PROCESS FOR MELT REDUCTION OF Cr STARTING MATERIAL AND MELT REDUCTION FURNACE

Abstract: A process for directly obtaining high Cr content melt by melt reduction of Cr starting materials such as Cr ore pel­ lets, etc. is disclosed, which comprises using a furnace equipped with a bottom-blowing nozzle, a side-blowing noz­ zle, and a top-blowing nozzle, blowing an inert gas or the like through the bottom-blowing nozzle to form a projection on the molten metal surface, blowing an inert gas against the projection through the side-blowing nozzle to diffuse the molten metal into a Cr material-floating region in the slug for accelerating reduction of the Cr-containing material with C contained in the molten metal, blowing O₂ for decarburiza­ tion into the molten metal through the top-blowing lance, and blowing O₂ for secondary combustion into slug to form a secondary combustion region mainly in slug, and strongly stirring slug by the side-blowing gas to give the heat pro­ duced by the secondary combustion to Cr ores with high effi­ ciency, with keeping secondary combustion ratio at 0.3 or more for assuring the high secondary combustion.

Description: The invention relates to a method of smelting reduction of Cr raw materials and a smelting reduction furnace for performing the method. In JP-A-61-279609 a furnace for producing high-chromium alloy by melt reduction is disclosed comprising bottom blowing tuyeres, side-blowing tuyeres and a top blowing lance. A metallic bath is contained in a furnace body and a slag is formed above the bath. The tip of the top blowing lance is arranged above the slag. A stirring gas is blown from the bottom blown tuyeres into the metallic bath. The side-blowing tuyeres are provided for blowing a gas containing oxygen and an inert gas into the furnace body. A chromium reduction is carried out in the slag, if chromium raw material, carbonaceous material and fluxing agent are fed. Furthermore, a furnace and a method for producing chromium-containing molten iron is known from JP-A-62-80214. This furnace comprises as well as the above-mentioned furnace a furnace body having bottom blowing tuyeres, side blowing tuyeres and a top blowing lance. Oxygen is blown from the top blowing lance into the furnace and a stirring gas is blown from the bottom blowing tuyeres into the furnace. High Cr steel like stainless steel has been conventionally produced using ferrochromium as raw material. In view of saving energy and securing low production cost, smelting reduction process is recently considered potentially attractive, which obtains high Cr molten metal directly using Cr raw ores (explanation will refer to "Cr ore" as example hereinafter). In the smelting reduction method, Cr ores, carbonaceous materials and others are supplied into a reduction furnace for directly obtaining high Cr molten metal. For the smelting reduction method, there have been several proposals hitherto. One of them blows respectively O₂ from bottom tuyeres and N₂ from side blowing tuyeres at the same time as blowing O₂ from a top lance. Another of them blows respectively O₂ from the bottom tuyeres and O₂ and N₂ from the side blowing tuyeres at the same time as blowing O₂ from the top lance. The latter is disclosed in, for example, Japanese Patent Application Laid-Open 61-279,608 (1986). However, each of the above mentioned methods has big problems that the Cr reduction speed is low and treatments take much time. With respect to the backgrounds of the prior art, following problems are solved by the features of claim 1. 1. The reduction of Cr ore was progressed by action of C in carbonaceous materials after Cr ore had been molten in the slag, and the melting of Cr ore was assumed to determine Cr reduction. Therefore, important technical interests for shortening the treating time were focused to specifying of the slag composition. But Cr ore was inherently less to be molten, and it was limited to speed up the reduction by accelerating the melting of Cr ore. 2. For accelerating the melting speed of Cr ore in the slag and the reduction speed, it was considered to make a post combustion of CO gas in the furnace and utilize the heat thereby. An existing method has been adopted, which blew O₂ for the post combustion from a furnace upper part. If a post combustion ratio was increased, the temperature of an exhaust gas went up, but there has not been a technique which efficiently tansmitted a sensitive heat of the exhaust gas to the molten metal, and as a result, a heat transfer efficiency was lowered and the exhaust gas at high temperature was removed inevitably. The heated exhaust gas considerably damaged the wall refractories and those of an exhaust gas food. Therefore, in general it has been considered that the post combustion ratio could not be heightened so much. For dealing with the above stated problems of the prior art, the inventors made studies on the mechanisms of the smelting reduction and the decarburization, and the actual measures therefor, and subsequently they found following facts. (1) As having been said above, it was assumed that Cr ore was reduced by the carbonaceous materials staying in the slag after Cr ore had been molten in the slag, but it has been found that almost all of the actual reductions were made by actions of C as the reducing material. Therefore, the reduction speed was determined by contacting of the molten metal to Cr ore heated at the high temperature, not by melting of Cr ore into the slag, so that the reduction speed could be effectively heightened by positively contacting of the molten metal to the ores. (2) It was basic concept in the prior art that the post combustion ratio could not be largely heightened in view of the technical limit with respect to increasing of the heat transfer efficiency and consumption of the refractories. If O₂ was blown so that the post combustion was mainly caused in the slag to forcibly agitate the slag, the heat transfer efficiency could be heightened effectively. Thus, by the high post combustion and the high heat transfer efficiency, the temperatures of the slag and Cr ore in the slag were heightened, and the reduction speed of Cr ore by C (in the molten metal) expressed by an under formula, may be raised effectively Cr₂O₃ + 3 C = 2Cr + 3CO. (3) The foregoing technique sometimes carried out the bottom blowing of O₂ in a certain period or in a full term, but such blowing was harmful to the post combustion. That is, if O₂ was blown from the bottom, CO gas was much generated in the molten metal and agitated the molten metal compulsively, and splashes of the molten metal reached the region of the post combustion, and since C reacted with O₂ or CO₂ and generated CO, the post combustion was hindered. Therefore the bottom blowing had to be avoided, irrespective of a part and the full term of the reduction period. Cr raw ores are very fine in grain diameters, and ordinarily around 90% contain those having grain diameters of not more than 1 mm. Therefore, when Cr raw ores such as powders are charged into the reduction furnace of the converter type from a top part, the powder ores fly outside of the furnace and lose up to 30%. For avoiding the flying losses, an injection charging may be suggested, but special facilities are required independently, and the transporting pipes are easily injured by the hard Cr ores. Thus, such measures could not be adopted actually. In view of these circumstances, Cr raw ores are formed into pellets or briquets, inviting high production costs. If the ores are agglomerated, the specific surface areas of the ores are made small so that a pre-heating time is made long and the reduction speed is lowered to lengthen the treating time. The inventors made studies also on those problems with respect to practical measures, and as a result it was found that the probability that grains of the Cr ores were exposed in the up-flowing gas, was decreased by heightening the charging speed of the ores and the flying loss was lowered, and especially if the charging speed of Cr raw ores is determined to be more than 4 kg/min-molten metal ton per pure Cr, the flying loss could be largely decreased. The invention is defined in the claims 1 and 7. Preferred embodiments are shown in dependent claims 2-6 and 8. The present invention as claimed in claim 1 is based on the above stated discoveries and specifies following conditions, whereby the smelting reduction at high treating speed can be realized. a) By the combination of the bottom tuyere blowing and the side tuyere lateral blowing of the agitating gases, the molten metal is positively diffused into a region of the slag where Cr ore exists so as to accelerate the reduction of Cr ore by C in the molten metal. b) O₂ for the post combustion is blown independently of decarburizing O₂ for providing the post combustion ratio more than a predetermined level. The post combustion O₂ is blown into the slag from the top blowing lance for forming the post combustion ragion therein, and the slag is agitated compulsively by the side tuyere blowing gas, and a heat generated by the post combustion is caused to transfer to Cr ores. c) The side tuyere blowing gas and the bottom tuyere blowing gas are CO or inert gas, and O₂ gas is not used because of avoiding hindrance of the reduction by C in the molten metal and the post combustion by the top-blowing O₂. Cr raw materials are reduced by maintaining the post combustion ratio to be more than 0.3. Depending upon the present invention as having stated above, the reduction of Cr ores is accelerated positively, securing the high post combustion ratio and the heat transfer efficiency, so that the reducing speed could be largely elevated in comparison with the conventional practices, and the smelting reduction could be performed effectively in a short period. Further, since the post combustion ratio is high, a unit consumption of the carbonaceous materials may be decreased, and P and S contents in the molten metal to be produced may be lowered. The invention proposes a method for controlling effectively the flying losses of the ores in the smelting reduction treatment. That is, in addition to the above stated conditions, the reduction of Cr raw ores is carried out as maintaining the charging speed of pure Cr (the charging speed of Cr raw ores calculated into the amount of pure Cr) more than 4 kg/min.molten metal ton. In the above mentioned smelting reduction, the invention proposes a method for grasping exactly progressing conditions of the smelting reduction and ends the blowing rapidly and appropriately. Paying attentions to a relation that the amount of the O₂ source in the exhaust gas decreases in response to decreasing of the smelting reduction, a reduction accomplishing time is judged in accordance with the difference between O₂ source in the exhaust gas and the blown O₂. Practically, during the smelting reduction, the amount of flowing the exhaust gas and the concentrations of CO and CO₂ in the exhaust gas are measured, and the reduction R of the Cr raw material is obtained from the above measured values, following an under formula, and the time of accomplishing the smelting reduction by the reduction R of the Cr raw material, and the smelting reduction treatment is ended. Herein, Wore: the amount of charging Cr raw materials (Ton) Oore: the amount of O₂ contained in Cr raw materials (Nm³/Ton) QE: the flowing amount of the exhaust gas (Nm³/min) (%CO): CO concentration in the exhaust gas (%) (%CO₂): CO₂ concentration in the exhaust gas (%) Fo₂: the flowing amount of the blown O₂ (Nm³/min) The smelting reduction furnace of the invention as claimed in claim 7 has the bottom blowing tuyeres and the side blowing tuyeres, and at least ones of the bottom blowing tuyeres and the side blowing tuyeres are arranged such that the both gas blowing lines are crossed. The smelting reduction furnace of the invention may have a plurality of bottom blowing tuyeres and side blowing tuyeres respectively, and in this case, it is preferable that one group comprises one bottom blowing tuyere and one side blowing tuyere, and the gas blowing lines of the respective groups agree with. Fig.1 and Fig.2 explain schematically the principle of the smelting reduction in the invention; Fig.3 (a) and (b) explain preferable jetting directions of the gas from the side tuyere with respect to the bottom blowing tuyeres; Fig.4 shows aimed post combustion ratio to observed post combustion ratio with respect to the bottom blown O₂ of the invention method and the comparative method; Fig.5 shows a relation between the height of the top blowing lance and the heat transfer efficiency; Fig.6 shows a relation between the amount of the gas blown from the side tuyere and the heat transfer efficiency; Fig.7 shows relations between the post combustion in the furnace and, S content, P content in the molten metal and the unit consumption of the carbonaceous material; Fig.8 shows briefly a relation of Cr increasing rate with respect to the amount of the gas blown from the bottom in the invention; Fig.9 shows changings as the time passes, of Cr concentration, C concentration, bath temperature, post combustion ratio, amount of oxygen sent from the lance, and amount of supplying raw materials; Fig.10 shows the reduction treating time of the invention in comparison with the conventional methods; Fig.11 (a) and (b) explain the treatings of the conventional methods (1) and (2) of Fig.10; Fig.12 shows a relation between the supplying speed of pure Cr and Cr increasing rate of the invention in comparison with the conventional method; Fig.13 shows influences of the supplying speed of powder Cr raw material to the splashing loss; Fig.14 shows changings as the time passes, of the temperature of the molten metal and Cr concentration in the slag in Example 3; Fig.15 shows a relation between R value and Cr concentration in the slag in Example 3; Fig.16 shows Cr concentration in the slag when the reduction is ended in Example 3; Fig.17 shows the temperature of the molten metal when the blowing is ended; Fig.18 explains one embodiment of the smelting furnace of the invention; Fig.19 shows influences of the amounts of the gases blown from the bottom and the side tuyeres to Cr increasing rate, when the smelting reduction was carried out in the furnace of Fig.18; Fig.20 explains a furnace of the comparative example where the bottom gas blowing line and the side gas blowing line do not cross; and Fig.21 shows influences of the amounts of the gases blown from the bottom and the side tuyeres to Cr increasing rate, when the smelting reduction was carried out in the furnace of Fig.20. In the drawings, the reference numerals 1, 1a, 1b are the bottom blowing tuyeres, 2 is the side blowing tuyere, 3 is the top blowing lance, and (A) is the upheaving part of the molten metal. The invention will be explained in detail. Fig.1 and Fig.2 show schematically the invention method. The furnace of the converter type is mainly used for carrying out the smelting reduction of Cr raw materials as Cr ores, Cr pellets and so on. Actually, the furnace has the bottom blowing tuyeres 1, the side blowing tuyere 2 and the top blowing lance 3. According to the invention method, Cr raw materials (explanation will refer to "Cr ore" as example hereinafter) carbonaceous materials and fluxes are supplied to a metal bath supported in the smelting reduction furnace, and the reducing treatment is performed under following conditions. The gases blown from the bottom tuyere 1, the side tuyere 2 and the top lance 3 during the smelting reduction treatment Gas blowings by the bottom tuyere 1 and the lateral tuyere 2 cooperate to diffuse the molten metal into the slag and heightens the reduction speed largely. The gas jetted from the side blowing tuyeres does not necessarily flow horizontally, and it is sufficient that the side blowing gas contacts the upheaving part (A) of the molten metal to splash or diffuse the molten metal into the slag. Accordingly, the gas blown from the side tuyere may flow at moderately downward or upward angles. As having mentioned above, the inventors found that the reduction of Cr ore in the slag was progressed by C in the molten metal as main of reducing substances, by which the molten metal was agitated compulsively to diffuse positively into the slag (range where Cr ores float) so as to increase the reducing rate. Therefore, in the invention, the agitating gas is supplied from the bottom blowing tuyere 1 to form an upheaving part (A) on the metal surface. At the same time, the agitating gas is supplied from the side tuyere 2 so that at least one part of the gas contacts the upheaving part (A), whereby the part (A) is splashed into the slag. An apparent specific gravity of the slag is ordinarily 0.3 to 0.5, and a bulk specific gravity of the Cr ore is about 3.0. Therefore, Cr ore in the slag gather around the lower region of the slag and float there as seen in Fig.2. If the upheaving part of the molten metal is splashed by the side blowing gas, the splashed one is diffused around the lower range of the slag where Cr ores exist as shown in Fig.2, and C in the splashed molten metal reduces Cr₂O₃, and thus the high reducing speed may be obtained. For providing such effects, it is of course necessary that the agitation must be caused compulsively by blowing more gas from the both of the bottom tuyere and the side tuyere, and an amount of gas to be blown is dete rmined in response to the amount and the depth of the molten metal. Fig.8 shows the relationship between the amount of the gas blown (Nm³/min·ton·tuyere) from the bottom tuyere and Cr increasing rate in the molten metal, from which is seen that Cr increasing rate, that is, Cr reducing rate is heightened in accordance with increasing of the amount of the bottom blowing gas, and an effective reducing reaction takes place. For obtaining such a behavior, it is preferable that the gas from the side tuyere exactly blows against the upheaving part (A) in the vertical directions and in the horizontal directions. For example, it is desirable to dispose the bottom blowing tuyere or tuyeres 1 and the side blowing tuyere or tuyeres 2 in the positional relation as shown in Figs.3 (a) and (b). The side blowing gas also agitates the slag where the post combustion range is formed, in addition to the diffusion of the molten metal as said above, which will be referred to later. The side blowing gas and the bottom blowing gas to be employed in the invention are limited to CO and the inert gas (N₂ or Ar), and O₂ is not used for following reasons. If O₂ is used for the side blowing, it reacts with C in the molten metal splashed for reducing Cr ore, and the reduction by C in the molten metal would be hindered. In addition, if O₂ is used, the temperature of the refractory become high and the refractory is damaged. Further, if O₂ is used for the bottom blowing, CO gas is much caused in the molten metal and the molten metal is agitated exceedingly. As a result, the splash reaches the post combustion range (refer to Fig.2), and C in the molten metal reacts with later mentioned O₂ for the post combustion so that the post combustion is hindered. Besides, if O₂ is used, a cooling gas (such as C₃H₈) must be added for the refractory whose temperature rises too much, so that the bottom blowing gas is increased, and splashes of the molten metal by the compulsive agitation are accelerated. Fig.4 shows the investigations of the actually measured post combustion ratio (CO₂+H₂O)/(CO+CO₂+H₂+H₂O) to the determined post combustion ratio (PCO₂)/(DCO₂+O₂ in ores)) with respect to the bottom blowing N₂ of the invention method and the bottom blowing O₂ of the comparative example, instead of N₂. It is seen that the post combustion is hindered by O₂ blown from the bottom. CO as the agitating gas and N₂ and Ar as the inert gas may be used independently or in mixture. The decarburizing O₂ is blown into the molten metal from the top lance 3, and concurrently O₂ for the post combustion is blown into the slag. The top blowing lance 3 is provided with a nozzle hole for the decarburizing O₂ and a nozzle hole for the post combustion O₂. The post combustion O₂ is supplied obliquely outside than the decarburizing O₂. In the invention, a high post combustion is provided, while the post combustion range is formed mainly within the slag. The post combustion range is thus formed in the slag, and the slag is forcibly agitated by blowing the gas from the side tuyere, whereby the high heat transfer efficiency is provided while the high post combustion is secured. Therefore, the post combustion O₂ must be blown into the slag such that the post combustion is formed in the slag. Actually, it is necessary that the height of the top blowing lance is determined at an appropriate level with respect to the levels of the slag or the molten metal. That is, the nozzle hole of the top blowing lance 3 can be positioned above a slag surface or thereunder. If it were too high, the post combustion range would not be formed in the slag so that the heat transfer efficiency is lowered. Conversely, if it were too low, the post combustion range would not be formed properly, since the post combustion O₂ is blown into the area where Cr ores float in the slag (see Fig.2). Fig.5 shows the relationship between the height of the lance nozzle from the slag surface (forming level) and the heat transfer efficiency, where if the lance is too high from the slag surface, a satisfied heat transfer efficiency cannot be obtained. Fig.6 shows the relationship between the amount of the gas blown from the side tuyere and the heat transfer efficiency, where the satisfied heat transfer can be obtained by blowing much the gas from the side tuyere so as to agitate the slag forcibly. The actually measured post combustion ratio is specified by (CO₂ + H₂O) / (CO + CO₂ + H₂ +H₂O) as the actually measured post combustion ratio which is the gas content bearing on an exhausted gas. In the invention, the above mentioned reducing treatment is performed at 0.3 of this post combustion ratio. Since the high heat transfer efficiency can be effected, and if this post combustion ratio is increased as said above, a high reduction treating ability (reducing speed) can be provided. In addition, if the post combustion ratio is increased, the addition amount of the carbonaceous materials (mainly coke) can be decreased. Consequently, the unit consumption of the carbonaceous materials may be decreased, and because almost all of P components in the molten metal are brought by the carbonaceous materials, P in the molten metal can be lowered. If the post combustion ratio is heightened, a gaseous desulfurization takes place vigorously, and S in the molten metal is decreased, too. Also from these view points, the present invention determines the post combustion ratio to be more than 0.3. Fig.7 shows the relationship, in the smelting reduction, between the post combustion ratio, the unit consumption of the coke, and P and S contents in the molten metal, where if the post combustion ratio is maintained to be more than 0.3, the unit consumption of the coke is controlled, and P and S are decreased appropriately. The above mentioned matters refer to the detailed contents of the invention, and when the invention is actually practised, following processes are dealt with of charging - slagging rising temperature - smelting reduction of Cr ores. The charging process herein means to charge Fe sources such as the molten metal and form a metal bath in the furnace. In the slagging and rising temperature process, the oxygen is supplied into the bath, and the carbonaceous materials and the flux are charged to the molten metal so as to form the slag to be a reduction region of Cr ores, and the bath temperature is raised enough for the reduction. In the smelting reduction, the Cr ores, the carbonaceous materials and the flux are supplied in succession. At the end of this process, a final reduction is carried out without supplying the Cr ore, and the reducing treatment is accomplished when the Cr concentration reaches an objective value. Example 1 The molten metal of 3.7 ton was charged into the smelting reduction furnace of the converter type (5 tons), and the smelting reduction was performed by supplying Cr ores, coke and flux, and 18% Cr molten metal of 5.5 ton was produced. Fig.9 shows changings of Cr and C concentrations in the metal, bath temperature and the post combustion ratio OD, the O₂ supplying amount, and the raw material charging amount. Fig.10 shows the smelting reduction time (from starting to ending) in the present example in comparison with the treating time of the conventional practices shown in Figs.11 (a) and (b) known from "Tetsu to Hagane" (iron and steel) Volume 71, 12 issue S928 (1985). The conventional practice (1) blew fine powder coal and O₂ from the top lance, and the agitating gas from the bottom tuyeres, and the conventional practice (2) blew O₂ onto the slag as blowing N₂ from the bottom tuyere as well as N₂ and O₂ from the side blowing tuyeres under following conditions. Fig.10 shows that the Cr concentration of the conventional method (2) was only about 6 to 7%, while Fig.12 shows that the Cr concentration of the conventional method (1) reached the objective 18%, but the treatment took much time as 120 minutes. On the other hand, according to the invention, the Cr concentration reached 18% for 60 minutes being one half of that of the conventional method (1), which tells the excellent treating function of the present invention. Fig.12 shows the Cr increasing speed with respect to the pure Cr supplying speed (supplying speed of Cr ore calculated as the pure Cr amount) of the invention, revealing the high Cr increasing speed in comparison with the above methods (1) and (2). With respect to the raw materials of Cr ores, it is preferable to perform the smelting reduction as maintaining the charging speed of the pure Cr to be more than 4 kg/min-molten metal Ton (the charging speed of raw Cr ore calculated into the amount of the pure Cr). Thus, by controlling the charging speed of the pure Cr, the probability that each of the grains of the raw ores is revealed in the upflow gas is decreased so that the splash loss is largely lowered. The post combustion O₂ by the top blowing lance should be blown into the slag such that the post combustion range is formed in the slag as having mentioned above, but when the high charging speed of Cr raw ores is required for avoiding the splash loss of Cr raw ores, the high transfer efficiency is necessarily provided as securing the high post combustion for maintaining the high charging speed while not decreasing the temperature of the molten metal. Example 2 The same smelting reduction furnace as in Example 1 was used for carrying out the smelting reduction as changing the charging speed of Cr powder raw ores. In this practice, the molten metal was charged into the furnace, and thereafter Cr ores, coke and flux were charged, and the smelting reduction was performed under the conditions, and 18%Cr molten metal of 5 ton was obtained. Top blowing decarburizing O₂: 1500 Nm³/Hr Top blowing post combustion O₂: 1100 Nm³/Hr The amount of the bottom blowing gas (N₂): 700 Nm³/Hr The amount of the side blowing gas (N₂): 300 Nm³/Hr The dispersions of the grains of the charged Cr raw ores were as follows. +1mm +0.5mm +0.25mm +0.149mm -0.149mm 1.7 % 3.8 % 20.1 % 42.9 % 31.5 % Total Cr contained in Cr raw ores was 30%. Fig.13 shows the relationship between the charging speed of Cr raw ores (charging speed of pure Cr) and the loss by splashing the powder ores, and it is seen that the loss was decreased considerably by determining the charging speed of Cr raw ores (pure Cr) ≧ 4 kg/min-molten metal Ton. The smelting reduction requires that the progressing conditions of the smelting reduction is exactly grasped and the treatment is accomplished in view of stabilization of the operation and securing of the yield. Especially, if the blowing is continued after finishing (accomplishing) of the reduction of Cr ores, the temperature of the molten metal goes up 10 to 50°C/min and injures the refractories. Therefore, it is indispensable to exactly to know the finishing of the reduction and to end the blowing instantly. In the prior art, the time to be taken to the reduction treatment was forecasted from supplying of the Cr raw materials so that the treatment was finished when a determined time passed after the treatment starts, but actually due to non-uniformity of the reducing speed, the treatment was finished too early or too late, or the temperature of the molten metal was increased, and problems were involved about the stable and economical operations. Paying attentions to that the amount of O₂ source bearing on the exhaust gas decreases, following the decreasing of the reduction, the inventors settled the above mentioned problems by judging the accomplishing time of the reduction based on the difference between O₂ source in the exhaust ags and the blown O₂. It has been believed conventionally that the Cr ores were reduced by the carbonaceous materials existing in the slag after Cr ores have been molten. However, the inventors have ascertained that almost all of the reductions were actually caused in that C in the molten metal acted as the reducing substances. The reduction of the molten metal of Cr ores goes advance by the reaction expressed by the following formula Cr₂O₃ (in Cr ore) + 3C (in the molten metal) = 2Cr (in the molten metal) + 3CO (the exhaust gas). The more vigorous is the reduction, the more is the generating amount of CO. Therefore, O₂ source contained in CO and CO₂ in the exhaust gas is measured, and an extent of progressing of the reduction can be grasped by the difference in the amount of the blown O₂ and the amount of O₂ source. The amount of O₂ contained in the waste gas can be obtained by the following formula (1) Q E x ((%CO x 1/2 + (%CO₂)) / 100 (1) herein, Q E : the flowing amount of the exhaust gas (Nm³/min) (%CO) : the concentration of CO in the exhaust gas (%) (%CO₂): the concentration of CO₂ in the exhaust gas (%). As shown in the following formula (2), the difference between the thus obtained value and O₂ to be blown into the furnace is obtained, and the rate of this value to the amount contained in the Cr raw material is obtained, the rate of reducing Cr raw material, i.e., the reduction ratio R of Cr raw material can be obtained. herein, Wore: the amount of charging Cr raw material (Ton) Oore: the amount of O₂ contained in Cr raw material (Nm³/Ton) Fo₂ : the flowing amount of the blown O₂ (Nm³/min) In the present method, the flowing amount of the exhaust gas and the concentrations of CO and CO₂ are measured, and the reduct ion is ended when the value of the reducing rate R of Cr raw material reaches the predetermined objective value in accordance with the above formula (2). Actually, it could be seen that the reduction of Cr ore is almost ended in the range where R value is below 0.01 (min⁻¹), and therefore it is desirous to end the blowing when R is 0.005 (min⁻¹). Further, the reducing speed of Cr ore may be understood by observing the R value, and for example, if it is judged that the reacting speed is low and the reduction is delayed, it is possible to employ such actions as increasing the agitation gas. In addition, the temperature of the molten metal may be assumed by the R value, and it is possible to employ the action for securing the temperature of the molten metal until the blowing is accomplished. Example 3 The molten metal of 2.7 ton was charged into the smelting reduction furnace (5 tons), Cr ore, coke and fluxes were charged for porforming the smelting reduction, and 18% Cr molten metal of 5.5 ton was obtained. In this smelting reduction, the gas blowing conditions at the finishing reduction period were as follows. The amount of FO₂ sent from the lance: 1500 Nm³/hr The amount of gas (N₂) blow from the bottom: 750 Nm³/hr The amount of gas (N₂) blown from the side: 360 Nm³/hr. In the above mentioned reduction treatment, the final reduction treatment was ended by the following conditions. (1) The invention method: the treatment was ended when the R value was below 0.005 (min⁻¹) (2) The comparative method: the treating time of the finish reduction was 15 min. constant Fig.14 shows one example of the final reduction of the comparative method where the final reduction ends at 13 min. but since the blowing for 15 minutes was carried out actually, the temperature of the molten metal rapidly goes up, and the once reduced Cr was re-oxidized. Fig.15 shows the relation between R value and Cr content in the slag corresponding to the former, and when R value is below 0.01, Cr content in the slag is not more than 1%. Figs.16 and 17 show the concentration of Cr in the slag at ending of the reduction and the temperature of the molten metal at stopping of the blowing in the invention method and the comparative method. According to the invention, Cr in the slag is effectively reduced, and the temperature of the molten metal is almost at the objective level. Therefore, it is seen in the present invention that the finish of the reduction is exactly grasped and the blowing is stopped instantly. On the other hand, in the comparative methods, the Cr concentration in the slag and the temperature of the moltem metal at stopping the blowing are non-uniform, and the the ending of the blowing is too early or too late, and the temperature of the molten metal is decreased or increased, and the yield is lowered. The smelting reduction furnace of the invention is, as seen in Fig.3, one bottom blowing tuyere and two side blowing tuyeres, and at least one bottom blowing tuyere and two side blowing tuyere are disposed such that the gas blowing lines of the both cross each other. The bottom blowing tuyere 1 and the side blowing tuyere 2 may be plural as shown in Fig.3(b), and in this regard, one pair is made of one bottom blowing tuyere and the side blowing tuyeres, and it is preferable that the respective tuyeres are disposed such that the gas blowing line of the tuyeres of each pair agrees with. It is important that the gas blown from the side tuyeres splashes the upheaval of the molten metal, and therefore, the positional relation of the side blowing tuyeres and the height of the molten metal is determined. Fig.18 illustrates one example of the invention, where the bottom blowing tuyeres 1a, 1b are provided at the center of the furnace bottom and at the outside of the center, and the side blowing tuyere 2 is disposed such that the gas blowing line X crosses with the gas blowing line of the bottom blowing tuyere 1a (period). The bottom blowing tuyere may be one as seen in Fig.3(a), but if all the gas is supplied from one bottom blowing tuyere, the pas pressure is high extraordinarily, and the gas blows through the molten metal, and an appropariate upheaving part A of the molten metal could not be often formed. Therefore, in the present example, there is provided another tuyere as a bottom blowing tuyere than the one 1a corresponding to the side tuyere. Such a furnace in the present example and the furnace in the comparative example where the side tuyere 2′ and the bottom tuyeres 1′ were used, and the the results of the smelting reduction are shown. The molten metal of 3.7 ton was charged into the furnace, and the amount of the gas blown from the bottom and the amount of the gas blown from the side tuyere were variously changed under the following conditions. Decarburizing O₂ from the furnace top: 1400 Nm³/hr Post combustion O₂ from the furnace top: 800 Nm³/hr Cr raw material: Pellets Charging speed of Cr ore (calculated in the amount of the pure Cr): 3.5 to 4.0 kg/min.molten metal ton Diameter of tuyere nozzle: 13 mm Fig.19 (the furnace of this invention) and Fig.21 (the furnace of Fig.20) show the relations between the amount of the gas blown from the furnace bottom and the amount of the gas blown from the side tuyere and (Cr) increasing rate into the molten metal, and in the smelting furnace of the invention, the high (Cr) increasing rate was obtained in response to the amount of the gas blown from the furnace bottom and the amount of the gas blown from the side tuyere. On the other hand, in the furnace of Fig.20, the splash of the molten metal is slightly vigorous in accompany with the increasing of the amount of the gas blown from the bottom, and the (Cr) increasing rate is more or less large, but in comparison with the present invention, these extents are very low, and effects of the laterally blown gas is very little. INDUSTRIAL APPLICATION The present invention may produce high Cr molten metal directly from Cr ores or Cr pellets, and therefore if it is combined with the decarburization, high Cr steel such as stainless steel can be produced directly from Cr ores.

Claims: A method of smelting reduction of Cr containing raw materials, in a smelting reduction furnace provided with bottom blowing tuyeres, side blowing tuyeres and a top blowing lance, comprising steps of reducing Cr ores by C in molten metal to produce high Cr molten metal, decarburizing said high Cr molten metal in the same furnace by below-mentioned gas blowings (a) to (c) during a period of the smelting reduction (a) blowing CO and/or inert gas (N₂, Ar) from the bottom blowing tuyeres, (b) blowing CO and/or inert gas from the side blowing tuyere such that at least a part of the gas contacts an upheaval of the molten metal made by the bottom blowing gas, and (c) blowing a decarburizing O₂ into the molten metal from the top blowing lance and a post-combustion O₂ into a slag concurrently, and reducing Cr containing raw material by maintaining a ratio of the actually measured post-combustion to be more than 0.3, wherein blowing from the side blowing tuyeres is sufficient to splash or diffuse the molten metal into the slag, and the molten metal bath is formed in the converter before feeding the Cr containing raw materials. The method as claimed in claim 1, comprising blowing O₂ for decarburization and O₂ for the post combustion through a lance, the tip of which is positioned just above a slag surface or thereunder. The method as claimed in claim 1 or 2, comprising maintaining a supplying speed in terms of the metallic Cr (the supplying speed of Cr raw ores calculated in terms of the amount of metallic Cr) where Cr ores are Cr raw material at more than 4 kg/min.molten metal ton. The method as claimed in claim 1, 2, or 3, comprising blowing the gas from the tuyeres selected from Ar, N₂ and CO, or more than two of them. The method as claimed in claim 1, 2, 3 or 4, comprising supplying the post combustion O₂ obliquely outside in respect to the decarburizing O₂ through the top blowing lance having a nozzle hole for the decarburizing O₂ and a nozzle hole for the post combustion O₂. The method as claimed in claim 1, 2, 3, 4 or 5 comprising, during the smelting reduction, measuring the amount of the exhaust gas and the compositions of CO, CO₂ and others in the exhaust gas, obtaining a reduction R of Cr raw material from the above measured values following an under formula, judging time of accomplishing the smelting reduction by the reduction R of the Cr raw material, and ending the smelting reduction treatment herein, Wore : the amount of charging Cr materials (Ton) Oore : the amount of O₂ contained in Cr materials (Nm³/Ton) QE : the amount of the exhaust gas (Nm³/min) (%CO) : CO concentration in the exhaust gas (%) (%CO₂) : CO₂ concentration in the exhaust gas (%) Fo₂ : the flow amount of the blown O₂ (Nm³/min). A smelting reduction furnace for performing the method according to claim 1 to 6, comprising a container having a lower part for holding molten metal, and an upper part for holding slag including chromium ore and floating on top of the said molten metal, at least one bottom blowing tuyere (1) disposed at the bottom of said container and arranged to blow an agitating inert gas into said molten metal so as to form an upheaved part (A) of said molten metal which upheaves above the surface of said molten metal and into the upper part of said container, side blowing means for blowing only an inert gas into said upheaved part of said molten metal, said side blowing means comprising at least one side blowing tuyere (2) disposed at the side of said upper part of said container and arranged to blow said inert gas from said side in a substantially horizontal direction into said upheaved part (A) of the molten metal so as to diperse said upheaved part (A) into the lower part of said slag disposed in the upper part of said container, said at least one bottom blowing tuyere (1) and said at least one side blowing tuyere (2) being so disposed that the respective inert gases blown therefrom travel in lines which intersect each other, and at least one top blowing lance (3) disposed in the upper part of said container and comprising a first nozzle hole for blowing decarburizing O₂ in a substantially vertical downward direction and a second nozzle hole for blowing a post-combustion O₂ said second nozzle hole being disposed obliquely to the first nozzle hole so that the post-combustion O₂ is blown obliquely outside the downward direction stream of decarburizing O₂ from said first nozzle hole. Furnace according to claim 7, provided with a plurality of bottom blowing tuyeres (1, 1a, 1b; 1') and a plurality of side blowing tuyeres (2; 2'), so that the line of the travel of gas from at least each of the side blowing tuyeres (2; 2') intersect the line of travel of gas on the bottom blowing tuyeres (1, 1a, 1b; 1').

Inventors: INOUE SHIGERU, IWASAKI KATSUHIRO, KAWAKAMI MASAHIRO, TAKAHASHI KENJI, TANABE HARUYOSHI, INOUE, SHIGERU, IWASAKI, KATSUHIRO, KAWAKAMI, MASAHIRO, TAKAHASHI, KENJI, TANABE, HARUYOSHI
Applicants: NIPPON KOKAN KK, NKK CORPORATION
Application year: 1988
Main classification: C22C33
IPC codes: C22B34, C22B5, C21C5, C21B13, C22C33