EP1203106B1 - Method and installation for hot dip galvanizing hot rolled steel strip - Google Patents
Method and installation for hot dip galvanizing hot rolled steel strip Download PDFInfo
- Publication number
- EP1203106B1 EP1203106B1 EP00958379A EP00958379A EP1203106B1 EP 1203106 B1 EP1203106 B1 EP 1203106B1 EP 00958379 A EP00958379 A EP 00958379A EP 00958379 A EP00958379 A EP 00958379A EP 1203106 B1 EP1203106 B1 EP 1203106B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- strip
- station
- hot
- pickling
- temperature
- 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.)
- Expired - Lifetime
Links
- 238000000034 method Methods 0.000 title claims abstract description 35
- 238000005246 galvanizing Methods 0.000 title claims abstract description 30
- 229910000831 Steel Inorganic materials 0.000 title claims abstract description 10
- 239000010959 steel Substances 0.000 title claims abstract description 10
- 238000009434 installation Methods 0.000 title 1
- 238000001035 drying Methods 0.000 claims abstract description 19
- 238000005554 pickling Methods 0.000 claims abstract description 19
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000011701 zinc Substances 0.000 claims abstract description 14
- 229910052725 zinc Inorganic materials 0.000 claims abstract description 13
- 239000000047 product Substances 0.000 claims abstract description 7
- 230000001681 protective effect Effects 0.000 claims abstract description 7
- 239000007795 chemical reaction product Substances 0.000 claims abstract description 4
- 238000007654 immersion Methods 0.000 claims abstract description 4
- 239000001301 oxygen Substances 0.000 claims description 11
- 229910052760 oxygen Inorganic materials 0.000 claims description 11
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 10
- 239000007789 gas Substances 0.000 claims description 8
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 4
- 229910000069 nitrogen hydride Inorganic materials 0.000 claims description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 claims description 2
- 239000001257 hydrogen Substances 0.000 claims description 2
- 229910052739 hydrogen Inorganic materials 0.000 claims description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 2
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen(.) Chemical compound [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 claims description 2
- 230000005855 radiation Effects 0.000 claims description 2
- 238000005406 washing Methods 0.000 claims 10
- 238000009736 wetting Methods 0.000 claims 1
- 235000021110 pickles Nutrition 0.000 abstract 1
- 238000000576 coating method Methods 0.000 description 5
- 238000005496 tempering Methods 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 239000011248 coating agent Substances 0.000 description 4
- 230000003647 oxidation Effects 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- 238000000137 annealing Methods 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 229910001297 Zn alloy Inorganic materials 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000003618 dip coating Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 238000013021 overheating Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 230000007704 transition Effects 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- 229910045601 alloy Inorganic materials 0.000 description 1
- 239000000956 alloy Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000009713 electroplating Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 1
- 235000013980 iron oxide Nutrition 0.000 description 1
- VBMVTYDPPZVILR-UHFFFAOYSA-N iron(2+);oxygen(2-) Chemical class [O-2].[Fe+2] VBMVTYDPPZVILR-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 239000002243 precursor Substances 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 239000005871 repellent Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 238000006557 surface reaction Methods 0.000 description 1
- 238000012549 training Methods 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C2/00—Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
- C23C2/003—Apparatus
- C23C2/0038—Apparatus characterised by the pre-treatment chambers located immediately upstream of the bath or occurring locally before the dipping process
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C2/00—Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
- C23C2/02—Pretreatment of the material to be coated, e.g. for coating on selected surface areas
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C2/00—Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
- C23C2/02—Pretreatment of the material to be coated, e.g. for coating on selected surface areas
- C23C2/022—Pretreatment of the material to be coated, e.g. for coating on selected surface areas by heating
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C2/00—Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
- C23C2/02—Pretreatment of the material to be coated, e.g. for coating on selected surface areas
- C23C2/024—Pretreatment of the material to be coated, e.g. for coating on selected surface areas by cleaning or etching
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23G—CLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
- C23G1/00—Cleaning or pickling metallic material with solutions or molten salts
- C23G1/02—Cleaning or pickling metallic material with solutions or molten salts with acid solutions
- C23G1/08—Iron or steel
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23G—CLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
- C23G1/00—Cleaning or pickling metallic material with solutions or molten salts
- C23G1/14—Cleaning or pickling metallic material with solutions or molten salts with alkaline solutions
- C23G1/19—Iron or steel
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23G—CLEANING OR DE-GREASING OF METALLIC MATERIAL BY CHEMICAL METHODS OTHER THAN ELECTROLYSIS
- C23G3/00—Apparatus for cleaning or pickling metallic material
- C23G3/02—Apparatus for cleaning or pickling metallic material for cleaning wires, strips, filaments continuously
- C23G3/027—Associated apparatus, e.g. for pretreating or after-treating
- C23G3/029—Associated apparatus, e.g. for pretreating or after-treating for removing the pickling fluid from the objects
Definitions
- the invention relates to a method and a system for hot dip galvanizing hot-rolled steel strip, the strip being in a first process step introduced into a pickling station and therein a layer of scale and reaction products be removed from the belt surface.
- the belt is inserted into a rinsing station and the Belt surface washed away from residues of the pickling and pickling products, and then inserted into a drying station and dried in it.
- the hot-dip coating in particular the hot-dip galvanizing of hot-rolled steel strip, so-called hot strip, is becoming more and more important economically compared to conventional cold-rolled strip coating.
- hot strip Through the development of thin slab technology in hot strip, there is the technical possibility of producing hot strips in the thickness range below 1.2 mm from the casting heat. There is also the possibility, depending on customer requirements, to replace cold strip with comparatively cheaper hot strip.
- the actual coating process is an annealing furnace upstream, in which at high temperatures a structural transformation to achieve the desired mechanical properties.
- the existing one Temperature difference between molten bath, preferably zinc or Zinc alloys, and the maximum strip temperature can be up to 400 ° C. With this tape overheating, however, a fire coating is not feasible, which is why the tape cools down before coating Temperatures close to the melting bath temperature must be made.
- Hot strip or pre-annealed cold strip do not require annealing in order to influence the mechanical properties, rather the Band temperature only adjusted to that of the melt pool to the desired Reaction of the steel strip surface with the alloy components to reach the weld pool. In contrast is a high temperature annealing often even disadvantageous for the mechanical properties of the belt.
- the present invention relates exclusively to the process variants for hot strip hot finishing or hot strip hot galvanizing.
- the desired temperature level lies with previously operated systems for fire coating still higher than the required 450 ° C of the zinc bath. reason for that is the required removal of all oxidation products and their precursors the steel strip surface. Oxidation products inevitably arise in the transition area from the pickling stage via the rinsing and drying stage into the oven entrance by exposure to atmospheric oxygen. The amount and training of in Oxidation products entering the furnace and those brought in from the belt Atmospheric oxygen determine the necessary process parameters of the treatment procedure, characterized by a required reduction potential, Temperature level and holding time. The temperature level used is often high so high that the strip is additionally cooled before entering the zinc bath must become.
- Document WO 83/00885 discloses a metal band, of which the iron oxides were removed by reduction in a protective gas atmosphere, and its Temperature brought a little higher than the melting temperature of the zinc bath with the metal strip immersed in the conventional zinc bath becomes.
- the bath contains mixed metal in a ratio between 0.01% and 0.5 % preferably between 0.02% and 0.08%.
- the object of the invention based on specifying a method and a hot strip galvanizing plant, which overcomes the aforementioned disadvantages and difficulties and hot-dip galvanized with an economical outlay on material and operating costs Steel strip delivers high and flawless surface quality.
- a corresponding plant for performing the method according to the invention accordingly provides that the outlet of the last rinsing stage of the rinsing station with the inlet of the dryer and its outlet with the inlet of the Furnace connected by locks and facing the surrounding Atmosphere are hermetically sealed.
- the above-mentioned measures preserve the optimal strip condition after pickling into the oven and achieve an optimal setting of the strip temperature when immersed in the zinc bath.
- the access of oxygen and the associated surface reactions, especially oxidation, are prevented.
- This enables furnace operation at temperatures in the range of the melt bath temperature. Overheating of the belt and an extension of the holding time in the oven are not necessary. A belt cooler becomes superfluous.
- the procedure according to the invention and the corresponding system allow a much more compact design of the furnace element and lower investment and operating costs.
- furnace operation with lower H 2 contents in the protective gas is possible.
- the disadvantages in the aforementioned conventional method with an increased zinc bath temperature are advantageously avoided.
- the strip is namely set to a temperature which is at most 50 ° K higher than the immersion temperature in the zinc bath.
- a strip 50 is transferred to a pickling station 10 introduced with three pickling stages 11 to 13 and in it a scale layer as well as reaction products removed from the belt surface.
- a pickling station 10 usually pickling in the pickling station 10 or in the pickling stages 11, 12, 13 using hydrochloric acid (HCL).
- HCL hydrochloric acid
- the belt 50 is brought into the rinsing station 20 the rinse stages 21 to 23 introduced and therein the belt surface of residues the stain and the stain products exempt. Then the tape is in the drying station 30 inserted and dried therein. From there the tape 50 in a further method step into an oven 40, comprising a preheating stage 41 and an integrated temperature control stage 42, introduced and therein preferably heated to a tempering temperature in a protective gas atmosphere, and passed through a galvanizing bath in a last process step. The surface of the strip 50 is coated with a hot-dip galvanizing layer overdrawn.
- a water-repellent or binding medium 25 is introduced into the rinsing stage 23.
- NH 3 or a solution of NH 3 can be used as the medium.
- a preferred embodiment of the method provides that the belt 50 is rinsed in the rinsing station 20 in the first stages 21, 22 with deionized water and in the third stage 23 with or with the addition of NH 3 as the drying medium.
- the measures according to the invention maintain the optimum strip state after pickling into the tempering furnace because the introduction of atmospheric oxygen is prevented.
- its design can be simplified due to the lower heating power required and the cooling section eliminated and can be realized with more favorable investment and operating costs. Oven operation is also possible with comparatively low H 2 contents in the protective gas.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Coating With Molten Metal (AREA)
- Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
Abstract
Description
Die Erfindung betrifft ein Verfahren sowie eine Anlage zum Feuerverzinken von warmgewalztem Stahlband, wobei in einem ersten Verfahrensschritt das Band in eine Beizstation eingeführt und darin eine Zunderschicht sowie Reaktionsprodukte von der Bandoberfläche entfernt werden. In einem weiteren Verfahrensschritt wird das Band in eine Spülstation eingeführt und darin die Bandoberfläche von Rückständen der Beize und Beizprodukten freigespült, und anschließend in eine Trockenstation eingeführt und darin getrocknet. Von dort wird das Band in einem weiteren Verfahrensschritt in einen Ofen eingeführt und darin unter Schutzgasatmosphäre auf Verzinkungstemperatur eingestellt, und in einem letzten Verfahrensschritt durch ein Verzinkungsbad hindurchgeführt und dabei die Oberfläche des Bandes mit einer Feuerverzinkungsschicht überzogen, wobei die Bandtemperatur im Ofen maximal auf 50°K über Eintauchtemperatur in das Zinkbad eingestellt wird.The invention relates to a method and a system for hot dip galvanizing hot-rolled steel strip, the strip being in a first process step introduced into a pickling station and therein a layer of scale and reaction products be removed from the belt surface. In a further process step the belt is inserted into a rinsing station and the Belt surface washed away from residues of the pickling and pickling products, and then inserted into a drying station and dried in it. From there in a further process step, the strip is introduced into an oven and set in a protective gas atmosphere to the galvanizing temperature, and in a final process step through a galvanizing bath and the surface of the strip is coated with a hot-dip galvanizing layer, the belt temperature in the furnace is a maximum of 50 ° K above the immersion temperature is placed in the zinc bath.
Die Feuerbeschichtung, insbesondere die Feuerverzinkung von warmgewalzten
Stahlband, sogenanntem Warmband, gewinnt gegenüber der herkömmlichen
Kaltbandfeuerbeschichtung wirtschaftlich mehr und mehr an Bedeutung.
Durch Entwicklung der Dünnbrammentechnologie bei Warmband besteht die
technische Möglichkeit, Warmbänder im Dickenbereich unter 1,2 mm aus der
Gießhitze zu erzeugen. Es besteht damit ferner die Möglichkeit, Kaltband in
Abhängigkeit der Kundenanforderungen durch vergleichsweise preisgünstigeres
Warmband zu substituieren.The hot-dip coating, in particular the hot-dip galvanizing of hot-rolled steel strip, so-called hot strip, is becoming more and more important economically compared to conventional cold-rolled strip coating.
Through the development of thin slab technology in hot strip, there is the technical possibility of producing hot strips in the thickness range below 1.2 mm from the casting heat. There is also the possibility, depending on customer requirements, to replace cold strip with comparatively cheaper hot strip.
Für die Feuerbeschichtung, insbesondere das Feuerverzinken von Stahlbändern, sind unterschiedliche Verfahren und Anlagen bekannt. Hierbei handelt es sich überwiegend um Anlagentypen, bei denen kaltgewalzte Bänder zum Einsatz kommen.For hot-dip coating, especially hot-dip galvanizing steel strips, different processes and systems are known. This is what it is about are mainly plant types in which cold-rolled strips are used come.
In solchen Anlagen ist dem eigentlichen Beschichtungsprozess ein Glühofen vorgeschaltet, worin bei hohen Temperaturen eine Gefügeumwandlung zur Erzielung der gewünschten mechanischen Eigenschaften erfolgt. Der dabei vorhandene Temperaturunterschied zwischen Schmelzbad, bevorzugt Zink oder Zinklegierungen, und der maximalen Bandtemperatur kann bis zu 400° C betragen. Mit dieser Bandüberhitzung ist jedoch eine Feuerbeschichtung nicht durchführbar, weshalb eine Abkühlung des Bandes vor der Beschichtung auf Temperaturen nahe der Schmelzbadtemperatur vorgenommen werden muß.In such systems, the actual coating process is an annealing furnace upstream, in which at high temperatures a structural transformation to achieve the desired mechanical properties. The existing one Temperature difference between molten bath, preferably zinc or Zinc alloys, and the maximum strip temperature can be up to 400 ° C. With this tape overheating, however, a fire coating is not feasible, which is why the tape cools down before coating Temperatures close to the melting bath temperature must be made.
Warmband bzw. vorgeglühtes Kaltband bedürfen dagegen keiner Glühung zwecks Beeinflussung der mechanischen Eigenschaften, vielmehr wird die Bandtemperatur lediglich der des Schmelzbades angepasst, um die gewünschte Reaktion der Stahlbandoberfläche mit den Legierungsbestandteilen des Schmelzbades zu erreichen. Dagegen ist eine Hochtemperaturglühung oftmals für die mechanischen Eigenschaften des Bandes sogar von Nachteil.Hot strip or pre-annealed cold strip, however, do not require annealing in order to influence the mechanical properties, rather the Band temperature only adjusted to that of the melt pool to the desired Reaction of the steel strip surface with the alloy components to reach the weld pool. In contrast is a high temperature annealing often even disadvantageous for the mechanical properties of the belt.
Die vorliegende Erfindung betrifft exemplarisch ausschließlich die Verfahrensvarianten zur Warmband-Feuerveredelung bzw. Warmband-Feuerverzinkung.By way of example, the present invention relates exclusively to the process variants for hot strip hot finishing or hot strip hot galvanizing.
Das angestrebte Temperatumiveau, insbesondere bei der Warmband-Feuerverzinkung, liegt bei bisher betriebenen Anlagen zur Feuerbeschichtung immer noch höher, als die erforderlichen 450° C des Zinkbades. Grund dafür ist die erforderliche Entfernung aller Oxidationsprodukte und ihrer Vorstufen aus der Stahlbandoberfläche. Oxidationsprodukte entstehen zwangsläufig im Übergangsbereich aus der Beizstufe über Spül- und Trocknungsstufe in den Ofeneingang durch Einwirkung von Luftsauerstoff. Die Menge und Ausbildung der in den Ofen eintretenden Oxidationsprodukte und der vom Band eingeschleppte Luftsauerstoff bestimmen die notwendigen Verfahrensparameter der Behandlungsprozedur, gekennzeichnet durch ein erforderliches Reduktionspotential, Temperaturniveau und Haltezeit. Vielfach liegt das angewendete Temperatumiveau so hoch, dass das Band vor Eintritt in das Zinkbad noch zusätzlich gekühlt werden muss.The desired temperature level, especially for hot-dip hot-dip galvanizing, lies with previously operated systems for fire coating still higher than the required 450 ° C of the zinc bath. reason for that is the required removal of all oxidation products and their precursors the steel strip surface. Oxidation products inevitably arise in the transition area from the pickling stage via the rinsing and drying stage into the oven entrance by exposure to atmospheric oxygen. The amount and training of in Oxidation products entering the furnace and those brought in from the belt Atmospheric oxygen determine the necessary process parameters of the treatment procedure, characterized by a required reduction potential, Temperature level and holding time. The temperature level used is often high so high that the strip is additionally cooled before entering the zinc bath must become.
Eine andere Arbeitsweise ist durch eine signifikante Erhöhung des Temperaturniveaus im Zinkbad auf Werte oberhalb von 460° C gekennzeichnet. Besonders nachteilig bei dieser Verfahrensführung ist der erhöhte Anfall an zinkhaltiger Schlacke. Dies führt einerseits zu erhöhten Material- und Betriebskosten für das Zinkbad, sowie andererseits zu qualitativen Einbußen am Band.Another way of working is by significantly increasing the temperature level marked in the zinc bath to values above 460 ° C. Especially a disadvantage of this procedure is the increased occurrence of zinc-containing Slag. On the one hand, this leads to increased material and operating costs for the Zinc bath, as well as loss of quality on the assembly line.
Der dokumentarisch belegte Stand der Technik zeigt darüber hinaus Folgendes:
- Vorheizen bis zu einer Temperatur, die geeignet ist zum Erreichen erwünschter mechanischer Eigenschaften des Bandes. Die Vorheiztemperatur wird zwischen 400° C und 950° C eingestellt. Abschrecken des Bandes in einem wässrigen Bad bei dessen Siedetemperatur. Herausnehmen des Bandes aus dem Bad. Dabei soll eine Oxydschicht von weniger als 2 g/m2 ausgebildet sein. Eliminieren der Oxydschicht von wenigstens einem Oberflächenbereich des Bandes und Einstellen der Temperatur im Bereich von 420° und 550° C und Aufrechterhalten dieser Temperatur.
- Preheat to a temperature suitable for achieving the desired mechanical properties of the belt. The preheating temperature is set between 400 ° C and 950 ° C. Quench the tape in an aqueous bath at its boiling temperature. Take the tape out of the bathroom. An oxide layer of less than 2 g / m 2 should be formed. Eliminate the oxide layer from at least one surface area of the tape and adjust the temperature in the range of 420 ° and 550 ° C and maintain that temperature.
Das Dokument WO 83/00885 offenbart ein Metallband, von dem die Eisenoxyde durch Reduktion in einer Schutzgasatmosphäre entfernt wurden, und dessen Temperatur ein wenig höher als die Schmelztemperatur des Zinkbades gebracht wurde, wobei das Metallband in das konventionelle Zinkbad eingetaucht wird. Das Bad enthält Mischmetall in einem Verhältnis zwischen 0,01 % und 0,5 % vorzugsweise zwischen 0,02 % und 0,08 %.Document WO 83/00885 discloses a metal band, of which the iron oxides were removed by reduction in a protective gas atmosphere, and its Temperature brought a little higher than the melting temperature of the zinc bath with the metal strip immersed in the conventional zinc bath becomes. The bath contains mixed metal in a ratio between 0.01% and 0.5 % preferably between 0.02% and 0.08%.
Ausgehend vom vorgenannten Stand der Technik liegt der Erfindung die Aufgabe zugrunde, ein Verfahren und eine Warmbandverzinkungsanlage anzugeben, welche die vorbezeichneten Nachteile und Schwierigkeiten überwindet und mit einem ökonomischen Aufwand an Material- und Betriebskosten feuerverzinktes Stahlband von hoher und fehlerloser Oberflächenqualität liefert.Starting from the aforementioned prior art, the object of the invention based on specifying a method and a hot strip galvanizing plant, which overcomes the aforementioned disadvantages and difficulties and hot-dip galvanized with an economical outlay on material and operating costs Steel strip delivers high and flawless surface quality.
Zur Lösung der Aufgabe wird bei einem Verfahren der im Oberbegriff von Anspruch 1 genannten Art mit der Erfindung vorgeschlagen, dass die Verfahrensschritte zwischen der letzten Spülstufe der Spülstation über die Trockenstation bis hin zum Einlass des Ofens unter hermetischer Abschirmung gegen Luft und Sauerstoff aus der Umgebung durchgeführt werden.To solve the problem is in a method in the preamble of claim 1 mentioned type with the invention that the method steps between the last rinsing stage of the rinsing station via the drying station to the inlet of the furnace under hermetic shielding against air and Oxygen can be carried from the environment.
Eine entsprechende Anlage zur Durchführung des Verfahrens nach der Erfindung sieht demgemäß vor, dass der Auslass der letzten Spülstufe der Spülstation mit dem Einlass des Trockners und dessen Auslass mit dem Einlass des Ofens durch Schleusen miteinander verbunden und gegenüber der umgebenden Atmosphäre hermetisch abgedichtet sind.A corresponding plant for performing the method according to the invention accordingly provides that the outlet of the last rinsing stage of the rinsing station with the inlet of the dryer and its outlet with the inlet of the Furnace connected by locks and facing the surrounding Atmosphere are hermetically sealed.
Weitere zweckmäßige Ausgestaltungen einerseits des Verfahrens und andererseits der Warmbandverzinkungsanlage sind entsprechend den Merkmalen von Unteransprüchen vorgesehen.Further expedient refinements of the method on the one hand and on the other hand the hot strip galvanizing plant are in accordance with the characteristics of Subclaims provided.
Mit Vorteil wird durch das Verfahren und durch die Anlage nach der Erfindung
sichergestellt, dass der nach Durchlauf des Bandes durch die Beizstation und
Spülstation erreichte optimale Oberflächenzustand des Bandes in der anschließenden
Trocknungsstufe sowie beim Übergang in den Ofenbereichen und aus
diesem in das Verzinkungsbad konserviert wird.
Dies wird erreicht durch:
- direkte Kopplung zumindest der letzten Spülstufe der Spülstation über die Trocknungsstufe mit dem Ofeneingang unter Abschirmung von Luftsauerstoff,
- Auftragen eines wasserbindenden Mediums, bevorzugt NH3, oder einer Lösung davon, auf das Band in der Spülstufe, wonach sich in der anschließenden Trocknungsstufe das wasserbindende Medium schnell und rückstandsfrei, das heißt ohne Eintrag von Sauerstoff oder flüssiges Reinigungsmedium vom Band entfernen lässt,
- alternativ durch einen Betrieb der Trockenstufe mit einer reduzierend wirkenden Atmosphäre, zum Beispiel N2/H2-Gasgemisch.
This is achieved through:
- direct coupling of at least the last rinsing stage of the rinsing station via the drying stage to the oven entrance with shielding from atmospheric oxygen,
- Applying a water-binding medium, preferably NH 3 , or a solution thereof, to the belt in the rinsing stage, after which the water-binding medium can be removed from the belt quickly and without residue in the subsequent drying stage, that is to say without oxygen or liquid cleaning medium being introduced,
- alternatively by operating the drying stage with a reducing atmosphere, for example N 2 / H 2 gas mixture.
Durch vorgenannte Maßnahmen wird der optimale Bandzustand nach dem Beizen
bis in den Ofen konserviert und eine optimale Einstellung der Bandtemperatur
beim Eintauchen in das Zinkbad erreicht. Der Zutritt von Sauerstoff und
die damit verbundenen Oberflächenreaktionen, insbesondere Oxidation, sind
unterbunden. Dies ermöglicht den Ofenbetrieb bei Temperaturen im Bereich der
Schmelzbadtemperatur. Eine Überhitzung des Bandes und eine Verlängerung
der Haltezeit im Ofen entfallen. Ein Bandkühler wird überflüssig. Insgesamt erlaubt
die Vorgehensweise nach der Erfindung und die entsprechende Anlage
eine wesentlich kompaktere Bauweise des Ofenelements und niedrigere Investitions-
und Betriebskosten. Zugleich ist der Ofenbetrieb mit niedrigeren H2-Gehalten
im Schutzgas möglich. Die Nachteile bei dem vorgenannten konventionellen
Verfahren mit erhöhter Zinkbadtemperatur werden vorteilhaft vermieden.
Erfindungsgemäß wird nämlich das Band auf eine Temperatur eingestellt, die
maximal 50 °K höher liegt, als die Eintauchtemperatur in das Zinkbad.The above-mentioned measures preserve the optimal strip condition after pickling into the oven and achieve an optimal setting of the strip temperature when immersed in the zinc bath. The access of oxygen and the associated surface reactions, especially oxidation, are prevented. This enables furnace operation at temperatures in the range of the melt bath temperature. Overheating of the belt and an extension of the holding time in the oven are not necessary. A belt cooler becomes superfluous. Overall, the procedure according to the invention and the corresponding system allow a much more compact design of the furnace element and lower investment and operating costs. At the same time, furnace operation with lower H 2 contents in the protective gas is possible. The disadvantages in the aforementioned conventional method with an increased zinc bath temperature are advantageously avoided.
According to the invention, the strip is namely set to a temperature which is at most 50 ° K higher than the immersion temperature in the zinc bath.
Weitere Einzelheiten, Merkmale und Vorteile der Erfindung ergeben sich aus der nachstehenden Erläuterung eines in den Zeichnungen schematisch dargestellten Ausführungsbeispieles. Es zeigen:
- Figur 1
- ein Layout einer Feuerverzinkungsanlage nach dem Stand der Technik,
- Figur 2
- ein Layout einer Feuerverzinkungsanlage nach der Erfindung.
- Figure 1
- a layout of a hot-dip galvanizing plant according to the prior art,
- Figure 2
- a layout of a hot-dip galvanizing plant according to the invention.
Gemäß dem in Figur 1 gezeigten Layout einer konventionellen Feuerverzinkungsanlage
wird in einem ersten Verfahrensschritt ein Band 50 in eine Beizstation
10 mit drei Beizstufen 11 bis 13 eingeführt und darin eine Zunderschicht
sowie Reaktionsprodukte von der Bandoberfläche entfernt. Üblicherweise wird
das Beizen in der Beizstation 10 bzw. in den Beizstufen 11, 12, 13 mittels Salzsäure
(HCL) vorgenommen.According to the layout of a conventional hot-dip galvanizing plant shown in FIG
in a first process step, a
In dem folgenden Verfahrensschritt wird das Band 50 in die Spülstation.20 mit
den Spülstufen 21 bis 23 eingeführt und darin die Bandoberfläche von Rückständen
der Beize und der Beizprodukte befreit. Anschließend wird das Band in
die Trockenstation 30 eingeführt und darin getrocknet. Von dort wird das Band
50 in einem weiteren Verfahrensschritt in einen Ofen 40, umfassend eine Vorwärmstufe
41 sowie eine integrierte Temperierstufe 42, eingeführt und darin
bevorzugt unter Schutzgasatmosphäre bis auf Veizinkungstemperatur erwärmt,
und in einem letzten Verfahrensschritt durch ein Verzinkungsbad hindurchgeführt.
Dabei wird die Oberfläche des Bandes 50 mit einer Feuerverzinkungsschicht
überzogen.In the following process step, the
Im Gegensatz zur konventionellen Verzinkungsanlage nach Figur 1 werden
nach dem erfindungsgemäßen Layout der Feuerverzinkungsanlage gemäß Figur
2 die Verfahrensschritte zwischen der letzten Spülstufe 23 der Spülstation
20 über die Trockenstation 30 bis hin zum Einlaß 43 des Temperierofens 40
unter hermetischer Abschirmung von Luftsauerstoff aus der Umgebung ausgeführt.In contrast to the conventional galvanizing plant according to Figure 1
according to the layout of the hot-dip galvanizing plant according to the invention according to FIG
2 the process steps between the
Unter Erweiterung der Spülstation 20 um eine Spülstufe 23 bzw. durch Abschotten
der Spülstufe 23 mit Hilfe einer Trennwand 24 von den vorhergehenden
Spülstufen 21, 22 wird ein wasserabweisendes bzw. -bindendes Medium
25 in die Spülstufe 23 eingegeben. Als Medium kann beispielsweise NH3, oder
eine Lösung von NH3 verwendet werden.By expanding the rinsing
Eine vorzugsweise Ausgestaltung des Verfahrens sieht vor, daß die Spülung
des Bandes 50 in der Spülstation 20 in den ersten Stufen 21, 22 mit deionisiertem
Wasser und in der dritten Stufe 23 mit oder unter Zusatz von NH3 als
Trocknuhgsmedium durchgeführt wird.A preferred embodiment of the method provides that the
Die Trocknung des Bandes 50 in der Trockenstation 30 erfolgt ohne Luftzufuhr.
Erfindungsgemäß wird die Trocknung mittels Wärmestrahlung unter Zusatz einer
Mischung von Stickstoff-, Wasserstoff- und Ammoniakgas (N2/NH3) bzw. H2
durchgeführt.The
Die Trockenstation 30 ist beiderseits mit Schleusen 70, 80 im Anschluß an die
benachbarten Stationen 20 und 40 hermetisch gegen Zutritt von Luftsauerstoff
abgeschlossen, wobei der Auslaß der letzten Spülstufe 23 der Spülstation 20
mit dem Einlaß der Trockenstation 30 und dessen Auslaß mit dem Einlaß 43
des Temperierofens 40 durch Schleusen 70, 80 miteinander verbunden und
gegenüber der umgebenden Atmosphäre hermetisch abgedichtet sind. The drying
Durch die erfindungsgemäßen Maßnahmen wird der optimale Bandzustand
nach dem Beizen bis in den Temperierofen erhalten, weil das Einschleppen von
Luftsauerstoff unterbunden wird. Infolgedessen kann, wie dies der Darstellung
des Temperierofens 40 in Figur 2 zu entnehmen ist, dessen Bauart aufgrund
der niedrigeren erforderlichen Heizleistung und Wegfall der Kühlstrecke vereinfacht
und mit günstigeren Investitions- und Betriebskosten realisiert werden.
Der Ofenbetrieb ist zudem mit vergleichsweise niedrigen H2-Gehalten im
Schutzgas möglich.The measures according to the invention maintain the optimum strip state after pickling into the tempering furnace because the introduction of atmospheric oxygen is prevented. As a result, as can be seen from the illustration of the tempering
Claims (6)
- Method of hot-galvanising hot-rolled steel strip, wherein:in a first step the strip (50) is introduced into a pickling station (10-13) and a scale layer as well as reaction products are removed from the strip surface,in a further step the strip (50) is introduced into a washing station (21-23) and the strip surface is freed therein from residues of the pickling and pickling products, and subsequentlythe strip is introduced and dried in a drying station and from thereintroduced in a further step into an oven (40) and adjusted therein to galvanising temperature under a protective gas atmosphere, andin a last step the strip is conducted through a galvanising bath and the strip surface (50) is then covered with a hot-galvanising layer, wherein the strip temperature in the oven (50) is set to at most 50° K above immersion temperature in the zinc bath,
- Method according to claim 1, characterised in that in the last washing stage (23) of the washing station (20) a water-repelling or water-binding medium (25) wetting the strip (50) is fed.
- Method according to claim 2, characterised in that the medium (25) fed in the third washing stage (23) is NH3 or a solution containing NH3.
- Method according to one or more of claims 1 to 3, characterised in that the drying of the strip (50) in the drying station (30) is carried out without feed of air from the outside by means of heat radiation with addition of a mixture of nitrogen, hydrogen and ammonia gas (N2/NH3) + H2 or a mixture of two of the said gases.
- Hot strip galvanising plant, comprising a pickling station (10), a washing station (20), a drier (30), an oven (40) as well as a downstream hot-galvanising bath (60), characterised in that the outlet of the last washing stage (23) of the washing station (20) is connected with the inlet of the drier (39), and the outlet thereof is connected with the inlet (43) of the furnace (40), by locks (70, 80) and are hermetically sealed off relative to the ambient atmosphere.
- Plant according to claim 5, characterised in that the washing stages (21, 23) and the heating stages (41) or the temperature-controlling stage (42) are partitioned off relative to one another by intermediate walls (24).
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19937216 | 1999-08-06 | ||
DE19937216 | 1999-08-06 | ||
DE19943238A DE19943238A1 (en) | 1999-08-06 | 1999-09-10 | Process and plant for hot-dip galvanizing hot-rolled steel strip |
DE19943238 | 1999-09-10 | ||
PCT/EP2000/007582 WO2001011099A2 (en) | 1999-08-06 | 2000-08-04 | Method and installation for hot dip galvanizing hot rolled steel strip |
Publications (2)
Publication Number | Publication Date |
---|---|
EP1203106A2 EP1203106A2 (en) | 2002-05-08 |
EP1203106B1 true EP1203106B1 (en) | 2004-03-17 |
Family
ID=26054519
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP00958379A Expired - Lifetime EP1203106B1 (en) | 1999-08-06 | 2000-08-04 | Method and installation for hot dip galvanizing hot rolled steel strip |
Country Status (14)
Country | Link |
---|---|
US (1) | US6761936B1 (en) |
EP (1) | EP1203106B1 (en) |
JP (1) | JP2003506573A (en) |
CN (1) | CN1201029C (en) |
AT (1) | ATE262049T1 (en) |
AU (1) | AU777644B2 (en) |
BR (1) | BR0012961A (en) |
CA (1) | CA2381247C (en) |
EG (1) | EG22474A (en) |
ES (1) | ES2216948T3 (en) |
MX (1) | MXPA02001283A (en) |
TR (1) | TR200200323T2 (en) |
TW (1) | TW500827B (en) |
WO (1) | WO2001011099A2 (en) |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100704692B1 (en) * | 2002-09-13 | 2007-04-10 | 제이에프이 스틸 가부시키가이샤 | Manufacturing method and apparatus for hot dip metal strip |
DE102005013103A1 (en) * | 2005-03-18 | 2006-09-28 | Sms Demag Ag | Controlled thickness reduction in hot-dip coated hot rolled steel strip and equipment used in this case |
DE102008005605A1 (en) * | 2008-01-22 | 2009-07-23 | Thyssenkrupp Steel Ag | Process for coating a 6-30% by weight Mn-containing hot or cold rolled flat steel product with a metallic protective layer |
CN103060829B (en) * | 2013-01-31 | 2015-03-11 | 汕尾市栢林电子封装材料有限公司 | Device for removing oxide on metal band surface |
TWI480422B (en) * | 2013-10-07 | 2015-04-11 | China Steel Corp | A device and method for cleaning the mouth of a zinc tank |
EP2927343A1 (en) | 2014-03-31 | 2015-10-07 | Primetals Technologies Austria GmbH | Installation and method for pickling and metal coating of a metal strip |
CN108265252B (en) * | 2018-01-19 | 2020-10-09 | 河北工业大学 | Environment-friendly hot-dip coating method |
CN108823584A (en) * | 2018-07-09 | 2018-11-16 | 宁波甬凌新材料科技有限公司 | A kind of pickling drying pretreating device for metal plate hot galvanizing |
Family Cites Families (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
LU77032A1 (en) * | 1976-04-01 | 1977-07-22 | ||
BE890256A (en) * | 1981-09-07 | 1982-03-08 | Centre Rech Metallurgique | IMPROVEMENTS IN GALVANIZING PROCESSES FOR STEEL SHEETS OR STRIPS |
JPS6179755A (en) * | 1984-09-28 | 1986-04-23 | Nisshin Steel Co Ltd | Continuous plating device in common use for hot dipping and vacuum deposition plating |
US4814210A (en) * | 1984-11-09 | 1989-03-21 | Werner Ackermann | Process and means for hot-dip galvanizing finned tubes |
US5284680A (en) * | 1992-04-27 | 1994-02-08 | Inland Steel Company | Method for producing a galvanized ultra-high strength steel strip |
US5677005A (en) * | 1993-06-25 | 1997-10-14 | Kawasaki Steel Corporation | Method for hot dip galvanizing high tensile steel strip with minimal bare spots |
DE4433946A1 (en) * | 1994-09-23 | 1996-03-28 | Henkel Kgaa | Phosphating process without rinsing |
WO1997031131A1 (en) * | 1996-02-22 | 1997-08-28 | Sumitomo Metal Industries, Ltd. | Galvannealed sheet steel and process for producing the same |
-
2000
- 2000-07-27 TW TW089114988A patent/TW500827B/en active
- 2000-08-04 CN CN00811204.5A patent/CN1201029C/en not_active Expired - Fee Related
- 2000-08-04 EP EP00958379A patent/EP1203106B1/en not_active Expired - Lifetime
- 2000-08-04 AT AT00958379T patent/ATE262049T1/en not_active IP Right Cessation
- 2000-08-04 MX MXPA02001283A patent/MXPA02001283A/en active IP Right Grant
- 2000-08-04 US US10/049,261 patent/US6761936B1/en not_active Expired - Fee Related
- 2000-08-04 BR BR0012961-5A patent/BR0012961A/en not_active Application Discontinuation
- 2000-08-04 TR TR2002/00323T patent/TR200200323T2/en unknown
- 2000-08-04 JP JP2001515344A patent/JP2003506573A/en not_active Withdrawn
- 2000-08-04 WO PCT/EP2000/007582 patent/WO2001011099A2/en active IP Right Grant
- 2000-08-04 CA CA002381247A patent/CA2381247C/en not_active Expired - Fee Related
- 2000-08-04 ES ES00958379T patent/ES2216948T3/en not_active Expired - Lifetime
- 2000-08-04 AU AU69923/00A patent/AU777644B2/en not_active Ceased
- 2000-08-05 EG EG20001001A patent/EG22474A/en active
Also Published As
Publication number | Publication date |
---|---|
CA2381247A1 (en) | 2001-02-15 |
EP1203106A2 (en) | 2002-05-08 |
CA2381247C (en) | 2009-02-03 |
MXPA02001283A (en) | 2002-08-12 |
AU777644B2 (en) | 2004-10-28 |
ATE262049T1 (en) | 2004-04-15 |
WO2001011099A3 (en) | 2001-09-07 |
JP2003506573A (en) | 2003-02-18 |
CN1201029C (en) | 2005-05-11 |
US6761936B1 (en) | 2004-07-13 |
BR0012961A (en) | 2002-04-30 |
EG22474A (en) | 2003-02-26 |
WO2001011099A2 (en) | 2001-02-15 |
ES2216948T3 (en) | 2004-11-01 |
AU6992300A (en) | 2001-03-05 |
TW500827B (en) | 2002-09-01 |
TR200200323T2 (en) | 2002-06-21 |
CN1420942A (en) | 2003-05-28 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
EP2732062B1 (en) | Method for producing a flat steel product which is provided with a metallic protective layer by means of hot dip coating | |
EP2010690B1 (en) | Hot dip coating process for a steel plate product made of high strengthheavy-duty steel | |
EP2812458B1 (en) | Process for the hot dip coating of a flat steel product | |
DE69507977T2 (en) | Chromium-containing aluminized steel alloys and process for their manufacture | |
EP2513346B1 (en) | Method for producing an easily deformable flat steel product | |
EP1819840B1 (en) | Method for hot dip coating a strip of heavy-duty steel | |
DE602005005462T2 (en) | METHOD FOR PRODUCING TAPES OF AUSTENITIC STAINLESS STEEL WITH MATTER SURFACE | |
EP1203106B1 (en) | Method and installation for hot dip galvanizing hot rolled steel strip | |
WO2006045570A1 (en) | Method for producing a steel sheet protected against corrosion | |
DE2928192C2 (en) | Process and device for continuous furnace brazing and gas soft nitriding | |
EP3749793B1 (en) | Method for producing a steel strip with improved bonding of metallic hot-dip coatings | |
EP3511430A1 (en) | Method for a continuous heat treatment of a steel strip, and installation for dip coating a steel strip | |
EP0106113A1 (en) | Process and apparatus for the bright annealing of metallic parts using nitrogen as the protective atmosphere | |
DE19943238A1 (en) | Process and plant for hot-dip galvanizing hot-rolled steel strip | |
EP2818571A1 (en) | Diffusion of aluminium-silicon into a steel sheet web | |
EP0026757B1 (en) | Process for hot galvanizing iron and steel articles | |
EP2821520A1 (en) | Method for the coating of steel flat products with a metallic protective layer and steel flat products with a metallic protective layer | |
DE102016011047A1 (en) | Flexible heat treatment plant for metallic strip in horizontal construction | |
DE19926102B4 (en) | Process and plant for producing an electrolytically coated hot strip | |
DE10258531B3 (en) | Production of a steel with a corrosion protection coating used in the production of an automobile chassis comprises annealing the steel, treating the surface of the steel using high energy, and coating the surface of the steel | |
DE60217344T2 (en) | METHOD FOR SCRUBBING STEEL BY MEANS OF COMPRESSED AIR | |
DE69500797T2 (en) | Process for hot-dip aluminum of a steel strip, containing at least 0.1% manganese, in particular stainless and / or alloy steel | |
DE19543804B4 (en) | Process for producing hot-dip galvanized steel strip and hot-dip galvanized sheet or strip made of steel made therewith | |
EP0959145B1 (en) | Method and apparatus for carrying out the heating of a galvannealed process | |
DE3050505C1 (en) | Method and device for manufacturing brass-shaped elongated products |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 20020130 |
|
AK | Designated contracting states |
Kind code of ref document: A2 Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE |
|
AX | Request for extension of the european patent |
Free format text: AL;LT;LV;MK;RO;SI |
|
17Q | First examination report despatched |
Effective date: 20020612 |
|
GRAP | Despatch of communication of intention to grant a patent |
Free format text: ORIGINAL CODE: EPIDOSNIGR1 |
|
GRAS | Grant fee paid |
Free format text: ORIGINAL CODE: EPIDOSNIGR3 |
|
GRAA | (expected) grant |
Free format text: ORIGINAL CODE: 0009210 |
|
AK | Designated contracting states |
Kind code of ref document: B1 Designated state(s): AT BE CH CY DE DK ES FI FR GB GR IE IT LI LU MC NL PT SE |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: CY Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20040317 Ref country code: IE Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20040317 |
|
REG | Reference to a national code |
Ref country code: GB Ref legal event code: FG4D Free format text: NOT ENGLISH |
|
REG | Reference to a national code |
Ref country code: SE Ref legal event code: TRGR |
|
REG | Reference to a national code |
Ref country code: CH Ref legal event code: EP Ref country code: CH Ref legal event code: NV Representative=s name: SCHMAUDER & PARTNER AG PATENTANWALTSBUERO |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: FG4D Free format text: GERMAN |
|
REF | Corresponds to: |
Ref document number: 50005709 Country of ref document: DE Date of ref document: 20040422 Kind code of ref document: P |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DK Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20040617 Ref country code: GR Free format text: LAPSE BECAUSE OF FAILURE TO SUBMIT A TRANSLATION OF THE DESCRIPTION OR TO PAY THE FEE WITHIN THE PRESCRIBED TIME-LIMIT Effective date: 20040617 |
|
GBT | Gb: translation of ep patent filed (gb section 77(6)(a)/1977) |
Effective date: 20040705 |
|
LTIE | Lt: invalidation of european patent or patent extension |
Effective date: 20040317 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: MC Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20040831 |
|
REG | Reference to a national code |
Ref country code: IE Ref legal event code: FD4D |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FG2A Ref document number: 2216948 Country of ref document: ES Kind code of ref document: T3 |
|
ET | Fr: translation filed | ||
PLBE | No opposition filed within time limit |
Free format text: ORIGINAL CODE: 0009261 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: NO OPPOSITION FILED WITHIN TIME LIMIT |
|
26N | No opposition filed |
Effective date: 20041220 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FI Payment date: 20060810 Year of fee payment: 7 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: LU Payment date: 20060814 Year of fee payment: 7 Ref country code: NL Payment date: 20060814 Year of fee payment: 7 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: CH Payment date: 20060815 Year of fee payment: 7 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: AT Payment date: 20060816 Year of fee payment: 7 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: FR Payment date: 20060817 Year of fee payment: 7 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: GB Payment date: 20060824 Year of fee payment: 7 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: ES Payment date: 20060830 Year of fee payment: 7 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: IT Payment date: 20060831 Year of fee payment: 7 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: BE Payment date: 20060914 Year of fee payment: 7 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: PT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20040817 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: SE Payment date: 20060814 Year of fee payment: 7 |
|
BERE | Be: lapsed |
Owner name: *SMS DEMAG A.G. Effective date: 20070831 |
|
EUG | Se: european patent has lapsed | ||
REG | Reference to a national code |
Ref country code: CH Ref legal event code: PL |
|
GBPC | Gb: european patent ceased through non-payment of renewal fee |
Effective date: 20070804 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: SE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20070805 Ref country code: LI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20070831 Ref country code: NL Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20080301 Ref country code: CH Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20070831 |
|
NLV4 | Nl: lapsed or anulled due to non-payment of the annual fee |
Effective date: 20080301 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FI Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20070804 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: AT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20070804 |
|
REG | Reference to a national code |
Ref country code: FR Ref legal event code: ST Effective date: 20080430 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: BE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20070831 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: FR Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20070831 |
|
REG | Reference to a national code |
Ref country code: ES Ref legal event code: FD2A Effective date: 20070806 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: GB Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20070804 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: ES Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20070806 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: LU Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20070804 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: IT Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20070804 |
|
PGFP | Annual fee paid to national office [announced via postgrant information from national office to epo] |
Ref country code: DE Payment date: 20110210 Year of fee payment: 11 |
|
REG | Reference to a national code |
Ref country code: DE Ref legal event code: R119 Ref document number: 50005709 Country of ref document: DE Effective date: 20120301 |
|
PG25 | Lapsed in a contracting state [announced via postgrant information from national office to epo] |
Ref country code: DE Free format text: LAPSE BECAUSE OF NON-PAYMENT OF DUE FEES Effective date: 20120301 |