WO1985004416A1 - Pneumatic charger for feeding pulverized and granular materials into metal melts - Google Patents

Pneumatic charger for feeding pulverized and granular materials into metal melts Download PDF

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Publication number
WO1985004416A1
WO1985004416A1 PCT/HU1985/000018 HU8500018W WO8504416A1 WO 1985004416 A1 WO1985004416 A1 WO 1985004416A1 HU 8500018 W HU8500018 W HU 8500018W WO 8504416 A1 WO8504416 A1 WO 8504416A1
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WO
WIPO (PCT)
Prior art keywords
spacer
box
charger
profile
wind
Prior art date
Application number
PCT/HU1985/000018
Other languages
French (fr)
Inventor
Béla SOMOGYI
István HOFFMANN
Original Assignee
Ceglédi Vas- Elektromos És Müszerészipari Szövetke
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 Ceglédi Vas- Elektromos És Müszerészipari Szövetke filed Critical Ceglédi Vas- Elektromos És Müszerészipari Szövetke
Priority to DE8585901541T priority Critical patent/DE3571463D1/en
Priority to AT85901541T priority patent/ATE44549T1/en
Publication of WO1985004416A1 publication Critical patent/WO1985004416A1/en

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Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D3/00Charging; Discharging; Manipulation of charge
    • F27D3/16Introducing a fluid jet or current into the charge
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21CPROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
    • C21C7/00Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00
    • C21C7/0037Treating molten ferrous alloys, e.g. steel, not covered by groups C21C1/00 - C21C5/00 by injecting powdered material
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B9/00General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals
    • C22B9/10General processes of refining or remelting of metals; Apparatus for electroslag or arc remelting of metals with refining or fluxing agents; Use of materials therefor, e.g. slagging or scorifying agents
    • C22B9/103Methods of introduction of solid or liquid refining or fluxing agents

Definitions

  • the invention relates to a charger operated on the principle of pneumatics which is suitable for feeding granular or pulverized inflammable and explosive materials as well asmaterials of high density into motal melts.
  • Metallurgical processes used in metallurgy show a new trend of development. A considerable part of the processes have been relocated from the metallurgic furnace into the ladle.
  • One of the most important branches of the ladle-metallurgic processes thus developed is represented by the blowing technologies, in course of which the gas carrying the diverse materials is blown, resp. transported pneumatically into the metal bath.
  • the most known equipment for treating steels is the blower available in sale with the trade-mark "SCANDINAVIAN LANCERS".
  • SCANDINAVIAN LANCERS pulverized treating material having a calcium-silicon content is introduced pneumatically into the steel.
  • the main part of the charger is a conical fluidizator, consisting of a dense screeing cloth and the nozzles with a small cross-section arranged behind the screeing cloth, which enables the uniform distribution of the gas.
  • the equipment is operated with an indifferent gas, with argon, pressure prevailing in the tank amounts to 6-8 bars.
  • the gas gets mixed with the pulverized reagent.
  • High pressure presses the mixture of gas and powder into the delivery pipeline and via the lancer into the metal bath.
  • Due to wear of thescreen and obstruction of the nozzles the fluidizator requires permanent maintenance.
  • the powder tends to clogging in the tank, material to be blown cannot be stored for a longer time.
  • a further disadvantageous feature of the equipment lies in that it can be operated with high-pressure gas only.
  • Another mechanical equipment is also known which is different from that specified above, in so far as its fluidizator is formed by a screening cloth arranged at an angle of 30° and it is provided with a lower discharge opening with variable cross-section. Speed of material stream is controlled by a mechanical feeder. In respect to construction this equipment is far more complicated, possibilities of failure are greater. At the same time vibrations of the mechanical feeder make weighing more difficult.
  • the aforementioned equipments operate on the principle of fluidization.
  • the carrier gas transfers its pulse to the material grains to be transported. If the force resulting from the pulse is higher, than the effect resulting from the weight of the grains and the frictional force arising inbetween, the particles are carried away by the gas, accordingly delivery is performed.
  • state of fluidization depends partly on the streaming conditions of the carrying gas, partly on the grainsize and density of the material to be transported. Accordingly, this condition cannot be realized with materials of large grain-size and density - e.g. with ferro-alloys - and if, with considerable difficulties only.
  • the aim of the invention is to develop a solution with which parameters of transport, so transport capacity, density of delivery, quantity of carrier gas are constant, while at the same time, in case of necessity these values could be easily changed to the desired extent and in dependence of mode of operation.
  • the solution according to the invention is well adapted for the transport of materials with a grain size of 3 to 5 mm and a density of 4 to 6 kg/dm 3 Construction of the equipment is resistant to increased load occuring under metallurgical circumstances.
  • the invention relates to a charger operated on the principle of pneumatics, which can be characterized by a wind-box provided with an inlet stud, on the inner part of which there is a vertically arranged cylindrical element made of a porous structural material.
  • the upper part of the box is connected to the material storage tank, while the lower part is closed with.a spacer having a cylindrical bore.
  • the spacer is connected with a tap in a releasable manner, which on its part is connected with the pipelinesystem by means of a T-profile having an oblique branch.
  • the material storage tank 1 receives the material to be transported, being a pressure-proof tank with a conical lower part and provided with an opening for material filling.
  • the cone of the tank 1 ends in the flanged connection 2.
  • the wind-box 4 is forming a unit with the counter-part of the flange 2. Said wind-box is formed with the sleeve 3 which is clamping the porous element 5 at the top, while the lower part of the element 5 is seated on the bottom of the box 4.
  • the box 4 communicates with the inlet stud 6 introducing the gas at a pre-set pressure.
  • the mixture of gas and material is flowing through the cylindrical bore of the spacer 7.
  • the spacer 7 is clamped with a releasable bond and it provided with the sealing 9.
  • Material flow is interrupted by the tap 10, while the mixture of gas and material flowing through the tap 10 streams by the aid of the T- prof ile 11 into the pipeline system.
  • Gas in a controlled quantity is introduced into the inlet stud of the T-profile 11, whereas its output branch is connected to the injecting lancer through the delivery duct.
  • the T-profile 11 does not contain any structural element which would impede material flow, it does not exert a higher flow resistance, than an average pipe tract. In such a manner it becomes possible to connect the feeders of two or more material storage tanks in series.
  • the pneumatic charger according to the invention operates, as follows:
  • Material storage tank 1 is filled with the material to be blown, now the tap 10 is closed. After having closed the filling opening, gas at a pre-set pressure is led to the tank 1 through the inlet stud 6.
  • gas at a pre-set pressure is led to the tank 1 through the inlet stud 6.
  • First one starts with the diving of the lancer into the metal bath and simultaneously gas in a controlled quantity is introduced into the inlet stud of the T-profile 11, the pressure of which prevents penetration of metal into the inside of the lancer.
  • material feeding begins by opening the tap 10.
  • gas is streaming among the material grains, through the porous element 5 to the spacer 7. Material grains to be found on the upper bevelled part of the spacer 7 are carried away by the streaming gas.
  • the gas-material mixture is considerably accelerated in the bore of the spacer and arrives with a significant kinetic energy to the T-profile 11. Taking into consideration that in respect to the proportion gas/solids this mixture is very dense, controlled gas quantity, as previously mentioned, is admixed here. In such a manner it can be achieved that the material arrives pneumatically from the storage tank to the metal bath through the delivery duct and the lancer. As the material to be transported is forwarded by its own weight to the spacer 7, it is to be considered as specifically advantageous, that feeding is independent of material density and grain size.
  • Delivery output is uniform, at the same time it can be easily controlled in dependence of mode of operation, magnitude depends on the flow velocity having been developed in the bore of the spacer 7. Control can be easily performed without changing any structural element, simply by regulating the pressure of gas streaming through the stud 6. In course of the blowing process, up to the full immersion of the lancer, the pressure of the streaming gas on the inlet side of the T-profile 11 prevents intrusion of metal into the inside of the lancer.
  • the siteaming of the oaaterial to be blown begins in the lower position of the lancer, i.e. in a completely immersed position, with the opening of the tap 10.
  • the charger according to the invention yield several new possibilities in the field ofblowing technology.
  • a plurality of metallurgic processes can be performed with the same equipment.
  • the tap 10 of one or of the other tank by openingthe tap 10 of one or of the other tank, different materials can be introduced one after the other, or by the simultaneous opening of the taps 10 mixing of the materials while blowing becomes also possible.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Furnace Charging Or Discharging (AREA)
  • Air Transport Of Granular Materials (AREA)

Abstract

A charger based on the principle of pneumatics for the transport of granular, pulverized inflammable and explosive materials, as well as materials of high density into the metal melt. The charger according to the invention consists of a wind-box (4) connected to the conical bottom of the material storage tank (1), of the cylindrical porous element (5) forming a structural unit therewith, of the exchangeably spacer (7), the tap (10) and the T-profile (11). The gas streaming through the porous element (5) is flowing into the bore of the spacer (7), carries the material particles with itself and the accelerated material arrives through the tap (10), by the aid of the T-profile (11) into the system of delivery ducts. In order to facilitate maintenance, the spacer (7) is connected to the wind-box (4) with a releasable bond (8).

Description

PNEUMATIC CHARGES FOR FEEDING PULVERIZED AND GRANULAR MATERIALS INTO METAL MELTS
Technical Field
The invention relates to a charger operated on the principle of pneumatics which is suitable for feeding granular or pulverized inflammable and explosive materials as well asmaterials of high density into motal melts.
Metallurgical processes used in metallurgy show a new trend of development. A considerable part of the processes have been relocated from the metallurgic furnace into the ladle. One of the most important branches of the ladle-metallurgic processes thus developed is represented by the blowing technologies, in course of which the gas carrying the diverse materials is blown, resp. transported pneumatically into the metal bath.
Background Art
Aa a result of the process several material qualities not having been manufactured as mass-produced goods up to now can be produced in a large quantity, or production of traditional qualities can be rendered more economical. In dependence of metallurgic processes the materials to be blown vary in respect to chemical composition and grain distribution within wide ranges. Accordingly, grain size may vary from a few microns to several millimetres, while chemical composition may vary from the treating materials on calcium basis through ground ferro-alloys to the granular alloys containing magnesium having a thermite character and being inflammable and explosive. In dependence of the quality of treating materials chargers of different structures are in use. In the initial period methods developed from mechanical feeders well proved in pneumatic material delivery to mechanic-pneumatic modes of feeding, arriving at last to chargers based exclusively on the principle of pneumatics.
The most known equipment for treating steels is the blower available in sale with the trade-mark "SCANDINAVIAN LANCERS". In course of said technologies pulverized treating material having a calcium-silicon content is introduced pneumatically into the steel. The main part of the charger is a conical fluidizator, consisting of a dense screeing cloth and the nozzles with a small cross-section arranged behind the screeing cloth, which enables the uniform distribution of the gas.
The equipment is operated with an indifferent gas, with argon, pressure prevailing in the tank amounts to 6-8 bars. In the fluidizator the gas gets mixed with the pulverized reagent. High pressure presses the mixture of gas and powder into the delivery pipeline and via the lancer into the metal bath. Due to wear of thescreen and obstruction of the nozzles the fluidizator requires permanent maintenance. The powder tends to clogging in the tank, material to be blown cannot be stored for a longer time. A further disadvantageous feature of the equipment lies in that it can be operated with high-pressure gas only. Another mechanical equipment is also known which is different from that specified above, in so far as its fluidizator is formed by a screening cloth arranged at an angle of 30° and it is provided with a lower discharge opening with variable cross-section. Speed of material stream is controlled by a mechanical feeder. In respect to construction this equipment is far more complicated, possibilities of failure are greater. At the same time vibrations of the mechanical feeder make weighing more difficult.
The aforementioned equipments operate on the principle of fluidization. When passing through the fluidizing element, the carrier gas transfers its pulse to the material grains to be transported. If the force resulting from the pulse is higher, than the effect resulting from the weight of the grains and the frictional force arising inbetween, the particles are carried away by the gas, accordingly delivery is performed. As a consequence, state of fluidization depends partly on the streaming conditions of the carrying gas, partly on the grainsize and density of the material to be transported. Accordingly, this condition cannot be realized with materials of large grain-size and density - e.g. with ferro-alloys - and if, with considerable difficulties only.
If - inapite of the arising difficulties - the desired condition can be achieved, streams of high speed occuring in course of fluidization are considerably wearing the fluidizing elements, simultaneously friction arising between the grains to be transported may lead to self-ignition. Hazard of fire and explosion increases with material having magnesium content. With these types inflammability is increased by the small grainsize and arising high speeds, being otherwise most advantageous for the fluidizing process. By these reasons alloys with magnesium content are blown in notfrequently. The aim of the invention is to develop a solution with which parameters of transport, so transport capacity, density of delivery, quantity of carrier gas are constant, while at the same time, in case of necessity these values could be easily changed to the desired extent and in dependence of mode of operation. The solution according to the invention is well adapted for the transport of materials with a grain size of 3 to 5 mm and a density of 4 to 6 kg/dm3 Construction of the equipment is resistant to increased load occuring under metallurgical circumstances.
Disclosure of Invention
Accordingly, the invention relates to a charger operated on the principle of pneumatics, which can be characterized by a wind-box provided with an inlet stud, on the inner part of which there is a vertically arranged cylindrical element made of a porous structural material. The upper part of the box is connected to the material storage tank, while the lower part is closed with.a spacer having a cylindrical bore. The spacer is connected with a tap in a releasable manner, which on its part is connected with the pipelinesystem by means of a T-profile having an oblique branch.
Brief Description of Drawings
The invention will now be described in detail by means of a preferred embodiment of the invention, by the aid of the drawing enclosed, illustrating the pneumatic charger in a sectional view.
Best Mode of Carrying out the Invention
The material storage tank 1 receives the material to be transported, being a pressure-proof tank with a conical lower part and provided with an opening for material filling. The cone of the tank 1 ends in the flanged connection 2. The wind-box 4 is forming a unit with the counter-part of the flange 2. Said wind-box is formed with the sleeve 3 which is clamping the porous element 5 at the top, while the lower part of the element 5 is seated on the bottom of the box 4. The box 4 communicates with the inlet stud 6 introducing the gas at a pre-set pressure. The mixture of gas and material is flowing through the cylindrical bore of the spacer 7. The spacer 7 is clamped with a releasable bond and it provided with the sealing 9. Material flow is interrupted by the tap 10, while the mixture of gas and material flowing through the tap 10 streams by the aid of the T- prof ile 11 into the pipeline system. Gas in a controlled quantity is introduced into the inlet stud of the T-profile 11, whereas its output branch is connected to the injecting lancer through the delivery duct.
As the T-profile 11 does not contain any structural element which would impede material flow, it does not exert a higher flow resistance, than an average pipe tract. In such a manner it becomes possible to connect the feeders of two or more material storage tanks in series.
This fact opens new possibilities in respect to blowing technology. The pneumatic charger according to the invention operates, as follows:
Material storage tank 1 is filled with the material to be blown, now the tap 10 is closed. After having closed the filling opening, gas at a pre-set pressure is led to the tank 1 through the inlet stud 6. First one starts with the diving of the lancer into the metal bath and simultaneously gas in a controlled quantity is introduced into the inlet stud of the T-profile 11, the pressure of which prevents penetration of metal into the inside of the lancer. In the lower position of the lancer, when it is already dipped into the metal bath, material feeding begins by opening the tap 10. Through the inlet stud 6 gas is streaming among the material grains, through the porous element 5 to the spacer 7. Material grains to be found on the upper bevelled part of the spacer 7 are carried away by the streaming gas. The gas-material mixture is considerably accelerated in the bore of the spacer and arrives with a significant kinetic energy to the T-profile 11. Taking into consideration that in respect to the proportion gas/solids this mixture is very dense, controlled gas quantity, as previously mentioned, is admixed here. In such a manner it can be achieved that the material arrives pneumatically from the storage tank to the metal bath through the delivery duct and the lancer. As the material to be transported is forwarded by its own weight to the spacer 7, it is to be considered as specifically advantageous, that feeding is independent of material density and grain size.
Operational safety of the equipment is far increased by the fact that in course of feeding no fluidization flow is taking place, the porous element is neither mechanically nor abrasively loaded. Plows with a higher velocity are transferred to the spacer 7, which can be easily manufactured from a wear-resistant structural material. At the same time the spacer 7 is clamped into the wind-box with a releasable bond 8, enabling an easy and quick exchange. The porous element 5 is a cylinder with a vertical axis, so powder fraction of the material to be delivered cannot deposit in the opening thereof, so required cleaning and maintenance are minimal.
Delivery output is uniform, at the same time it can be easily controlled in dependence of mode of operation, magnitude depends on the flow velocity having been developed in the bore of the spacer 7. Control can be easily performed without changing any structural element, simply by regulating the pressure of gas streaming through the stud 6. In course of the blowing process, up to the full immersion of the lancer, the pressure of the streaming gas on the inlet side of the T-profile 11 prevents intrusion of metal into the inside of the lancer. The stieaming of the oaaterial to be blown begins in the lower position of the lancer, i.e. in a completely immersed position, with the opening of the tap 10. In contrast to known equipments, by using the solution according to the invention accidents resulting from considerable squirting - occuring frequently with alloys containing magnesium - can be avoided. This phenomenon can be observed especially, if in course of the immersion of the lancer material is blown into low bath depth.
The charger according to the invention yield several new possibilities in the field ofblowing technology. In case, if the T-profiles 11 of the blowers of two or more material storage tanks are connected in series, a plurality of metallurgic processes can be performed with the same equipment. In the immersed state of the lancer, by openingthe tap 10 of one or of the other tank, different materials can be introduced one after the other, or by the simultaneous opening of the taps 10 mixing of the materials while blowing becomes also possible.
As it becomes obvious from all what has been said, inspite of the simple construction, the equipment performs all the functions required by the special circumstances of blowing technology in course of pneumatic transport. Some advantageous features of the invention will be demonstrated by the way of examples.
Example 1
In course of the experiment calcium containing mineral material and - without lifting the lancer - magnesium containing auxiliary alloy were introduced by the aid of a blower with two storage tanks.
Particulars of the treatment ;
grain-size density transport output mm kg/dm3 kg/min
Calcium containing material 0 to 4 1,8 - 2 8
Magnesium containing alloy 0 - 3,5 3,6 - 4,0 14
Materials were delivered uniformly into the metal bath, stoppage could not be observed. Example 2
In course of this experiment chemical composition of the metal melt was set by blowing ferro-alloy into the melt.
Particulars of treatment:
Grain-size 0 to 5 mm Density 4,8 to 5,0 kg/dm3
Transport output 18 kg/min
In course of blowing process no failure could be observed in material transport.

Claims

C L A I M S
1. Pneumatic charger for the transport of pulverized and granular materials into metal melts, char a c t e r i z e d in that it comprises a wind-box (4) connected to the conical bottom of the material storage tank (1), a porous element (5) of cylindrical shape and arranged in a vertical position forming a structural unit with said wind-box, an exchangeable spacer (7), as well as the tap (10) communicating therewith, and a T-profile (11) with a three-way outlet.
2. Pneumatic charger as claimed in claim 1, c h ar a c t e r i z e d in that its cylindrical spacer (7) is formed with a concentric bore and the part of the outer mantle facing the porous element (5) is bevelled, while the spacer (7) is. fixed in the house having been formed in the wind-box (4) with a releasable bond (8) with the insertion of the seal (9).
3. Pneumatic charger as claimed in claims 1 and 2, c h ar ac t e r i z e d in that it is connected via the T-profile (11) to a delivery duct or when connected in series with the T-profile (11) of another charger, diverse materials, can be mixed while being delivered, or it is well suitable for allowing the gas to stream.
PCT/HU1985/000018 1984-03-28 1985-03-27 Pneumatic charger for feeding pulverized and granular materials into metal melts WO1985004416A1 (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
DE8585901541T DE3571463D1 (en) 1984-03-28 1985-03-27 Pneumatic charger for feeding pulverized and granular materials into metal melts
AT85901541T ATE44549T1 (en) 1984-03-28 1985-03-27 PNEUMATIC LOADING DEVICE FOR FEEDING POWDERY AND GRAINY SUBSTANCES IN METAL METAL.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
HU122484A HU190268B (en) 1984-03-28 1984-03-28 Pneumatic feeding device for delivering powder and granular materials into metal fusion
HU1224/84 1984-03-28

Publications (1)

Publication Number Publication Date
WO1985004416A1 true WO1985004416A1 (en) 1985-10-10

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/HU1985/000018 WO1985004416A1 (en) 1984-03-28 1985-03-27 Pneumatic charger for feeding pulverized and granular materials into metal melts

Country Status (5)

Country Link
EP (1) EP0178310B1 (en)
DE (1) DE3571463D1 (en)
HU (1) HU190268B (en)
SU (1) SU1440338A3 (en)
WO (1) WO1985004416A1 (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1558184A1 (en) * 1966-02-02 1970-03-19 Centalny Nii Tchornoy Metallou Method and device for distributing slag or covering agents on the melt surface in molds for continuous metal casting
DE2105733A1 (en) * 1971-02-08 1972-08-17 Süddeutsche Kalkstickstoff-Werke AG, 8223 Trostberg : Removal process of a fluidizable solid from a pressure vessel and device for carrying out the process
DE2248859B2 (en) * 1972-10-05 1975-10-23 Claudius Peters Ag, 2000 Hamburg Method and device for the pneumatic conveying of powdery or granular bulk material
DE2736212A1 (en) * 1976-08-12 1978-02-16 Battelle Memorial Institute POWDER DISTRIBUTOR
CH618659A5 (en) * 1976-12-10 1980-08-15 Colmant Cuvelier

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE1558184A1 (en) * 1966-02-02 1970-03-19 Centalny Nii Tchornoy Metallou Method and device for distributing slag or covering agents on the melt surface in molds for continuous metal casting
DE2105733A1 (en) * 1971-02-08 1972-08-17 Süddeutsche Kalkstickstoff-Werke AG, 8223 Trostberg : Removal process of a fluidizable solid from a pressure vessel and device for carrying out the process
DE2248859B2 (en) * 1972-10-05 1975-10-23 Claudius Peters Ag, 2000 Hamburg Method and device for the pneumatic conveying of powdery or granular bulk material
DE2736212A1 (en) * 1976-08-12 1978-02-16 Battelle Memorial Institute POWDER DISTRIBUTOR
CH618659A5 (en) * 1976-12-10 1980-08-15 Colmant Cuvelier

Also Published As

Publication number Publication date
HU190268B (en) 1986-08-28
DE3571463D1 (en) 1989-08-17
EP0178310B1 (en) 1989-07-12
SU1440338A3 (en) 1988-11-23
EP0178310A1 (en) 1986-04-23
HUT36401A (en) 1985-09-30

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