DK160263B - PROCEDURE FOR COATING IN AN OVEN HEATED STRING MATERIAL OF IRON METAL WITH TREATMENT OF THE STRING MATERIAL IN STANDING, REDUCING GASA MOSPHERE AND APPLICATION FOR IMPLEMENTATION OF PROCEDURE - Google Patents

PROCEDURE FOR COATING IN AN OVEN HEATED STRING MATERIAL OF IRON METAL WITH TREATMENT OF THE STRING MATERIAL IN STANDING, REDUCING GASA MOSPHERE AND APPLICATION FOR IMPLEMENTATION OF PROCEDURE Download PDF

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DK160263B
DK160263B DK355581A DK355581A DK160263B DK 160263 B DK160263 B DK 160263B DK 355581 A DK355581 A DK 355581A DK 355581 A DK355581 A DK 355581A DK 160263 B DK160263 B DK 160263B
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Prior art keywords
protective cap
string
gas
strand
cap
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DK355581A
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Danish (da)
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DK355581A (en
DK160263C (en
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Richard Charles Barrett
Malcolm Robert John Grove
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Lysaght Australia Ltd
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    • 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
    • C21D9/00Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor
    • C21D9/52Heat treatment, e.g. annealing, hardening, quenching or tempering, adapted for particular articles; Furnaces therefor for wires; for strips ; for rods of unlimited length
    • C21D9/54Furnaces for treating strips or wire
    • C21D9/56Continuous furnaces for strip or wire
    • C21D9/561Continuous furnaces for strip or wire with a controlled atmosphere or vacuum
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C2/00Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
    • C23C2/003Apparatus
    • C23C2/0038Apparatus characterised by the pre-treatment chambers located immediately upstream of the bath or occurring locally before the dipping process
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C2/00Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
    • C23C2/003Apparatus
    • C23C2/0038Apparatus characterised by the pre-treatment chambers located immediately upstream of the bath or occurring locally before the dipping process
    • C23C2/004Snouts
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C2/00Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
    • C23C2/02Pretreatment of the material to be coated, e.g. for coating on selected surface areas
    • C23C2/022Pretreatment of the material to be coated, e.g. for coating on selected surface areas by heating
    • CCHEMISTRY; METALLURGY
    • C23COATING 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
    • C23CCOATING 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
    • C23C2/00Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor
    • C23C2/34Hot-dipping or immersion processes for applying the coating material in the molten state without affecting the shape; Apparatus therefor characterised by the shape of the material to be treated
    • C23C2/36Elongated material

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Coating With Molten Metal (AREA)

Description

55

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Opfindelsen vedrører en fremgangsmåde til overtrækning af i en ovn opvarmet strengmateriale af jernholdige metaller med et metallisk overtræksmedie, hvorved strengen bevæges i længderetning gennem en beskyttelseshætte, som har en strengafgangs-10 ende, som dykker ned i et bad af det metalliske overtræksmedie, og som omslutter en brøkdel af mediets overflade, hvorved beskyttelseshætten er fyldt med en reducerende gas, og hvorved strengen før indmundingen i beskyttelseshætten gennemløber en strengovn og en dertil tilsluttet udgangskanal, 15 og et apparat til gennemførelse af en sådan fremgangsmåde med en strengopvarmningsovn, med en til denne tilgrænsende strengudgangskanal, som ender i en beskyttelseshætte, hvis længst borte fra strengudgangskanalen liggende strengafgangsende dykker ned i et bad af smeltet, metallisk overtræksmedie, og med 20 indretninger til fremføring af strengen fra ovnen gennem strengudgangskanalen gennem beskyttelseshætten og badet.BACKGROUND OF THE INVENTION The present invention relates to a method of coating ferrous metal heated material in a furnace with a metallic coating medium whereby the string is moved longitudinally through a protective cap having a strand outlet end plunging into a bath of the metallic coating medium. encloses a fraction of the surface of the medium, whereby the protective cap is filled with a reducing gas, whereby the string passes through a string furnace and an output channel connected thereto prior to the opening of the protective cap, and an apparatus for carrying out such a method with a string heating furnace, with a adjoining strand exit channel ending in a protective cap whose strand outlet end furthest away from the strand exit duct is immersed in a bath of molten metallic coating medium, and having 20 devices for passing the strand from the furnace through the strand exit channel through the protective cap and bath.

En sådan fremgangsmåde og et sådant apparat kendes allerede fra GB patentskrift nr. 1 436 213. Ved den kendte varmdyp-25 ningsmetode udmunder en fra en glødeovn udført materialestreng af jernholdige metaller først i en ovnafgangskanal. Materialestrengen føres gennem denne kanal ind i en til kanalen tilsluttet beskyttelseshætte. Denne beskyttelseshætte er med sin bort fra afgangskanalen vendende ende dykket ned i et væskebad 30 af en smeltet aluminium/zinklegering. Materialestrengen føres gennem denne beskyttelseshætte og dykker gennem den i væskebadet delvis neddykkende ende, som udgør strengafgangsenden, ned i væskebadet. Materialestrengen dukker derefter, overtrukket med et zink/aluminiumlag, igen op af væskebadet og tilføres 35 til en videre behandling. Ovnafgangskanalen er opdelt i et tilSuch a method and apparatus are already known from GB patent specification 1 436 213. In the known hot dipping method, a material string made of a glowing furnace first emits in an furnace outlet channel. The material strand is passed through this channel into a protective cap connected to the channel. This protective cap, with its end facing away from the outlet channel, is immersed in a liquid bath 30 of a molten aluminum / zinc alloy. The material strand is passed through this protective cap and dives into the liquid bath, which is partially submerged in the liquid bath, which constitutes the strand outlet end. The material strand then reappears, coated with a zinc / aluminum layer, again from the liquid bath and added to a further treatment. The furnace outlet duct is divided into one more

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2 glødeovnen tilsluttet område, i hvilket glødeovnens temperatur opretholdes, og i et dertil tilsluttet område, i hvilket strengmaterialet afkøles til en temperatur, der ikke ligger over væskebadets temperatur. Gennem tilgangskanaler, som er 5 ført gennem beskyttelseshættens vægge i nærheden af væskebadets overflade og i retning mod denne, blæses til mindst 340°C opvarmet, reducerende gas ind i beskyttelseshætten. Den indblæste gas stryger først over væskebadets overflade og strømmer så mod strengmaterialets løberetning langs dette ind i 10 strengafgangskanalen. Derved opnås, at strengmaterialet, som dykker ned i væskebadet, er fri for oxygen og vanddamp. Oxygen og vanddamp forårsager en oxydering af væskebadet, som igen forårsager nålehuller og ikke med overtræk forsynede pletter.2, the incinerator is connected to a region in which the temperature of the incinerator is maintained and in a connected area in which the strand material is cooled to a temperature not above the temperature of the liquid bath. Through inlet ducts which are passed through the walls of the protective cap near the surface of the liquid bath and towards it, at least 340 ° C heated reducing gas is blown into the protective cap. The blown gas first floats across the surface of the liquid bath and then flows towards the flow direction of the strand material along it into the strand discharge channel. Thereby, the strand material which dives into the liquid bath is obtained free of oxygen and water vapor. Oxygen and water vapor cause an oxidation of the liquid bath, which in turn causes needle holes and non-coated patches.

15 Ved den beskrevne, kendte fremgangsmåde, som udføres med det ligeledes beskrevne apparat, viser det sig dog, at på trods af fortrængningen af oxygen og vanddamp i beskyttelseshætten optræder der alligevel små nålehuller i strengmaterialets overtræk. Sådanne nålehuller fører især ved efterfølgende lakering 20 af strengmaterialet til diskontinuiteter i laklaget under den efterfølgende tørring. Det viser sig, at disse nålehuller i strengmaterialets overtræk har deres årsag i nedslag af fordampet zink på strengmaterialet før dettes neddykning i væskebadet. Den fordampede zink kommer med strømmen af reducerende 25 gasatmosfære på materialestrengen før dennes neddykning i væskebadet .15 However, in the described known method, which is carried out with the apparatus also described, it turns out that despite the displacement of oxygen and water vapor in the protective cap, small needle holes nevertheless appear in the coating material of the strand material. Such needle holes, in particular upon subsequent lacquering 20 of the strand material, lead to discontinuities in the lacquer layer during the subsequent drying. It turns out that these needle holes in the strand material have their cause in the impact of evaporated zinc on the strand material before its immersion in the liquid bath. The evaporated zinc comes with the flow of reducing gas atmosphere on the material strand before its immersion in the liquid bath.

Opfindelsens opgave består i at angive en fremgangsmåde til overtrækning af i en ovn opvarmet strengmateriale af jernhol-30 digt metal i et væskebad og et apparat til gennemførelse af fremgangsmåden, ved hvilken der ikke optræder nogen nålehuller i overtrækket især forårsaget af nedslag af fordampet zink på strengmaterialet før dettes neddykning i væskebadet.SUMMARY OF THE INVENTION The object of the invention is to provide a method for coating iron-containing metal-heated strand material in a liquid bath and an apparatus for carrying out the method, in which no needle holes occur in the coating, in particular caused by the evaporation of evaporated zinc on the the strand material prior to its immersion in the liquid bath.

35 Denne opgave løses ved en fremgangsmåde af den i indledningen35 This task is solved by a method of the one in the introduction

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3 beskrevne slags med følgende kendetegn: a) opretholdelse af den reducerende, i det væsentlige i det mindste i strengafgangens område stillestående gasatmosfæ- 5 re i beskyttelseshætten; b) indledning af den reducerende gas i den i strømmen før beskyttelseshætten anbragte afgangskanal, gennem hvilken strengmaterialet løber på sin vej til beskyttelseshætten, 10 på en sådan måde, at gassen diffunderer ind i beskyttel seshætten, og c) begrænsning af diffusionsmængden og hastigheden fra afgangskanalen ind i beskyttelseshætten til værdier, som er 15 nødvendige for at holde mængden og sammensætningen af gas sen i beskyttelseshætten i det væsentlige konstant.3 described with the following characteristics: a) maintaining the reducing gas atmosphere, at least in the region of the outlet, in the protective cap; b) introducing the reducing gas into the outlet duct placed in the stream prior to the protective cap through which the strand material travels on its way to the protective cap 10 in such a way that the gas diffuses into the protective cap, and c) limiting the amount of diffusion and velocity from the outlet duct into the protective cap to values necessary to keep the amount and composition of gas late in the protective cap substantially constant.

Ved apparatet af den i indledningen beskrevne slags til gennemførelse af denne fremgangsmåde løses den til grund for op- 20 findelsen liggende opgave ved følgende kendetegn: a) indretninger til indføring af en reducerende gas i strengafgangskanalen til opretholdelse af en fyldt tilstand i denne, og 25 b) drøvleindretninger, hvilke i det væsentlige er anbragt i overgangen mellem strengafgangskanalen og beskyttelseshætten til styring af den ind i beskyttelseshætten indtrædende gasmængde.In the apparatus of the kind described in the preamble to carry out this method, the object of the invention is solved by the following characteristics: a) devices for introducing a reducing gas into the discharge channel to maintain a filled state therein; and (b) throttle devices which are substantially disposed in the transition between the discharge channel and the protective cap to control the amount of gas entering the protective cap.

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Nedslaget af fordampet zink på strengmaterialet før dettes neddykning i væskebadet forhindres ved en forholdsvis enkel, men meget virkningsfuld forholdsregel, som består i, at holde den reducerende gasatmosfære i nærheden af beskyttelseshætte- 35 udgangen i det væsentlige i ro og konstant i sin sammensæt-The impact of evaporated zinc on the strand material prior to its immersion in the liquid bath is prevented by a relatively simple but very effective precaution which consists in keeping the reducing gas atmosphere near the protective cap outlet substantially at rest and constant in its composition.

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4 ning. Dette opnås ved indføring af den reducerende gas i den før beskyttelseshætten anbragte afgangskanal, hvorigennem gassen kun ved diffusion kommer ind i beskyttelseshætten, og ved begrænsning af diffusionsmængde og -hastighed. Forholdsreglen 5 forringer zinkindholdet i den reducerende gasatmosfære i nærheden af beskyttelseshætteafgangen væsentligt, og forbedrer dermed overtrækningen af strengmaterialet. Zinkpartikler, som kommer i nærheden af beskyttelseshætten, træffer på en rolig atmosfære og blæses ikke på metalstrengen.4 ning. This is achieved by introducing the reducing gas into the outlet duct placed before the protective cap, through which the gas enters the protective cap only by diffusion, and by limiting the amount of diffusion and velocity. Precaution 5 significantly degrades the zinc content of the reducing gas atmosphere in the vicinity of the protective cap outlet, thereby improving the coating of the strand material. Zinc particles, which come close to the protective cap, strike in a calm atmosphere and do not blow on the metal strand.

1010

Fordelen ved opfindelsen ligger i et fejlfrit metallisk overtræk til jernholdigt strengmateriale og dermed i en vidtgående forhindring af senere korrosion af det jernholdige strengmateriale, og også i muligheden for bagefter at kunne påføre et 15 laklag uden diskontinuiteter på dette strengmateriale. En yderligere fordel ved opfindelsen ligger deri, at der til den i vidt omfang stillestående, reducerende gasatmosfære kan anvendes en gas med omgivelsestemperatur, medens gastemperaturen ved den kendte fremgangsmåde skal tilpasses til det flydende 20 metalbads smeltetemperatur. Denne kendsgerning bevirker en forenkling af apparatet ifølge opfindelsen, da en yderligere opvarmning af gassen før indledningen i ovnafgangskanalen bortfalder.The advantage of the invention lies in a flawless metallic coating for ferrous strand material and thus in a far prevention of later corrosion of the ferrous strand material, and also in the possibility of subsequently being able to apply a lacquer layer without discontinuities to this strand material. A further advantage of the invention lies in the fact that a largely ambient reducing gas atmosphere can be used with an ambient temperature gas, while the gas temperature in the known process must be adapted to the melting temperature of the liquid metal bath. This fact causes a simplification of the apparatus according to the invention, since a further heating of the gas before the introduction into the furnace outlet duct lapses.

25 Foretrukne enkeltheder ved opfindelsen er anført i underkravene.Preferred details of the invention are set forth in the subclaims.

Eksempler på dette apparat illustreres i vedlagte tegning, hvor: 30Examples of this apparatus are illustrated in the accompanying drawings, in which: 30

Fig. 1 viser en tværsnitsprojektion, som viser en stréng-ovnsudgangskanal, en hætte, som er koblet sammen med denne udgangskanal, og et bad med smeltet overtræks-materiale.FIG. 1 is a cross-sectional view showing a string furnace exit channel, a cap coupled to this exit channel, and a bath of molten coating material.

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5 fig. 2 viser i hovedsagen en gentagelse af den til højre side viste del af fig. 1 i større målestok, og den viser en mindre modifikation.5 FIG. 2 generally shows a repetition of the part of FIG. 1 on a larger scale, and it shows a minor modification.

5 Med henvisning til fig. 1 vises en streng, som skal overtrækkes ved henvisningstallet 3. Denne streng føres gennem ovnudgangskanalen 4 til hætten 5, herfra ned i badet 6, som er smeltet overtræksmateriale, og derfra igennem afdrypningszonen 7, hvori overskydende overtræksmateriale eventuelt kan fjernes 10 ved luftaftørring eller på anden konventionel måde. Hætten 5 har en strengudgangsende 5A, som dykker ned i badet 6 med det smeltede overtræksmateriale.5 Referring to FIG. 1, a string is shown to be coated by reference numeral 3. This string is passed through the furnace exit channel 4 to the cap 5, from here into the bath 6, which is molten coating material, and thence through the drip zone 7, in which excess coating material may be removed by air drying or on other conventional way. The cap 5 has a strand outlet end 5A which dives into the bath 6 with the molten coating material.

Medens strengen befinder sig i kanal 4 (selve ovnen er ikke 15 vist, den kan være af konventionel udformning), udsættes den for en luftformig reducerende atmosfære, som forsøg har vist kan være en gasblanding, hovedsageligt sammensat af nitrogen men kan indeholde hydrogen i mængder, som ikke overstiger 15 volumenprocent i blandingen. Denne gas bør være affugtet. Den 20 reducerende gas kan fødes ind i kanalen 4 på konventionel måde; for eksempel gennem en serie indstrømningsdyser 8, som forsynes fra en hovedledning 9. Anvendt eller overskydende gas kan bortledes fra kanalen 4, også på konventionel måde, for eksempel via udstrømningsåbninger 10, som fører til en hoved-25 afgangsledning 11. Gassen kan føres ind i kanalen 4 med enhver egnet temperatur; normal omgivelsestemperatur er helt anvendelig.While the string is in channel 4 (the furnace itself is not shown, it may be of conventional design), it is subjected to an gaseous reducing atmosphere which experimentally has shown to be a gaseous mixture, composed mainly of nitrogen but may contain hydrogen in amounts. , which does not exceed 15% by volume of the mixture. This gas should be dehumidified. The reducing gas may be fed into the duct 4 in a conventional manner; for example, through a series of inflow nozzles 8 provided from a main conduit 9. Used or excess gas may be discharged from the conduit 4, also in a conventional manner, for example via effluent orifices 10 leading to a main discharge conduit 11. The gas may be introduced. in the channel 4 at any suitable temperature; normal ambient temperature is perfectly applicable.

Kanalen 4 indeholder et antal skillevægge med huller i som 12, 30 13 og 14. Strengen passerer fra ovnen til badet gennem skille vægshullerne, som er afgrænset så tæt som det er muligt under opretholdelse af tilstrækkelig mekanisk frigang for den gennemløbende streng.Channel 4 contains a plurality of partitions with holes in as 12, 30, 13 and 14. The string passes from the furnace to the bath through separating the wall holes, which are delimited as closely as possible while maintaining sufficient mechanical clearance for the continuous strand.

35 Det bemærkes, at der kan være et tilbagestrømningstab af gas 635 It should be noted that there may be a backflow loss of gas 6

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gennem adskillelsesvæggene 12 og 13 med huller. Et sådant gastab er ikke væsentligt. Gas vil også diffundere gennem en åbning 14 ind i hætten 5, hvor den tjener som erstatningsluft til opretholdelse af luftindholdet i hætten og til at holde 5 gassammensætningen deri i hovedsagen konstant. Det er indlysende, at noget gas vil gå tabt ved medrivning med den streng, som løber ud af hætten, og der kan forekomme meget små gastab i hætten på grund af oxydering.through the separation walls 12 and 13 with holes. Such a gas loss is not significant. Gas will also diffuse through an opening 14 into the cap 5 where it serves as replacement air to maintain the air content of the cap and to keep the gas composition therein substantially constant. It is obvious that some gas will be lost by entrapment with the string running out of the cap, and very small gas losses may occur in the cap due to oxidation.

10 Den luftmængde, som strømmer ind i ovnkanalens 4 udstrømningsåbninger, bør på fore trukken måde kun have så lidt overtryk, i forhold til den omgivende atmosfære, at det er tilstrækkeligt til at opretholde overtrykstilstand i udløbskanalen, men under alle omstændigheder kan såvel gasindstrømningen som -udstrøm-15 ningen styres, så det ikke blot resulterer i den nævnte over-tryksvirkning, men samtidig sikrer, at den gas, som strømmer ind i hætten, i det mindste er tilstrækkelig til at ophæve gastab, forårsaget af lækage eller på anden måde.The amount of air flowing into the outlet openings of the furnace duct 4 should preferably only have so little overpressure relative to the ambient atmosphere that it is sufficient to maintain the overpressure state in the outlet duct, but in any case both the gas inflow and - the outflow is controlled so that it not only results in said overpressure effect but at the same time ensures that the gas flowing into the cap is at least sufficient to eliminate gas losses, caused by leakage or otherwise.

20 Den gasmængde, som fødes ind i hætten 5, skal være i det mindste en indstrømning, som tjener som den krævede erstatnings-funktion i hætten, medens den samtidig skal bevare lufttilstandsvilkåret i hætten, i det mindste i området ved hættens udløb. Til dette formål tilbageholdes gas, som i modsat fald 25 ville passere fra kanalen 4 ind i hætten 5, på konventionel måde, for eksempel ved anvendelse af sædvanlige tætningsvalser som indikeret ved 15 eller ved anvendelse af drøvlere eller andre lignende indretninger anbragt i ovnudløbskanalen i nærheden af dennes strengudløbsende.The amount of gas fed into the cap 5 must be at least an influx which serves as the required replacement function in the cap while at the same time maintaining the air condition condition of the cap, at least in the area at the outlet of the cap. For this purpose, gas which would otherwise pass 25 from passageway 4 into cap 5 is retained in conventional manner, for example, by using conventional sealing rollers as indicated by 15 or by using throttles or other similar devices located in the furnace outlet duct in the vicinity. of its strand outlet end.

3030

Med henvisning til fig. 2 er der her vist et arrangement, som i hovedsagen er det samme som allerede beskrevet, undtagen for så vidt angår drøvleindretningerne, som er placeret i området for forbindelsen mellem kanalen 4A og hætten 5A.Referring to FIG. 2, there is shown an arrangement which is substantially the same as already described, except as regards the throttle devices which are located in the region of the connection between the channel 4A and the cap 5A.

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77

Prøvekørsel med opfindelsen har vist, at opretholdelse af de krævede gasvilkår i hætten effektivt opnås, særligt hvor strengen, som håndteres, har form af en kontinuerlig strimmel, hvis bredde ret tæt nærmer sig hættens indvendige mål ved 5 hjælp af et par drøvlere som de, der vises ved 16 og 17.Testing of the invention has shown that maintaining the required gas conditions in the cap is effectively achieved, especially where the string being handled is in the form of a continuous strip whose width is quite close to the inner dimensions of the cap by means of a pair of droppers such as those shown at 16 and 17.

Drøvleren 16 er en indbygget væg af ildfast materiale, som strækker sig tværs over hættens indløbsende, og som opad rækker fra hættens bund til et niveau netop under niveauet for 10 streng 3A.The throttle 16 is a built-in wall of refractory material which extends across the inlet end of the hood and which extends upward from the bottom of the hood to a level just below the level of 10 string 3A.

Drøvleren 17 kan have form af en bjælke fremstillet af egnet, armeret keramisk fiber eller andet ildfast materiale. Denne bjælke kan være indbygget, men det foretrækkes, at den er mon-15 teret på en roterende aksel 18, således at bjælken kan drejes til den stilling, der vises med den stiplede linie 17A til lettelse af gennemtrækningen af strengens forreste ende ind i og gennem hætten. Med samme formål foretrækkes det, at der anbringes et adgangshul 19 med dæksel i hætten. Når apparatet 20 anvendes, lukkes denne åbning med dækslet, som indikeres med 20, og som kan fjernes.The throttle 17 may take the form of a beam made of suitable reinforced ceramic fiber or other refractory material. This beam may be built-in, but it is preferred that it be mounted on a rotating shaft 18 so that the beam can be rotated to the position shown by the dotted line 17A to facilitate the passage of the forward end of the string into and through the cap. For the same purpose, it is preferred that an access hole 19 with a cover be placed in the cap. When the apparatus 20 is used, this opening is closed with the cover which is indicated by 20 and which can be removed.

Claims (9)

1. Fremgangsmåde til overtrækning af i en ovn opvarmet strengmateriale af jernholdige metaller med et metallisk overtræks- 5 materiale, hvorved strengen (3) bevæges i længderetning gennem en beskyttelseshætte (5), hvilken har en strengafgangsende (5A), som dykker ned i et bad (6) af det metalliske ovetræks-materiale, og som omslutter en brøkdel af materialets overflade, hvorved beskyttelseshætten (5) er fyldt med en reducerende 10 gas, og hvorved strengen (3) før indmundingen i beskyttelseshætten (5) gennemløber en strengovn og en dertil tilsluttet afgangskanal (4), kendetegnet ved følgende kendetegn: 15 a) opretholdelse af den reducerende, i det mindste i området ved strengafgangen (5A) stillestående gasatmosfære i beskyttelseshætten; b) indføring af den reducerende gas i den i strømmen før be- 20 skyttelseshætten (5) anbragte afgangskanal (4), gennem hvilken strengmaterialet (3) løber på sin vej til beskyttelseshætten (5) på en sådan måde, at gassen diffunderer ind i beskyttelseshætten (5), og 25 c) begrænsning af gassens diffusionsmængde og hastighed fra afgangskanalen (4) ind i beskyttelseshætten (5) til værdier, som er nødvendige for i det væsentlige at holde mængden og sammensætningen af gassen i beskyttelseshætten (5) konstant. 30A method of coating ferrous heated strand material of ferrous metals with a metallic coating material, wherein the strand (3) is moved longitudinally through a protective cap (5) which has a strand exit end (5A) which dives into a bath (6) of the metallic coating material, which encloses a fraction of the surface of the material, whereby the protective cap (5) is filled with a reducing gas, and whereby the string (3) passes through the opening cap of the protective cap (5) and a discharge channel (4) connected thereto, characterized by the following characteristics: a) maintaining the reducing atmosphere, at least in the region of the strand outlet (5A), of the gas atmosphere in the protective cap; b) introducing the reducing gas into the outlet duct (4) located in the stream prior to the protective cap (5), through which the string material (3) runs on its way to the protective cap (5) in such a way that the gas diffuses into the and (c) limiting the amount of gas diffusion and velocity from the outlet duct (4) into the protective cap (5) to values necessary to substantially keep the amount and composition of the gas in the protective cap (5) constant. 30 2. Fremgangsmåde ifølge krav 1, kendetegnet ved, at der som overtræksmateriale anvendes en aluminium/zinklege-ring.Process according to claim 1, characterized in that an aluminum / zinc alloy is used as a coating material. 3. Fremgangsmåde ifølge krav 1 eller 2, kendetegnet DK 160263 B ved, at der som reducerende gas anvendes en tørret blanding af hydrogen og nitrogen, hvorved hydrogenmængden ikke overstiger 15 volumenprocent.Process according to claim 1 or 2, characterized in that a dried mixture of hydrogen and nitrogen is used as reducing gas, whereby the amount of hydrogen does not exceed 15% by volume. 4. Apparat til gennemførelse af fremgangsmåden ifølge krav 1, med en strengopvarmningsovn, med en til denne grænsende strengafgangskanal (4), som udmunder i en beskyttelseshætte (5), hvis bort fra strengafgangskanalen (4) liggende strengafgangsende (5A) dykker ned i et bad (6) af smeltet, metallisk 10 overtræksmateriale, og med indretninger til fremføring af strengen fra ovnen gennem strengafgangskanalen (4), gennem beskyttelseshætten (5) og gennem badet (6), kendeteg- . net ved følgende kendetegn: 15 a) indretninger (8, 9) til indledning af en reducerende gas i strengafgangskanalen (4) til opretholdelse af en fyldt tilstand i denne kanal (4), og b) drøvleindretninger, som i det væsentlige er anbragt ved 20 overgangen mellem strengafgangskanalen (4) og beskyttel seshætten (5) til styring af den ind i beskyttelseshætten (5) indtrædende gasmængde.Apparatus for carrying out the method according to claim 1, with a string heater, with a string outlet duct (4) adjacent to it, which opens into a protective cap (5) if the strand outlet duct (5A) lying in the bottom of the duct outlet duct (4) dives into a bath (6) of molten metallic coating material, and with means for conveying the string from the furnace through the string outlet duct (4), through the protective cap (5) and through the bath (6), characterized by. networks having the following characteristics: (a) devices (8, 9) for introducing a reducing gas into the string outlet duct (4) to maintain a filled state in said duct (4); and b) throttle devices substantially arranged by 20, the passage between the string outlet channel (4) and the protective cap (5) for controlling the amount of gas entering the protective cap (5). 5. Apparat ifølge krav 4, kendetegnet ved, at 25 strengafgangskanalen (4) har et antal indvendige skillevægge (12, 13, 14), som er anbragt forløbende på tværs af denne, hvorved hver skillevæg har en deri udformet åbning, gennem hvilken strengmaterialet frit kan vandre igennem.Apparatus according to claim 4, characterized in that the string outlet channel (4) has a plurality of internal partitions (12, 13, 14) arranged transversely thereof, each partition having an aperture formed therein, through which the string material can roam freely. 6. Apparat ifølge krav 5, kendetegnet ved, at drøvleindretningen omfatter et par tætningsvalser (15), mellem hvilke og en af skillevæggene strengen bevæges igennem ved sin bevægelse i retning mod beskyttelseshætten.Apparatus according to claim 5, characterized in that the throttle device comprises a pair of sealing rollers (15) between which and one of the partitions the string is moved through in its movement towards the protective cap. 7. Apparat ifølge krav 5, kendetegnet ved, at DK 160263 B drøvleindretningen omfatter en ildfast væg (16), som strækker sig vinkelret på beskyttelseshætten (5A) og når fra bunden af beskyttelseshætten (5A) til et niveau, som ligger tæt ved, men dog noget under det niveau, i hvilket strengen (3A) bevæges 5 gennem beskyttelseshætten (5A), og at en af ildfast materiale bestående bjælke (17) strækker sig vinkelret på beskyttelseshætten (5A) og når fra beskyttelseshættens overside nedad til et niveau, som ligger tæt ved, men dog noget over strengens (3A) niveau.Apparatus according to claim 5, characterized in that the DK 160263 B throttle device comprises a refractory wall (16) extending perpendicular to the protective cap (5A) and reaching from the bottom of the protective cap (5A) to a level adjacent to it. but, however, slightly below the level at which the string (3A) moves 5 through the protective cap (5A) and that a beam (17) of refractory material extends perpendicular to the protective cap (5A) and reaches from the upper side of the protective cap downwards to a level, which is close by, but somewhat above the level of the string (3A). 8. Apparat ifølge krav 7, kendetegnet ved, at bjælken (17) er monteret på en drejelig aksel (18), som strækker sig vinkelret på beskyttelseshætten (5A), for derved at kunne dreje bjælken til forstørrelse af bjælkens (17) afstand 15 til strengen (3A).Apparatus according to claim 7, characterized in that the beam (17) is mounted on a rotatable shaft (18) extending perpendicular to the protective cap (5A), thereby being able to rotate the beam to increase the distance of the beam (17). to the string (3A). 9. Apparat ifølge krav 8, kendetegnet ved, at beskyttelseshætten (5A) har en deri udformet indgangsåbning (19) i området ved bjælken (17), og at åbningen (19) er forsynet 20 med et aftageligt dæksel (20).Apparatus according to claim 8, characterized in that the protective cap (5A) has an inlet opening (19) formed therein in the region of the beam (17) and that the opening (19) is provided with a removable cover (20).
DK355581A 1980-08-19 1981-08-11 PROCEDURE FOR COATING IN AN OVEN HEATED STRING MATERIAL OF IRON METAL WITH TREATMENT OF THE STRING MATERIAL IN STANDING, REDUCING GASA MOSPHERE AND APPLICATION FOR IMPLEMENTATION OF PROCEDURE DK160263C (en)

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AUPE512280 1980-08-19
AUPE512280 1980-08-19

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DK160263B true DK160263B (en) 1991-02-18
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JPS58175520A (en) * 1982-04-09 1983-10-14 松下電器産業株式会社 Bevarage maker
US4713154A (en) * 1985-08-08 1987-12-15 Kawasaki Steel Corporation Continuous annealing and pickling method and apparatus for steel strips
JPS62266073A (en) * 1986-05-14 1987-11-18 テルモ株式会社 Apparatus for purifying body fluids
DE3933244C1 (en) * 1989-10-05 1990-06-13 Hoesch Stahl Ag, 4600 Dortmund, De Continuous zinc coating appts. for coating metal strip - comprises melt alloy bath covered with hood having hydrogen, steam and inert gas atmos. and control system
SE9101053L (en) * 1990-04-13 1991-10-14 Centre Rech Metallurgique PROCEDURES FOR COATING A CONTINUOUS STEEL BAND
JP2517169B2 (en) * 1990-10-09 1996-07-24 新日本製鐵株式会社 Method for producing hot dip galvanized steel sheet
FR2782326B1 (en) 1998-08-13 2000-09-15 Air Liquide METHOD FOR GALVANIZING A METAL STRIP

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US3320085A (en) * 1965-03-19 1967-05-16 Selas Corp Of America Galvanizing
SE393403B (en) * 1972-08-09 1977-05-09 Bethlehem Steel Corp WAY TO COVER THE SURFACE OF AN IRON STRING WITH AN AL-ZN ALLOY
JPS5198634A (en) * 1975-02-27 1976-08-31 Kohanno renzokuyojuaenmetsukini okeru maeshoryokangengasuno shoho
JPS51128610A (en) * 1975-05-02 1976-11-09 Nippon Steel Corp A method for reduction of steel strips in reduction furnace of continu ous heat treatment lines for steel plates for plating
JPS51149130A (en) * 1975-06-18 1976-12-21 Nippon Steel Corp Method of producing zincccoated iron plate with good workability
US4183983A (en) * 1978-08-17 1980-01-15 Selas Corporation Of America Method for reducing metal oxide formation on a continuous metal sheet in the hot dip coating thereof
FR2477900A1 (en) * 1980-03-14 1981-09-18 Heurtey Metallurgie METHOD AND DEVICE FOR SEPARATING GASEOUS ATMOSPHERES IN ATMOSPHERE HEAT TREATMENT PLANTS

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GB2082206A (en) 1982-03-03
BR8105280A (en) 1982-04-27
IT8149111A0 (en) 1981-08-13
JPS5760014A (en) 1982-04-10
MX156647A (en) 1988-09-22
ES512591A0 (en) 1983-04-01
IT1171464B (en) 1987-06-10
IN156849B (en) 1985-11-16
NL8103803A (en) 1982-03-16
DE3132120C2 (en) 1989-12-14
IE811781L (en) 1982-02-19
PH16269A (en) 1983-08-25
SE8104720L (en) 1982-02-20
FR2488913B1 (en) 1984-06-29
GB2082206B (en) 1984-05-16
JPH0338322B2 (en) 1991-06-10
DE3132120A1 (en) 1982-03-25
AU543013B2 (en) 1985-03-28
IE51782B1 (en) 1987-04-01
ZA815392B (en) 1982-08-25
DK355581A (en) 1982-02-20
NZ197931A (en) 1984-07-31
FR2488913A1 (en) 1982-02-26
BE889991A (en) 1981-12-16
AR226738A1 (en) 1982-08-13
CA1192101A (en) 1985-08-20
LU83562A1 (en) 1981-12-01
MY8500883A (en) 1985-12-31
SG66784G (en) 1985-03-15
ES8306390A3 (en) 1983-04-01
AU7400581A (en) 1982-02-25
DK160263C (en) 1991-07-22

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