EP0110806A1 - Regulating system for delivering solid materials to a blowing lance - Google Patents
Regulating system for delivering solid materials to a blowing lance Download PDFInfo
- Publication number
- EP0110806A1 EP0110806A1 EP83630175A EP83630175A EP0110806A1 EP 0110806 A1 EP0110806 A1 EP 0110806A1 EP 83630175 A EP83630175 A EP 83630175A EP 83630175 A EP83630175 A EP 83630175A EP 0110806 A1 EP0110806 A1 EP 0110806A1
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- EP
- European Patent Office
- Prior art keywords
- gas
- circuit
- lance
- pressure
- carbonaceous material
- Prior art date
- Legal status (The legal status 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 status listed.)
- Granted
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- 238000007664 blowing Methods 0.000 title claims abstract description 9
- 230000001105 regulatory effect Effects 0.000 title claims description 7
- 239000011343 solid material Substances 0.000 title description 3
- 239000003575 carbonaceous material Substances 0.000 claims abstract description 22
- 230000001413 cellular effect Effects 0.000 claims abstract description 6
- 238000010926 purge Methods 0.000 claims abstract description 4
- 229910052751 metal Inorganic materials 0.000 claims description 6
- 239000002184 metal Substances 0.000 claims description 6
- 238000007670 refining Methods 0.000 claims description 6
- 238000009434 installation Methods 0.000 claims description 5
- 238000000034 method Methods 0.000 claims description 5
- 230000008569 process Effects 0.000 claims description 5
- 239000007787 solid Substances 0.000 claims description 5
- 238000010408 sweeping Methods 0.000 claims description 5
- 229910001018 Cast iron Inorganic materials 0.000 claims description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 abstract description 27
- 239000007789 gas Substances 0.000 abstract description 21
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 abstract description 14
- 229910052757 nitrogen Inorganic materials 0.000 abstract description 13
- 229910052786 argon Inorganic materials 0.000 abstract description 7
- 230000009467 reduction Effects 0.000 abstract description 4
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 8
- 239000001301 oxygen Substances 0.000 description 8
- 229910052760 oxygen Inorganic materials 0.000 description 8
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 239000012159 carrier gas Substances 0.000 description 4
- 230000001276 controlling effect Effects 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000001066 destructive effect Effects 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 230000007935 neutral effect Effects 0.000 description 2
- 239000007800 oxidant agent Substances 0.000 description 2
- 230000001590 oxidative effect Effects 0.000 description 2
- 230000002028 premature Effects 0.000 description 2
- 239000005997 Calcium carbide Substances 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 1
- 239000003830 anthracite Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000005243 fluidization Methods 0.000 description 1
- 230000004907 flux Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 150000001247 metal acetylides Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- CLZWAWBPWVRRGI-UHFFFAOYSA-N tert-butyl 2-[2-[2-[2-[bis[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]amino]-5-bromophenoxy]ethoxy]-4-methyl-n-[2-[(2-methylpropan-2-yl)oxy]-2-oxoethyl]anilino]acetate Chemical compound CC1=CC=C(N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)C(OCCOC=2C(=CC=C(Br)C=2)N(CC(=O)OC(C)(C)C)CC(=O)OC(C)(C)C)=C1 CLZWAWBPWVRRGI-UHFFFAOYSA-N 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/28—Manufacture of steel in the converter
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21C—PROCESSING OF PIG-IRON, e.g. REFINING, MANUFACTURE OF WROUGHT-IRON OR STEEL; TREATMENT IN MOLTEN STATE OF FERROUS ALLOYS
- C21C5/00—Manufacture of carbon-steel, e.g. plain mild steel, medium carbon steel or cast steel or stainless steel
- C21C5/28—Manufacture of steel in the converter
- C21C5/42—Constructional features of converters
- C21C5/46—Details or accessories
- C21C5/4606—Lances or injectors
Definitions
- the present invention relates to a system for adjusting the supply of solids to a lance used to supply a metal bath, in particular a cast iron bath in the process of refining.
- the invention describes in particular a system, suitable for the introduction of granulated combustible material using neutral carrier gases into the metal being refined in the context of the LD, LD-AC or LBE processes.
- patent application FR 2 459 835 provides for blowing calcium carbide on the surface of the bath, and this by using refining oxygen as the vehicle for the carbide. It turns out that the carbide carried by the oxygen does not oxidize in the jet, which may a priori surprise.
- carbides are compounds that are obtained by reactions consuming large amounts of energy which should exclude such a process at a time when energy is expensive.
- the constraint of recarburizing the bath in reduced time is also reinforced if nitrogen is chosen as the carrier gas for reasons of cost price.
- the nitrogen jet strikes the surface of the metal bath in the immediate vicinity of the refining oxygen.
- the degree of dissolution of nitrogen in liquid steel increases with temperature.
- the object of the invention is to propose a system capable of rapidly injecting a high quantity of granulated combustible material into a metal bath from above.
- the adjustment system which comprises at least one source of compressed gas, a circuit supplying carbonaceous material suspended in a gas, at least one circuit supplying sweeping gas, means for metering the different gas and carbonaceous material flow rates and means for separately or jointly connecting said circuits to a conduit leading to the lance.
- FIG. 1 shows a possible embodiment of the system for adjusting the supply of the lance.
- the insufflation lance 1 which can be a multiflux lance used to supply the bath jointly with oxygen and granulated material, as described for example in patent application LU 84.176, or else a monoflux lance used to inject only granulated material in the bath. In the latter case, the refining oxygen and possibly the post-combustion oxygen is supplied by a separate lance.
- the lance 1 is mounted on a quick fixing system 2, integral with a carriage or any other mobile system, not shown, used to approach the lance at the desired distance from the surface of the bath.
- the fastening system is connected to a set 5 of rigid tubes 3 and articulations 4, known as shears as well as to a safety device 6 which detects possible leaks in the body of the lance 1.
- the leak detection is particularly important in multiflow lances which jointly supply the fuel which is normally abrasive and the oxidizer and can for example be carried out using a sheath filled with a fluid, which surrounds the duct of carbonaceous material the lance and a pressure sensor which monitors the fluid pressure. In case of breaking the sensor records a Variati - one pressure it transmits to the safety device 6 which stops the blowing operation.
- the shears 5 can be connected at will to the circuit 7 supplying carbonaceous material or to the circuit 8 supplying sweep gas by acting on the respective electromagnetic valves 9 ment 10.
- the circuit-8 is used to send a determined flow of argon from the source 30 or nitrogen from the source 31 to the lance 1 by opening / closing the valves 21 resp. 22 and by adequately controlling the flow regulator 11.
- the regulator 11 essentially consists of a pressure sensor 19, a pressure variation sensor 18 and a temperature sensor 20 connected respectively to converters 17 , 16 and 15 which transform the signals picked up into electrical signals that can be processed by the computer 14. The latter determines, depending on the operating mode of the crucible or the state of blockage of the conduits, the required flow rate which it transmits to the regulating valve 12 by means of the amplifier 13. Note that for reasons of clarity, the calculator figure has been drawn in several different places (provided with the references 14a and 14b).
- valves 24 and 26 are located between the valve 22 and the nitrogen source 31 as well as a pressure regulator 25 which prevents the source 31 from applying pressures. excessive to the purge gas supply circuit 8.
- a one-way valve 53 prevents any feedback from the carbon material supply circuit 7 to the purge gas supply circuit 8.
- the circuit 7 supplying carbonaceous material is only connected to the nitrogen source 31 and essentially comprises a flow regulator 11a as well as a blast airlock with a cellular metering device 40.
- the airlock allows the flow rate of the mixture to be continuously varied. introduce and this by simply acting on the speed of rotation of the wheel of the cellular metering device 48. The flow rate of carrier gas passing through the blowing lance can thus be modified independently of the quantity of solid matter.
- the airlock includes a conduit 41 leading to the pressurization system of the carbonaceous material reservoir 47, as well as conduits 42 to 46 connected to the fluidization system of the carbonaceous material.
- a sensor 50 monitors the pressure in the conduits downstream of the airlock 40 and acts via the converter 49 and the computer 14b on the speed of rotation of the cellular metering device 48.
- the flow regulator lIa of the circuit supplying carbonaceous material 7 is of a conception close to that of the regula 11 controlling the flow of sweeping gas and the elements performing equivalent functions are identified by the same numbers increased by the letter a. Note that the pressure prevailing in the duct is identified using the sensor 19a upstream of the pressure regulator 25a and the valves 24a and 26a and practically indicates the pressure of the nitrogen source 31.
- the installation also includes several manometers 51 as well as electromagnetic valves 52.
- valve 9 is closed and the valve 10 open and allows a small flow of gas (nitrogen, preferably argon) to flow through the shears 5 and the lance 1 so as to prevent clogging of the conduits due to an agglomeration of carbonaceous material deposited in the tubes or blockage of the lance head caused by projections.
- gas nitrogen, preferably argon
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Carbon Steel Or Casting Steel Manufacturing (AREA)
- Furnace Charging Or Discharging (AREA)
- Treatment Of Steel In Its Molten State (AREA)
- Air Transport Of Granular Materials (AREA)
- Crystals, And After-Treatments Of Crystals (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
- Discharge Heating (AREA)
- Endoscopes (AREA)
- Glass Compositions (AREA)
- Coating Apparatus (AREA)
- Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
- Control And Other Processes For Unpacking Of Materials (AREA)
- Physical Vapour Deposition (AREA)
- Luminescent Compositions (AREA)
- Color Printing (AREA)
- Inorganic Insulating Materials (AREA)
Abstract
Une lance d'insufflation (1 montée sur un système de fixation rapide (2) qui est relié à un ensemble (5) de tubes rigides (3) et d'articulations (4) peut être branchée à volonté sur un circuit (8) fournisseur de gaz de balayage ou un circuit (7) fournisseur de matière carbonée. Le circuit (8) envoie un débit déterminé d'argon en provenance d'une source (30) ou d'azote en provenance d'une autre source (31) en contrôlant de façon adéquate un régulateur de débit (11). Le circuit fournisseur de matière carbonée (7) est relié à la source d'azote (31) et comporte essentiellement un régulateur de débit (11a) ainsi qu'un sas de soufflage à doseur alvéolaire (40). Lorsque les conduits accusent, lors de la phase de récarburation, un léger bouchage, la pression répérée par un capteur (50) augmente et un calculateur (14b) commande une réduction de la vitesse de rotation de la roue (48) du doseur. Lorsque des réductions successives de la vitesse de rotation du doseur n'aboutissent pas au débouchage des conduits, le calculateur (14b) commance l'arrêt du circuit de récarburation (7) et l'envoi d'azote ou d'argon sous pression élevée (circuit de balayage 8) sur les conduits de sorte à provoquer le débauchage désiré et à redémarrer ensuite l'opération de récarburation. An insufflation lance (1 mounted on a quick fixing system (2) which is connected to a set (5) of rigid tubes (3) and joints (4) can be connected at will to a circuit (8) purge gas supplier or a circuit (7) supplier of carbonaceous material. The circuit (8) sends a determined flow of argon from one source (30) or nitrogen from another source (31 ) by adequately controlling a flow regulator (11). The carbonaceous material supply circuit (7) is connected to the nitrogen source (31) and essentially comprises a flow regulator (11a) as well as an airlock blowing with a cellular metering device (40). When the conduits show a slight blockage during the recarburization phase, the pressure detected by a sensor (50) increases and a computer (14b) controls a reduction in the speed of rotation of the metering wheel (48) When successive reductions in the metering speed do not result in unclogging conduits, the computer (14b) starts the shutdown of the recarburization circuit (7) and the sending of nitrogen or argon under high pressure (sweep circuit 8) on the conduits so as to cause the desired poaching and then restart the recarburization operation.
Description
La présente invention concerne un systéme de réglage de' l'alimentation en matières solides d'une lance servant à approvisionner un bain de métal, notamment un bain de fonte en voie d'affinage. L'invention décrit en particulier un système, adapté à l'introduction de matière combustible granulée à l'aide de gaz porteurs neutres dans le métal en voie d'affinage dans le cadre des procédés LD, LD-AC ou LBE.The present invention relates to a system for adjusting the supply of solids to a lance used to supply a metal bath, in particular a cast iron bath in the process of refining. The invention describes in particular a system, suitable for the introduction of granulated combustible material using neutral carrier gases into the metal being refined in the context of the LD, LD-AC or LBE processes.
On connait des procédés qui prévoient de recarburer des bains de métal par addition de carbone par le haut. Ainsi la demande de brevet FR 2.459.835 prévoit de souffler sur la surface du bain du carbure de calcium, et ceci en utilisant l'oxygène d'affinage comme véhicule du carbure. Il s'avère que le carbure véhiculé par l'oxygène ne s'oxyde pas dans le jet, ce qui peut à priori surprendre. D'un autre c8té, les carbures sont des composés que l'on obtient par des réactions consommatrices de grandes quantités d'énergie ce qui devrait exclure un tel procédé à une époque où l'énergie est chère.Processes are known which plan to recarburize metal baths by adding carbon from above. Thus, patent application FR 2 459 835 provides for blowing calcium carbide on the surface of the bath, and this by using refining oxygen as the vehicle for the carbide. It turns out that the carbide carried by the oxygen does not oxidize in the jet, which may a priori surprise. On the other hand, carbides are compounds that are obtained by reactions consuming large amounts of energy which should exclude such a process at a time when energy is expensive.
Il serait par conséquent logique de prévoir l'utilisation de carbone sous forme d'anthracite, de poussier de coke ou autre matière carbonée appropriée. Or dans ce cas il est peu probable que l'on puisse opérer l'insufflation de la manière décrite dans la demande de brevet FR 2.459.835 sans qu'il y ait oxydation prématurée, éventuellement sous forme d'une combustion véhémente, destructrice de l'équipement. Il faut par conséquent injecter la matière carbonée à l'aide d'un gaz non comburant et prévoir éventuellement un écran protecteur gazeux entre le flux de matière carbonée et les jets avoisinnants d'oxygène d'affinage.It would therefore be logical to provide for the use of carbon in the form of anthracite, coke dust or other suitable carbonaceous material. In this case, it is unlikely that insufflation can be carried out in the manner described in patent application FR 2 459 835 without premature oxidation, possibly in the form of vehement combustion, destructive of equipment. It is therefore necessary to inject the carbonaceous material using of a non-oxidizing gas and possibly provide a gaseous protective screen between the flow of carbonaceous material and the neighboring jets of refining oxygen.
Les expériences des déposants ont montré que pour avoir une bonne absorption de la matière carbonée par le bain, il faut que celui-ci présente non seulement des concentrations d'oxygène et de carbone bien déterminées, mais qu'il faut en plus que la matière carbonée ait une énergie cinétique suffisante à la sortie de la lance pour pénétrer dans le bain. Cette énergie cinétique élevée, qui est également requise pour éviter une combustion prématurée de la matière carbonée au dessus du bain, est obtenue à l'aide d'un flux puissant de gaz. Etant donné que ce jet de gaz neutre exerce un effet refroidissant il est essentiel d'introduire la quantité requise de matière carbonée dans le bain dans un temps de soufflage aussi court que possible. Or un jet de gaz ayant une concentration en matières solides élevée crée des problèmes de bouchage des conduits d'amenée et de la tuyère de la lance.The experiments of the depositors have shown that in order to have a good absorption of the carbonaceous material by the bath, it is necessary that the latter not only present well-defined oxygen and carbon concentrations, but that in addition the material carbonaceous has sufficient kinetic energy at the outlet of the lance to enter the bath. This high kinetic energy, which is also required to avoid premature combustion of the carbonaceous material above the bath, is obtained using a powerful flow of gas. Since this neutral gas jet exerts a cooling effect, it is essential to introduce the required quantity of carbonaceous material into the bath in as short a blowing time as possible. However, a gas jet having a high solids concentration creates problems of clogging of the supply conduits and of the nozzle of the lance.
La contrainte de recarburer le bain en temps réduit est par ailleurs renforcée si on choisit pour des raisons de prix de revient l'azote comme gaz porteur. Le jet d'azote frappe en effet la surface du bain métallique au voisinage immédiat de l'oxygène d'affinage. Or il est bien connu que le degré de dissolution de l'azote dans l'acier liquide augmente avec la température.The constraint of recarburizing the bath in reduced time is also reinforced if nitrogen is chosen as the carrier gas for reasons of cost price. The nitrogen jet strikes the surface of the metal bath in the immediate vicinity of the refining oxygen. However, it is well known that the degree of dissolution of nitrogen in liquid steel increases with temperature.
L'invention a comme but de proposer un système capable d'injecter rapidement par en haut une quantité élevée de matière combustible granulée dans un bain de métal.The object of the invention is to propose a system capable of rapidly injecting a high quantity of granulated combustible material into a metal bath from above.
Ce but est atteint grâce au système de réglage selon l'invention qui comporte au moins une source de gaz comprimé, un circuit fournisseur de matière carbonée en suspension dans un gaz, au moins un circuit fournisseur de gaz de balayage, des moyens de dosage des différents débits de gaz et de matière carbonée et des moyens pour brancher séparément ou conjointement lesdits circuits sur un conduit aboutissant à la lance. Des formes d'exécution préférentielles de l'invention sont décrites dans les sous-revendications.This object is achieved thanks to the adjustment system according to the invention which comprises at least one source of compressed gas, a circuit supplying carbonaceous material suspended in a gas, at least one circuit supplying sweeping gas, means for metering the different gas and carbonaceous material flow rates and means for separately or jointly connecting said circuits to a conduit leading to the lance. Preferred embodiments of the invention are described in the subclaims.
D'autres caractéristiques et avantages ressortiront de la description du schema de principe représenté en Fig.l qui montre une forme d'exécution possible du système de réglage de l'alimentation de la lance.Other characteristics and advantages will emerge from the description of the schematic diagram shown in FIG. 1 which shows a possible embodiment of the system for adjusting the supply of the lance.
On distingue la lance d'insufflation 1 qui peut être une lance multiflux servant à alimenter le bain conjointement en oxygène et en matière granulée, comme décrit par exemple dans la demande de brevet LU 84.176, ou bien une lance monoflux servant à injecter uniquement de la matière granulée dans le bain. Dans ce dernier cas l'oxygène d'affinage et éventuellement l'oxygène de post-combustion est fourni par une lance séparée. La lance 1 est montée sur un système de fixation rapide 2, solidaire d'un chariot ou de tout autre système mobile, non représenté, servant à approcher la lance à la distance voulue de la surface du bain. Le système de fixation est relié à un ensemble 5 de tubes rigides 3 et d'articulations 4, connu sous le nom de cisaille ainsi qu'à un dispositif de sécurité 6 qui détecte d'éventuelles fuites dans le corps de la lance 1. La détection de fuites est particulièrement importante dans les lances multiflux qui fournissent conjointement le combustible qui est normalement abrasif et le comburant et peut par exemple être réalisée à l'aide d'une gaine remplie d'un fluide, qui entoure le conduit de matière carbonée dans la lance et d'un capteur de pression qui surveille la pression du fluide. En cas de rupture le capteur enregistre une variati- on de pression qu'il transmet au dispositif de sécurité 6 qui arrête l'opération de soufflage. On peut également concevoir un circuit de refroidissement de façon à réaliser en même temps une séparation entre les conduits de combustible et de comburant, comme décrit dans la demande de brevet LU (A 733). Une surveillance de la pression du circuit de refroidissement permet dans ce cas également une détection des fuites.We distinguish the insufflation lance 1 which can be a multiflux lance used to supply the bath jointly with oxygen and granulated material, as described for example in patent application LU 84.176, or else a monoflux lance used to inject only granulated material in the bath. In the latter case, the refining oxygen and possibly the post-combustion oxygen is supplied by a separate lance. The lance 1 is mounted on a quick fixing system 2, integral with a carriage or any other mobile system, not shown, used to approach the lance at the desired distance from the surface of the bath. The fastening system is connected to a set 5 of rigid tubes 3 and articulations 4, known as shears as well as to a safety device 6 which detects possible leaks in the body of the lance 1. The leak detection is particularly important in multiflow lances which jointly supply the fuel which is normally abrasive and the oxidizer and can for example be carried out using a sheath filled with a fluid, which surrounds the duct of carbonaceous material the lance and a pressure sensor which monitors the fluid pressure. In case of breaking the sensor records a Variati - one pressure it transmits to the safety device 6 which stops the blowing operation. One can also design a cooling circuit so as to achieve at the same time a separation between the fuel and oxidizer conduits, as described in patent application LU (A 733). In this case, monitoring of the cooling circuit pressure also allows leak detection.
La cisaille 5 peut être branchée à volonté sur le circuit 7 fournisseur de matière carbonée ou sur le circuit 8 fournisseur de gaz de balayage en agissant sur les vannes électromagnétiques 9 respectivement 10.The shears 5 can be connected at will to the circuit 7 supplying carbonaceous material or to the circuit 8 supplying sweep gas by acting on the respective electromagnetic valves 9
Le circuit-8 sert à envoyer un débit déterminé d'argon en provenance de la source 30 ou d'azote en provenance de la source 31 sur la lance 1 en ouvrant/fermant les vannes 21 resp. 22 et en contrôlant de façon adéquate le régulateur de débit 11. Le régulateur 11 se compose essentiellement d'un capteur de pression 19, d'un capteur de variation de pression 18 et d'un capteur de température 20 reliés respectivement à des convertisseurs 17, 16 et 15 qui transforment les signaux captés en signaux électriques traitables par le calculateur 14. Celui-ci détermine en fonction du régime de fonctionnement du creuset ou de l'état de bouchage des conduits le débit requis qu'il transmet à la vanne régulatrice 12 par l'intermédiaire de l'amplificateur 13. Notons que pour des raisons de clarté de la figure calculateur a été dessiné en plusieurs endroits différents (muni des références l4a et 14b). Entre la vanne 22 et la source d'azote 31 sont situés les vannes 24 et 26 ainsi qu'un régulateur de pression 25 qui évite que la source 31 n'applique des pressions. excessives au circuit fournisseur de gaz de balayage 8. Une valve unidirectionnelle 53 évite toute rétroaction du circuit fournisseur de matière carbonée 7 sur le circuit fournisseur de gaz de balayage 8.The circuit-8 is used to send a determined flow of argon from the
Le circuit 7 fournisseur de matière carbonée est uniquement relié à la source d'azote 31 et comporte essentiellement un régulateur de débit 11a ainsi qu'un sas de soufflage à doseur alvéolaire 40. Le sas permet de régler en variation continue le débit du mélange à introduire et ceci en agissant simplement sur la vitesse de rotation de la roue du doseur alvéolaire 48. Le débit de gaz porteur passant par la lance de soufflage peut ainsi être modifié indépendamment de la quantité de matière solide. Le sas comporte un conduit 41 menant au système de pressurisation du réservoir de matière carbonée 47, ainsi que des conduits 42 à 46 reliés au système de fluidisation de la matière carbonée. Un capteur 50 surveille la pression dans les conduits en aval du sas 40 et agit par l'intermédiaire du convertisseur 49 et du calculateur 14b sur la vitesse de rotation du doseur alvéolaire 48. Le régulateur de débit lIa du circuit fournisseur de matiére carbonée 7 est d'une conception proche de celle du régulateur 11 contrôlant le flux de gaz de balayage et les éléments remplissant des fonctions équivalentes sont répérés par les mêmes chiffres augmentés de la lettre a. Notons que la pression régnant dans le conduit est répérée à l'aide du capteur 19a en amont du régulateur de pression 25a et des vannes 24a et 26a et indique pratiquement la pression de la source d'azote 31.The circuit 7 supplying carbonaceous material is only connected to the
Il est bien évident qu'au lieu d'un calculateur unique on peut également utiliser des calculateurs individuels, dans ce cas de préférence analogiques, pour les régulations de débit de gaz porteur de matière carbonée et de gaz de balayage et pour la régulation du doseur alvéolaire. Dans ce cas les amplificateurs 13 et 13a sont remplacés par des amplificateurs-régulateurs qui recoivent leur consigne du calculateur 14b qui contr8le alors la concentration de matière solide dans le gaz en agissant sur l'amplificateur-régulateur 13a et sur la vitesse de rotation de la roue du doseur. Le calculateur 14b est alors également relié à l'amplificateur-régulateur 13 pour doser le flux de gaz de balayage. Une coordination supplémentaire entre les différents éléments de l'installation pourra être assurée par un opérateur.It is obvious that instead of a single computer, individual computers, in this case preferably analog, can also be used for regulating the flow rate of carbonaceous matter and sweeping gas and for regulating the metering device. alveolar. In this case the
L'installation comporte en outre plusieurs manomètres 51 ainsi que des vannes électromagnétiques 52.The installation also includes
Le fonctionnement du système est le suivant:
- Lors de la phase de recarburation la vanne 9 est ouverte tandis que la
vanne 10 est fermée. Le débit de gaz porteur ainsi que celui de matière carbonée sont réglés aux valeurs maximales compatibles avec les capacités de l'installation (source, conduites, sas etc.) et les exigences métallurgiques (capacité d'absorption du carbone par le bain etc.). Dès que les conduites accusent un début de bouchage, qui peut nattre dans les conduits situés en aval du sas de soufflage à doseur alvéolaire, la pression répérée par lecapteur 50 augmente et le calculateur 14 commande une réduction de la vitesse de rotation de la roue dudoseur 48 de sorte à diminuer la charge en matière solide dans le flux gazeux. Si ensuite la pression chute, la vitesse de rotation de laroue 48 est de nouveau augmentée. Dans le cas contraire une réduction supplémentaire de la vitesse de rotation est commandée. Lorsque des opérations successives de réduction de la vitesse de rotation de laroue 48 n'aboutissent pas au débouchage des conduits, le calculateur 14 commande l'arrêt du circuit 7, la fermeture de la vanne 9 et l'ouverture de lavanne 10. Ensuite la vanne régulatrice 12 est ouverte au maximum de sorte à envoyer selon l'ouverture ou la fermeture des vannes 21 et 22, de l'azote ou de l'argon sous pression élevée sur la cisaille 5 et la lance 1. Si le débouchage désiré s'opère, la pression mesurée par lecapteur 50 chute et la recarburation peut reprendre.
- During the recarburization phase, the valve 9 is open while the
valve 10 is closed. The carrier gas flow rate as well as that of carbonaceous material are adjusted to the maximum values compatible with the capacities of the installation (source, conduits, airlock, etc.) and metallurgical requirements (capacity for absorbing carbon by the bath, etc.). . As soon as the pipes show a start of blockage, which can occur in the pipes located downstream of the blast airlock with a honeycomb metering device, the pressure detected by thesensor 50 increases and the computer 14 commands a reduction in the speed of rotation of the wheel. of themetering device 48 so as to reduce the load of solid material in the gas flow. If the pressure then drops, the speed of rotation of thewheel 48 is again increased. Otherwise, an additional reduction in rotation speed is ordered. When successive operations to reduce the speed of rotation of thewheel 48 do not result in the unblocking of the conduits, the computer 14 controls the stopping of the circuit 7, the closing of the valve 9 and the opening of thevalve 10. Then the regulatingvalve 12 is opened to the maximum so as to send, depending on the opening or closing of thevalves 21 and 22, nitrogen or argon under high pressure on the shears 5 and the lance 1. If the unblocking desired operation takes place, the pressure measured by thesensor 50 drops and recarburation can resume.
Entre deux opérations de recarburation la vanne 9 est fermée et la vanne 10 ouverte et permet à un faible flux de gaz (azote, de préfé- férence argon) de circuler à travers la cisaille 5 et la lance 1 de façon à empêcher un bouchage des conduits dû à une agglomération de matière carbonée déposée dans les tubes ou un bouchage de la tête de lance provoqué par des projections.Between two recarburization operations the valve 9 is closed and the
Le fonctionnement du système a été expliqué en utilisant des sources d'argon ou d'azote. Il est bien évident que l'on peut envisager l'utilisation de n'importe quel gaz compatible avec les contraintes d'ordre chimique c.à d. tout gaz non-oxydant, ce qui n'exclut pas l'utilisation de gaz de recyclage. De même, les opérations de débouchage des conduits ont été décrites en ouvrant respectivement fermant les valves électromagnétiques 9 et 10. On peut également ouvrir conjointement les vannes 9 et 10 et ajuster les différents débits de matière gazeuse et solide de sorte a aboutir au débouchage désiré. On peut aussi sans sortir du cadre de l'invention envisager de commander la valve électromagnétique 10 par impulsions. Dans ce dernier cas il faut choisir la fréquence ainsi que les temps de montée des signaux commandant l'ouverture/fermeture de la valve 10 de manière a éviter la création de vibrations dans les conduits ou l'apparition de pressions excessives,destructrices du matériel.The operation of the system has been explained using sources of argon or nitrogen. It is quite obvious that one can envisage the use of any gas compatible with the constraints of a chemical order ie. any non-oxidizing gas, which does not exclude the use of recycling gas. Similarly, the operations of unclogging the conduits have been described by opening respectively closing the
Claims (8)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AT83630175T ATE32351T1 (en) | 1982-10-27 | 1983-10-20 | CONTROL SYSTEM FOR SUPPLYING A BLOWING LANCE WITH SOLID SUBSTANCES. |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| LU84444A LU84444A1 (en) | 1982-10-27 | 1982-10-27 | SYSTEM FOR ADJUSTING THE SOLID MATERIAL SUPPLY OF A BLOWER LANCE |
| LU84444 | 1982-10-27 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| EP0110806A1 true EP0110806A1 (en) | 1984-06-13 |
| EP0110806B1 EP0110806B1 (en) | 1988-02-03 |
Family
ID=19729972
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP83630175A Expired EP0110806B1 (en) | 1982-10-27 | 1983-10-20 | Regulating system for delivering solid materials to a blowing lance |
Country Status (16)
| Country | Link |
|---|---|
| US (1) | US4519587A (en) |
| EP (1) | EP0110806B1 (en) |
| JP (1) | JPS59133315A (en) |
| KR (1) | KR840006371A (en) |
| AT (1) | ATE32351T1 (en) |
| AU (2) | AU558520B2 (en) |
| BR (1) | BR8305162A (en) |
| CA (1) | CA1210833A (en) |
| DE (1) | DE3375583D1 (en) |
| ES (1) | ES8407570A1 (en) |
| FI (1) | FI73463C (en) |
| IN (1) | IN160933B (en) |
| LU (1) | LU84444A1 (en) |
| NO (1) | NO833910L (en) |
| PT (1) | PT77554B (en) |
| ZA (1) | ZA837907B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0165198A3 (en) * | 1984-05-15 | 1987-03-18 | Arbed S.A. | Lance for accelerating solid particles |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4747584A (en) * | 1987-05-19 | 1988-05-31 | Inland Steel Company | Apparatus for injecting alloying ingredient into molten metal stream |
| US6976489B2 (en) | 2000-06-30 | 2005-12-20 | Northgate Technologies, Inc. | Method and apparatus for humidification and warming of air |
| AUPR817201A0 (en) * | 2001-10-09 | 2001-11-01 | Technological Resources Pty Limited | Supplying solid feed materials for a direct smelting process |
| US6835229B2 (en) | 2002-01-22 | 2004-12-28 | Isg Technologies Inc. | Method and apparatus for clearing a powder accumulation in a powder delivery tube |
| ATE498696T1 (en) * | 2004-10-12 | 2011-03-15 | Tech Resources Pty Ltd | PROVIDING SOLID STARTING MATERIALS FOR A DIRECT MELTING PROCESS |
| US8211052B1 (en) | 2006-07-13 | 2012-07-03 | Lexion Medical Llc | Charged hydrator |
| US8496412B2 (en) * | 2006-12-15 | 2013-07-30 | General Electric Company | System and method for eliminating process gas leak in a solids delivery system |
| EP2422134A1 (en) * | 2009-04-24 | 2012-02-29 | FLSmidth A/S | A burner |
| JP5585517B2 (en) * | 2011-04-07 | 2014-09-10 | 新日鐵住金株式会社 | Refining equipment for blowing powder into molten steel, leak detection method and program for powder blowing tank |
| JP6019565B2 (en) * | 2011-11-16 | 2016-11-02 | 株式会社Ihi | Fine powder fuel supply method for oxyfuel boiler and oxyfuel boiler system |
| EP2994708A4 (en) * | 2013-05-06 | 2016-12-21 | Tech Resources Pty Ltd | INJECTION LANCE OF SOLID MATERIALS |
| CN112981036A (en) * | 2019-12-17 | 2021-06-18 | 新疆八一钢铁股份有限公司 | Method for rapidly treating blockage of charging hole of converter |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AT225213B (en) * | 1960-05-27 | 1963-01-10 | Oesterr Alpine Montan | Method and device for introducing additives into carbonaceous iron baths |
| DE1608619B1 (en) * | 1959-04-29 | 1969-09-11 | Polysius Ag | Device for feeding fine-grained or powdery substances by means of a carrier gas onto the surface of molten metal |
| FR2224546A1 (en) * | 1973-04-04 | 1974-10-31 | Krupp Gmbh | |
| US4045213A (en) * | 1974-11-28 | 1977-08-30 | Creusot-Loire | Method of injecting a powder containing carbon into a metal bath |
| FR2459835A1 (en) * | 1979-06-27 | 1981-01-16 | Sueddeutsche Kalkstickstoff | Molten iron treatment in converter - using oxygen contg. calcium carbide, so increased amt. of scrap iron can be added |
| BE893659A (en) * | 1982-06-25 | 1982-10-18 | Centre Rech Metallurgique | Top blown converter steel refining process - with fuel injection into oxygen jet |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3891196A (en) * | 1974-01-21 | 1975-06-24 | Thyssen Niederrhein Ag | Apparatus for treating a melt |
| US4264059A (en) * | 1980-03-12 | 1981-04-28 | Victor Benatar | Condition responsive control means for use in discharging powdered reagent into a pool of molten metal |
| LU82336A1 (en) * | 1980-04-04 | 1980-07-02 | Wurth Anciens Ets Paul | METHOD AND DEVICE FOR PRESSING AND FLUIDIZING A PULVERULENT MASS IN A DISTRIBUTION ENCLOSURE |
| US4286774A (en) * | 1980-04-22 | 1981-09-01 | Victor Benatar | System for automatically injecting a measured quantity of powdered reagent into a pool of molten metal |
-
1982
- 1982-10-27 LU LU84444A patent/LU84444A1/en unknown
-
1983
- 1983-09-20 CA CA000437113A patent/CA1210833A/en not_active Expired
- 1983-09-21 BR BR8305162A patent/BR8305162A/en unknown
- 1983-10-20 DE DE8383630175T patent/DE3375583D1/en not_active Expired
- 1983-10-20 EP EP83630175A patent/EP0110806B1/en not_active Expired
- 1983-10-20 AT AT83630175T patent/ATE32351T1/en not_active IP Right Cessation
- 1983-10-21 US US06/544,073 patent/US4519587A/en not_active Expired - Fee Related
- 1983-10-21 FI FI833858A patent/FI73463C/en not_active IP Right Cessation
- 1983-10-24 ZA ZA837907A patent/ZA837907B/en unknown
- 1983-10-25 PT PT77554A patent/PT77554B/en unknown
- 1983-10-26 ES ES526779A patent/ES8407570A1/en not_active Expired
- 1983-10-26 NO NO833910A patent/NO833910L/en unknown
- 1983-10-27 KR KR1019830005086A patent/KR840006371A/en not_active Withdrawn
- 1983-10-27 IN IN1322/CAL/83A patent/IN160933B/en unknown
- 1983-10-27 JP JP58201881A patent/JPS59133315A/en active Pending
- 1983-10-27 AU AU20667/83A patent/AU558520B2/en not_active Ceased
- 1983-10-31 AU AU20817/83A patent/AU2081783A/en not_active Abandoned
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE1608619B1 (en) * | 1959-04-29 | 1969-09-11 | Polysius Ag | Device for feeding fine-grained or powdery substances by means of a carrier gas onto the surface of molten metal |
| AT225213B (en) * | 1960-05-27 | 1963-01-10 | Oesterr Alpine Montan | Method and device for introducing additives into carbonaceous iron baths |
| FR2224546A1 (en) * | 1973-04-04 | 1974-10-31 | Krupp Gmbh | |
| US4045213A (en) * | 1974-11-28 | 1977-08-30 | Creusot-Loire | Method of injecting a powder containing carbon into a metal bath |
| FR2459835A1 (en) * | 1979-06-27 | 1981-01-16 | Sueddeutsche Kalkstickstoff | Molten iron treatment in converter - using oxygen contg. calcium carbide, so increased amt. of scrap iron can be added |
| BE893659A (en) * | 1982-06-25 | 1982-10-18 | Centre Rech Metallurgique | Top blown converter steel refining process - with fuel injection into oxygen jet |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0165198A3 (en) * | 1984-05-15 | 1987-03-18 | Arbed S.A. | Lance for accelerating solid particles |
Also Published As
| Publication number | Publication date |
|---|---|
| PT77554A (en) | 1983-11-01 |
| DE3375583D1 (en) | 1988-03-10 |
| CA1210833A (en) | 1986-09-02 |
| AU2081783A (en) | 1984-05-03 |
| FI73463C (en) | 1987-10-09 |
| FI73463B (en) | 1987-06-30 |
| JPS59133315A (en) | 1984-07-31 |
| IN160933B (en) | 1987-08-15 |
| ES526779A0 (en) | 1984-09-16 |
| FI833858A7 (en) | 1984-04-28 |
| ZA837907B (en) | 1984-06-27 |
| NO833910L (en) | 1984-04-30 |
| BR8305162A (en) | 1984-05-02 |
| AU2066783A (en) | 1984-05-03 |
| ATE32351T1 (en) | 1988-02-15 |
| KR840006371A (en) | 1984-11-29 |
| US4519587A (en) | 1985-05-28 |
| EP0110806B1 (en) | 1988-02-03 |
| PT77554B (en) | 1986-03-12 |
| FI833858A0 (en) | 1983-10-21 |
| AU558520B2 (en) | 1987-01-29 |
| ES8407570A1 (en) | 1984-09-16 |
| LU84444A1 (en) | 1984-05-10 |
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