EP1047504A1 - Buse a jet eventail destine a pulveriser un liquide de refroidissement sur un produit de coulee continue - Google Patents

Buse a jet eventail destine a pulveriser un liquide de refroidissement sur un produit de coulee continue

Info

Publication number
EP1047504A1
EP1047504A1 EP98959851A EP98959851A EP1047504A1 EP 1047504 A1 EP1047504 A1 EP 1047504A1 EP 98959851 A EP98959851 A EP 98959851A EP 98959851 A EP98959851 A EP 98959851A EP 1047504 A1 EP1047504 A1 EP 1047504A1
Authority
EP
European Patent Office
Prior art keywords
spray nozzle
nozzle according
spray
outlet opening
inlet openings
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP98959851A
Other languages
German (de)
English (en)
Other versions
EP1047504B1 (fr
Inventor
Adrian Stilli
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Concast Standard AG
Original Assignee
Concast Standard AG
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Concast Standard AG filed Critical Concast Standard AG
Publication of EP1047504A1 publication Critical patent/EP1047504A1/fr
Application granted granted Critical
Publication of EP1047504B1 publication Critical patent/EP1047504B1/fr
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21DMODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D1/00General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
    • C21D1/62Quenching devices
    • C21D1/667Quenching devices for spray quenching
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B1/00Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means
    • B05B1/02Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to produce a jet, spray, or other discharge of particular shape or nature, e.g. in single drops, or having an outlet of particular shape
    • B05B1/04Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to produce a jet, spray, or other discharge of particular shape or nature, e.g. in single drops, or having an outlet of particular shape in flat form, e.g. fan-like, sheet-like
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B1/00Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means
    • B05B1/02Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to produce a jet, spray, or other discharge of particular shape or nature, e.g. in single drops, or having an outlet of particular shape
    • B05B1/04Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to produce a jet, spray, or other discharge of particular shape or nature, e.g. in single drops, or having an outlet of particular shape in flat form, e.g. fan-like, sheet-like
    • B05B1/042Outlets having two planes of symmetry perpendicular to each other, one of them defining the plane of the jet
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B21MECHANICAL METAL-WORKING WITHOUT ESSENTIALLY REMOVING MATERIAL; PUNCHING METAL
    • B21BROLLING OF METAL
    • B21B45/00Devices for surface or other treatment of work, specially combined with or arranged in, or specially adapted for use in connection with, metal-rolling mills
    • B21B45/02Devices for surface or other treatment of work, specially combined with or arranged in, or specially adapted for use in connection with, metal-rolling mills for lubricating, cooling, or cleaning
    • B21B45/0203Cooling
    • B21B45/0209Cooling devices, e.g. using gaseous coolants
    • B21B45/0215Cooling devices, e.g. using gaseous coolants using liquid coolants, e.g. for sections, for tubes
    • B21B45/0233Spray nozzles, Nozzle headers; Spray systems
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B22CASTING; POWDER METALLURGY
    • B22DCASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
    • B22D11/00Continuous casting of metals, i.e. casting in indefinite lengths
    • B22D11/12Accessories for subsequent treating or working cast stock in situ
    • B22D11/124Accessories for subsequent treating or working cast stock in situ for cooling
    • B22D11/1246Nozzles; Spray heads
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B05SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
    • B05BSPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
    • B05B1/00Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means
    • B05B1/26Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means with means for mechanically breaking-up or deflecting the jet after discharge, e.g. with fixed deflectors; Breaking-up the discharged liquid or other fluent material by impinging jets

Definitions

  • the invention relates to a spray nozzle for spraying a continuous casting product with a cooling liquid according to the preamble of claim 1.
  • a continuous casting product is produced which is continuously produced from the mold in the form of a strand, the surface of which is formed by a solidified crust and which still has a liquid core made of molten metal is pulled.
  • the strand is conveyed through a secondary cooling zone, in which it is sprayed with a coolant, generally water, in order to continue to extract heat from it until it has completely solidified and to bring it to the temperature desired for further processing.
  • a coolant generally water
  • the secondary cooling directly affects or affects the solidification of the strand, the secondary cooling process and the devices required for its implementation are decisive for the quality of the end products.
  • the components used for the distribution of the coolant, in particular the spray nozzles, are of particular importance.
  • the secondary cooling intensity which determines the speed of the strand shell growth and, depending on the application, is set to a greater or lesser extent “hard” or “soft”, and the spatial distribution of the coolant loading density, which should be as homogeneous as possible in order to achieve the most homogeneous strand shell growth possible guarantee.
  • the spray nozzles used in a secondary cooling section for spraying a coolant are usually optimized with regard to the requirements for the secondary cooling intensity and the homogeneity of the coolant supply.
  • the secondary cooling intensity is determined by the kinetic energy of the sprayed coolant drops and, in particular, the coolant loading density. Decisive for the homogeneity of the coolant loading density is not only the homogeneity of the droplet distribution in the spray generated with a single spray nozzle.
  • the angular distribution of the droplet paths is also relevant for the homogeneity of the coolant loading density. The angular distribution determines the shape and size of the area on a strand that can be sprayed with a spray jet.
  • the known full cone nozzles deliver spray jets with a conical angular distribution of the droplets. Because of their conical shape, the spray jets of several full cone nozzles cannot cover large spray areas perfectly; the superimposition of several spray jets results in a coolant loading density with a large inhomogeneity.
  • a spray nozzle with all the features of the preamble of claim 1 is known from US Pat. No. 3,072,346.
  • This spray nozzle has a nozzle body with a mixing chamber which is rotationally symmetrical about the longitudinal axis of the nozzle body and which is equipped with two inlet openings through which a liquid, forming a first and a second liquid flow, and with an outlet opening arranged downstream for a spray jet .
  • this nozzle has essential features of a known type of a full cone nozzle:
  • the two inlet openings are integrated in a guide structure for the liquid flows entering the mixing chamber in such a way that the liquid flows when entering the mixing chamber in addition to a speed component in the direction receive a velocity component tangential to the mixing chamber wall on the outlet opening. Because of this tangential velocity component, the two liquid flows combine after entering the mixing chamber to form a liquid flow directed towards the outlet opening, which has a swirl around the longitudinal axis of the nozzle body.
  • the spray nozzle described in US Pat. No. 3,072,346 has - like a conventional full cone nozzle - a round outlet opening.
  • the outlet opening is widened in a funnel shape on the outlet side such that the emerging spray jet is distorted in the direction of the diagonals of a square.
  • the nozzle delivers a spray jet with an approximately square droplet distribution - based on a plane perpendicular to the longitudinal axis of the nozzle body.
  • a disadvantage of this spray nozzle is that the shape of the droplet distribution of the spray jet is more and more distorted due to the imposed swirl as the inlet pressure of the liquid increases. Therefore, with such a nozzle, the requirements that are placed on the homogeneity of the coolant loading density in a secondary cooling section cannot be met.
  • a flat jet nozzle is described in US Pat. No. 4,988,043. It has a through channel for the liquid to be sprayed with an outlet slot for the spraying steel.
  • the spray jet is fanned out in the slot direction over a wide angular range, while it hardly widens transversely to the longitudinal direction of the slot with increasing distance from the outlet slot.
  • the quasi-one-dimensional fanning leads to a flat spray jet. Because of the small expansion of the spray jet across the outlet slot, the spraying of large rectangular areas is associated with complications, be it that a large number of these flat jet nozzles have to be used or that a single flat jet nozzle has to be moved in order to have a larger area with the spray jet to paint over.
  • the object of the present invention is to create a spray nozzle which is suitable for use in a secondary cooling section of a continuous casting installation and for this purpose enables the largest possible area to be as homogeneous as possible from the greatest possible distance to be sprayed with drops of liquid with the greatest possible kinetic energy.
  • the spray nozzle according to the invention comprises a mixing chamber, into which a liquid, forming a first and a second liquid flow, can flow through two inlet openings and which has a downstream outlet opening for a spray jet, at least one mixing chamber wall is designed as a guide surface for the liquid streams and is shaped at the outlet opening in such a way that the liquid streams meet at an angle at or immediately in front of the outlet opening and thereby form the spray jet.
  • the fact that the two liquid streams are directed towards the outlet opening and collide at the outlet opening results in relatively large liquid drops which, based on the inlet pressure at the inlet openings, can leave the outlet opening with relatively large kinetic energy. Energy losses due to vortex formation in the mixing chamber are largely avoided.
  • the high kinetic energy enables a large working distance when spraying a surface.
  • the atomization of the two liquid streams enables the directions of propagation of the drops to be widely scattered and therefore a wide spread of the spray jet emerging from the outlet opening.
  • drops, which are scattered across the direction of propagation of the liquid streams when the liquid streams collide make an important contribution to the fanning out of the spray jet. Since the spreading of the liquid flows in the mixing chamber is essentially determined by the geometry of the mixing chamber, the inlet pressure can be varied over a relatively large range without the fanning out of the spray jet being changed significantly.
  • the cross-section of an inlet opening is basically understood to mean a section transverse to the respective liquid flow in the inlet opening and the cross-section of the outlet opening is a section transverse to the spray jet.
  • the properties of a spray jet generated with the spray nozzle according to the invention essentially depend on the angle of incidence at which the liquid streams meet at or immediately in front of the outlet opening. It is advantageous to choose the angle of incidence in a range between 60 ° and 130 °, preferably between 80 ° and 100 °. This creates the prerequisites for the formation of liquid drops which leave the outlet opening with particularly high kinetic energy and form a spray jet which is distinguished by the fact that the drops are distributed particularly evenly over a particularly large solid angle over a central direction of propagation.
  • the mixing chamber has a taper at the outlet opening with an opening angle at the outlet opening between 60 ° and 130 °, preferably between 80 ° and 100 °, on.
  • the taper forms the part of the guide surface for the liquid flows that determines the angle of incidence.
  • the taper brings the two liquid flows together at the outlet opening at an angle of incidence that corresponds to the opening angle of the taper.
  • the drops formed at the outlet opening during the interaction of the two liquid flows have a particularly large velocity component in the direction of the bisector of the opening angle of the taper. This direction corresponds to the central direction of propagation of the drops that can leave the outlet opening.
  • the outlet opening also clears the way for drops whose paths are scattered at a solid angle around the central direction of propagation.
  • the taper can be conical, for example.
  • Another embodiment of the spray nozzle according to the invention has a slot as the outlet opening.
  • An outlet slot - with a suitable shape of a cross-sectional area transverse to the direction of propagation of the spray jet - offers the possibility, for example, of spraying a rectangular area.
  • the long sides of the rectangular spray surface are essentially parallel to the direction of the longitudinal extent of the slot.
  • the angular range over which the spray jet fanned out in the direction of the longitudinal extent of the outlet slit is greater the longer the slit is. This effect is due to the fact that the longer the outlet slot, the greater the angular range in which drops can leave the interaction zone of the two liquid flows at the outlet opening through the outlet slot, in the direction of the longitudinal extent of the slot.
  • a number of further developments of the spray nozzle according to the invention have further features which, alone and / or in combination with one another, offer the prerequisites for homogeneous droplet distribution on a spray surface.
  • the outlet opening and the mixing chamber have a common plane of symmetry. Under this condition, the two liquid flows are symmetrical with respect to the plane of symmetry. This can result in drops whose paths run symmetrically to the plane of symmetry.
  • the inlet openings each have a cross-sectional area with an elongated shape and the directions of their longitudinal extension are arranged essentially parallel to the direction of the longitudinal extension of the outlet slot.
  • the two liquid flows are on "preformed" in the sense of the inlet openings and adapted to the outlet slot so that the lines of the same flow speed - with respect to a plane transverse to the respective liquid flow - already have the same or almost the same shape as the cross-sectional area of the outlet opening at the inlet openings ( transverse to the central direction of propagation of the liquid drops).
  • Another embodiment of the spray nozzle according to the invention has an outlet slot and is designed such that the mixing chamber and the outlet slot have a common plane of symmetry, the longitudinal direction of the outlet slot being in the plane of symmetry and the inlet openings being arranged on different sides of the plane of symmetry.
  • the spray jet is in the plane of symmetry, i.e. in the longitudinal direction of the outlet slot, particularly wide.
  • the droplet distribution becomes particularly homogeneous if - as in the exemplary embodiment discussed above - the inlet openings have a cross-sectional area with an elongated shape and the directions of their longitudinal extension lie essentially parallel to the plane of symmetry.
  • a particularly uniform droplet distribution is achieved if the ratio of the sum of the two cross-sectional areas of the inlet openings to the cross-sectional area of the outlet opening is between 1.5 and 2, preferably between 1.6 and 1.8.
  • the mixing chamber has a taper of the type mentioned above, which is arranged at the outlet opening, and a cylindrical segment between the taper and the inlet openings.
  • the cylindrical segment acts as a side wall limiting the liquid flows.
  • the length of the cylindrical element has an influence on how the two liquid streams mix at the outlet opening and with what efficiency the liquid streams are converted into drops that leave the outlet opening unhindered.
  • the length of the cylindrical segment can be optimized accordingly.
  • a spray nozzle with a structurally particularly simple mixing chamber is obtained when the inlet openings between a crosspiece, which connects opposite parts of the lateral boundary of the liquid flows, and the lateral boundary are formed.
  • the inlet openings In the case of a side wall which is rotationally symmetrical about an axis and a cuboid crosspiece, the inlet openings have cross sections in the form of circular sections. According to the invention, such inlet openings can be combined with an outlet slot, the longitudinal direction of which is essentially parallel to the chords of the circular sections.
  • the drop distribution in the spray jet can be influenced by defined widening of the cross section of the outlet opening in the direction of propagation of the spray jet.
  • One embodiment of the spray nozzle according to the invention has an outlet slot, the cross-sectional area of which is widened at the narrow ends in the direction of propagation of the spray jet. This results in a particularly large fanning out of the spray jet in the longitudinal direction of the outlet slot.
  • the cross section of the outlet slot is widened in the middle of the long sides of the outlet slot in the direction of propagation of the spray jet. This measure allows the proportion of drops that spread in the direction of the central direction of propagation to be increased.
  • the outlet opening and the mixing chamber have a common plane of symmetry and guide walls are arranged to limit the spray jet emerging from the outlet opening.
  • the spray nozzles are asymmetrical insofar as the inlet openings have different cross-sectional areas and / or the guide walls are arranged on opposite sides of the outlet opening at different distances from the outlet opening.
  • These two design measures induce asymmetry of the spray nozzle on the inlet and / or outlet side, which - even with an otherwise symmetrical mixing chamber - affects the drop distribution in the spray jet.
  • a suitable quantitative expression of this asymmetry makes it possible to shift the center of gravity of the droplet distribution by a predetermined distance, to influence the homogeneity of the droplet distribution and to vary the shape of the spray surface in comparison to a symmetrical nozzle.
  • a spray nozzle according to the invention which is provided with a suitable outlet slit, it is possible, for example, to uniformly spray a rectangular surface with a width of 10 cm and a length of 50 cm from a distance of approximately 45 cm.
  • spray nozzles of this type can advantageously be used to cool billets with billet or bloom block format, one of the spray nozzles 4 - 6 replacing conventional full cone nozzles and additionally allowing a more uniform application of coolant.
  • the nozzle according to the invention can be realized with an outlet slot with a length of more than 10 mm and a width of more than 5 mm.
  • the risk that the outlet slot of the spray nozzle according to the invention becomes clogged due to contamination during operation is low, in contrast to conventional spray nozzles.
  • the inlet openings which can be chosen to be approximately the same size as the outlet openings.
  • the asymmetrical embodiments of the spray nozzle according to the invention have various applications in a continuous casting installation.
  • sections of a curved strand with a rectangular cross section can be cooled on the different sides by superimposing spray surfaces in the form of rectangles and sections of circular rings.
  • Such spray surfaces can be generated with the spray nozzle according to the invention by suitable dimensioning of its components.
  • 1A A longitudinal section through a spray nozzle
  • Fig. 2 B a plan view of the spray nozzle in Fig. 1 A along the arrow C in Fig. 1 B and
  • FIG. 2 C as in Fig. 2 B, but another example
  • F Fiigg .. 3 3 AA like FIG. 2 A, but with inlet openings of different sizes;
  • 3 B as in FIG. 2 B, but with exit-side guide surfaces at different distances from the exit opening; 3 C: like FIG. 1 A, but with the modifications according to FIGS. 3 A and
  • the two spray nozzles shown in FIGS. 1A-B and 2A-C are intended for spraying a rectangular surface with liquid drops.
  • the spray nozzle 5 shown in FIGS. 1A and B is symmetrical to a plane 35.
  • the spray nozzle 5 comprises a nozzle body 4 which has a cavity composed of a cylindrical section 16 and a conical section 17.
  • the cylindrical part has an opening 6 through which a liquid to be sprayed can be let in under a certain pressure p and is rotationally symmetrical with respect to a longitudinal axis 38.
  • the conical section 17 tapers in the direction of the longitudinal axis 38 according to an opening angle ⁇ and has an outlet slot 30 for a spray jet 40 at the cone tip.
  • the exit slot 30 is symmetrical with respect to the plane of symmetry 35, the longitudinal direction of the cross-sectional area of the exit slot 30 lying in the plane of symmetry 35.
  • a transverse web 8 in the cylindrical section 16 separates a mixing chamber 15 consisting of a part of the cylindrical section 16 and the conical section 17 and leaves two on the wall of the cylindrical section 16 Entry openings 9 and 10 free.
  • the cross-sectional areas of the inlet openings 9 and 10 have the shape of a circular segment and are arranged symmetrically on different sides of the plane of symmetry 35.
  • the cross-sectional areas of the inlet openings 9 and 10 have an elongated shape, the directions of their longitudinal extension or the chords of the circular segments being parallel to the plane of symmetry 35.
  • the spray nozzle 5 is supplied with a liquid to be sprayed along flow lines 7 at a pressure p through the opening 6 and through the inlet openings 9 and 10, forming a first liquid flow 12 and a second liquid flow 13, into the mixing chamber 15.
  • the opening angle ⁇ of the conical section 17 the diameter D and the length L of the part of the cylindrical section 16 which delimits the mixing chamber 15 (FIG. 1B)
  • the two liquid flows 12 and 13 along the walls of the cylindrical section 16 or the conical section 17 to meet at the outlet opening 30 and thereby form the spray jet 40.
  • an enlargement 31 of the cross-sectional area of the outlet slot 31 in the direction of propagation 39 of the spray jet 40 is provided at the narrow ends of the outlet slot 30.
  • 2 C indicates an alternative embodiment of the outlet slot 30.
  • the cross section of the outlet slot 30 in FIG. 2C has extensions 32 in the middle of the long sides in the direction of propagation 39 of the spray jet 40. The extensions lead to an accumulation of drops within the plane of symmetry 35 in the direction of the longitudinal axis 38.
  • Guide walls 45, 46 are arranged essentially parallel to the plane of symmetry 35. Depending on the distance from the plane of symmetry 35, the guide walls act as a limitation of the spray jet 40 emerging from the outlet opening 30 and / or to protect the spray jet 40 against external disturbances, for example movements of the ambient air.
  • the spray nozzle according to the invention is also functional for 60 ° ⁇ ⁇ 130 °, with 80 ° ⁇ ⁇ 00 ° being a preferred range.
  • the operating pressure p is between 1 bar and at least 10 bar.
  • the optimal ratio is the sum of the cross-sectional areas of the inlet opening to the cross-sectional area of the outlet opening between 1.5 and 2, preferably between 1.6 and 1.8, and the optimal ratio of the diameter D of the cylindrical segment 16 to the length L of the cylindrical segment 16 in the mixing chamber 15 between 2 and 3.
  • the impact pressure in the same reference di punch becomes correspondingly smaller or larger.
  • a - C represent an asymmetrical spray nozzle 50 which can be regarded as a modification of the spray nozzle 5 described above which is distinguished by the plane of symmetry 35.
  • the asymmetrical spray nozzle 50 differs from the symmetrical spray nozzle 5 in that the transverse web 8 is offset with respect to the plane of symmetry 35, the inlet openings 9 and 10 consequently form circular segments with different surfaces A 1 and A2 and the guide surfaces 45 and 46 have different distances ti or 12 with respect to the center of the outlet opening 30.
  • the inlet openings 9 and 10 with the smaller cross-sectional area is arranged on the same side of the plane of symmetry 35 as that of the guide walls 45 and 46, which is at a greater distance from the plane of symmetry 35. Due to the different shape or dimensioning of the inlet openings 9 and 10, the liquid streams 12 and 13 transport different amounts of liquid (indicated in FIG. 3 C by arrows with a stroke width corresponding to the amount of liquid).
  • the spray jet 40 is dependent on the distance x from the plane of symmetry 35 by a drop distribution P ( x) characterized, the maximum of which is at a distance x ⁇ from the plane of symmetry 35 on the side opposite the inlet opening 10.
  • the distance x ⁇ can be determined by appropriately specifying the widths w-
  • a rectangular spray surface with a homogeneous drop distribution P (x) is created in a plane perpendicular to the plane of symmetry 35.
  • a spray surface deviating from the rectangular shape can arise, for example in the form of a section of a circular ring.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Organic Chemistry (AREA)
  • Thermal Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Physics & Mathematics (AREA)
  • Continuous Casting (AREA)
  • Nozzles (AREA)
  • Coating With Molten Metal (AREA)
  • On-Site Construction Work That Accompanies The Preparation And Application Of Concrete (AREA)
  • Heat Treatments In General, Especially Conveying And Cooling (AREA)
  • Heat Treatment Of Articles (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
EP98959851A 1997-11-14 1998-11-05 Buse a jet eventail destinee a pulveriser un liquide de refroidissement sur un produit de coulee continue Expired - Lifetime EP1047504B1 (fr)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
CH263997 1997-11-14
CH263997 1997-11-14
PCT/EP1998/007069 WO1999025481A1 (fr) 1997-11-14 1998-11-05 Buse a jet eventail destine a pulveriser un liquide de refroidissement sur un produit de coulee continue

Publications (2)

Publication Number Publication Date
EP1047504A1 true EP1047504A1 (fr) 2000-11-02
EP1047504B1 EP1047504B1 (fr) 2001-10-24

Family

ID=4238287

Family Applications (1)

Application Number Title Priority Date Filing Date
EP98959851A Expired - Lifetime EP1047504B1 (fr) 1997-11-14 1998-11-05 Buse a jet eventail destinee a pulveriser un liquide de refroidissement sur un produit de coulee continue

Country Status (20)

Country Link
US (1) US6360973B1 (fr)
EP (1) EP1047504B1 (fr)
JP (1) JP2001523554A (fr)
CN (1) CN1107551C (fr)
AT (1) ATE207389T1 (fr)
AU (1) AU733220B2 (fr)
BR (1) BR9814137A (fr)
CA (1) CA2308507C (fr)
CZ (1) CZ295473B6 (fr)
DE (1) DE59801901D1 (fr)
DK (1) DK1047504T3 (fr)
ES (1) ES2165708T3 (fr)
PL (1) PL194516B1 (fr)
PT (1) PT1047504E (fr)
RU (1) RU2213627C2 (fr)
TR (1) TR200001364T2 (fr)
TW (1) TW477722B (fr)
UA (1) UA49098C2 (fr)
WO (1) WO1999025481A1 (fr)
ZA (1) ZA9810418B (fr)

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CA2308507A1 (fr) 1999-05-27
PL194516B1 (pl) 2007-06-29
CA2308507C (fr) 2012-01-10
BR9814137A (pt) 2000-10-03
RU2213627C2 (ru) 2003-10-10
CN1278748A (zh) 2001-01-03
CN1107551C (zh) 2003-05-07
PL340464A1 (en) 2001-02-12
DE59801901D1 (de) 2001-11-29
AU733220B2 (en) 2001-05-10
AU1560599A (en) 1999-06-07
PT1047504E (pt) 2002-04-29
DK1047504T3 (da) 2002-02-18
CZ20001760A3 (cs) 2001-03-14
TW477722B (en) 2002-03-01
JP2001523554A (ja) 2001-11-27
TR200001364T2 (tr) 2000-11-21
US6360973B1 (en) 2002-03-26
ATE207389T1 (de) 2001-11-15
ZA9810418B (en) 1999-05-14
ES2165708T3 (es) 2002-03-16
WO1999025481A1 (fr) 1999-05-27
EP1047504B1 (fr) 2001-10-24
UA49098C2 (uk) 2002-09-16
CZ295473B6 (cs) 2005-08-17

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