diameter serving as a passage 66 for the supply of oxygen. This lance permits the powder to be blown against the surface of the mel-t 68 as it is mixed with oxygen being jetted from the three surrounding points.
This invention will be further described in conjunction with the working examples.
Example 1 A conventional oxygen conver-ter wi-th the capacity of 250 -tons was used to carry out this invention. Four nozzles 10 mm in diame-ter were ins-tallecl at -the bot-tom of the conver-ter~
Into this converter, as main s-tarting materials, 215 tons of mol-ten iron and 35 tons of scrap iron, and, as other starting material, 3 -tons of quick lime were charged. The composi-tion of the molten iron was9 by weight percent, 4.63% C~
0.48% Si, 0.45% Mn9 0.123% P, 0.0018% S, 0.0038~ N and the balance iron and incidental impurities. The temperature thereof was 1385C.
The gas blowing from the top and from the bottom was s~t ~
~ 17 -carried out as in the following.
The top~blowing of oxygen was carried out at a flow rate of 409000 Nm3/hr in accordance with the flow pattern shown in Fig. 2. The bottom blowing was also carried out following the flow pattern shown in Fig. 2. As shown in Fig, 2, the bottom blowing was initiated at a flow rate of 50 Nm3/hr and the rate was încreased to 100 Nm3/hr when the top-blowing of oxygen was initiated. At the end stage of the blowing, the rate of the bottom blowing was increased to 200 Nm3/hr and was then reduced to 50 Nm3/hr after the top-blowing was finished. The bottom blowing gas was an exhaust gas obtained from an oxygen converter and comprised, by weight percent, 18% C0, 63% C02, 16% N2 and 3% H2.
For the purpose of comparisonJ a conventional oxygen steel making process was also carried out using the same oxygen converter. The composition of the starting material charged into the converter and the manner of top-blowing were the same as in the above. In this case, however, the bottom blowing was not applied. The intended product steel was low-carbon rimmed steel. Table 1 below summarizes the finalcomposition of -the molten steel.
Table _ Composition (% by weight) Tem. in Tapp ng ~ c-- ~ -n-T--P~ r---- (c,l s17)g (%) Ths l l l ( _ _ invention 0.063 0.16¦0.017 0.012 0.0025 1625 11 13.8 96.3 . I _ _ . ~ _, tional 0.065 0.12¦0.021 0.015 0.0011 1618l 19.5 95 8 18 ~
As ls apparent from the data show~ in Table ] above 9 the produc-t steel o:E the me-thod of this invention has -the composition falling within that of low carbon rimmed steel and also shows a remarkably efficierlt dephosphorization and tapping yield.
In this example 9 Example 1 was repeated except that various kinds of gases were used as the bottom blowing gas.
As hereinbefore mentioned, the bottom blowing gas of this invention may be an exhaust gas discharged from an iron making plan-t, or a s-teel making plant. In this example, therefore, such kind of exhaust gas was used as the bottom blowing gas. Gas No. 1 was derived from an exhaust gas discharged from an oxygen converter and was made rich in carbon dioxide. Gas No. 2 was derived from an exhaust gas discharged from a hot stove and was made rich in carbon dioxide.
The final composition of the molten s-teel in each run is summarized in Table 2 be]ow.
Table 2 ___ _ Gas composition (% by volume) Gas No. C2 CO N2 2 2 1 9~ O 5 O
2 ~2.6 O 4~ 3.2 ~ ~; ?~ .3~
~ 19 -Table 3 Final composition ~ _ ~ 1 Gas~ by ~:gl:l~ T Fe Ten~lp. ¦
No. C Mn j N (%) __ _ .
1 0.058 0.15~.0019 14~2 1632 2 '~r, 1 = o, ODC5 1~.5 1619 According to this invention, an exhaus-t gas discharged from the oxygen converter may be used as the bo-ttom blowing gas. If the nitrogen content of the exhaust gas is below 5C%
by volume, the nitrogen content of the resulting steel product is accep-table. In addition, according to this inven-tion, the agita-tion of the melt was effected thoroughly, resulting in sufficient degree of decarburization and dephosphorization to make the method of -this invention practical.
Example 3 The following star-ting materials were charged lnto an oxygen converter shown in Fig. 1. The capacity of the conver--ter was 250 -tons and the bath depth was 250 cm. Two concen-tric nozzle were provided at the bottom (the inner nozzle was 12.7 mm in inner diameter and 15.4 mm in outer diameter, -the slit width was 1.15 mm9 and the ou-ter nozzle was 17.7 mm in inner diame-ter and 19.1 mm in outer diameter.
Mo]-ten iron. 220 tons The [Mn] is about 0.40% and ~p] is about 0.150%
in molten iron.
Scrap irono 30 tons Other materials:
quick llme 9 tons iron ore 4.5 tons light dolomite 3~0 tons fluorite 0.2 ton converter slag 1.8 tons According to the method of this invention, various kinds of bottom blowing gas were injected into the melt while top-klowing pure oxygen through a lance. The blowing condi-tions and the resulting uniform mixing time are summarizedin the following Table 4.
r-. _ . .. _ _ _ . .. . . _ . _ . _ .. _ .. _ . ... . .
hO O
.~ ~ ~ ~ o 1-~ ~
P~r-l~ . . . O
P~ a) ~~) ~) Lt~
0 ~ I c~ , ~ :~ a) ~1 _... _ .. _ _... .. _._ _ .. ~ . .
~1 o a~ _~LO L~ L~`\
t~ `o~ O O O a~ OC) ~ h ~_ . . .
1 0 o O o o ~ ~ P
tH C.) t) r-l o ~a~
.. ___ -- __ __ ~ h h 0 ~ r-l ~ O
S~ r~ 1--l r~ J r-lrl E-- ~l tn a) t~
. _ _ __ . ~a~
h ~0 ~ ~ ~ +' ~i:~
O s: O . ~ tn ~cu tH ~ O ~ r-l a) u~ .
. ~ ~ ~ a~ ~ L~ tn ~r-l n ~ ~r-l ~ e ~ h ~
_ ___ .________.___ ___ Pr~ O O O rJ O
+' ~ V O O O C~ ~
a)O ~ ~ ~o ~ ~~1 ,D ~_, r-lr~l ~1 a~ ~3 a>___~ ___ _______._ ~ ll r-l r~\ O N\ O a~
P_~ ~ \ O \ O I r~ Z
0F~ ~ r~ \ r~J r-J \ r~J ~ +
E~___ ___. _ __.__ __ _ N r-~
_ o ^ a~ O
m+~ ~ ~ ~ ~, 0 ,~ (\ a) .,~
h E3 N r~ r; r~ O O 0 3: ~ ~ r-J ~ ,-1 ~.,'H
0 ~3 _~ ~ O
~ trH Z S ~~H
.~ ._ _.___ _ ___ __. _ ___ ~ ~a~
r-l 0 a,h ~D~r-l~ ~ o a~
a) .. .~ ~o :~
,~ ~ o o a) O ln ~ ~ ~::t a) ,~~-1 N
~ O l-J 11 11 S~ +~~:
+~ ~ O N C\l O O'd O O O O S~ N r~l0 ~ 0 a)~n __ .. _.. _ ._.__ .___.._______ __ _ r-l I~ ~
~-~o ~-10 ~ ~ +~J .~~
r~ h ~ 8 g g ~ ~ ~
~ O ~3: ~ ~ D r~ a) ~I) $ r~ ,0~ ~ H C) bD
t~ 0 ~0 __--_____ _ _____ ^ h rl ~ O r-l (~Jr~ ~ t~ ~o c~: ~; o c~
___ _ _ In this example, an oxygen top-blowing converter with the capacity of 2 tons was usèd. Two nozzles 6 mm in diameter were provided in the bottom of the converter.
Carbon dioxide gas was injected into the mol-ten metal through the nozzles. The top-blowing oxygen was supplied through the straight type nozzles and Laver-type nozzles.
In one series of experiments, the flow rate of the bottom blowing carbon dioxide gas was varied. In another series of experiments, the outlet velocity of the top-blowing oxygen was varied.
Other experimental conditions were:
molten iron: 2000 kg, 1380C,
In a preferred embodiment of this invention, a blow of gas predominantly comprised of carbon dioxide and supplied by way of conduits 5 is introduced into the molten metal 3 through concentric nozzles Z provided in the bottom of said basic oxygen furnace at least partly during the period of time from the beginning of blowing to the tapping of the melt and the M ow rate of the bottom blowing gas is less than 9/100 the rate of oxygen blown onto the melt through lance 4.
In one embodiment of this invention, the uniform mixing time is adjusted to 20 seconds or more.
Another embodiment of this invention is now described by reference to Fig. 3, an oxygen steel furnace 31 has an oxygen top-blowing lance 32 and a series of gas bottom-blowing nozzles 33. Oxygen gas is blown from the top-blowing lance 32 into the furnace 31 to perform decarburization and is discharged primarily as carbon monoxide gas. A gas primarily consisting of carbon dioxide is jetted from the bottom-blowing nozzles 33 into the furnace 31 where it is decomposed .535~i~
following the course C + C02 ~ 2C0 and discharged from -the furrlace. These two supplies of carbon monoxide gas are caught in a hood 34 on top of the furnace 31. They contain less than 20 vol% of nitrogen gas since they entail a-tmosphere as they are being caught in the hood.
The gas caught in the hood 34 is first freed of dust through a dust collector 35 and transferred to a gas holder 36 where it is stored temporarily before proceeding to sub sequent treatments. The gas in the holders 36 is mixed with oxygen and/or steam prior to entering into a burner 37. The gas in the holder 36 may be burnt with oxygen coming from an oxygen holder 41 for supplying oxygen to the oxygen top-blowing lance 329 and is optionally dehumidified before i~
is transferred to a carbon dioxide holder 399 or after the burning, the gas may be denitrified in a C02/N2 separator 38 to increase the C02 content before it is transferred to the carbon dioxide holder 39.
The carbon dioxide transferred to its holder 39 is supplied to the gas bottom-blowing nozzle 33 through the flow regulator 40. Alternatively, it may be combined with untreated gas from the gas holder 36 before it is supplied to the nozzle 33.
The gas Jetted from the bottom-blowing nozzle 33 into the bath is again caught in the hood 34 together with the carbon monoxide resulting from decarburization. Thus, each supply of carbon monoxide gas and carbon dioxide gas keeps recycling through the path described above.
Another embodiment of this invention is now described ~ 16 -by reference to Figs. 6 and 7. A 2~ton pure oxygen -top-blow ing converter is provided wi-th -two bo-ttom nozzles (I~D~ 8rnm) -through which a gas is -to be blown f`rom below the rnelr bath.
The oxygen top-blowing lance used is a three-sheathed lance (four coaxial tubes) 61 as shown in the bottom view and longitudinal cross section of Fi~s. 6 and 79 wherein -the center of the disc 63 of i-ts tip 62 is provided with a single nozzle opening 659 10 mm in diameter serving as a passage 64 for the supply of a flux powder and said opening is surrounded by -three nozzle openings 67 each 4.2 mm in diameter serving as a passage 66 for the supply of oxygen. This lance permits the powder to be blown against the surface of the mel-t 68 as it is mixed with oxygen being jetted from the three surrounding points.
This invention will be further described in conjunction with the working examples.
Example 1 A conventional oxygen conver-ter wi-th the capacity of 250 -tons was used to carry out this invention. Four nozzles 10 mm in diame-ter were ins-tallecl at -the bot-tom of the conver-ter~
Into this converter, as main s-tarting materials, 215 tons of mol-ten iron and 35 tons of scrap iron, and, as other starting material, 3 -tons of quick lime were charged. The composi-tion of the molten iron was9 by weight percent, 4.63% C~
0.48% Si, 0.45% Mn9 0.123% P, 0.0018% S, 0.0038~ N and the balance iron and incidental impurities. The temperature thereof was 1385C.
The gas blowing from the top and from the bottom was s~t ~
~ 17 -carried out as in the following.
The top~blowing of oxygen was carried out at a flow rate of 409000 Nm3/hr in accordance with the flow pattern shown in Fig. 2. The bottom blowing was also carried out following the flow pattern shown in Fig. 2. As shown in Fig, 2, the bottom blowing was initiated at a flow rate of 50 Nm3/hr and the rate was încreased to 100 Nm3/hr when the top-blowing of oxygen was initiated. At the end stage of the blowing, the rate of the bottom blowing was increased to 200 Nm3/hr and was then reduced to 50 Nm3/hr after the top-blowing was finished. The bottom blowing gas was an exhaust gas obtained from an oxygen converter and comprised, by weight percent, 18% C0, 63% C02, 16% N2 and 3% H2.
For the purpose of comparisonJ a conventional oxygen steel making process was also carried out using the same oxygen converter. The composition of the starting material charged into the converter and the manner of top-blowing were the same as in the above. In this case, however, the bottom blowing was not applied. The intended product steel was low-carbon rimmed steel. Table 1 below summarizes the finalcomposition of -the molten steel.
Table _ Composition (% by weight) Tem. in Tapp ng ~ c-- ~ -n-T--P~ r---- (c,l s17)g (%) Ths l l l ( _ _ invention 0.063 0.16¦0.017 0.012 0.0025 1625 11 13.8 96.3 . I _ _ . ~ _, tional 0.065 0.12¦0.021 0.015 0.0011 1618l 19.5 95 8 18 ~
As ls apparent from the data show~ in Table ] above 9 the produc-t steel o:E the me-thod of this invention has -the composition falling within that of low carbon rimmed steel and also shows a remarkably efficierlt dephosphorization and tapping yield.
In this example 9 Example 1 was repeated except that various kinds of gases were used as the bottom blowing gas.
As hereinbefore mentioned, the bottom blowing gas of this invention may be an exhaust gas discharged from an iron making plan-t, or a s-teel making plant. In this example, therefore, such kind of exhaust gas was used as the bottom blowing gas. Gas No. 1 was derived from an exhaust gas discharged from an oxygen converter and was made rich in carbon dioxide. Gas No. 2 was derived from an exhaust gas discharged from a hot stove and was made rich in carbon dioxide.
The final composition of the molten s-teel in each run is summarized in Table 2 be]ow.
Table 2 ___ _ Gas composition (% by volume) Gas No. C2 CO N2 2 2 1 9~ O 5 O
2 ~2.6 O 4~ 3.2 ~ ~; ?~ .3~
~ 19 -Table 3 Final composition ~ _ ~ 1 Gas~ by ~:gl:l~ T Fe Ten~lp. ¦
No. C Mn j N (%) __ _ .
1 0.058 0.15~.0019 14~2 1632 2 '~r, 1 = o, ODC5 1~.5 1619 According to this invention, an exhaus-t gas discharged from the oxygen converter may be used as the bo-ttom blowing gas. If the nitrogen content of the exhaust gas is below 5C%
by volume, the nitrogen content of the resulting steel product is accep-table. In addition, according to this inven-tion, the agita-tion of the melt was effected thoroughly, resulting in sufficient degree of decarburization and dephosphorization to make the method of -this invention practical.
Example 3 The following star-ting materials were charged lnto an oxygen converter shown in Fig. 1. The capacity of the conver--ter was 250 -tons and the bath depth was 250 cm. Two concen-tric nozzle were provided at the bottom (the inner nozzle was 12.7 mm in inner diameter and 15.4 mm in outer diameter, -the slit width was 1.15 mm9 and the ou-ter nozzle was 17.7 mm in inner diame-ter and 19.1 mm in outer diameter.
Mo]-ten iron. 220 tons The [Mn] is about 0.40% and ~p] is about 0.150%
in molten iron.
Scrap irono 30 tons Other materials:
quick llme 9 tons iron ore 4.5 tons light dolomite 3~0 tons fluorite 0.2 ton converter slag 1.8 tons According to the method of this invention, various kinds of bottom blowing gas were injected into the melt while top-klowing pure oxygen through a lance. The blowing condi-tions and the resulting uniform mixing time are summarizedin the following Table 4.
r-. _ . .. _ _ _ . .. . . _ . _ . _ .. _ .. _ . ... . .
hO O
.~ ~ ~ ~ o 1-~ ~
P~r-l~ . . . O
P~ a) ~~) ~) Lt~
0 ~ I c~ , ~ :~ a) ~1 _... _ .. _ _... .. _._ _ .. ~ . .
~1 o a~ _~LO L~ L~`\
t~ `o~ O O O a~ OC) ~ h ~_ . . .
1 0 o O o o ~ ~ P
tH C.) t) r-l o ~a~
.. ___ -- __ __ ~ h h 0 ~ r-l ~ O
S~ r~ 1--l r~ J r-lrl E-- ~l tn a) t~
. _ _ __ . ~a~
h ~0 ~ ~ ~ +' ~i:~
O s: O . ~ tn ~cu tH ~ O ~ r-l a) u~ .
. ~ ~ ~ a~ ~ L~ tn ~r-l n ~ ~r-l ~ e ~ h ~
_ ___ .________.___ ___ Pr~ O O O rJ O
+' ~ V O O O C~ ~
a)O ~ ~ ~o ~ ~~1 ,D ~_, r-lr~l ~1 a~ ~3 a>___~ ___ _______._ ~ ll r-l r~\ O N\ O a~
P_~ ~ \ O \ O I r~ Z
0F~ ~ r~ \ r~J r-J \ r~J ~ +
E~___ ___. _ __.__ __ _ N r-~
_ o ^ a~ O
m+~ ~ ~ ~ ~, 0 ,~ (\ a) .,~
h E3 N r~ r; r~ O O 0 3: ~ ~ r-J ~ ,-1 ~.,'H
0 ~3 _~ ~ O
~ trH Z S ~~H
.~ ._ _.___ _ ___ __. _ ___ ~ ~a~
r-l 0 a,h ~D~r-l~ ~ o a~
a) .. .~ ~o :~
,~ ~ o o a) O ln ~ ~ ~::t a) ,~~-1 N
~ O l-J 11 11 S~ +~~:
+~ ~ O N C\l O O'd O O O O S~ N r~l0 ~ 0 a)~n __ .. _.. _ ._.__ .___.._______ __ _ r-l I~ ~
~-~o ~-10 ~ ~ +~J .~~
r~ h ~ 8 g g ~ ~ ~
~ O ~3: ~ ~ D r~ a) ~I) $ r~ ,0~ ~ H C) bD
t~ 0 ~0 __--_____ _ _____ ^ h rl ~ O r-l (~Jr~ ~ t~ ~o c~: ~; o c~
___ _ _ In this example, an oxygen top-blowing converter with the capacity of 2 tons was usèd. Two nozzles 6 mm in diameter were provided in the bottom of the converter.
Carbon dioxide gas was injected into the mol-ten metal through the nozzles. The top-blowing oxygen was supplied through the straight type nozzles and Laver-type nozzles.
In one series of experiments, the flow rate of the bottom blowing carbon dioxide gas was varied. In another series of experiments, the outlet velocity of the top-blowing oxygen was varied.
Other experimental conditions were:
molten iron: 2000 kg, 1380C,
4.20% C, 0.52% Si, 0.61% Mn, 0.121% P, 0.020% S
scrap : 360 kg oxygen flow rate: 6 Nm3/min oxygen pressure before passing into the lance:
scrap : 360 kg oxygen flow rate: 6 Nm3/min oxygen pressure before passing into the lance:
5 kg/mm distance between the lance tip and the bath surface: 300 mm carbon dioxide flow rate: 0.1 - 2.3 Nm3/min. ton oxygen jet velocity: Mach 0.3 - 2.3 blowing period: 18.6 minutes Under these conditions, the tapping yield and the oxygen effect were determined. The results are summarised in Figs. 4 and 5. Fig. 4 shows the results obtained when the flow rate of carbon dioxide was varied as indicated with an - 2~ -outlet velocity of oxygen of Mach 1. Fig. 5 shows the resulls obtained when the outlet velocity of oxygen was varied as indicated at a carbon dioxide ~low rate of 1 Nm3/min. ton.
The data plotted in Figs. 4 and 5 are shown in com-parison with those obtained in the conventional oxygen top-blowing process9 and no bottom-blowing is employed.
From the results shown in Fig. 4 it is noted that improved tapping yield (shown by graph A) and oxygen effect (shown by graph B) in comparison with those of the conven-tional process were obtained when an flow rate of carbondioxide of 0.3 - 2.0 Nm3/min. ton was employed at an outlet velocity of oxygen of Mach 1. It is also noted from Fig. 5 that improved tapping yield (shown by graph A) and oxygen e~fect (shown by graph B) in comparison with those obtained 15 in the conventional process were obtained when an outlet velocity of oxygen of Mach 0.8 - 2.0, preferably Mach 0.8 -1. 5 was employed at a carbon dioxide flow rate of 1 Nm3/min.
ton.
Example 5 The steel making apparatus comprised a 2~0-ton oxygen top-blowing converter provided with four bottom-blowing nozzles and the gas circulation system comprising the com-ponents described above in conjunction with Fig. 3. The refining conditions were as followso the molten iron consisted f 4.63% C, 0.51% Si, 0.43% Mn, 0.115% P, 0.023% S and the remainder Fe9 the melt temperature was 1358C, the hot metal ratio was 87%, and 3.5 tons of iron ore was charged together with auxiliary materials composed of 11 tons of quick lime -- 24 _ and 8 tons of dolomi-te. The supply ra-te of:-top-blowr-l oxygen was 40,000 Nm3/hr. The was-te gas recovered -through the abo~Je circulation sys-tem was burnt, denitrified, and supplied at a 1OW rate of 1,500 Nm3/hr as a bottom-blown gas that consisted of 98.5 vol~o C0~ and 1.5 vol% N2. The refining pattern was adapted for the production of low-carbon rimmed steelo oxygen was blown in the same marmer as in the conventional me-thod whereas a constan-t flow of bottom-blown gas was supplied up to the time of start of tapping.
The results of the refining were- a waste gas con-sisting of 71.1 vol% C0, 15.2 vol% C029 10.5 vol% N2 and 3.2 vol% H20 could be recovered from the furnace in a quan-tity of 108,000 Nm3/hr. The steel obtained had a final analysis of 0.0058% C, 0.01% Si, 0.11% Mn, 0.018% P, 0.020/~ S, 0.0011% N and -the remainder Fe, and its temperature was 1628C. This indicates the fact that refining operations such as decarburization and denitrification were adequate for the making of the desired s-teel.
Example 6 The converter equipped with such sys-tem was opera-ted by four differen-t me-thods: the process of this invention (I)9 the LD-AC process (II), the process wherein oxygen was blown from above and a gas was blown from below and a flux was supplied as a mass (III), and the conventional oxygen -top-blowing process (IV). In each case, the following conditions were employed, and the resul-ts shown in Table 5 below were obtained. Composi-tion of molten iron 4.3/0 C, 0.50% Si, 0.58% Mn, 0~125% P and 0.023% S.
Temperature 1380C
Charge ~ 2000 kg of molten iron and 370 kg of scrap Flow rate of top-blown oxygen o 6 Nm3/min. ton Powder carrier gas : argon gas at 1 Nm3/min Bottom-blown gas o carbon dioxide gas at 1 Nm3/min Distance (h) between lance and molten metal surface : 300 mm Blowing period : 17.3 min Table 5 T Fe Chemical analysis (%) I Tem in C Si ~ - ~ (C) Slopping slag Yie d I 0.38 _ 0.30 0.012 0.019 1680 no 6.3 ~0.5 II 0.~9 _ 0.15 0.013 0.021 1685 much 21.8 -0.7 III 0.38 _ 0.27 0.035 0.021 1680 no 6.5 +O.h IV 0.41 _ 0.14 0,044 O.OZ3 1690 no 7.3 0 As is apparent from the foregoing, the method of this invention is very practical, since the existing oxygen conver-ter may be utilized merely by installing a nozzle at the bot-tom or at the side wall of i-t. In addition, the gas to be used as the bottom blowing gas may be an exhaust gas obtained from the converter with or without further treatment of increasing -the concentration of carbon dioxide. Thus, the method of this invention is easily applicable to the existing oxygen converter and will bring about practical advantages.
The data plotted in Figs. 4 and 5 are shown in com-parison with those obtained in the conventional oxygen top-blowing process9 and no bottom-blowing is employed.
From the results shown in Fig. 4 it is noted that improved tapping yield (shown by graph A) and oxygen effect (shown by graph B) in comparison with those of the conven-tional process were obtained when an flow rate of carbondioxide of 0.3 - 2.0 Nm3/min. ton was employed at an outlet velocity of oxygen of Mach 1. It is also noted from Fig. 5 that improved tapping yield (shown by graph A) and oxygen e~fect (shown by graph B) in comparison with those obtained 15 in the conventional process were obtained when an outlet velocity of oxygen of Mach 0.8 - 2.0, preferably Mach 0.8 -1. 5 was employed at a carbon dioxide flow rate of 1 Nm3/min.
ton.
Example 5 The steel making apparatus comprised a 2~0-ton oxygen top-blowing converter provided with four bottom-blowing nozzles and the gas circulation system comprising the com-ponents described above in conjunction with Fig. 3. The refining conditions were as followso the molten iron consisted f 4.63% C, 0.51% Si, 0.43% Mn, 0.115% P, 0.023% S and the remainder Fe9 the melt temperature was 1358C, the hot metal ratio was 87%, and 3.5 tons of iron ore was charged together with auxiliary materials composed of 11 tons of quick lime -- 24 _ and 8 tons of dolomi-te. The supply ra-te of:-top-blowr-l oxygen was 40,000 Nm3/hr. The was-te gas recovered -through the abo~Je circulation sys-tem was burnt, denitrified, and supplied at a 1OW rate of 1,500 Nm3/hr as a bottom-blown gas that consisted of 98.5 vol~o C0~ and 1.5 vol% N2. The refining pattern was adapted for the production of low-carbon rimmed steelo oxygen was blown in the same marmer as in the conventional me-thod whereas a constan-t flow of bottom-blown gas was supplied up to the time of start of tapping.
The results of the refining were- a waste gas con-sisting of 71.1 vol% C0, 15.2 vol% C029 10.5 vol% N2 and 3.2 vol% H20 could be recovered from the furnace in a quan-tity of 108,000 Nm3/hr. The steel obtained had a final analysis of 0.0058% C, 0.01% Si, 0.11% Mn, 0.018% P, 0.020/~ S, 0.0011% N and -the remainder Fe, and its temperature was 1628C. This indicates the fact that refining operations such as decarburization and denitrification were adequate for the making of the desired s-teel.
Example 6 The converter equipped with such sys-tem was opera-ted by four differen-t me-thods: the process of this invention (I)9 the LD-AC process (II), the process wherein oxygen was blown from above and a gas was blown from below and a flux was supplied as a mass (III), and the conventional oxygen -top-blowing process (IV). In each case, the following conditions were employed, and the resul-ts shown in Table 5 below were obtained. Composi-tion of molten iron 4.3/0 C, 0.50% Si, 0.58% Mn, 0~125% P and 0.023% S.
Temperature 1380C
Charge ~ 2000 kg of molten iron and 370 kg of scrap Flow rate of top-blown oxygen o 6 Nm3/min. ton Powder carrier gas : argon gas at 1 Nm3/min Bottom-blown gas o carbon dioxide gas at 1 Nm3/min Distance (h) between lance and molten metal surface : 300 mm Blowing period : 17.3 min Table 5 T Fe Chemical analysis (%) I Tem in C Si ~ - ~ (C) Slopping slag Yie d I 0.38 _ 0.30 0.012 0.019 1680 no 6.3 ~0.5 II 0.~9 _ 0.15 0.013 0.021 1685 much 21.8 -0.7 III 0.38 _ 0.27 0.035 0.021 1680 no 6.5 +O.h IV 0.41 _ 0.14 0,044 O.OZ3 1690 no 7.3 0 As is apparent from the foregoing, the method of this invention is very practical, since the existing oxygen conver-ter may be utilized merely by installing a nozzle at the bot-tom or at the side wall of i-t. In addition, the gas to be used as the bottom blowing gas may be an exhaust gas obtained from the converter with or without further treatment of increasing -the concentration of carbon dioxide. Thus, the method of this invention is easily applicable to the existing oxygen converter and will bring about practical advantages.
Claims (13)
1. A method of producing carbon steel and low-alloy steel in a basic oxygen furnace comprising preparing a molten metal suitable for producing the steel in said basic oxygen furnace, carrying out the top-blowing and bottom-blowing and then tapping the resulting molten steel, characterized in that a blow of the bottom-blowing gas predominantly comprised of carbon dioxide is introduced into the molten metal through at least one nozzle provided in the bottom or side wall of said basic oxygen furnace at least partly during the period of time from the beginning of blowing to the tapping of the melt, the flow rate of the bottom-blowing gas being 1/200 - 9/100 the rate of oxygen impinged upon the melt through a lance.
2. A method as defined in Claim 1 above, in which the nitrogen content in said bottom blowing gas is limited to not more than 20% by volume.
3. A method as defined in any one of Claims 1 and 2, in which the bottom-blowing gas contains a small amount of oxygen.
4. A method as defined in Claim 1, in which the amount of the bottom-blowing gas is adjusted so that the uniform mixing time is longer than 20 seconds.
5. A method as defined in Claim 4, in which the unit form mixing time is 20 - 70 seconds.
6. A method as defined in Claim 1, which further comprises collecting a waste gas discharged from said basic oxygen furnace, combining the waste gas with oxygen and/or steam, burning the the mixture thereof and then recovering the resulting combustion gas to blow it into the molten metal as at least a portion of the bottom-blowing gas.
7. A method as defined in Claim 6, in which carbon dioxide is recovered from the combustion gas and is blown into the molten metal as at least a portion of the bottom-blowing gas.
8. A method as defined in Claim l, in which the top-blowing gas is impinged onto the molten metal at an outlet velocity of Mach 0.8 - 2Ø
9. A method as defined in Claim 8, in which the top-blowing gas is impinged onto the molten metal at an outlet velocity of Mach 0.8 - 1.5.
10. A method as defined in Claim 1, in which a powder of a slag-forming agent is introduced into the molten metal together with the top-blowing oxygen jet.
ll. A method as defined in Claim 10, in which said slag-forming agent is at least one of quick lime, limestone, fluorite, dolomite, iron ore and mixtures thereof.
12. A steel making apparatus having a gas circulation system, which comprises, in combination, a furnace permit-ting both top-blowing of pure oxygen and bottom-blowing of a gas mainly composed of carbon dioxide, means for collecting the waste gas generated from the furnace, means for mixing the waste gas with oxygen and/or steam, means for burning the mixture thereof, and means for passing the resulting combustion gas through a piping system to inject it into the molten metal within said furnace.
13. A steel making apparatus as defined in Claim 13, which further comprises a means for separating carbon dioxide from the combustion gas, the separated carbon dioxide being injected into the molten metal as at least a portion of the bottom-blowing gas.
Applications Claiming Priority (10)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP54064223A JPS6013402B2 (en) | 1979-05-24 | 1979-05-24 | Steel refining equipment with gas circulation system |
| JP6422179A JPS55158208A (en) | 1979-05-24 | 1979-05-24 | Refining method of steel |
| JP6422279A JPS55158209A (en) | 1979-05-24 | 1979-05-24 | Composite blowing method of steel |
| JP64222/1979 | 1979-05-24 | ||
| JP64221/1979 | 1979-05-24 | ||
| JP64223/1979 | 1979-05-24 | ||
| JP84521/1979 | 1979-07-03 | ||
| JP54084521A JPS6023163B2 (en) | 1979-07-03 | 1979-07-03 | steel smelting method |
| JP54084522A JPS6040486B2 (en) | 1979-07-03 | 1979-07-03 | steel refining method |
| JP84522/1979 | 1979-07-03 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CA1153560A true CA1153560A (en) | 1983-09-13 |
Family
ID=27523828
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA000352347A Expired CA1153560A (en) | 1979-05-24 | 1980-05-21 | Production of carbon steel and low-alloy steel with bottom blowing basic oxygen furnace |
Country Status (10)
| Country | Link |
|---|---|
| AT (1) | AT377007B (en) |
| AU (2) | AU2829080A (en) |
| BR (1) | BR8003268A (en) |
| CA (1) | CA1153560A (en) |
| DE (1) | DE3019899C2 (en) |
| FR (1) | FR2457325A1 (en) |
| GB (1) | GB2054655B (en) |
| IT (1) | IT1130459B (en) |
| LU (1) | LU82481A1 (en) |
| NL (1) | NL183413C (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10781499B2 (en) | 2018-01-17 | 2020-09-22 | Air Products And Chemicals, Inc. | Bottom stirring tuyere and method for a basic oxygen furnace |
Families Citing this family (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5623215A (en) * | 1979-08-02 | 1981-03-05 | Nippon Kokan Kk <Nkk> | Converter steel making method |
| JPS5816013A (en) * | 1981-07-17 | 1983-01-29 | Kawasaki Steel Corp | Operating method for top and bottom blown converter and top blowing lance for operation of top and bottom blown converter |
| NL8201269A (en) * | 1982-03-26 | 1983-10-17 | Hoogovens Groep Bv | METHOD FOR MANUFACTURING STEEL IN A CONVERTER FROM CRUDE IRON AND SCRAP. |
| JPS58185707A (en) * | 1982-04-23 | 1983-10-29 | Sumitomo Metal Ind Ltd | Refining method of steel |
| LU84390A1 (en) * | 1982-09-27 | 1984-04-24 | Arbed | METHOD AND DEVICE FOR HEATING A STEEL BATH FILLED WITH SCRAP |
| US4599107A (en) * | 1985-05-20 | 1986-07-08 | Union Carbide Corporation | Method for controlling secondary top-blown oxygen in subsurface pneumatic steel refining |
| JPS62136513A (en) * | 1985-12-10 | 1987-06-19 | Nippon Steel Corp | Refining method by top and bottom blowing in converter |
| DE4328045C2 (en) * | 1993-08-20 | 2001-02-08 | Ald Vacuum Techn Ag | Process for decarburizing carbon-containing metal melts |
| GB0209365D0 (en) | 2002-04-24 | 2002-06-05 | Boc Group Plc | Injection of solids into liquids |
| GB0213376D0 (en) | 2002-06-11 | 2002-07-24 | Boc Group Plc | Refining ferroalloys |
| CN114275784B (en) * | 2021-12-24 | 2023-05-19 | 上海大学 | CO utilization 2 System and method for preparing CO gas |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AT337736B (en) * | 1973-02-12 | 1977-07-11 | Voest Ag | METHOD OF REFRESHING BIG IRON |
| FR2273873A1 (en) * | 1974-06-07 | 1976-01-02 | British Steel Corp | Refining alloy steel - by top blowing with oxygen and introducing a fluid to agitate the melt |
-
1980
- 1980-05-20 AU AU2829080A patent/AU2829080A/en active Pending
- 1980-05-20 AU AU58590/80A patent/AU525023B2/en not_active Expired
- 1980-05-21 CA CA000352347A patent/CA1153560A/en not_active Expired
- 1980-05-22 GB GB8016879A patent/GB2054655B/en not_active Expired
- 1980-05-23 IT IT67813/80A patent/IT1130459B/en active
- 1980-05-23 FR FR8011588A patent/FR2457325A1/en active Granted
- 1980-05-23 NL NLAANVRAGE8003012,A patent/NL183413C/en not_active IP Right Cessation
- 1980-05-23 AT AT0277580A patent/AT377007B/en not_active IP Right Cessation
- 1980-05-23 DE DE3019899A patent/DE3019899C2/en not_active Expired
- 1980-05-23 LU LU82481A patent/LU82481A1/en unknown
- 1980-05-26 BR BR8003268A patent/BR8003268A/en not_active IP Right Cessation
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US10781499B2 (en) | 2018-01-17 | 2020-09-22 | Air Products And Chemicals, Inc. | Bottom stirring tuyere and method for a basic oxygen furnace |
Also Published As
| Publication number | Publication date |
|---|---|
| GB2054655A (en) | 1981-02-18 |
| IT1130459B (en) | 1986-06-11 |
| AU525023B2 (en) | 1982-10-14 |
| DE3019899C2 (en) | 1986-04-30 |
| LU82481A1 (en) | 1980-10-08 |
| AU2829080A (en) | 1980-11-27 |
| FR2457325A1 (en) | 1980-12-19 |
| NL183413B (en) | 1988-05-16 |
| IT8067813A0 (en) | 1980-05-23 |
| NL183413C (en) | 1988-10-17 |
| GB2054655B (en) | 1983-03-30 |
| AT377007B (en) | 1985-01-25 |
| ATA277580A (en) | 1984-06-15 |
| DE3019899A1 (en) | 1980-12-04 |
| NL8003012A (en) | 1980-11-26 |
| FR2457325B1 (en) | 1983-11-10 |
| BR8003268A (en) | 1980-12-30 |
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