WO1996021046A1 - Method and equipment for treatment in molten cast iron baths with reaction materials having a low or high production of gas - Google Patents

Method and equipment for treatment in molten cast iron baths with reaction materials having a low or high production of gas Download PDF

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Publication number
WO1996021046A1
WO1996021046A1 PCT/IT1995/000223 IT9500223W WO9621046A1 WO 1996021046 A1 WO1996021046 A1 WO 1996021046A1 IT 9500223 W IT9500223 W IT 9500223W WO 9621046 A1 WO9621046 A1 WO 9621046A1
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WO
WIPO (PCT)
Prior art keywords
chamber
molten bath
bath
reagent
molten
Prior art date
Application number
PCT/IT1995/000223
Other languages
French (fr)
Inventor
Ettore Bennati
Original Assignee
Ettore Bennati
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ettore Bennati filed Critical Ettore Bennati
Priority to EP95940416A priority Critical patent/EP0795037B1/en
Priority to BR9510130A priority patent/BR9510130A/en
Priority to AU41877/96A priority patent/AU4187796A/en
Priority to DE69516170T priority patent/DE69516170T2/en
Priority to JP8520833A priority patent/JPH10511741A/en
Priority to AT95940416T priority patent/ATE191516T1/en
Priority to PL95321183A priority patent/PL321183A1/en
Publication of WO1996021046A1 publication Critical patent/WO1996021046A1/en
Priority to MXPA/A/1997/005056A priority patent/MXPA97005056A/en

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Classifications

    • C—CHEMISTRY; METALLURGY
    • C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22C—ALLOYS
    • C22C33/00—Making ferrous alloys
    • C22C33/08—Making cast-iron alloys
    • C22C33/10—Making cast-iron alloys including procedures for adding magnesium
    • 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
    • C21C1/00—Refining of pig-iron; Cast iron
    • C21C1/02—Dephosphorising or desulfurising
    • 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
    • C21C1/00—Refining of pig-iron; Cast iron
    • C21C1/10—Making spheroidal graphite cast-iron
    • 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
    • C21C7/00—Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
    • C21C7/04—Removing impurities by adding a treating agent
    • C21C7/06—Deoxidising, e.g. killing

Definitions

  • This invention concerns metallurgical treatments in molten baths obtained by means of the delivery of reaction materials that can be vaporized with a high or low generation of gas and other inoculating or refining materials.
  • metallurgical treatments in molten baths for instanc ductile iron - which use as the reaction material pure magnesium, or its alloys, which is vaporized in the molten bath to obtain spheroidal graphite and modifications thereof, or for desulphurization , deoxidation or similar treatments.
  • vaporization is obtained by means of direct contact between the reaction material and the molten metal.
  • the required quantity of reaction material is placed directly in the molten metal and heated and vaporized by it.
  • the supply of reaction material and the metallurgical treatment are generally discontinuous, and also involve significant loss of vapour and and deformities of the bath treatment.
  • the invention is applicable to treatments in discontinuous molten baths in containers that can be emptied, for example, into ladles, with continuous delivery during the process of reagent and, if necessary, inoculant based on the metallurgical quantities and characteristics found, and thus known, of the bath to treat.
  • This invention is also applicable to continuous molten baths, which transit in a basin or channel, by means of a continuous supply of reagent and, if necessary, of inoculant depending on the variable conditions of the metal arriving.
  • Reagents and inoculating materials are fed through a special chamber, called a reactor, the pressure of which is kept the same as the metallostatic pressure of the bath in which it is immersed and having a vaporization chamber and an expansion chamber.
  • the reagents are introduced continuously into the vaporization chamber and pass from a solid state to a vapour by means of the high temperature of the bath or, in the case of reagents with a higher boiling point, with a supplementary supply of heat from the outside.
  • the reagents vaporize without direct contact with the molten metal but with heat transmission by conduction and radiation, before passing through the expansion chamber into a deep area of the bath and circulating therein.
  • the inoculants are introduced through the expansion chamber, the bottom of which is formed by the bath itself, and melted by direct contact with the molten metal, supersaturating it locally and circulating in the bath due to the combined action of the vapours drawing the reagent materials leaving the chamber and the metallostatic thrust exercised by the bath which has a greater density than the superinoculated metal.
  • solubilizing they perform the chemical and physical actions necessary to obtain a bath with a high homogeneity, without impurities and ready to be poured into the moulds, thereby reducing the consumption of reagents and inoculants, energy loss and pollution.
  • the aims of this invention are:
  • Fig.1 shows, in vertical section, an example of equipment suitable for discontinuous metallurgical treatment in a molten bath in a ladle
  • Fig.2 shows, in vertical section, an example of equipment suitable for continuous metallurgical treatment in a molten bath passing into a basin or channel;
  • Fig.3 shows a horizontal section according to arrows Ill-Ill in Fig.2;
  • Fig.4 shows a vertical section according to arrows IV-IV in Fig.2;
  • Fig.5 shows, in horizontal section, an example of multi-reactor equipment for continuous metallurgical treatment in a molten bath passing into a basin or channel;
  • Fig.6 shows a longitudinal section according to arrows VI-VI in Fig.5;
  • Fig.7 shows a cross section according to arrows VII-VII in Fig.5;
  • Fig.8 shows another cross section according to arrows VIII-VIII in Fig.5;
  • Fig.9 shows a cross section of a further configuration of the reactor for metallurgical treatment according to the invention.
  • the method of treatment according to the invention includes continuous delivery of a reagent 10 and, if necessary, inoculant 11 into a continuous or discontinuous molten bath, namely a known or indefinite quantity.
  • the bath if of a known and definite quantity, may be contained in a ladle 13 and changed after each treatment; if of an indefinite quantity, it may flow through a basin or along a channel 14.
  • Such delivery of the reagent 10 or inoculant 11 is obtained by means of at least one special unit 15 immersed in the molten bath to be treated 12, hereinafter referred to as a reactor and having a vaporization chamber 16 and an expansion chamber 17, interconnecting by means of a passage 18 situated at a set level above the vaporization chamber 16 and/or the free surface.
  • Each reactor may be in a single piece or comprised of various parts, even not homogeneous, but made of a gas -tight material with appropriate physical and mechanical properties to withstand operating stress and maintain the internal pressure which is generated inside during the reactions and which prevents the molten metal from returning into the expansion chamber. It should be noted that the reactor can be installed in a fixed or movable position.
  • the vaporization chamber 16 and the expansion chamber 17 may be coaxial or placed side by side.
  • the geometry of the reactor 15 may vary widely from execution to execution, as may the configuration of the reactor in or in relation to the bath to treat.
  • the reactor 15 may be in the shape of an immersed bell in the centre or to one side of the molten bath in a ladle 13, as shown in Fig.1.
  • the reactor 15 may be in the shape of a block placed along the wall of a tank or channel 14 as shown in Figs.5-8.
  • the vaporization chamber 16 is open at the top and communicates only with the expansion chamber 17 through the passage 18, and not with the bath.
  • the molten bath is only in contact with the side walls and/or bottom of the vaporization chamber 16.
  • the expansion chamber 1 communicates at the top with the vaporization chamber 16 through the passage 18, whereas at the bottom and/or side it is completely or partially open directly towards the molten bath through possible passages 17'.
  • a first duct 19 for delivering the reagent material contained in and coming from a first supply tank/metering unit 20, 20' (in the drawings this tank/metering unit is represented for granular materials, but it may be envisaged for materials in wire or powder form.)
  • a second duct 21 for delivering inoculating material 11 contained in and coming from a second tank/metering unit 22, 22'.
  • the tanks/metering units 20, 22 are situated superiorly over or anyway out of the bath to treat 12 and the ducts 19, 21 from said tanks/metering units may be united in a single assembly or separate from each other.
  • the reagent 10 and the inoculant 11 are delivered separately, although concomltantly, into the vaporization chamber 16 and the expansion chamber 17, respectively.
  • the latter and the equipment for supplying the reagent and inoculant are suitably pressure sealed and fitted with efficient control and safety systems.
  • the molten bath 12 whether it be in a ladle 13 or passing into a basin or channel 14, when coming into contact with the reactor 15 transfers the fusion/vaporization heat to the reagent 10 contained in the chamber 16.
  • the vapour produced passes through the passage 18 placed in a higher position than the level of the bath in the expansion chamber 17 and from this it is blown into the bath 12 through the passages 17' in the bottom of the chamber.
  • the vapour rises towards the surface solubilizing and distributing itself for the desired reactions.
  • the metal can not rise back up into the expansion chamber 16 in that the pressure in the same is in constant equilibrium with the metallostatic pressure.
  • the delivery of reagent material 10 into the vaporization chamber 16 is actuated by means of the metering system 20, 20' controlled by a regulator and contained in a hopper that can be pressurized with inert gas equipped with a stop valve 20" (Fig.7) which, as the reagent passes from the hopper 20 at atmospheric pressure into the relevant duct 19, prevents the vapour from escaping.
  • the metering unit 20' is hermetically sealed and ensures maintenance of the pressure inside the hopper 20 during metering and acts as a base for the hopper holding a definite quantity of reagent.
  • the opening of the metering unit 20' is controlled by a minimum level gauge 23 to ensure the constant presence of reagent.
  • the level of reagent varies and parallelly the degree of vaporization and the quantity of reagent passing into the bath in the unit of time.
  • the tank/metering unit 22, 22' which is designed for feeding inoculating materials 12 into the expansion chamber 17 through the distribution duct, operates in the same way.
  • the metal treated and possibly 5 inoculated is tapped by a spout 24 (Fig.6) whereas the slag 25 produced collects on the wall of the basin from which it can easily be removed manually or automatically.
  • the basin is emptied through a discharge outlet 26 which allows gradual tapping of the metal and the simultaneous reduction of pressure to atmospheric 0 level in the chambers 16, 17 of the reactor 15.
  • the system designed for continuous operation is equipped with the necessary control and safety systems represented by a probe 27 (Figs. 2 and 9) for controlling the level of the reagent 10 which regulates closing of the valve; a system 28 (Fig.6) for continuous measurement of 5 the pressure inside the reactor which shuts off the valve when set values are exceeded; a safety valve 29 with instant opening; a basin cover 30; a siphoning system 31 (Fig.6) - shown in the rest position; a protection bulkhead 32 which circumscribes the system ; and a gas suction and removal system (not rapresented).
  • each reactor 15 may be equipped 0 with a unit 33 operated by electricity.gas.etc.for heating the reagent 10 in the vaporization chamber when the reagent has a vaporization point exceeding the temperature of the melt.

Abstract

This invention covers the method and equipment for the continuous or discontinuous addition of reaction/inoculation materials necessary for desulphurization or the production of ductile iron obtainable during the passage of the base iron through a basin containing the chamber for melting, vaporizing and distributing the reaction-inoculation materials into the melt (e.g. magnesium vapour-Ferrum Silicon). The treatment can be conducted continuously for unlimited or freely definable quantities of iron.

Description

METHOD AND EQUIPMENT FOR TREATMENT IN MOLTEN BATHS WITH REACTION MATERIALS HAVING A LOW OR HIGH
PRODUCTION OF GAS
DESCRIPTION
This invention concerns metallurgical treatments in molten baths obtained by means of the delivery of reaction materials that can be vaporized with a high or low generation of gas and other inoculating or refining materials. There already exist known metallurgical treatments in molten baths - for instanc ductile iron - which use as the reaction material pure magnesium, or its alloys, which is vaporized in the molten bath to obtain spheroidal graphite and modifications thereof, or for desulphurization , deoxidation or similar treatments. Using traditional techniques, vaporization is obtained by means of direct contact between the reaction material and the molten metal. The required quantity of reaction material is placed directly in the molten metal and heated and vaporized by it. The supply of reaction material and the metallurgical treatment are generally discontinuous, and also involve significant loss of vapour and and deformities of the bath treatment.
More recently there has been proposed a method for metallurgical treatment in a molten bath of a vaporizable reaction material in which said reaction material is placed in at least one chamber immersed in the molten metal and vaporized without direct contact with the metal. In effect, the reaction material is heated and vaporized through the walls of the chamber and the vapour produced is conveyed out of the chamber towards the molten metal. However, this method too is discontinuous although it provides some advantages in the use and distribution of vapour in the molten metal for a more homogenous treatment. In other words, metallurgical treatments conducted with known methods are discontinuous considering the discontinuous supply of reaction material. On the other hand, for some treatments, apart from the vaporizable material it is necessary to have inoculating or refining material for the bath. Metering and delivery to the bath of these materials are generally effected by simple addition during transfer of the metal and cause oxidation and the formation of residue leading to defects in the castings produced. The concomitant, but separate, delivery of reaction and inoculating materials effected from inside the bath in a protected atmosphere is not known in the current state of the art.This invention aims to prevent the limitations of continuous or discontinuous metallurgical treatments according to known methods by means of a method and equipment alfowing the continuous treatment of molten material, even with a concomitant supply of reaction materials and inoculating materials directly into the bath his invention applies in particular to the metallurgical treatments of desulphurization, nodularization, etc. of iron, but without excluding a more general application to the treatment of other hot liquids whether metallic or otherwise.The invention was conceived, at least as far as treatment in melt baths-particularly ductile iron - is concerned, starting from the known technique of placing the reaction material in a chamber immersed in the molten bath, but with the innovation of feeding continuously from the external environment at atmospheric pressure, by means of a pressure -tight metering system controlled by a regulator depending on the data relating to the metal to treat, materials promoting the formation of spheroids even with a high gas generation, called reagents, and separately but concomitantly, other materials for refining or solidifying the graphite in the bath according to the stable system, hereinafter referred to as inoculants. The invention is applicable to treatments in discontinuous molten baths in containers that can be emptied, for example, into ladles, with continuous delivery during the process of reagent and, if necessary, inoculant based on the metallurgical quantities and characteristics found, and thus known, of the bath to treat.This invention is also applicable to continuous molten baths, which transit in a basin or channel, by means of a continuous supply of reagent and, if necessary, of inoculant depending on the variable conditions of the metal arriving. Reagents and inoculating materials are fed through a special chamber, called a reactor, the pressure of which is kept the same as the metallostatic pressure of the bath in which it is immersed and having a vaporization chamber and an expansion chamber. The reagents are introduced continuously into the vaporization chamber and pass from a solid state to a vapour by means of the high temperature of the bath or, in the case of reagents with a higher boiling point, with a supplementary supply of heat from the outside. The reagents vaporize without direct contact with the molten metal but with heat transmission by conduction and radiation, before passing through the expansion chamber into a deep area of the bath and circulating therein. The inoculants are introduced through the expansion chamber, the bottom of which is formed by the bath itself, and melted by direct contact with the molten metal, supersaturating it locally and circulating in the bath due to the combined action of the vapours drawing the reagent materials leaving the chamber and the metallostatic thrust exercised by the bath which has a greater density than the superinoculated metal. Thus, by solubilizing they perform the chemical and physical actions necessary to obtain a bath with a high homogeneity, without impurities and ready to be poured into the moulds, thereby reducing the consumption of reagents and inoculants, energy loss and pollution. The aims of this invention are:
- to perform a discontinuous treatment, namely with definite quantites of metal and with known homogeneous characteristics, thus - by means of the continuous feeding system - reducing the quantity of reaction material contained in the bath and hence the development of any violent reactions should the solid or liquid reagents accidentally come into contact with the bath; - to vaporize and solubilize elements with a boiling point higher than the temperature of the bath:
- to effect the addition and distribution of inoculants to favour - in cast iron - solidification of the graphite according to the stable system, even simultaneously with the vaporizable element promoting the formation of spheroidal graphite and/or variants thereof;
- to effect a continuous treatment, namely for indefinite quantities of metal with continually varying characteristics of temperature, chemical composition and capacity, obtaining after the treatment a bath with the required features; - to control continuously the process of vaporization and inoculation, regulating it to ensure the complete solubilization of the reagents/ inoculants added, thus avoiding loss due to oxidation or the formation of impurities;
- to eliminate difficult metallurgical operations thank to complete automation and control of the production cycle which, in the case of spheroidal cast iron and its variants (e.g. vermiculite), gives an inoculated material ready for casting.
Another important point is the possibility of using reagent raw materials with a high boiling point, such as Ca, Sr, Ba or La, which promote favourable metallurgical structures, and the possibility of adapting the process in real time to the actual conditions of the metal to be processed with extremely good prospects on account of the current state of the art. Further details and characteristics of the invention are made more evident in the course of the description provided with reference to the attached drawings, in which:
Fig.1 shows, in vertical section, an example of equipment suitable for discontinuous metallurgical treatment in a molten bath in a ladle; Fig.2 shows, in vertical section, an example of equipment suitable for continuous metallurgical treatment in a molten bath passing into a basin or channel;
Fig.3 shows a horizontal section according to arrows Ill-Ill in Fig.2; Fig.4 shows a vertical section according to arrows IV-IV in Fig.2; Fig.5 shows, in horizontal section, an example of multi-reactor equipment for continuous metallurgical treatment in a molten bath passing into a basin or channel;
Fig.6 shows a longitudinal section according to arrows VI-VI in Fig.5; Fig.7 shows a cross section according to arrows VII-VII in Fig.5; Fig.8 shows another cross section according to arrows VIII-VIII in Fig.5; and Fig.9 shows a cross section of a further configuration of the reactor for metallurgical treatment according to the invention. The method of treatment according to the invention includes continuous delivery of a reagent 10 and, if necessary, inoculant 11 into a continuous or discontinuous molten bath, namely a known or indefinite quantity. The bath, if of a known and definite quantity, may be contained in a ladle 13 and changed after each treatment; if of an indefinite quantity, it may flow through a basin or along a channel 14. Such delivery of the reagent 10 or inoculant 11 is obtained by means of at least one special unit 15 immersed in the molten bath to be treated 12, hereinafter referred to as a reactor and having a vaporization chamber 16 and an expansion chamber 17, interconnecting by means of a passage 18 situated at a set level above the vaporization chamber 16 and/or the free surface. Each reactor may be in a single piece or comprised of various parts, even not homogeneous, but made of a gas -tight material with appropriate physical and mechanical properties to withstand operating stress and maintain the internal pressure which is generated inside during the reactions and which prevents the molten metal from returning into the expansion chamber. It should be noted that the reactor can be installed in a fixed or movable position.
The vaporization chamber 16 and the expansion chamber 17 may be coaxial or placed side by side. Correspondingly, the geometry of the reactor 15 may vary widely from execution to execution, as may the configuration of the reactor in or in relation to the bath to treat. Correspondingly, the reactor 15 may be in the shape of an immersed bell in the centre or to one side of the molten bath in a ladle 13, as shown in Fig.1. Alternatively, the reactor 15 may be in the shape of a block placed along the wall of a tank or channel 14 as shown in Figs.5-8. In all cases, the vaporization chamber 16 is open at the top and communicates only with the expansion chamber 17 through the passage 18, and not with the bath.The molten bath is only in contact with the side walls and/or bottom of the vaporization chamber 16. On the other hand, the expansion chamber 1 communicates at the top with the vaporization chamber 16 through the passage 18, whereas at the bottom and/or side it is completely or partially open directly towards the molten bath through possible passages 17'. To the vaporization chamber 6 there is connected a first duct 19 for delivering the reagent material contained in and coming from a first supply tank/metering unit 20, 20' (in the drawings this tank/metering unit is represented for granular materials, but it may be envisaged for materials in wire or powder form.) To the expansion chamber there is connected a second duct 21 for delivering inoculating material 11 contained in and coming from a second tank/metering unit 22, 22'. The tanks/metering units 20, 22 are situated superiorly over or anyway out of the bath to treat 12 and the ducts 19, 21 from said tanks/metering units may be united in a single assembly or separate from each other. In any case, the reagent 10 and the inoculant 11 are delivered separately, although concomltantly, into the vaporization chamber 16 and the expansion chamber 17, respectively.
For treatment in a molten bath 12 in a ladle 13, the latter and the equipment for supplying the reagent and inoculant are suitably pressure sealed and fitted with efficient control and safety systems. In practice, the molten bath 12, whether it be in a ladle 13 or passing into a basin or channel 14, when coming into contact with the reactor 15 transfers the fusion/vaporization heat to the reagent 10 contained in the chamber 16. The vapour produced passes through the passage 18 placed in a higher position than the level of the bath in the expansion chamber 17 and from this it is blown into the bath 12 through the passages 17' in the bottom of the chamber. The vapour rises towards the surface solubilizing and distributing itself for the desired reactions. The metal can not rise back up into the expansion chamber 16 in that the pressure in the same is in constant equilibrium with the metallostatic pressure.
The delivery of reagent material 10 into the vaporization chamber 16 is actuated by means of the metering system 20, 20' controlled by a regulator and contained in a hopper that can be pressurized with inert gas equipped with a stop valve 20" (Fig.7) which, as the reagent passes from the hopper 20 at atmospheric pressure into the relevant duct 19, prevents the vapour from escaping. The metering unit 20' is hermetically sealed and ensures maintenance of the pressure inside the hopper 20 during metering and acts as a base for the hopper holding a definite quantity of reagent.The opening of the metering unit 20' is controlled by a minimum level gauge 23 to ensure the constant presence of reagent. Depending on the quantity of reagent introduced into the chamber 16 via the distribution duct 19, the level of reagent varies and parallelly the degree of vaporization and the quantity of reagent passing into the bath in the unit of time.
The tank/metering unit 22, 22', which is designed for feeding inoculating materials 12 into the expansion chamber 17 through the distribution duct, operates in the same way.The metal treated and possibly 5 inoculated is tapped by a spout 24 (Fig.6) whereas the slag 25 produced collects on the wall of the basin from which it can easily be removed manually or automatically. Upon completion of the treatment, the basin is emptied through a discharge outlet 26 which allows gradual tapping of the metal and the simultaneous reduction of pressure to atmospheric 0 level in the chambers 16, 17 of the reactor 15.
The system designed for continuous operation is equipped with the necessary control and safety systems represented by a probe 27 (Figs. 2 and 9) for controlling the level of the reagent 10 which regulates closing of the valve; a system 28 (Fig.6) for continuous measurement of 5 the pressure inside the reactor which shuts off the valve when set values are exceeded; a safety valve 29 with instant opening; a basin cover 30;a siphoning system 31 (Fig.6) - shown in the rest position; a protection bulkhead 32 which circumscribes the system ; and a gas suction and removal system (not rapresented). Lastly each reactor 15 may be equipped 0 with a unit 33 operated by electricity.gas.etc.for heating the reagent 10 in the vaporization chamber when the reagent has a vaporization point exceeding the temperature of the melt.

Claims

1. A method for the metallurgical treatment of desulphurization , deoxidation, refining, nodularization and the like in molten baths by means of the delivery into the bath of at least one vaporizable reagent
05 material with low or high gas generation and possibly of at least one inoculating material, the reagent material being vaporized by the heat of the molten bath by thermal exchange without direct contact with the same, the inoculating material melting in direct contact with the molten bath, characterized in that the reagent material is delivered
10 continuously from outside the molten bath kept under pressure and is metered according to the final characteristics required for the molten bath treated.
2. A method for metallurgical treatment according to claim 1 , further characterized in that the inoculating material is continuously fed
15 separately from, but concomitantly with, delivery of the reagent material.
3. A method for metallurgical treatment according to claims 1 or 2, characterized in that the reagent material is heated by vaporization with a source of heat in addition to the significant heat of the molten bath.
204. A method for metallurgical treatment according to claims 1 and 2, characterized in that the vaporized reagent material and the inoculant are distributed concomitantly in the bath, blending together and being drawn towards each other.
5. A method for metallurgical treatment according the previous claims, 25 applied to discontinuous molten baths placed in containers that can be emptied after each treatment.
6. A method for metallurgical treatment according to claims 1-4, applied to continuous molten baths transiting in a basin or pouring channel.
7. Equipment for metallurgical treatment in a molten bath with a method 30 of treatment as claimed in claims 1-6, characterized by at least one reactor (15) arranged, in a fixed or movable position, in the molten bath to be treated and having a first vaporization chamber (16) designed to receive the reagent material (10), a second expansion chamber (17) designed to receive the inoculating material (11) and the vapours of the
35 reagent coming from the first chamber, and a passage (18) intercommunicating between the first and the second chamber, and by means for metering and delivering (20, 22) continuously and separately reagent material into the first chamber (16) and inoculating material into the second chamber (17). 0 8. Equipment according to claim 7, in which the first chamber (16) has side and/or bottom walls in contact with the molten bath, whereas the second chamber (17) is open towards the molten bath, the chambers being kept under pressure so as to prevent the molten bath from returning into the second chamber.
9. Equipment according to claims 7 and 8, in which the passage (18) intercommunicating between the first and second chamber (16,17) is preferably at a higher level than the molten bath. 05
10. Equipment according to claims 7-9, in which the first and second chamber (16,17) are united in a body concentrically with respect to each other or one beside the other, said body being comprised of a single piece, or several parts assembled together.
11. Equipment according to claims 7-10, in which the first vaporization 10 chamber is associated with a heating unit for heating the reagent material.
12. Equipment according to any of claims 7-11 , in which the first and second chamber are connected to ducts (19, 21) for delivering the reagent material and inoculating material coming from metering means
15 (20, 22), said ducts being united in a single assembly or separate.
13. Equipment according to any of claims 7-12, in which the reactor (15) is immersed in the to be treated.
14. Equipment according to any of claims 7-12, in which the reactor (15) is placed along the walls of a tank or channel.
20 15. Method and equipment for the treatment of molten baths with reaction materials having a high or low generation of gas, as substantially described above, illustrated and claimed for the specified . aims.
PCT/IT1995/000223 1995-01-05 1995-12-20 Method and equipment for treatment in molten cast iron baths with reaction materials having a low or high production of gas WO1996021046A1 (en)

Priority Applications (8)

Application Number Priority Date Filing Date Title
EP95940416A EP0795037B1 (en) 1995-01-05 1995-12-20 Equipment for treatment in molten cast iron baths with reaction materials having a low or high production of gas
BR9510130A BR9510130A (en) 1995-01-05 1995-12-20 Method and equipment for treatment in molten metal bath with reaction materials having a high or low gas production
AU41877/96A AU4187796A (en) 1995-01-05 1995-12-20 Method and equipment for treatment in molten cast iron baths with reaction materials having a low or high production of gas
DE69516170T DE69516170T2 (en) 1995-01-05 1995-12-20 DEVICE FOR TREATING MELT WITH REACTIVE MATERIALS THAT GENERATE LOW OR HIGH GAS CONTENTS
JP8520833A JPH10511741A (en) 1995-01-05 1995-12-20 Method and apparatus for handling reactants with low or high gas evolution in a molten cast iron bath
AT95940416T ATE191516T1 (en) 1995-01-05 1995-12-20 DEVICE FOR TREATING MELTS WITH REACTIVE MATERIALS THAT PRODUCE LOW OR HIGH GAS CONTENT
PL95321183A PL321183A1 (en) 1995-01-05 1995-12-20 Method of and apparatus for introducing into a molten metal body materials reacting therewith and producing small or large quantities of gas
MXPA/A/1997/005056A MXPA97005056A (en) 1995-01-05 1997-07-04 Method and equipment for treating in iron / cast iron baths with reaction materials which have a low or high production

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
IT95BS000003A IT1278916B1 (en) 1995-01-05 1995-01-05 METHOD AND EQUIPMENT FOR THE TREATMENT OF METAL BATHS WITH LOW OR HIGH GAS DEVELOPMENT REACTION MATERIALS
ITBS95A000003 1995-01-05

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WO1996021046A1 true WO1996021046A1 (en) 1996-07-11

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PCT/IT1995/000223 WO1996021046A1 (en) 1995-01-05 1995-12-20 Method and equipment for treatment in molten cast iron baths with reaction materials having a low or high production of gas

Country Status (13)

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US (1) US6099614A (en)
EP (1) EP0795037B1 (en)
JP (1) JPH10511741A (en)
CN (1) CN1046553C (en)
AT (1) ATE191516T1 (en)
AU (1) AU4187796A (en)
BR (1) BR9510130A (en)
CZ (1) CZ210297A3 (en)
DE (1) DE69516170T2 (en)
IT (1) IT1278916B1 (en)
PL (1) PL321183A1 (en)
RU (1) RU2154111C2 (en)
WO (1) WO1996021046A1 (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6235079B1 (en) 1997-12-20 2001-05-22 Pohang Iron & Steel Co., Ltd. Two step twin-single fluidized bed pre-reduction apparatus for pre-reducing fine iron ore, and method therefor
WO2003068996A1 (en) * 2002-02-15 2003-08-21 Nucor Corporation Model-based system for determining process parameters for the ladle refinement of steel

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TWI600770B (en) * 2015-07-01 2017-10-01 國立成功大學 Method of adding high vapor pressure magnesium to steel liquid and apparatus for performing the method

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Cited By (5)

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Publication number Priority date Publication date Assignee Title
US6235079B1 (en) 1997-12-20 2001-05-22 Pohang Iron & Steel Co., Ltd. Two step twin-single fluidized bed pre-reduction apparatus for pre-reducing fine iron ore, and method therefor
WO2003068996A1 (en) * 2002-02-15 2003-08-21 Nucor Corporation Model-based system for determining process parameters for the ladle refinement of steel
US6808550B2 (en) 2002-02-15 2004-10-26 Nucor Corporation Model-based system for determining process parameters for the ladle refinement of steel
US6921425B2 (en) 2002-02-15 2005-07-26 Nucor Corporation Model-based system for determining process parameters for the ladle refinement of steel
US7211127B2 (en) 2002-02-15 2007-05-01 Nucor Corporation Model-based system for determining process parameters for the ladle refinement of steel

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MX9705056A (en) 1997-10-31
EP0795037A1 (en) 1997-09-17
PL321183A1 (en) 1997-11-24
EP0795037B1 (en) 2000-04-05
ITBS950003A0 (en) 1995-01-05
CZ210297A3 (en) 1998-04-15
AU4187796A (en) 1996-07-24
ATE191516T1 (en) 2000-04-15
CN1046553C (en) 1999-11-17
ITBS950003A1 (en) 1996-07-05
BR9510130A (en) 1997-12-30
DE69516170D1 (en) 2000-05-11
IT1278916B1 (en) 1997-11-28
US6099614A (en) 2000-08-08
CN1177383A (en) 1998-03-25
DE69516170T2 (en) 2000-11-16
RU2154111C2 (en) 2000-08-10
JPH10511741A (en) 1998-11-10

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