EP1543171A1

EP1543171A1 - Rotor, device and method for introducing fluids into a molten bath

Info

Publication number: EP1543171A1
Application number: EP03769205A
Authority: EP
Inventors: Ralf Scheid; Reiner Bauer
Original assignee: Hoesch Metallurgie GmbH
Current assignee: Hoesch Metallurgie GmbH
Priority date: 2002-09-19
Filing date: 2003-09-18
Publication date: 2005-06-22
Also published as: DE10393540D2; WO2004029307A1; AU2003277809A1

Abstract

The invention relates to a rotor, a device, and a method for introducing fluids into a molten bath. Molten baths are often degassed by introducing a liquid. In known trough degassers, rotors are arranged in the flowing melt and are used to introduce the fluid. Said rotors enable the fluid and molten metal to be mixed thoroughly, but damaging eddies can also occur. The aim of the invention is to improve one such trough degasser in such a way that fluids are mixed better with a lower risk of eddy formation. To this end, rotor buttons (30) provided with concave lateral grooves (31) are arranged on the rotors. The trough degasser also comprises rotors and dividing walls such that at least two rotors are arranged between two submerged walls. In the inventive method, the molten metal also flows through a contact chamber comprising at least two rotors. In this way, the aim of the invention is achieved to a surprisingly large extent.

Description

Rotor. Device and method for introducing fluids into a molten metal

The invention relates to a rotor, a device and a method for introducing fluids into a molten metal.

The task in the metalworking industry is often to bring molten metal into a desired shape with desired properties by casting or comparable processes. All processes in which a molten metal is to harden and ultimately fulfill certain properties are to be understood as comparable here. The metal melts are usually removed from a melting furnace or similar devices before entering the casting or hardening phase. Most of the time, however, they do not have the required purity at this point and thus threaten. to influence a resulting metallic product in its properties in a hardly predictable way. It is therefore advisable to subject the metal melt to an intermediate treatment after it has left the melting furnace and before it is processed.

For example, hydrogen inclusions, non-metallic inclusions and reactive components are found in the molten metal as it emerges from the melting furnace. When the metal cools, the hydrogen comes out of the solution and creates pores in the solid metal. The non-metallic inclusions also remain in the metal during cooling and can contaminate it to an uncertain degree. The reactive components also remain and influence the physical and / or chemical properties of the end product.

As a tried and tested means of removing the unwanted components from the molten metal in good time. the degassing has prevailed. In this method, an inert gas or a reaction gas is injected into the molten metal by suitable devices. This has a lower density than the melt and rises in bubble form to the surface of the melt. On the way up, it adsorbs the unwanted dissolved gases and carries them with them to the surface of the melt. At the same time, it induces a certain flow as it rises, which also drives the non-metallic inclusions to the surface with the bubbles and usually also holds them there. these can then easily removed from the metal melt. Certain gases can even react with the reactive components in the melt and bring them to the surface in the same train

In principle, the method can essentially be used at three different locations, namely either inside the melting furnace, in a separate crucible or in flow, preferably on the direct route to casting. The latter two advantages are advantageous compared to degassing within the melting furnace the molten metal on the way from the melting furnace to the casting table through a channel. It has been found to be useful to arrange the degassing device in the course of this channel. The molten metal is treated here while it flows through the channel on the way to the casting table. Therefore, in the case of such degassing devices, one speaks of “ Rmnenentgasem "

It is therefore the essence of the puncture degasser. that the metal melt is only in the area of the degasifier for a relatively short time. However, what is decisive for the quality of the degassing is to bring the introduced inert gas or, in general, the injected fluid as close as possible into contact with the metal melt.The intensity is determined on the one hand by how as long as the introduced fluid remains in contact with the molten metal. On the other hand, the size of the reaction surface, that is the total surface of the injected fluid bubbles. crucial for this

These two essential parameters. Contact time and contact path are improved in a channel degasser in that the metal melt has the highest possible level in the area of the fluid injection and that the fluid is injected into the melt with the smallest possible bubbles

In order to obtain as many small bubbles as possible in the melt, it has become established to provide the gas projectors with fast-rotating rotors in the area of the fluid injection. The sharp-edged rotor heads break any larger fluid bubbles into many small bubbles when they exit the injector

A conventional channel degasser and information on the degassing process can be found, for example, in WO 95/21273.This application describes in detail many aspects that need to be taken into account in the degassing of the gutter, and at the same time reveals a number of exemplary embodiments. In particular, various designs of rotors are disclosed, by which Fluid m the molten metal is injected In all variants, channel-like openings through which the fluid flows outwards when the rotors are in operation are shown, which are delimited on the outside by the said sharp edges The sharp edges can even extend in square side channels up to the upper end of the rotor head

DE 697 00 963 T2 discloses a rotor which proposes a substantially parallelepiped-shaped rotor blade arranged radially around a central shaft below a cover disk, in which the second rotor blade is reduced by a recess at the lower edge. This is intended to reduce turbulence on the surface of the molten metal As a device of older technology, the document also shows a rotor head with the same design, radially outstanding and essentially elongated parallelepiped-shaped rotor blades which lie parallel to one another on a central shaft

In order to avoid cavitation phenomena on the rotor, DE 197 03 062 C proposes a rotor head with a largely closed, smooth surface. The smooth surface is only broken through by necessary openings in the interior of the rotor head running tubular channels. The openings have a slight oval shape in the surface of the Rotor head because the channels meet the surface at a slight angle

JP 01259135 A shows in FIGS. 1 and 2 a rotor with a likewise largely closed rotor head. In particular, this has an almost smooth area on its bottom surface.This is only covered by very shallow grooves into which gas flows from a collecting space via various feed holes Zuftihrlocher are distributed along the entire grooves on the bottom surface of the rotor as only a very small amount of gas can remain in the flat grooves during rotation. The rest flows over the smooth surface of the rotor and directly hits the outer contour of the rotor head in the rotor 6 and 7, an alternative embodiment is proposed. Here, the rotor head has deeper grooves on its bottom surface. In this construction, at least a larger part of the gas supplied to the rotor head can flow outwards in the grooves, where it flows into rectangular notches and is broken up there

JP 07055365 A discloses a rotor with a mixing disk, within which inflowing gas can be introduced via a distribution channel through a molten metal. The distribution channels are connected to a central gas supply inside the rotor head and run through teeth of the mixing disk to the outer surface of the disk. The channels are rectangular and open to the bottom of the pane

US 5,160,693 shows a rotor head for introducing gases into metal melts, in which a tubular central gas guide ends at the lower end of the rotor head and the gas radially around the entire cylindrical circumference at the lower end of the rotor head m flows out in all directions In the molten metal it rises and meets a solid flange, along the bottom of which it flows outwards There it meets isolated narrow teeth, which are arranged along a curved flange outer contour An outwardly directed deflection lip is arranged in the middle of the curly flange outer contour between two teeth

WO 00/73240 AI shows a rotor disk for mixing a molten metal, the disk optionally having gas nozzles on circumferential profiles. The gas nozzles are fed by a central gas supply and lie on the profiles relatively close to the envelope of the rotor disk

Some other publications, for example in US Pat. No. 3,849,119, US Pat. No. 3,870,511, UK 1,400,338 and US Pat. No. 3,839,019, also show alternative configurations of fluid injectors with rotors

Now it is common to all these rotors that they break up the injected fluid increasingly better into small bubbles at higher rotational speed.While this is exactly the desired effect, the risk of a vortex formation of the melt increases along the surface of the injector as soon as a vortex is formed In an undesirable and uncontrollable way, on the one hand, outside air, but also the undesired melt inclusions carried to the surface by the injected fluid, are re-introduced into the melt. When the vortex reaches the effective range of the rotor, the unwanted components are even distributed relatively homogeneously in the metal melt

A large number of arrangements of the injectors and of different variants of the design in the area of the channel degasser can also be found in the prior art, in particular there are also built-in baffles after each rotor in WO 95/21273. However, all of these designs are only unsatisfactory in able to distribute the fluid introduced while avoiding the risk of harmful and unwanted vortex formation

The inventor has therefore set himself the task of developing a rotor, a device and an associated method, by means of which a fluid to be introduced can be introduced into a molten metal in a significantly more homogeneous and finely divided manner and at the same time minimizes the risk of vortex formation on the injectors becomes

This task is solved surprisingly well a rotor for receiving fluids in a molten metal, the rotor comprising a shaft and a rotor head attached to the shaft. which has a lateral surface with a component parallel to an axis of rotation of the rotor and which is characterized in that. that at least one side channel with a concavely curved cross section is provided in the lateral surface,

a device for introducing fluids into a molten metal, the device having a melt channel and in the course of which a contact area, in which the fluids are introduced into the molten metal, with rotors arranged there, with baffles, in which at least two rotors are arranged between two baffles. are net, as well

a method for introducing fluids into a molten metal, in which the fluids are introduced into the molten metal by rotors arranged between baffles, each delimiting a contact chamber in pairs, which is characterized in that the molten metal flows through a contact chamber with at least two rotors

The rotor achieves astonishing advantages with the side surfaces with a concavely curved cross section provided on the side surface. The fluid bubbles are broken up well in a wide range of speeds and are thus formed into many small bubbles. Fluid bubbles emerging, which adhere to the surface of the rotor at first hiking upwards can neither escape the chopping action of the edges nor are they jerkily accelerated, as is the case with angular channel shapes and which leads to elongated bubble shapes, which affects the chopping action.Rather, they are constantly accelerated within the side walls until they finally Reach the side surface in an even more rounded shape and be chopped up by the sharp edges. In addition, there are considerably fewer whirlpools than with known rotors

The fluid can flow to the rotor head via a fluid supply, which is preferably designed as a fluid passage in the inside of the shaft. In the rotor head, it can be diverted via a fluid distribution in such a way that it flows into the side channels in the lateral surface of the rotor head. The fluid distribution can have channels which carry the central fluid supply connects the side surface, in particular directly to the side channels in the side surface It should be pointed out that although a side channel of the proposed type m of the lateral surface of the rotor is able to support the homogeneous distribution of the fluid to be introduced in the molten metal, in particular a plurality of lateral sides with a concavely curved cross section in the lateral surface of the rotor head should be considered Experiments have shown excellent results with four to twelve, in particular six to ten, preferably eight or about eight. Pages of this type have been found to be particularly effective

In the present context, the lateral surface is an envelope of the rotor head that runs around the axis of rotation and thus always comprises a component in the tangenural direction about the axis of rotation. It then also has a component parallel to the axis of rotation. if the normal on the side surface is not parallel to the axis of rotation The side surface is therefore not a surface lying in a normal plane to the axis of rotation, such as a bottom surface or a cover surface. Here we mean side surfaces, such as those on cylinders as a surface and / or can be found analogously on conical or frustoconical bodies. The rotor head is preferably constructed point-symmetrically or rotationally symmetrically with respect to its axis of rotation. In this way it can rotate as balanced as possible about the axis of rotation

The lateral surface is thus an outer surface on the rotor head.Many cases, particularly in the case of a configuration of the rotor head in the shape of a cylinder or cone or truncated cone, can coincide with the lateral surface of the rotor head. In the case of a conical rotor head, a development of the lateral surface accordingly results in a circular area In the case of a truncated cone-shaped rotor head, a development of the lateral surface essentially results in a circular surface. The lateral surface does not run completely continuously, since at least the proposed lateral grooves are arranged in it and these take up part of the lateral surface

For example, the lateral surface of a conical or frustoconical rotor head with its surface normal to the axis of rotation of the shaft or also of the rotor head may assume an angle of approximately 10 ° to 30 °, preferably approximately 15 ° to 25 °

According to the invention, the sides are to have a concavely curved cross section. An envelope of a section through the rotor head at any height of the axis of rotation always has a circular shape. If the rotor head has side channels, these can be recognized in the guided cut by the fact that the outer edge profile of the sectional figure is at the height of the side channel deviates from the envelope These deviations then go from the course of the circle on the envelope in the direction of Inside the circle, until you come across the enveloping circle again in the further course. Due to the symmetry, the outer edge course of the guided cut deviates several times in the described shape from the circular envelope. Also due to the symmetry, the outer edge course of the guided cut has between the areas, m which he runs with the envelope, preferably at least in pairs the same shape

It is particularly advantageous if the sides are exclusively concavely curved, so that their respective course does not have a point that points outwards. Any point in the course that points outwards can behave like a deflection lip when the rotor head rotates, so that fluid flowing upwards through the side channels can experience a sudden radial acceleration to the outside and thereby leave the rotor head as a large fluid bubble through the opening of the side channel without the bubble being able to be broken at the boundary edge of the side channel. In contrast, an exclusively concave curved side channel ensures a very Controlled guidance of the fluid so that it flows along the shape of the side channel onto the laterally delimiting edges. As a result, the present invention differs considerably from US Pat. No. 5,160,693

The lateral surface according to the invention is cumulatively or alternatively characterized in that between those points at which the outer edge profile of the sectional figure leaves the envelope. and those points at which the outer edge course of the sectional figure again joins the circular envelope, the outer edge course of the sectional figure has curved sections over the entire connecting path and that these curved sections are curved against the curvature of the envelope

It is advantageous if at least one of the side channels extends from channel openings in the direction of the shaft, the channel openings being caused by channels that point essentially radially outward from the axis of rotation. The fluid or inert gas introduced can pass through the channels, which are known per se, to the outside Leaving the rotor head If the side channels are directly connected to the channel openings or if they propagate from the upper area directly in the direction of the shaft, i.e. upwards, through the side surface during operation, injected fluid bubbles that adhere to the rotor can immediately enter the side channels arrive without having to walk along the envelope beforehand, from where they could tear off without being chopped off. A connection of the described type thus again requires the degree to which the fluid bubbles are chopped up. Cumulatively or alternatively, the channels can have channel openings which have at least one area. the is open vertically upward It goes without saying that the arrangement of the channel openings is also advantageous regardless of the usual features

It is particularly advantageous if the channels in their radial fluid guidance only meet the side channels, not directly on the side surface.This ensures a targeted inflow of the fluid to the side channels.Therefore, the present invention differs significantly from JP 07055365 A in particular In the present invention, the channels preferably already hit the side channels in the interior of the rotor head and already open up there into the side channels

It is particularly advantageous if the channels meet the sides of the rotor as deeply as possible inside the rotor head, i.e. as close as possible to the axis of rotation. In the case of symmetrical sides, it is also preferred if the channels meet the side channels in the middle, that is to say at their respective mirrors. Symmetry axes in the middle of the curved sides of the sides If the fluid flow passes relatively far inside the rotor head from the channels into the side gutters, the fluid in the operation of the rotor is advantageously guided in the side gutter as long as possible. The arrangement also enables the rotor to be run in opposite directions with the same quality of result. In contrast, the rotor disk according to WO 00/73240 AI is hardly applicable on both sides. In addition, the gas nozzles there meet the profiles relatively far outside, so that the advantageous possibility the guidance of the fluid along the concave profiles is not used anyway. However, this is not considered in the rotor disk proposed there anyway, since the profiles do not have sufficient extension in the direction of the rising gas, that is to say parallel to the axis of rotation

In a particularly preferred embodiment of the proposed rotor head, the channels are open in the direction pointing away from the shaft and have a channel height of at least about a quarter, preferably at least about half, particularly preferably at least about three-quarters of the width of the side. at the same time, however, preferably also with a channel height of at least approximately half, preferably at least approximately three quarters, the width of a tooth between two adjacent side channels. Surprisingly, extensive tests have shown that such a proportioning between channels. A particularly excellent breakdown of the fluid takes place in the side channels and teeth. Among other things, this results in better guidance of the fluid in contact with the molten metal to the outside, which is not the case, for example, with the rotor according to JP 01259135 A. In a further advantageous embodiment, the channels have a cross section which is variable along the axis of rotation. which expands into an embossing direction of the rotor. The immersion direction here is understood to be the direction which, when the rotor has not yet been immersed, points in the direction of the molten metal If the channels widen along the axis of rotation, this has the consequence that the fluid to be introduced into the molten metal m a stream that has a variable width m reaches the molten metal. Specifically, the fluid to be bound will be due to the Compared to the lower density of the molten metal, fit into the upper boundary of the channel and therefore the fluid flow widens in the direction of the bottom surface.When the channel widens downwards, the outflow velocity of the fluid from the rotor head decreases with the depth due to the continuity of the flow In particular, the lower layers of the fluid flow emerge from the rotor head at a comparatively low speed. After the fluid has been chopped up, the low speed at which it is discharged means that the resulting bubbles are still in the effective range of the rotor head and - if necessary, by adhesion or Turbulence remaining on the rotor head - with an increased likelihood of being chopped into smaller bubbles again at the upper area of the rotor head. This results in a better distribution with smaller bubbles

The immersion device can in particular lie parallel to an axis of symmetry of the rotor shaft. It is directed from the shaft to the rotor head, since the rotors are usually immersed in such a way that the rotor head gets into the molten metal, while the shaft at least partially often remains largely outside the molten metal

A widening of the cross section of the channels along the axis of rotation is understood to mean those sections of cutting planes which are perpendicular to the axis of rotation and which do not lie in the material of the rotor head, but rather between material sections in the air space of the channels - delimited externally by the lateral surface - lie, become larger in the direction of immersion. The channels can expand in particular in the rotor head towards the free end of the rotor head, ie facing away from the shaft

It is particularly advantageous here if the channel cross section does not widen to a subtle extent in the immersion direction, but rather a degree of expansion increases with the immersion direction

Widening is understood to mean the differential Mali with which the channel cross-section follows widening towards the bottom This geometry on the rotor head means that the speed of the exit decreases more than linearly with increasing depth. It has been found that the mechanism caused by the widening occurs as a result to an increased extent

More precisely, it is advisable to design the channels so that the degree of expansion increases by leaps and bounds.Selecting the channel geometry in a targeted manner can, for example, ensure that the fluid over a certain height at a constant speed and then downwards with a decreasing speed from the rotor head It has been shown empirically that the gas bubbles are broken up particularly well here

The configuration of the channels and / or the corresponding channel openings with a variable cross section is also advantageous, regardless of the other features of the present invention, these advantages already being apparent in the corresponding configuration of only one channel

As an alternative and cumulatively, it is recommended that the channels lie between teeth that have a length of at least 40 mm along the side surface. Teeth are defined here as bodies that lie between two adjacent channels and that define the channels in the tangential course around the rotor head at the height of the teeth and thus also at the height of the channels, these two elements are therefore preferably found alternately. Therefore, the envelope around the teeth generally forms at the same time that part of the lateral surface which is in the high area of the channels

It has been shown in tests that the teeth should have a length of at least 40 mm in order to achieve a satisfactory degree of homogeneous breaking up of the introduced fluid. With shorter teeth, the desired mechanism also occurs, the probability of multiple chopping of the ascending fluid bubbles on the sharp edges of the teeth, however, it is hardly possible to speak of a satisfactory result below the limit mentioned

In addition, it is advantageous if the rotor head m has an immersion direction on the shaft and has a cylindrical fluid space.Through such a rotationally symmetrical fluid space, a point is created at which the fluid collects before it flows through the channels m the molten metal.This results in the continuity of the flow due to the continuity on the one hand, the vertical speed of the inflowing fluid is reduced, which leads to a calming of the flow within the rotor head and enables the fluid to an increased degree along the upper wall of the channels emanate. On the other hand, material for manufacturing the rotor head is of course also saved and its weight is reduced.

It is recommended that a passage running essentially with the axis of rotation in the rotor shaft for introducing the fluid opens into the fluid space with an opening area of at most 64 mm ² , preferably of 12 to 36 mm ² . The passage should also run along an axis of shaft rotation and be filled with the fluid to be introduced above the shaft. The fluid therefore flows along a certain distance at an at least partially very strongly heated passage wall, as a result of which it can also be strongly heated. In the case of a mouth surface, essentially the cross-sectional area of the mouth, which is limited to 64 mm ² , the fluid to be introduced flows into the space at a relatively high speed and advantageously swirls the fluid in the space and the melt located nearby, so that a finer distribution of the fluid in the melt can be ensured.

If the mouth surface is too small, fluid may possibly be added to maintain sufficient pressure under the melt surface. It is therefore also advisable to provide a mouth area of at least 12 mm ² . The fluid space and the configuration of the mouth surface also show the described advantages independently of the other features of the present invention.

The rotor has a particularly advantageous suitability regardless of the other features of the present invention. when the rotor head has a substantially frustoconical shape. With such a shape, different speeds occur on the circumference of the rotor head. This is particularly advantageous when the rotor head tapers in the direction of the shaft, since then lower speeds occur on the circumference of the rotor upwards, that is to say during operation in the direction of the molten metal surface.

On the one hand, it has been found that if there are low speeds at the upper end of the rotor head, the risk of vortex formation is drastically reduced. The degassing process can therefore be carried out with increased rotor speeds and / or lower immersion depths in the molten metal than is the case with conventional rotor heads. This is reflected in increased process reliability with a simultaneous increase in process quality.

Furthermore, comparatively high peripheral speeds occur at the lower end of the rotor head. Fluid bubbles escaping there are broken up with a comparatively high momentum. This results in good breakdown results in the lower area of the emerging fluid, which are then improved in the course of the ascent along the rotor head

In addition, a frustoconical surface also results in a flatter and thus more homogeneous distribution of the fluid bubbles in the metal melt. Since the bubbles tend to rise essentially vertically upwards through the metal melt, it is of great advantage here if the area in which the Bubbles m enter the melt, a comparatively large horizontal surface coverage is achieved, which means that when projected onto the surface of the melt, a circular disc results. With increasing difference between the upper and lower circumference of the rotor head, this base area of the ascending bubbles becomes larger. For comparison, this base area can be seen with a zyhndπ- Rotor head zero, since it only results in a circular ring on the melt surface

In addition, the high shear strength of the molten metal in combination with the downwardly widening rotor head - conical or in some other way - induces a secondary flow whereby the melt is mixed more intensely and the ascending bubbles are removed from their vertical ascent path.The bubbles thus pass through a longer one Range within the molten metal

In a recommended embodiment of the rotor, the rotor head is fastened to the shaft by means of a self-sealing fastening means.This is preferably a thread or a bacconet lock, whereby these should be designed so that they are under the load which occurs when the rotor head rotates As a result of the resistance of the molten metal as torque, tighten it. As a result, as little melt as possible enters the slot between the head and shaft without the use of other means, regardless of the other features of the present invention. This makes it easier to replace a rotor head, if necessary

Further advantages can be achieved - if necessary also independently of what has been said - if the lateral surface of the rotor head at a transition seam between the rotor head and the shaft merges essentially flush into a lateral surface of the shaft.This in particular achieves two advantages.Firstly, a smooth transition is made more difficult a possible accumulation of molten metal residues, which also ensures better detachability of the rotor head. On the other hand, there are no speed jumps at the circumference of the transition between the shaft and the rotor head. This significantly reduces the risk of vortex formation The transition seam here is understood to mean the point at which the rotor head adjoins the shaft along the circumference. The transition seam therefore borders downwards on the lateral surface of the rotor head and upwards on the lateral surface of the likewise rotationally symmetrical shaft. A flush transition is understood to mean that at the transition seam neither the lateral surface of the rotor head nor the lateral surface of the shaft have a tangential surface perpendicular to the axis of rotation

The results achieved in this way can be improved even more if a transition at the transition seam is essentially concave with respect to the lateral surface of the rotor head and the lateral surface of the shaft. Experiments have shown that an essentially concave transition from rotor head to shaft is undesirable can be avoided

It has been shown that, alternatively and cumulatively, it is advantageous if the shaft tapers towards the rotor head. As the depth increases, the shaft thus has a decreasing circumferential speed in the molten metal.This also minimizes undesired swirls Essentially a truncated cone shape

Regardless of this, it is advantageous if the shaft is fastened to a shaft receptacle by means of a self-sealing fastening device. The shaft receptacle is generally arranged above the melt level and has a fastening device for the shaft. It is essential that the shaft be removed from the shaft receptacle with the simplest possible means A thread or a bayonet lock are preferably used for the self-sealing fastening device, which tighten themselves under load when the rotor is running.This simply and reliably ensures that no splashes of the melt can penetrate into the slot between the shaft and the receptacle Hardened metal can make it difficult to detach the shaft from the holder and can also destroy seals located there

It is also advantageous if the shaft has axial projections. In general, the shaft will have a rather smooth surface. However, this makes the handling of the shaft very difficult, in particular when attaching to and detaching from the shaft holder, by arranged projections, regardless of whether they are of of the surface facing outwards or inwards, the shaft can be gripped more easily by lifting means, for example, and can also be rotated more easily the latter is particularly advantageous if the shaft is to be screwed into a thread in the shaft holder

In a preferred embodiment of the rotor, the outer surface of the shaft merges essentially flush into a peripheral surface of the shaft receptacle at a connecting seam. This also largely prevents melt splashes from being able to penetrate between the flat end surface of the shaft and the shaft receptacle The surface at the connecting seam is kept low in the case of a flush transition

In an advantageous variant of the rotor, a splash guard or means for attaching a splash guard are arranged on the shaft. In particular, clampable annular disks or the like are suitable as splash protection. When using a splash guard, the build-up of melt splashes or the penetration of melt splashes between the shaft and the holder is prevented as best as possible

It should be pointed out that the suggestions relating to the shaft holder do not relate to the end of the shaft facing the rotor head, but to the opposite side, that is to say where the shaft is connected to a machine

It goes without saying that all the features described as advantageous, which do not explicitly relate to preceding features, also achieve advantageous effects independently of one another, in any alternation or addition, and are also inventive in themselves

The device according to the invention for introducing fluids into a molten metal achieves the stated task because an adjacent arrangement of at least two rotors without baffles arranged between them significantly improves the effect of the degassing process compared to the prior art. In such a space between two rotors, in particular with one another arranged shafts, a macroscopically swirling flow occurs due to the influence of two rotor heads. The center of the swirl is not directly on the rotor, but lies in the space between the rotors. This minimizes the risk of vortex formation on the rotor

In addition, an increase in the melt level occurs in the area between the rotors, which causes a secondary flow perpendicular to the direction of the melt channel. This further improves the distribution of the fluid bubbles in the melt This applies in particular to rotors in which the fluid flows to the rotating rotor heads via an internal fluid supply. However, an advantageous effect also arises if the fluid is different, for example via bottom blowers. side nozzles etc is supplied

Surprisingly, it has been found that the arrangement of at least two rotors between two baffles - regardless of their shape - can advantageously influence the fluid distribution. It goes without saying that this effect can be significantly increased again when using the proposed rotor design

In an advantageous embodiment of the device, this is characterized. that the contact area is delimited by baffles. In this case, in the course of the molten metal there is already a first baffle in front of the first rotor and a last baffle after the last rotor. At least it is advantageous if a first is in front of the first rotor Baffle wall is arranged The baffle walls cause a vertical flow within the metal melt. By arranging a first baffle wall in front of the first rotor there is already a strong vertical swirling of the melt. This makes it possible to distribute the fluid bubbles as homogeneously as possible

It is particularly recommended that the contact area has at least three baffles. It has been found in extensive tests that an arrangement of three baffles compared to an arrangement of two or only one baffle achieves significantly better degassing results. The arrangement of further baffles can further increase the results The more baffles are arranged, the stronger the vertical flow. It can be observed here that the strength of the vertical flow increases steadily in the course of the melt channel within the contact area

It is particularly recommended that the baffles reach at least half a melt channel depth in the contact area during operation. The farther the baffles reach. the stronger the vertical turbulence becomes. In addition, the melt flow on the baffle becomes stuck, which increases the melt level and the fluid bottles have to travel a longer distance within the melt

Alternatively and cumulatively, it is advantageous if the rotors in the Betneb closer to a channel bottom of the

Melt channel are arranged as the baffles The melt channel generally has a substantially rectangular shape with a designated sole surface. walls and rotors in the described manner, the contact chambers, which are each defined by the delimitation of two baffles, are coupled with each other in relation to the horizontal flow. This regularly leads to longer path lines of melt particles within the contact area and, at the same time, to a stronger secondary flow

In an advantageous embodiment variant, the device according to the invention is characterized in that the rotors are arranged at a distance which is at least one width of the melt channel in the contact area. The advantage is already achieved if only two adjacent rotors are spaced apart by the specified amount below the width of the melt channel in the contact area, the width of the melt surface is essentially understood. In the case of cross-sectional shapes of melt channels that differ substantially from the rectangular shape, the specified dimension m can be meaningfully related to an effective width of the melt channel at the height of the rotor heads

Such an arrangement avoids dead areas in the melt flow. In particular, pronounced longitudinal flows will occur within a contact chamber, which will minimize the size of a Sclucht flow at the Stokes' sticking area

It has also been shown empirically that it is beneficial. if the rotors have a circumferential diameter that is at most a quarter, preferably a fifth, of a width of the melt channel in the contact area. The circumferential diameter of truncated cone-shaped rotor heads is understood to be the largest circumferential diameter that occurs on the rotor head but also the least possible formation of vortexes and the occurrence of splashes as narrow as possible on the other hand, the above-mentioned diameter has proven to be advantageous since the fluid bubbles are introduced into the melt over a large area and strong secondary flows are also produced, but at the same time the formation of Swirling and splashing is successfully avoided

It should be mentioned in this connection that the highest possible speeds also lead to good chopping of bubbles and should therefore be aimed for

At the same time, it has also been shown to be an advantage. If the rotors have a circumferential diameter that is at least one sixth of the width of the melt channel in the contact area. For smaller rotors, the speeds must be too high, which in turn causes an increased risk of vortex formation and, at the same time, increased material wear rotors with smaller diameters do not cause a satisfactory horizontal secondary flow within the contact chambers

The size of the rotor heads should preferably be within the upper and lower limits described in order to achieve the best possible degassing effect, it being understood that the rotor head size can also bring about the advantages shown, regardless of the essential features of the present invention

As an alternative and cumulatively, it is particularly advantageous if the rotors run in the same rotations. In particular, this relates to the rotors within a contact chamber or at least to two adjacent rotors. Due to the same direction of rotation of two adjacent rotors, the intermediate area between the two rotors is particularly high a suggestion for vortex formation. Dead areas are avoided and better mixing of the entire melt-fluid mixture is achieved

In two adjoining contact chambers, it can be advantageous to drive different rotations within one contact chamber with the same direction of rotation of rotors. This creates scope for the design of flow fields within the melt channel, which enables the process to be optimized for different operating conditions

Regardless of this, the device according to the invention can advantageously be characterized in that the melt channel essentially consists of an outer jacket, an intermediate layer and a ceramic lining on the melt side. The outer jacket is expediently made of steel or a similar material, care being taken. that connections can be arranged with sufficient precision and strength to the outer jacket, for example, for mounting sockets of the device or for connecting various elements of the device

The intermediate layer can have, for example, a highly porous cast concrete. Its main function is to ensure good insulation of the outside from the hot molten metal on the inside with good stability and sufficient weight for the stability of the channel

The ceramic lining on the melt side has a long service life even under the extreme stress during channel degassing. It is highly resistant to temperature changes and at the same time ensures good insulation of the layers located outside from the molten metal

Due to the structure of the melt channel, a good insulation effect and stability, a service life of generally more than 2 years and good handling with an inexpensive construction are made possible

Regardless of this, it is advantageous if a feed element has a ceramic lining. In the case of channel degassing, filter elements are generally arranged after the contact area in the further course of the molten metal. A ceramic lining of such a filter element likewise brings about a long service life and good insulation

In a preferred embodiment, the ceramic lining of the melt channel and / or the filter element is monolithic. A monolithic lining in particular brings the advantage of very reliable guidance of the molten metal within the channel or the filter element. When composed of several elements, connection seams are inevitable, which pose the risk that liquid melt in the seams passes through the lining. The seams must therefore be closed in one subsequent operation. However, cracks can occur again under the enormous heat during operation of the sewer. A monolithic lining therefore makes a particularly high contribution to occupational safety

A feeding element can advantageously be characterized in that it has ceramic foam filters. These can expediently be removed and thus be easily exchangeable. On the one hand, training as a foam filter has the advantage that the filters are inexpensive and light in weight. On the other hand, a foam filter offers one Good compromise between a high filtering effect and the least possible loss of flow energy. Foam filter can easily be made from ceramic material. This is a great advantage because the foam filter is very resistant to lutz and in particular also resistant to temperature changes and therefore a long service life can be expected

Regardless of this, the device according to the invention can advantageously be characterized in that the channel bottom of the melt channel runs essentially horizontally between the contact area and the feed element E Falling of the channel bottom in the direction of the lining element accelerates the melt flow.This lowers the melt level.In addition to the resulting shortened dwell time of the fluid bubbles in the melt, the acceleration also increases the risk that the melt will start to shoot.A subsequent inevitable alternating change adversely affects the degassing performance

On the other hand, an increase in the surface of the sole between the contact area and the lining element means that the molten metal cannot flow out of the contact area as a whole without external influence. However, molten metal must normally be avoided in the contact area after the casting process. Is the metal? once cooled, it is hardly possible anymore. cleaning the channel from the metal If a melt of another metal flows through the channel degasser in the next batch, this will inevitably become contaminated. In addition, undesirable flow fields arise at least initially in the contact area due to the channel bottom changed by the metal deposit

A substantially horizontal arrangement of the channel bottom between the contact area and the lining element is able to rule out these undesirable effects

In an advantageous embodiment, the device has a heater for heating a filter insert. As a result, the filter insert can be heated to its operating temperature before the metal melt arrives at the feeding element, or at least heated to such an extent that the temperature change resistance of the filter element is not overused by the heater the service life of the filter insert can be increased significantly on a regular basis

In a preferred variant of the heater, it has a blower. The simplest way to heat the filter insert is to have hot fluid flowing through it. preferably with hot gas. Such a gas can easily be passed through the feed element by means of a blower. For example, a closed circuit of hot air is appropriate here. which circulates through the feeding element, a heating area and the blower

In a preferred form of heating with the blower, this is arranged outside the filter element and the heating interacts with a wall of the filter element.For example, this can be carried out in such a way that a passage pipe for the heated gas is installed in a wall and / or a further pipe in the same or a different one, preferably the opposite one. Wall is arranged for the heated air to flow out. The blower sits together with the heating rich outside the filter element With such an arrangement, the blower and the heating area are removed from the direct heat of the molten metal. In addition, the blower and the heating area are more easily accessible for maintenance or repair

It is particularly preferred that the heated gas flows through the filter in the same orientation as later through the molten metal. On the one hand, the heater can work with the same efficiency even with an anisotropically acting filter insert. On the other hand, the number of openings of the filter element can be kept smaller as a result become

The filter insert of a filter element for the device according to the invention should advantageously be selected such that it has a fineness of at least 60 ppi. Satisfactory results can only be expected to a very limited extent below this femininity limit. However, it should be noted that if the fineness of the filter insert is too great, the melt flow can experience excessive resistance

Regardless of this, it is preferable that the melt channel has a curvature between a filler area and the contact area. The filler area here is understood to be the point at which the molten metal flows into the melt channel. The curvature of the channel in the course of the melt flow deflects it and am Baffle bank increases the level of the mirror.This induces a secondary flow that runs essentially along the channel walls and the surface perpendicular to the flow of the melt.This is particularly advantageous in order to avoid the formation of dead areas in the further course of the channel.In addition, the baffle bank successfully absorbs the surge energy of a filling surge on

In addition, channel degasser can advantageously be characterized in that the melt channel widens in the contact area and / or in the feed element. Due to the continuity, this slows down the melt flow, which regularly leads to improved degassing or feeding results. It may be advisable not to jump the channel , but let it expand in a steady course with a certain maximum angle

Irrespective of this, it is recommended that the melt channel have an indicator, preferably a shoulder, for a melt level. The indicator then serves as a full level control. This makes it possible with simple means to ensure that the metal melt is filled in to a required minimum full level, even for positioning work Such a display can be useful when setting up the duct or installing the rotors The device according to the invention can furthermore be characterized in a profitable manner by the fact that a rotor lifting device has means for moving the rotors in the horizontal direction. Conventional channel degassers usually have a rotor lifting device. Using these, the rotors can be moved - usually vertically - with respect to the metal melt. It is advantageous if The rotors can also be moved horizontally.This makes maintenance or replacement of rotors significantly easier. In particular, a lifting column with a horizontal trolley can be used.With such an arrangement, the horizontal movement can be carried out completely independently of the vertical movement great reliability can be inserted exactly vertically and only be carried out horizontally when the machine is at a standstill

Finally, the device can advantageously be characterized in that it has means for adjusting a speed and / or a fluid flow rate. It has been found that a fluid current rate of 10 to 25 liters of fluid per rotor per rotor supports very positive degassing results Strong fluid flow. regardless of this, of course, also the rotor speed, the device according to the invention has a high adaptability to different metals or degassing fluids

It goes without saying that all advantageous features of the device according to the invention are advantageous and inventive, even in isolation or in addition. Exceptions to this are only those features that explicitly relate only to certain previous features

It should be pointed out that the proposals relating to the device offer advantages in particular when introducing fluids into a molten metal Also for similar devices in which liquid metal from a melting furnace, for example to a casting table, is required - in particular, but not necessarily, with the completion of a melt treatment However, the features are also advantageous and inventive

The method according to the invention achieves the object with the same inventive concept. If the metal melt flows through a contact chamber with at least two rotors, in particular with shafts arranged next to one another, it gets into strong vortices which occur in the contact chamber due to the direct vicinity of two rotors. As a result, the melt is mixed thoroughly In addition, the melt level rises in the impact areas of the two rotor currents and thus induces an additional secondary flow All these effects increase the desired effect of the channel degasser. without there being an increased risk of vortex formation in the immediate vicinity of the rotor

It should be pointed out that a mere application of the proposed method can achieve a better fluid distribution in the metal melt compared to the prior art. If the method also uses a rotor of the proposed type, the advantageous effect can be increased considerably

In a preferred variant of the method, this is characterized in that a melt channel is cleaned and dried before the metal melt is poured in. The metal melt is guided through a melt channel in a conventional manner. If this is cleaned and dried before the melt is poured in, the starting product contains Channel degasser has less contamination of the metal

Regardless of this, it is advisable to provide a feeding element with a filter insert before filling the molten metal.A removable filter insert enables practical, inexpensive and long-lasting use of a filter element on the melt channel behind the contact area. A ceramic foam feeder can be used with high suitability at the end of the channel degasser, the filter has the best possible metal cleaned of unwanted components

The filter insert can preferably be heated by a heater before the molten metal reaches it. This primarily requires a long service life of the filter insert. In particular, a ceramic filter insert has a high resistance to temperature changes and heat, but the load on the material can be significantly reduced by preheating

Regardless of this, it is advantageous if the metal melt is subsequently filled into the melt channel in the method according to the invention until a certain melt height is reached in the contact chamber. The melt height m of the contact chamber is a significant influencing factor on the quality of the degassing result the minimum melt height has been reached, preferably takes place on the basis of a display which the melt channel has. For example, this can have a shoulder which is visible in the minimum height for the metal melt

It is advantageous here if the melt height is between 200 and 250 mm. These are positive values that have been found to be particularly advantageous for the degassing result It is advantageous here if the rotors are set in rotation after reaching the melt height. This also ensures to a high degree that the degassing process achieves the desired quality. A contribution is also made to occupational safety

As an alternative and cumulatively, it is advantageous if the rotors are moved into a target position before they are set in rotation.The target position should be fixed or dependent on the melt level in the contact area.The target position ensures a high reproducibility of the degassing results and at the same time reduces the Danger of dangerous splashes of hot metal occurring, for example, if the rotors are not sufficiently immersed

The method is particularly advantageous if a rotational speed of the rotors and a fluid flow rate of the fluid introduced by the rotors are set such that the vector sum of a speed of the fluid parallel to the axis of rotation - determined by the size of the mouth area of the fluid passage in the rotor head or the set fluid flow rate - and a speed of the fluid perpendicular to the axis of rotation - determined by the rotor head geometry and the set number of revolutions - in the speed space lies within a channel movement volume caused by the movement of the channels.This results in very good results in chopping the fluid bubbles, since each fluid particle with the teeth at least once of the rotor comes into contact

It is also beneficial if the fluid flow is strong. which passes through a rotor, amounts to 10 to 25 1 / mm. It has been shown empirically that very good degassing results can be achieved by choosing a strong fluid flow within this spectrum

It goes without saying that all advantageous features of the method for capturing fluids in a molten metal also have an advantageous effect on their own in alternation or addition and are inventive if they do not explicitly relate only to a previous feature or features. that the proposed method features not only have an advantageous effect and are inventive for a method for introducing fluids into a molten metal, but also generally for a method for preparing a method for introducing fluids into a molten metal, and for a method for preparing a device for Conduction of a molten metal from a melting furnace, for example to a casting table or the like - preferably, but not necessarily involving treatment of the molten metal Various exemplary embodiments of the rotor according to the invention and the device according to the invention can be seen in the drawing

FIG. 1 shows a longitudinal section through a rotor,

FIG. 2 shows a section through a rotor head corresponding to the section in FIG. 1,

FIG. 3 shows a top view of the rotor head according to FIG. 2,

FIG. 4 shows a section through an alternative rotor head in a representation similar to that in FIG

2

FIG. 5 shows a section through a further alternative rotor head in a representation similar to that in FIG. 2,

FIG. 6 shows a schematic section through a degassing device with three baffles with four rotors,

FIG. 7 schematically shows a section through a degassing device with four baffles with four rotors,

FIG. 8 shows an exemplary structure of a device according to the invention in a view from above,

Figure 9 shows an exemplary structure of an alternative device according to the invention

sideview

Figure 10 shows the same exemplary device in a view along the channel axis, wherein

Rotors are shown in both a working and an assembly position,

FIG. 11 shows an exemplary arrangement in the area of the rotors with a lifting device,

Figure 12 shows an exemplary embodiment of a filter element as well

Figure 13 shows the same feeding element in the maintenance state

The rotor 1 in FIG. 1 essentially consists of a rotor head 2, a shaft 3 and a shaft holder 4. The rotor head 2 is fastened to the shaft 3 by means of a thread 5. thread 6 attached to the shaft receptacle 4, which in turn can be connected, for example, directly to a lifting device by means of receiving holes 7.

In the example shown, a fluid passage 8 runs from the shaft holder 4 through the vertically arranged shaft 3 to the area of the rotor head 2 where the fluid passage 8 opens into a cylindrical fluid space 9. From there, the fluid flows between the teeth, two of which are exemplarily designated 10, 11, in channels 12 to the lateral surface 13 of the rotor head 2 and enters the metal melt 14 in the form of bubbles. The fluid is chopped by the sharp tooth edges, in particular when exiting from the channels 12. In the example of the channel 12, this chopping intent fulfills the edge 16 of the tooth 10 with a direction of rotation 15 of the rotor head.

FIG. 1 also shows a widening of the channel 12 with increasing depth. Here, the degree of expansion increases abruptly when the rectangular section 17 of the channel 12 merges into the trapezoidal section 18.

The thread 5 does not have to reach the upper limit of the channels 12, but can already end further above.

At the upper end of the shaft 3, the projections 19 are shown, by means of which the shaft can be gripped and / or screwed tight, so that there is an essentially flush transition between the lateral surface 21 of the shaft 3 and the peripheral surface 22 of the shaft receptacle 4 at the connecting seam 20 ,

At the transition seam 23 of the lateral surface 13 of the rotor head 2 into the lateral surface 21 of the shaft 3, a concave, flush transition results between the head tangent 24 and the lateral surface 21.

It is also clearly shown that in this exemplary embodiment the rotor head 2 has a pronounced frustoconical shape. has an expanding shape. The shaft 3 has a slightly frustoconical shape that tapers downward.

FIG. 2 shows a rotor head 30 according to the invention with a pronounced frustoconical shape. Compared to FIG. 1, the channel 25 in particular has a different cross-sectional shape. The channel 25 also widens downward. however, the degree of expansion is constant. In addition, here the thread 26 is drawn through to the beginning of the tooth numbered 27, 28, for example, and thus forms a very large cylindrical fluid space 29, the fluid space 29 opening downwards in the direction of the axis of rotation, so that relatively large gas volume downwards and can flow out into the channels 25 or into the side channels 31. In this way, the entire gas runs at least over the length of the channels 25 in the channels and can be accelerated in accordance with the rotor movement

In the rotor head 30 shown in FIG. 2, however, the pronounced geometry of the side channels 31, the half of which lying beyond the cutting plane is shown in FIG. 2, is particularly clear. In the region of the side channel 31, the lateral surface 32 goes back to the inner groove 33 of the side channel 31

As can be seen in particular from FIG. 3, the side walls 31 extend from the openings of the channels 25 in the direction of the shaft, which is not shown here, but lies on the observer side of the figure. It also follows directly from FIGS. 2 and 3 that the channels 25 Extend radially outward from the fluid space 29 perpendicular to the axis of rotation

Characteristic for the rotor head 30 provided with sides 31 according to the present exemplary embodiment is that both the boundary line 34a. 34b as well as the boundary height 35a 35b alternately have convex and concave curved elements

Figure 4 shows an alternative rotor head 36 with a channel 37, which again has a rectangular section 38 and on the underside of which subsequently has a trapezoidal section 39. At the same time, however, the thread 40 goes down the entire outside of the cylindrical fluid space 41 and thus extends to the height of the beginning the teeth 42, 43 The side channels 44 are very weak in this exemplary embodiment

FIG. 5 shows a further exemplary rotor head 46 which, with an otherwise identical design as the rotor head 36 of FIG. 4, has more pronounced side walls 45

FIG. 6 shows a device 47 according to the invention, which has a melt channel 48 and a contact area 49 with rotors 50, 52, 53 54 arranged there, together with diving walls 51, 55, 56, both between the diving walls 56, 55 and between the diving walls 55, 51 In each case two rotors 50, 52 and 53. 54 arranged. In the further course of the melt channel 48, the device 47 has the feed element 57. In the example shown, the rotors 50, 52 53. 54 attached to the common lifting device 58. The channel base 59 runs horizontally between the contact area 49 and the feeding element 57. In the feeding element 57 it lies lower than in the rest of the device 47. In this exemplary embodiment, the dividing walls 51, 55, 56 do not project as far down as the rotors 50, 52, 53, 54

FIG. 7 shows with the device 60 an alternative to the device 47, in which four baffle walls 66, 67, 68, 69 are arranged in the contact area 61 with four rotors 62, 63, 64, 65. In the example shown here, the baffle wall 67 and 68 large contact chamber formed 70 m from the center of the contact area 61 In other embodiments, however, the structure can also be asymmetrical and / or have mixed large and small contact chambers

FIG. 8 shows the course of the melt channel 71 with a curvature 72 between the filler area 73 and the contact area 74. The contact area 74 is widened relative to the melt channel 71 at points 75a, 75b. Likewise, the melt channel 71 at points 76a, 76b widens into that Feeding element 77

In addition to the elements of a device 78 already described, FIG. 9 shows, in particular, an opened cover wall 79 of a filter element 80 with a hot air passage 81 of a heater (not shown). Furthermore, the three rotors 82a, 82b, 82c are fastened to a rotor stroke device 83 designed as a lifting column moved vertically in the present example by two motors 84a, 84b

In Figure 11, a rotor 88 is in its submerged target position 89 within the melt channel 90, attached to a hoist winch 91a. 91b shown. The hoist 91a, 91b can move the rotor 88 by winding the rope 92 along the vertical direction 93. Independently of this, the means for moving 94 designed as a trolley, to which the hoist winch 91a, 91b is attached, can move along the horizontal direction 95 A possible position into which the rotor 88 can be moved is shown in the dashed position 96

The three-vaulted structure of the melt channel 90 is also shown. In the example shown, the melt channel 90 consists of the outer jacket 90a made of steel, the intermediate layer 90b made of highly porous concrete and the monolithic ceramic lining 90c made of a mixture of quartz glass and additives FIGS. 12 and 13 show how a feed element 97 can have a heated ventilation in its cover 98, which can blow hot air through a pipe 99 through the cover 98 into the feed element 97.

The lid 98 is firmly connected to the arm 100. This is in turn firmly connected to the collar 101 and articulated on the joint 102. By means of the hydraulic cylinder 103, the cover 98 can be folded by the feed element 97 about the axis of rotation of the joint 102 and the feed element 97 can thus be opened. From the connection 104, the hot air pipe is either to be flexible or to be separated from the connection 104 before the cover 98 is opened.

Claims

claims

1 rotor (1) for introducing fluids into a molten metal (14), the rotor (1) comprising a shaft (3) and a rotor head (2) attached to the shaft, which has a lateral surface (13) with a component in parallel to an axis of rotation of the rotor (1), characterized in that at least one side nominal (31) with a concavely curved cross section is provided on the lateral surface (13)

2 Rotor according to claim 1, characterized in that at least one of the side channels (31) of channel openings. which are caused by channels (12, 25, 37) which extend essentially radially outward from the axis of rotation and extend in the direction of the shaft (3)

3 Rotor according to claim 1 or 2, characterized in that the channels (12, 25, 37) have a variable cross-section (38, 39) along the axis of rotation, which widens into an immersion direction of the rotor (1)

4 rotor according to claim 3, characterized in that a degree of expansion with the

Immersion increased

5 rotor according to claim 4, characterized in that the degree of expansion increases by leaps and bounds

6 rotor according to one of the preceding claims, characterized in that the channels

(12, 25, 37) lie between teeth (10, 11) which have a length of at least 40 mm along the lateral surface (13)

7 rotor according to one of the preceding claims, characterized in that the rotor head

(2) in an immersion direction on the shaft (3) then has a cylindrical fluid space (9)

8 rotor according to one of the preceding claims, characterized in that an essentially with the axis of rotation passage (8) for introducing the fluid with a mouth surface of at most 64 mm ² , preferably from 12 to 36 mm ² , in the fluid space (9) mundet

9. Rotor according to one of the preceding claims, characterized in that the rotor head (2) has a substantially frustoconical shape.

10. Rotor according to one of the preceding claims, characterized in that the rotor head

(2) is fastened to the shaft (3) via a self-sealing fastening means (5).

11, rotor according to one of the preceding claims, characterized in that the lateral surface (13) at a transition seam (23) between the rotor head (2) and the shaft (3) is essentially flush with a lateral surface (21) of the shaft (3 ) transforms.

12. The rotor according to claim 11, characterized in that a transition at the transition seam (23) with respect to the lateral surface (13) of the rotor head (2) and the lateral surface (21) of the shaft (3) is substantially concave.

13. Rotor according to one of the preceding claims, characterized in that the shaft (3) tapers towards the rotor head (2).

14. Rotor according to one of the preceding claims, characterized in that the shaft (3) is fastened to a shaft receptacle (4) via a self-sealing fastening device (6).

15. Rotor according to one of the preceding claims, characterized in that the shaft (3) has axial projections (19).

16. Rotor according to one of the preceding claims, characterized in that the outer surface (21) of the shaft (3) at a connecting seam (20) merges substantially flush into a peripheral surface (22) of the shaft holder (4).

17. Rotor according to one of the preceding claims, characterized in that on the shaft

(3) a splash guard or means for attaching a splash guard are arranged.

18. Device (47) for introducing fluids into a molten metal (14), the device (47) having a melt channel (48) and in the course of which a contact area (49) in which the fluids are introduced into the molten metal (14) , with rotors (50, 52, 53, 54) arranged there, together with baffle walls (51, 55, 56), characterized in that between two baffle walls (51, 55, 56) at least two rotors (50, 52, 53, 54 ) are arranged.

19. The apparatus according to claim 18, characterized in that the contact area (49) is delimited by baffles (51, 56).

20. The apparatus according to claim 18 or 19, characterized in that the contact area (49) has at least three diving walls (51, 56).

21. Device according to one of claims 18 to 20, characterized in that the baffles (51, 55, 56) reach at least half a melt channel depth in the contact region (49) during operation.

22. Device according to one of claims 18 to 21, characterized in that the rotors (50, 52, 53, 54) are in operation closer to a channel bottom (59) of the melt channel (48) than the baffles (51, 55. 56).

23. Device according to one of claims 18 to 22, characterized in that the rotors (50, 52, 53, 54) are arranged at a distance which is at least a width of the melt channel (48) in the contact region (49).

24. Device according to one of claims 18 to 23, characterized in that the rotors (50, 52, 53, 54) have a circumferential diameter which is at most a quarter, preferably a fifth, of a width of the melt channel (48) in the contact area (49 ) is.

25. Device according to one of claims 18 to 24, characterized in that the rotors (50, 52, 53, 54) have a circumferential diameter which is at least one sixth of a width of the melt channel (48) in the contact region (49).

26. Device according to one of claims 18 to 25, characterized in that the rotors run in the same directions of rotation.

27. Device according to one of claims 18 to 26, characterized in that the melt channel (90) consists essentially of an outer jacket (90a), an intermediate layer (90b) and a ceramic lining (90c) on the melt side.

28. Device according to one of claims 18 to 27, characterized in that a feeding element (57) has a ceramic lining. Device according to claim 27 or 28, characterized in that the ceramic lining is monolithic

Vornchtung according to one of claims 18 to 29, characterized in that the feeding element (57) has ceramic foam feeders

Device according to one of claims 18 to 30, characterized in that the channel base (59) of the melt channel (48) runs essentially horizontally between the contact area (49) and the feeding element (57)

Device according to one of claims 18 to 31, characterized in that the device (47) has a heater for heating a filter insert

Apparatus according to claim 32, characterized in that the heater has a blower

Apparatus according to claim 33, characterized in that the blower is arranged outside the filter element (97) and the heater cooperates with a wall (98) of the filter element (97)

Device according to one of claims 18 to 34. characterized in that the filter insert has a fineness of at least 60 ppi

Device according to one of claims 18 to 35, characterized in that the melt channel (48) has a curvature (72) between a filling area (73) and the contact area (74)

Device according to one of claims 18 to 36. characterized in that the

The melt channel (71) widens in the contact area (74) and / or in the feed element (77)

Device according to one of claims 18 to 37, characterized in that the melt channel (71) has an indicator, preferably a shoulder, for a melt height

Device according to one of claims 18 to 38, characterized in that a rotor lifting device (83) means (94) for moving the rotors (88) in a horizontal direction

(95)

40. Device according to one of claims 18 to 39. characterized in that the device (47) has means for setting a speed and / or a fluid flow rate.

41. Method for introducing fluids into a molten metal, in which the fluids are introduced into the molten metal by rotors (62, 63, 64, 65) arranged between baffle walls (66, 67, 68, 69), which each delimit a contact chamber in pairs characterized in that the molten metal flows through a contact chamber (70) with at least two rotors (63, 64),

42. The method according to claim 41, characterized in that a melt channel (48) is cleaned and dried before filling the metal melt.

43. The method according to any one of claims 41 or 42, characterized in that a feed element (57) is provided with a filter insert before filling the metal melt.

44. The method according spoke 43, characterized in that the filter insert is heated by a heater before the molten metal reaches it.

45. The method according to any one of claims 41 to 44, characterized in that the metal melt is then filled into the melt channel (48) until in the contact chamber

(70) a certain melt height has been reached.

46. Method according to 45. characterized in that the melt height is 200 to 250 mm.

47. Method according to one of claims 45 or 46, characterized in that the rotors (62, 63, 64, 65) are set in rotation after reaching the melt height.

48. The method according to any one of claims 41 to 47. characterized in that the rotors (62. 63. 64, 65). before they are set in rotation, are moved into a target position (89).

49. The method according to any one of claims 41 to 48, characterized in that a speed and a fluid flow rate are set so that the vector sum of a speed of the fluid parallel to the axis of rotation - determined by the size of the mouth surface of the

Fluid passage in the rotor head or the set fluid flow rate - and the speed of the fluid perpendicular to the axis of rotation - determined by the rotor head geometry and the set number of revolutions - lies within a channel movement volume in the speed space caused by the movement of the channels.

50. The method according to any one of claims 41 to 49. characterized in that the fluid flow rate is 10 to 25 1 / min.