EP1068364A1

EP1068364A1 - Method for alloying steels and device for carrying out the method

Info

Publication number: EP1068364A1
Application number: EP99924705A
Authority: EP
Inventors: Ralf Evertz; Stefan Evertz
Original assignee: Egon Evertz KG GmbH and Co
Current assignee: Egon Evertz KG GmbH and Co
Priority date: 1998-04-02
Filing date: 1999-03-27
Publication date: 2001-01-17
Anticipated expiration: 2019-03-27
Also published as: ATE209260T1; DE19814748A1; EP1068364B1; DE59900687D1; ES2168015T3; WO1999051785A1; US6383253B1

Abstract

Alloying and/or reducing powder is pumped directly into the steel melt at a pressure of at least 20 bar, preferably at least 40 bar, with at most 20% of a fluidizing agent and the powder is discharged from the delivery line by a plunger extending across the cross section thereof.

Description

description

Method of alloying steels and device for carrying out the method

The invention relates to a method for alloying steels by introducing metallic additives and / or reducing agents in powder form into a liquid metal melt. The invention further relates to a device for performing this method.

The present invention belongs to the field of so-called secondary metallurgy, i.e. aftertreatment of the steel produced, for example, by the fresh process in the converter or in the electric arc furnace. This post-treatment includes, in particular, the alloy setting of the steels, in which the desired metal surcharges are introduced. Possibly. additional deoxidation, decarburization and desulfurization of trace elements must be carried out in this phase.

From DE 42 37 177 AI a controllable mechanical metering conveyor system for dusty goods is known which presses one or more different types of dust in a quantity-controlled manner through a conveyor line with a final immersion lance into a pig iron melt. This metering conveyor system is used for blowing in, in particular for the co-injection of calcium carbide and magnesium dusts into pig iron melts.

Correspondingly, DE 44 00 029 AI also strives for controllable metered addition of additives in the electric arc furnace, in ladle furnaces or ladles. In all these cases, the pulverulent solid in question is introduced by means of a carrier gas which, according to the prior art, makes up about 80% and more of the total gas-solid mixture amount. Different flow or flow rates of the carrier gases used and the solids lead, however as a result, that precise metering or control of the alloying elements or alloying elements to be introduced in connection with deoxidizing agents is not possible, which has a negative effect on the quality of the alloy steel produced.

For this reason, when setting the alloy of the steel, a hollow body-shaped wire is used, in the interior of which the metals and / or deoxidizing agents are pressed in in powder form. This wire is wound directly into the bath by means of a winding machine, where the wire melts and releases the alloying elements. For example, wires with a diameter of up to 23 mm and a wall thickness of 0.5 mm are used, in which the filling material is arranged. The manufacture of such wires filled with powdery alloy elements is complex and expensive. In addition, the wire winding process has the disadvantage that the melting wire end is not always at the desired location below the bath surface, so that different concentrations of alloying elements result in the melt.

The cheaper and technically simpler technique, to let the alloy powder trickle from above onto the bath surface, has the disadvantage that, due to the existing bath movements, which are directed radially outwards on the metal bath surface, the alloying agents are rinsed on the edge of the pan or converter , where they adhere to slag deposits or the inner jacket of the melting tank. Since this happens in an uncontrollable manner depending on the different bath movement, this method also threatens an undesired alloy setting, which in any case does not correspond to the metal alloy surcharges.

It is therefore an object of the present invention to develop the method mentioned at the outset in such a way that with better 3

Dosing accuracy Alloy surcharges alone or alloy surcharges in connection with reducing agents are introduced into the melt in exact doses.

This object is achieved by the method according to claim 1, which is characterized according to the invention in that the alloy surcharges and / or the alloy surcharges and reducing agents as powder from a storage container via a delivery line directly to one or more lances and / or under bath nozzles (dry) in the Melt or in a mixture with a fluidizing agent, the proportion of which is blown in <20%, are introduced into the melt, the pressure to be used for powder conveying being at least 20 bar, preferably 40 bar, or the powder in the conveying line being by means of of a plunger covering the delivery line cross section.

The generally known blowing technique of solids via lances or under-bath nozzles is therefore used in a modified way that the additives concerned are blown into the melt dry (i.e. without gases or other fluidizing agents) under a delivery pressure of 40 bar or more, or that the quantity of the fluidizing agent is limited to a maximum of 1/5 in the gas-powder solid mixture and the mixture is blown in under a delivery pressure of more than 20 bar. The delivery pressure decreases in accordance with the friction losses towards the lance or under bath nozzle, whereby the pressure under which the powder flows out is minimized to values that are slightly above the ferrostatic pressure. Surprisingly, it has been shown that, despite the considerable frictional losses which exist and which, based on previous assumptions, have led to fears that a uniform input of the supplements is not possible, an optimal dosage can be achieved. It was also surprising that, depending on whether or not with a lower proportion of fluidizing agents Fluidizing agents is working, pressures between 20 bar and 40 bar are sufficient to overcome the existing frictional resistance.

Alternatively, there is the possibility of expelling the quantity of powder filled in the delivery line and / or lance via a reciprocating piston, which covers the entire delivery line cross section. In this method, the amount of powder that can be introduced is limited by the piston stroke and the cross section of the delivery line in which the piston is moved. The relevant conveyor line or lance section must be refilled after each powder discharge. The powder exit point on the lance is expediently closed during refilling by a cover which melts away when the lance is introduced into the melt.

Developments of the invention are described in the subclaims.

As already mentioned, however, fluidizing agents, such as small amounts of inert gas, in particular argon or nitrogen, or of liquid hydrocarbons, such as heating or diesel oil, heavy oil, waste oil, rapeseed oil or paraffin, can also be used. The use of liquid hydrocarbons, such as waste oil in particular, which burns in the melt, creates disposal options that prevent the treatment of waste oil as hazardous waste.

For example, powders with a maximum grain size of 1 mm, preferably a maximum of 0.1 mm, are preferably used, in particular for "dry" blowing without gases or liquids.

A fluidization of the powders is also possible in such a way that pressed alloy aggregates form a core which is covered with a shell containing a lubricant, for example made of paraffin, wax, oil or the like. Concerning core and Shell-existing particles can be used without adding further fluidizing agents (dry) or with further small proportions of gaseous or liquid fluidizing agents, which, however, should not exceed the amount stated in claim 1.

According to a further embodiment of the invention, the alloy surcharges are blown in in powder form via a pivotable lance.

This includes both swiveling movements that make it possible to move the lance outlet opening out of the bath, and also swiveling movements that allow different lance outlet locations to be set below the bath surface.

The lance is preferably designed as an annular nozzle and, in a further embodiment, as a double-walled ring nozzle, inert gases being blown into the melt through one of the double-walled outflow openings, as a result of which the lance is cooled and / or a melt stirring movement is generated. This stirring movement can be optimized if the lance outflow openings are designed in such a way that the inert gases flow out tangentially. The dry or fluidized powder, which consists of the additives, is then pressed in through the second outflow opening. In this way it is possible to use the pure inert gases blown in via the lance to generate different bath movements depending on the dosage of the additives, which should be more intensive the greater the amount of metal or deoxidation introduced per unit of time. In contrast to the methods known from the prior art, the dosage amount per unit time and the bath movement can thus be regulated independently of one another.

According to a development of the invention, a pressure between 50 bar and 100 bar, under which the powdery additives are injected, is applied. The method according to the invention described above, which can be used both in steelworks and foundries, offers several possibilities for adding alloy components, such as aluminum, silicon, magnesium, calcium, various carbides, into the melt: in addition to the volumetric dry transport via a metering and pressure piston, the volumetric Conveying the gas / powder mixture or the gas / liquid mixture, the gas or liquid fraction being at most 20% of the mixture. The fourth possibility consists in the above-described volumetric transport of the mixture with a "dry core" of the additives to be introduced and a moist shell or a paste-like powder mixture, which preferably consists of hydrocarbons which are lubricant-compatible.

This has the following advantages:

The proportion of fluidizing agents (inert gas, liquid) is reduced to a minimum. The dosing takes place via a volume measurement, which is more precise than the conventional gravitational method or flow measurement. The discharge pressure can be varied according to the flowability of the powdery solids. Finally, alloys can be adjusted to specification during treatments. The doses to be carried out can be carried out dust-free and with low emissions. Because there is no large amount of transport gas (as is customary according to the prior art) or only a small amount of fluidization in the feed product, the additives, the duration of the additives in the reaction area of the lance mouth in the melt also increases.

To carry out the method described above, a device is used in which a delivery line having a high-pressure pump leads directly from a storage container to a lance or an underbath nozzle. This measure considerably reduces the energy investment compared to conventional techniques. The maintenance and repair work is also reduced. Further developments of the device described are described in the subclaims.

According to a further development of the invention, the delivery line has an air or liquid inlet, preferably with a controllable metering device depending on the quantities conveyed from the storage container, whereby the desired mixing ratios of powder: (fluidizing agent or lubricant) can be set.

The lance has a double jacket with two outflow openings, one of which flows through the powdered metal or reducing agent, which may be fluidized, and through the other inert gases. The outflow opening or outflow openings of the lance are ideally arranged to open tangentially. The lance itself is preferably pivotable. The bath (the melt) can be arranged in a converter, a pan or a torpedo car.

Embodiments of the invention are shown in the drawings. Show it

1 shows a schematic view of a device according to the invention,

Fig. 2 is a schematic enlarged view of a

Inlet point in the delivery line for the fluid admixture,

3 shows a cross-sectional view of a lance with tangential outflow openings and

Fig. 4 is a longitudinal cross-sectional view of a lance with two outflow channels.

The device shown in Fig. 1 consists essentially of a metallurgical vessel 10 with a melt bath 11, in α P- et P- er ι-a NP "TJ φ d er to" σ T Ct j - • n to Ct rt d = Cd o ω and others cn α tr <P d et dd Φ d Φ Φ d DJ: d P- DJ Φ P- φ Φ d φ Hl DJ P- φ Φ d σ dd O Φ P- Φ DJ: φ P- d DJ

P d P cn Ω d P ^J dd 'ω Ω cn P- P φ EP among others P d Φ rt ≤ s: d 3 P- P dd cn

Ω φ • τ P- tr Φ and others <! Φ Φ P- - rt cn <! DJ P- cn • Φ uq P d Φ d = Ct rt σ and others d ^* PT d rt dd cn Φ N rt rt cn TS Φ PP ^J rt P ^J Pl DJ Φ P- d and others φ d Hl Φ ^ and others φ HN P- rt DJ P § d N d rt P- P rt φ Φ IV) φ φ P> Φ d "P rt cn 3 and others P d O: P ¹ P- O

Φ Φ <rt ^* dd cn P- rt d O Φ cn cn P- Ω Oπ P- 3 Ω Φ Pi Ct P oo d VO

Pi to P- Φ Φ cn P o ua Hi rt NP ^J N dd ^* d Φ φ α tr tr • P ¹ Φ 3 φ VO d: o P Φ er tr p- er er Ct d Hi cn P d IV) Φ Φ P d Φ Φ P- Φ et P - ~ J d P- d Öi tr tr Φ Pi P- Φ 3 Ω N Φ Φ d Ct ^ CO and others P ¹ P- P- P- P- DJ d 3 Φ Φ t and others d ρ <^ j

PPO d? φ tr ≤ -> P rt Φ cn Φ 3 Φ Hi and others Ω? d <nd P φ φ rt DJ oe rt IV) P Φ DJ d et • er Φ cn DJ P- H d = d: rt tr uq d ω d 2 Φ Ct d P- DJ Φ d ω <X> 3 dd • Φ P- P cn nd: er P et σ φ 3 DJ d P- d rt dd PN s: o "* • d φ TJ s: 3 d ^* * XI φ α d ^" φ Φ d Φ uq Ό φ cn rt cn D - d cn d ^" Φ φ DJ τ rt α P- d Φ DJ Hi o φ PP er d? φ Φ P- Φ Ω o rt o Ct and others DJ

P P- d 3 P- * « _* P- du Pl Φ et * - P rt d Φ ua DJ er d er P tr cn P- 3 P- Φ P ¹ et d cn p- d Φ φ <! d et er P- Φ o φ Φ Φ d Φ d φ α φ Φ d p- o φ er er IV)

Φ ua rt ia 3 P Φ d Φ P ^J P P- d P- P Hl ddd DJ 3 P- Φ d φ d φ P- _* d to Φ f p- ir ¹ P uq J Ct φ σ dd rt DJ rt cn

* ia P- ia P cn d d: et φ

P- rt O DJ rt DJ Ct uq P- ¹ Φ cn ^ p- ^ φ ua Hl φ s: cn Φ d cn <! 3 φ er Ct Φ P-

Ω P et ddo φ P- Pi cn Φ cn? Σ DJ d: P- cn DJ 3 Φ O P- Φ Φ P d et tr P- Φ DJ Φ N Ό 3 d D ⁾ IV) cn P- d ta Cn cn P 2 P DJ cn φ 3 Φ P rt T3 P rt and others

Φ et Φ PP "P- φ Ό P- co .fc- rt cπ Ω P- p- Φ Φ Ct cn σ d PP rt d ro Φ cn drd *» φ cn pσ DJ cn O 'Ct d P- Ct EP • Φ ua D tr P- Φ Φ P- DJ rt cn d Φ O IV) φ P ^< Ω P- Ct N rt rt P- ua O d P- Φ p- tr rt P DJ: Ω P- cn α DJ

Φ ua d tr CD P et s: d "Ω P- cn d O er d cn et φ P- sd DJ: d P ^J d- φ d rt oddd _^ P- DJ Φ d- di P Hl DJ d P- Φ φ Φ d P- t, Ω rt rt he P Φ " _^ σ Ω et 5Ξ Φ CΛ Φ d cn rt P- Hi P ua φ P- P P- DP Ω Φ rt Φ? Rdd Φ Hl Φ tr σ Φ φ d: Ω Ct d rt φ t → \> P rt do P- d ^" p- φ P P- d P- O: o P- P rt d cn P ^ d er d" s: P- Φ d DJ ia DJ ^ ia Ct dd <- Φ cn Ω rt d P Ct cn ia ia P d cn Hl _^

P α P "Φ DJ P- ia P uq d φ d - Φ Φ dd P- P p- d ^' φ φ o Φ Φ 3 3 rt

Ω TJ Φ d P 3 φ 3 uq - N d: Pi cn and others d = Φ rt Ct PP ¹ dd O d and others P- Ό D ⁾ : € co tr H d P- o DJ O: Ct Φ cn φ cn O: cn cn cn P d DJ 00 TJ Φ ua φ 3 Ω o cn Φ • Ct α rt φ d ua Φ d cn P TJ 3 ro cn Ω dd P Cd cn 3 rt <er Φ P- "er rt P - P- Φ rt er cn H "P rt P- Ct Pi p- tv> P- tr d uq uq p- O P- P- o Φ P ¹ rt Φ φ

P -> LSI cn d DJ Φ and others P- P- d IV) uq φ φ rt and others Φ and others Φ Φ d s: P "d 3 P d 2 O P-

O: Φ d P- dd Φ Ω <v D cn 7 - P P- rt Φ? 3 d cn ω o ¹ α DJ and others Φ Φ P>

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3 he P- cn φ Φ <! Φ cn P φ α 00 P TS ^• » ^' ddd Ω cn cn d O d tsi and others DJ φ N Ω 3 rt ddd and others IV) P- O: rt 3 - 3 φ φ Ct 3 cn and others d tr rt • _^ φ ω d rt dds: tr P- DJ d DJ <cn Hl P- d φ P- et d Φ P- P- rt P- rv Φ d Φ Hl • N ua • rt - ua Ω t ^"1 • φ Hi cn s: dd cn P- d rt d tv> Φ φ o ≤ rt P φ d: Φ

Φ? rt d ^* D ⁾ α d P- Ω o rt and others rt Φ> α o P d- φ d P- tr α d oo DJ Φ P- IV) d ^ Φ DJ d P tr et Φ Φ d cn σ rt- er Φ o 2 d P P- DJ er! V> d ¹ cn ^ 1 et N P- ω dd α d P d ≤ P- cn P- Φ d P- D DJ d Ω 3 Φ φ d Φ d

N d • _^ Ω Φ Φ ia cn ia er P Φ d P- d rt DJ d P Ct P d rt 3 d cn cn

€ Φ d ^" d 3 • DJ \ -> φ P- Ω D ω P Ω P Ω d P- H" Φ φ DJ among others

• P- d: P- φ 3 P- d DJ d D tr P P- Ct to d ^" • Φ ^' et Ω φ including DJ d P- ¹ <cn P d er dd tr CΛ cn oo cn d P- α d Ω φ P- rt Hi P-? cn Φ cn et o tr ¹ P- t cn Φ d: rt rt - ω Po IV) Φ Φ cn Ω tr d Ω Hi φ DJ P cn DJ ≤ ua P Φ DJ rt n

Φ HP to IN) DJ • rt Φ Cn rt p-? • tr φ Φ φ d 3 O: Φ cn p- Φ P P- d rt H cn d P- d P ¹ d ^ P d tr ¹ » _* Ω 3 rt P- d 3 r <s: p- P d P 3 DJ rt N cn

Ω Φ et Ω cn rt Ct P- d O: DJ d- <P- σ dd Ct Φ φ rt α • P- rt d Φ O: Ö tr P DJ d ^" Ω and others p- 3 d Ct d α 0 rt P- d φ Φ co P- d rt Φ • cn ω d Pi s: rt cn rt tr P- Ct • d φ d P- N DJ Φ d Φ ia d rt 1 et Φ P Ω er ia Pi SO

P- ia d cn Φ Φ d et Φ Φ cn P- et Cd DJ d rt cn d ^" Φ Ct 1 o

P DJ d DJ: rt P _-- et d Φ α P- dd cn Φ ia 1 P> P- o 1 cn ia ua P- 3 Φ d Ct ia d Hl oπ φ Φ dd cn 1

can be regulated independently of the flow of the aggregate (alloying agent, reducing agent).

Pumps and dosing devices of the type used are basically known according to the prior art, for example from the cement industry, in which mixed paste-like cement is conveyed under high pressure.

The metallurgical vessel 10 can be a pan, a torpedo car or a converter.

Claims

10 patent claims

1. A method for alloying steels by introducing metallic aggregates and / or metallic aggregates and reducing agents in powder form in a liquid metal melt, characterized in that the alloying aggregates and / or the alloying aggregates and reducing agents as powder from a storage container via a delivery line directly to one or several lances (12) and / or under bath nozzles are introduced into the melt or in a mixture with a fluidizing agent, the proportion of which is <20% of the amount blown in, into the melt, the pressure to be used for powder conveyance being at least 20 bar, preferably 40 bar, or or the powders in the delivery line are expelled by means of a plunger covering the delivery line cross section.

2. The method according to claim 1, characterized in that the powders are fluidized or pasteus by adding small amounts of inert gas, such as argon or nitrogen, or a liquid hydrocarbon, such as heating oil / diesel, heavy oil, waste oil, rapeseed oil or paraffin.

3. The method according to claim 1 or 2, characterized in that the powders have a maximum grain size of <1 mm, preferably <0.1 mm.

4. The method according to any one of claims 1 or 2, characterized in that the powder is injected in a pressed form as a core with a shell containing a lubricant. 11

5. The method according to any one of claims 1 to 4, characterized in that the powder is injected via a pivotable lance (12), which is preferably designed as an annular nozzle.

6. The method according to any one of claims 1 to 5, characterized in that the lance is double-walled and that inert gases are blown into the melt through one of the double-walled outflow openings, thereby cooling the lance and / or producing a melt stirring movement, in particular by tangential outflow of the inert gases from the lance.

7. The method according to any one of claims 1 to 6, characterized by a pressure between 50 bar and 100 bar.

8. Apparatus for carrying out the method according to claims 1 to 7, characterized in that from a storage container (17) has a high-pressure pump (16) having delivery line (15) leads directly to a lance (12) or under bath nozzle.

9. The device according to claim 8, characterized in that in the delivery line (15), an air or liquid inlet (20), preferably with a controllable metering device depending on the quantities fed from the reservoir (17).

10. Device according to one of claims 8 or 9, characterized in that the lance (12) has a double jacket with two outflow openings, one of which flows through the powdered metal or reducing agent, which is possibly fluidized, and through the other inert gases . 12

11. Device according to one of claims 8 to 10, characterized in that the outflow opening (s) open tangentially from the lance (12), which is preferably pivotable in the bathroom.

12. Device according to one of claims 8 to 11, characterized in that the bath is a pan, a torpedo car or a converter.