EP0106113A1 - Process and apparatus for the bright annealing of metallic parts using nitrogen as the protective atmosphere - Google Patents

Process and apparatus for the bright annealing of metallic parts using nitrogen as the protective atmosphere Download PDF

Info

Publication number
EP0106113A1
EP0106113A1 EP83108799A EP83108799A EP0106113A1 EP 0106113 A1 EP0106113 A1 EP 0106113A1 EP 83108799 A EP83108799 A EP 83108799A EP 83108799 A EP83108799 A EP 83108799A EP 0106113 A1 EP0106113 A1 EP 0106113A1
Authority
EP
European Patent Office
Prior art keywords
nitrogen
bright annealing
cooling section
liquid nitrogen
protective gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
EP83108799A
Other languages
German (de)
French (fr)
Other versions
EP0106113B1 (en
Inventor
Gottfried Böhm
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Messer Griesheim GmbH
Original Assignee
Messer Griesheim GmbH
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Messer Griesheim GmbH filed Critical Messer Griesheim GmbH
Priority to AT83108799T priority Critical patent/ATE23197T1/en
Publication of EP0106113A1 publication Critical patent/EP0106113A1/en
Application granted granted Critical
Publication of EP0106113B1 publication Critical patent/EP0106113B1/en
Expired legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21DMODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D1/00General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
    • C21D1/56General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering characterised by the quenching agents
    • C21D1/613Gases; Liquefied or solidified normally gaseous material
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21DMODIFYING THE PHYSICAL STRUCTURE OF FERROUS METALS; GENERAL DEVICES FOR HEAT TREATMENT OF FERROUS OR NON-FERROUS METALS OR ALLOYS; MAKING METAL MALLEABLE, e.g. BY DECARBURISATION OR TEMPERING
    • C21D1/00General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
    • C21D1/74Methods of treatment in inert gas, controlled atmosphere, vacuum or pulverulent material

Definitions

  • the invention relates to a method and a device for bright annealing metallic workpieces in a bright annealing furnace with a connected cooling section and nitrogen as a protective gas.
  • the workpieces are annealed under protective gas in bright annealing furnaces for workpieces made of steel, iron or non-ferrous metals.
  • Either exogas or nitrogen is used as the protective gas. If nitrogen is used, liquid nitrogen is evaporated in an air evaporator and, like the exogas, introduced at several points in the annealing furnace and the cooling section. The valuable cold of liquid nitrogen is lost unused.
  • the invention has for its object to improve the bright annealing process with nitrogen as a protective gas in such a way that the system costs are reduced while simultaneously utilizing the cold content of the liquid nitrogen and an increase in performance and at least with some metals an improvement in quality becomes possible.
  • the spray direction is preferably 15 ° to 20 ° deviating from the vertical and counter to the direction of movement of the annealing material. This results in an optimal heat exchange between the annealing material and liquid nitrogen, as well as excellent flow conditions for the evaporated nitrogen through the cooling section and the bright annealing furnace.
  • the nitrogen consumption is the same.
  • the liquid nitrogen is evaporated in the cooling section according to the invention, there is no need to set up an air evaporator.
  • an increase in performance is possible due to the greater cooling of the workpieces and an improvement in quality, at least for some metals. Because of the strong cooling of the workpieces in the method according to the invention, they no longer start after leaving the cooling section, in contrast to methods according to the prior art.
  • liquid nitrogen When using liquid nitrogen according to the invention, 152 kg / h of liquid nitrogen, which corresponds to 130 m 3 / h of gaseous nitrogen, were required.
  • the outlet temperature of the copper pipes or copper coils was only 95 ° C, so that the workpieces no longer started.
  • both the outlet temperature and the throughput can be varied in a simple manner. This is a particular advantage of the method according to the invention. If, on the other hand, one wanted to increase the throughput in the case of methods according to the prior art, the cooling section would have to be extended.
  • a bright annealing furnace 1 is shown in section, at the entrance of which an inlet section 2 and at the exit of which a cooling section 3 are connected.
  • the annealed material is conveyed on transport rollers 4 through the bright annealing furnace 1, the direction of movement of the annealed material is indicated by arrow 5.
  • Nitrogen serves as protective gas, which is supplied in liquid form from the insulated tank 6 and through the insulated line 7 to the bright annealing furnace 1. According to the invention, the liquid nitrogen is sprayed directly into the end region 8 of the cooling section 3 without prior evaporation.
  • the metering takes place by means of a regulating valve 9, and conventional conveying and monitoring devices, such as phase separators, thermometers and manometers, which are not shown in the drawing, are also provided.
  • the sprayed-in liquid nitrogen evaporates by heat exchange with the still hot annealing material, flows in gaseous form through the cooling section 3 and the bright annealing furnace 1 and leaves the system through the inlet section 2.
  • the direction of flow of the gaseous nitrogen is indicated by an arrow 10.
  • FIGS. 2 and 3 A preferred device for spraying the liquid nitrogen into the cooling section 3 is shown in FIGS. 2 and 3.
  • the nozzle assembly 12 is arranged in the ceiling 11, to which the liquid nitrogen is supplied through the control valve 9.
  • the nozzle assembly 12 there are bores which are arranged so that the liquid nitrogen deviates from the vertical at an angle of 15 ° opposite to the movement Direction of the annealing material 13 emerges, as shown in Figure 3.
  • the sprayed liquid nitrogen thus impinges almost perpendicularly on the annealing material 13, which causes an intensive heat exchange and rapid evaporation of the nitrogen.
  • a movement toward the annealing furnace 1 and the inlet section 2 is impressed on the nitrogen.
  • the invention is not limited to this device.
  • the exit angle of 15 ° can e.g. can also be achieved in that the inlet pipe for the liquid nitrogen in the cooling section 3 is angled accordingly.
  • Several nozzle assemblies can also be arranged one behind the other.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Heat Treatment Of Strip Materials And Filament Materials (AREA)
  • Heat Treatments In General, Especially Conveying And Cooling (AREA)

Abstract

Metallic work pieces are annealed under protective gas in bright annealing furnaces with subsequent cooling line. Exogas or nitrogen is used as protective gas. In the latter case, liquid nitrogen is evaporated and introduced at several locations in the bright annealing furnace and the cooling line. For the purpose of decreasing the installation costs, increasing the performance and improving the quality, the liquid nitrogen is sprayed without prior evaporation onto the material to be annealed, namely in the end zone of the cooling line.

Description

Die Erfindung betrifft ein Verfahren und eine Vorrichtung zum Blankglühen von metallischen Werkstücken in einem Blankglühofen mit angeschlossener Kühlstrecke und Stickstoff als Schutzgas.The invention relates to a method and a device for bright annealing metallic workpieces in a bright annealing furnace with a connected cooling section and nitrogen as a protective gas.

In Blankglühöfen für Werkstücke aus Stahl, Eisen oder NE-Metallen werden die Werkstücke unter Schutzgas geglüht. Als Schutzgas verwendet man hierfür entweder Exogas oder Stickstoff. Im Falle der Stickstoffverwendung wird flüssiger Stickstoff in einem Luftverdampfer verdampft und ähnlich wie das Exogas an mehreren Stellen des Glühofens und der Kühlstrecke eingeleitet. Hierbei geht die wertvolle Kälte des flüssigen Stickstoffes ungenutzt verloren.The workpieces are annealed under protective gas in bright annealing furnaces for workpieces made of steel, iron or non-ferrous metals. Either exogas or nitrogen is used as the protective gas. If nitrogen is used, liquid nitrogen is evaporated in an air evaporator and, like the exogas, introduced at several points in the annealing furnace and the cooling section. The valuable cold of liquid nitrogen is lost unused.

Der Erfindung liegt die Aufgabe zugrunde, das Blankglühverfahren mit Stickstoff als Schutzgas so zu verbessern, daß bei gleichzeitiger Ausnutzung des Kälteinhaltes des flüssigen Stickstoffes die Anlagekosten verringert und eine Leistungssteigerung und zumindest bei einigen Metallen eine Qualitätsverbesserung möglich wird.The invention has for its object to improve the bright annealing process with nitrogen as a protective gas in such a way that the system costs are reduced while simultaneously utilizing the cold content of the liquid nitrogen and an increase in performance and at least with some metals an improvement in quality becomes possible.

Bei einem Verfahren zum Blankglühen von metallischen Werkstücken in einem Blankglühofen mit angeschlossener Kühlstrecke und Stickstoff als Schutzgas wird dies gemäß der Erfindung erreicht, indem der Stickstoff in flüssiger Form im Endbereich der Kühlstrecke auf das Glühgut gesprüht wird.In a method for bright annealing of metallic workpieces in a bright annealing furnace with a connected cooling section and nitrogen as a protective gas, this is achieved according to the invention by spraying the nitrogen in liquid form on the annealing material in the end region of the cooling section.

Die Sprührichtung beträgt vorzugsweise 15° bis 20° abweichend von der Vertikalen und entgegen der Bewegungsrichtung des Glühgutes. Hierbei ergibt sich ein optimaler Wärmeaustausch zwischen Glühgut und flüssigem Stickstoff, sowie ausgezeichnete Strömungsverhältnisse für den verdampften Stickstoff durch die Kühlstrecke und den Blankglühofen.The spray direction is preferably 15 ° to 20 ° deviating from the vertical and counter to the direction of movement of the annealing material. This results in an optimal heat exchange between the annealing material and liquid nitrogen, as well as excellent flow conditions for the evaporated nitrogen through the cooling section and the bright annealing furnace.

Gegenüber dem bisherigen Verfahren, bei dem der flüssige Stickstoff in einem Luftverdampfer verdampft wird, ist der Stickstoffverbrauch gleich. Da aber erfindungsgemäß der flüssige Stickstoff in der Kühlstrecke verdampft wird, erübrigt sich das Aufstellen eines Luftverdampfers. Gegenüber dem Verfahren mit Exogas oder gasförmigem Stickstoff als Schutzgas ist wegen der stärkeren Abkühlung der Werkstücke eine Leistungssteigerung möglich und zumindest bei einigen Metallen eine Qualitätsverbesserung. Wegen der starken Abkühlung der Werkstücke bei dem erfindungsgemäßen Verfahren laufen diese nämlich nach Verlassen der Kühlstrecke nicht mehr an, im Gegensatz zu Verfahren nach dem Stand der Technik.Compared to the previous process, in which the liquid nitrogen is evaporated in an air evaporator, the nitrogen consumption is the same. However, since the liquid nitrogen is evaporated in the cooling section according to the invention, there is no need to set up an air evaporator. Compared to the process with exogas or gaseous nitrogen as a protective gas, an increase in performance is possible due to the greater cooling of the workpieces and an improvement in quality, at least for some metals. Because of the strong cooling of the workpieces in the method according to the invention, they no longer start after leaving the cooling section, in contrast to methods according to the prior art.

Dies zeigen die nachfolgend beschriebenen Vergleichsversuche.This is shown by the comparative tests described below.

Es wurden jeweils 2000 kg/h gestreckte Kupferrohre oder 1500 kg/h aufgewickelte Kupfercoils geglüht. Bei Verwendung von Exogas wurden hierfür 130 m/h benötigt. Die Auslauftemperatur der Kupferrohre bzw. der Kupfercoils aus der Kühlstrecke betrug 140° C. Die Kupfercoils und die Kupferrohre liefen an.In each case, 2000 kg / h stretched copper tubes or 1500 kg / h wound copper coils were annealed. When using Exogas, 130 m / h were required. The outlet temperature of the copper pipes or the copper coils from the cooling section was 140 ° C. The copper coils and the copper pipes started up.

Bei dem erfindungsgemäßen Einsatz von flüssigem Stickstoff wurden 152 kg/h flüssiger Stickstoff, das entspricht 130 m3/h gasförmigem Stickstoff,benötigt. Die Auslauftemperatur der Kupferrohre oder Kupfercoils betrug nur 95° C, so daß die Werkstücke nicht mehr anliefen.When using liquid nitrogen according to the invention, 152 kg / h of liquid nitrogen, which corresponds to 130 m 3 / h of gaseous nitrogen, were required. The outlet temperature of the copper pipes or copper coils was only 95 ° C, so that the workpieces no longer started.

Durch entsprechende Dosierung des flüssigen Stickstoffes kann sowohl die Auslaustemperatur als auch die Durchsatzmenge in einfacher Weise variiert werden. Dies ist ein besonderer Vorteil des erfindungsgemäßen Verfahrens. Wollte man dagegen bei Verfahren nach dem Stand der Technik die Durchsatzleistung steigern, so müßte die Kühlstrecke verlängert werden.By appropriately metering the liquid nitrogen, both the outlet temperature and the throughput can be varied in a simple manner. This is a particular advantage of the method according to the invention. If, on the other hand, one wanted to increase the throughput in the case of methods according to the prior art, the cooling section would have to be extended.

Ein Ausführungsbeispiel der Erfindung soll anhand der beigefügten Zeichnungen erläutert werden.An embodiment of the invention will be explained with reference to the accompanying drawings.

Es zeigen

  • Fig.1 einen Schnitt durch einen Blankglühofen mit angeschlossener Kühlstrecke und Zufuhr von flüssigem Stickstoff in den Endbereich der Kühlstrecke,
  • Fig.2 einen Schnitt entlang der Linie A-A in Fig.1,
  • Fig.3 einen Schnitt entlang der Linie B-B in Fig.2.
Show it
  • 1 shows a section through a bright annealing furnace with a connected cooling section and supply of liquid nitrogen into the end region of the cooling section,
  • 2 shows a section along the line AA in FIG. 1,
  • 3 shows a section along the line BB in Fig.2.

In Fig.1 ist im Schnitt einBlankglühofen 1 dargestellt, an dessen Eingang eine Einlaufstrecke 2 und an dessen Ausgang eine Kühlstrecke 3 angeschlossen sind. Das Glühgut wird auf Transportrollen 4 durch den Blankglühofen 1 gefördert, die Bewegungsrichtung des Glühgutes ist durch den Pfeil 5 angegeben. Als Schutzgas dient Stickstoff, der in flüssiger Form aus dem isolierten Tank 6 und durch die isolierte Leitung 7 dem Blankglühofen 1 zugeführt wird. Erfindungsgemäß wird der flüssige Stickstoff ohne vorherige Verdampfung direkt in den Endbereich 8 der Kühlstrecke 3 eingesprüht. Die Dosierung geschieht mittels eines Regulierventils 9, außerdem sind in der Zeichnung nicht dargestellte übliche Förder- und Überwachungseinrichtungen, wie Phasentrenner, Thermometer und Manometer, vorgesehen. Der eingesprühte flüssige Stickstoff verdampft durch Wärmeaustausch mit dem noch heißen Glühgut, strömt in gasförmiger Form durch die Kühlstrecke 3 und den Blankglühofen 1 und verläßt die Anlage durch die Einlaufstrecke 2. Die Strömungsrichtung des gasförmigen Stickstoffs ist durch einen Pfeil 10 angegeben.In Fig. 1, a bright annealing furnace 1 is shown in section, at the entrance of which an inlet section 2 and at the exit of which a cooling section 3 are connected. The annealed material is conveyed on transport rollers 4 through the bright annealing furnace 1, the direction of movement of the annealed material is indicated by arrow 5. Nitrogen serves as protective gas, which is supplied in liquid form from the insulated tank 6 and through the insulated line 7 to the bright annealing furnace 1. According to the invention, the liquid nitrogen is sprayed directly into the end region 8 of the cooling section 3 without prior evaporation. The metering takes place by means of a regulating valve 9, and conventional conveying and monitoring devices, such as phase separators, thermometers and manometers, which are not shown in the drawing, are also provided. The sprayed-in liquid nitrogen evaporates by heat exchange with the still hot annealing material, flows in gaseous form through the cooling section 3 and the bright annealing furnace 1 and leaves the system through the inlet section 2. The direction of flow of the gaseous nitrogen is indicated by an arrow 10.

Eine bevorzugte Vorrichtung zum Einsprühen des flüssigen Stickstoffes in die Kühlstrecke 3 ist in den Fig.2 und 3 dargestellt. Im Endbereich 8 der Kühlstrecke 3 ist in der Decke 11 der Düsenstock 12 angeordnet, dem durch das Regelventil 9 der flüssige Stickstoff zugeführt wird. In dem Düsenstock 12 befinden sich Bohrungen, die so angeordnet sind, daß der flüssige Stickstoff unter einem Winkel von 15° abweichend von der Vertikale entgegen der Bewegungsrichtung des Glühgutes 13 austritt, wie es in Fig.3 dargestellt ist. Der ausgesprühte flüssige Stickstoff prallt somit nahezu senkrecht auf das Glühgut 13 auf, was einen intensiven Wärmeaustausch und rasche Verdampfung des Stickstoffs bewirkt. Gleichzeitig wird dem Stickstoff jedoch eine Bewegung hin zum Glühofen 1 und zur Einlaufstrecke 2 aufgeprägt.A preferred device for spraying the liquid nitrogen into the cooling section 3 is shown in FIGS. 2 and 3. In the end region 8 of the cooling section 3, the nozzle assembly 12 is arranged in the ceiling 11, to which the liquid nitrogen is supplied through the control valve 9. In the nozzle assembly 12 there are bores which are arranged so that the liquid nitrogen deviates from the vertical at an angle of 15 ° opposite to the movement Direction of the annealing material 13 emerges, as shown in Figure 3. The sprayed liquid nitrogen thus impinges almost perpendicularly on the annealing material 13, which causes an intensive heat exchange and rapid evaporation of the nitrogen. At the same time, however, a movement toward the annealing furnace 1 and the inlet section 2 is impressed on the nitrogen.

Die Erfindung ist nicht auf diese Vorrichtung beschränkt. Der Austrittswinkel von 15° kann z.B. auch dadurch erreicht werden, daß das Eintrittsrohr für den flüssigen Stickstoff in der Kühlstrecke 3 entsprechend abgewinkelt wird. Es können auch mehrere Düsenstöcke hintereinander angeordnet werden.The invention is not limited to this device. The exit angle of 15 ° can e.g. can also be achieved in that the inlet pipe for the liquid nitrogen in the cooling section 3 is angled accordingly. Several nozzle assemblies can also be arranged one behind the other.

Claims (4)

1. Verfahren zum Blankglühen von metallischen Werkstücken in einem Blankglühofen (1) mit angeschlossener Kühlstrecke (3) und Stickstoff als Schutzgas,
dadurch gekennzeichnet,
daß der Stickstoff in flüssiger Form im Endbereich (8) der Kühlstrecke auf das Glühgut gesprüht wird.
1. Method for bright annealing of metallic workpieces in a bright annealing furnace (1) with connected cooling section (3) and nitrogen as protective gas,
characterized,
that the nitrogen in liquid form is sprayed onto the annealing material in the end region (8) of the cooling section.
2. Verfahren nach Anspruch 1,
dadurch gekennzeichnet,
daß der Stickstoff unter einem Winkel von 15° bis 20° abweichend von der Vertikalen entgegen der Bewegungsrichtung (5) des Glühgutes (13) eingesprüht wird.
2. The method according to claim 1,
characterized,
that the nitrogen is sprayed at an angle of 15 ° to 20 ° deviating from the vertical against the direction of movement (5) of the annealing material (13).
3. Vorrichtung zur Durchführung des Verfahrens nach Anspruch 1,
mit einem Blankglühofen und einer angeschlossenen Kühlstrecke, gekennzeichnet durch einen im Endbereich (8) der Kühlstrecke (3) unter dessen Decke (11) quer zur Bewegungsrichtung (5) des Glühgutes (13) angeordneten Düsenstock (12) mit Düsen zum Aufsprühen von flüssigem Stickstoff auf das Glühgut.
3. Device for performing the method according to claim 1,
with a bright annealing furnace and a connected cooling section, characterized by a nozzle assembly (12) with nozzles for spraying liquid nitrogen in the end region (8) of the cooling section (3) under its cover (11) transversely to the direction of movement (5) of the annealing material (13) on the annealing material.
4. Vorrichtung nach Anspruch 3,
dadurch gekennzeichnet,
daß die Düsen unter einem Winkel von 15° bis 20° abweichend von der Vertikalen entgegen der Bewegungsrichtung des Glühgutes angeordnet sind.
4. The device according to claim 3,
characterized,
that the nozzles are arranged at an angle of 15 ° to 20 ° deviating from the vertical against the direction of movement of the annealing material.
EP83108799A 1982-09-21 1983-09-07 Process and apparatus for the bright annealing of metallic parts using nitrogen as the protective atmosphere Expired EP0106113B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT83108799T ATE23197T1 (en) 1982-09-21 1983-09-07 METHOD AND DEVICE FOR BRIGHT ANNEALING OF METALLIC WORKPIECES USING NITROGEN AS A PROTECTIVE GAS.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3234863 1982-09-21
DE3234863A DE3234863C2 (en) 1982-09-21 1982-09-21 Process and device for bright annealing of metallic workpieces with nitrogen as protective gas

Publications (2)

Publication Number Publication Date
EP0106113A1 true EP0106113A1 (en) 1984-04-25
EP0106113B1 EP0106113B1 (en) 1986-10-29

Family

ID=6173723

Family Applications (1)

Application Number Title Priority Date Filing Date
EP83108799A Expired EP0106113B1 (en) 1982-09-21 1983-09-07 Process and apparatus for the bright annealing of metallic parts using nitrogen as the protective atmosphere

Country Status (5)

Country Link
US (1) US4515645A (en)
EP (1) EP0106113B1 (en)
AT (1) ATE23197T1 (en)
DE (1) DE3234863C2 (en)
ZA (1) ZA836972B (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0189759A1 (en) * 1985-01-17 1986-08-06 Linde Aktiengesellschaft Method and apparatus for heat treating work pieces
EP2227570B1 (en) 2007-11-29 2017-01-25 Benteler Automobiltechnik GmbH Method for producing a shaped component comprising at least two joining areas having different ductility

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4643401A (en) * 1985-08-28 1987-02-17 Mg Industries Apparatus for cooling a vacuum furnace
JPH01287221A (en) * 1988-05-13 1989-11-17 Usui Internatl Ind Co Ltd Method and device for high-frequency heat treatment of long-sized metallic material
DE4234285A1 (en) * 1992-10-10 1994-04-14 Heimsoth Verwaltungen Process for the heat treatment of metallic goods
DE19652607A1 (en) * 1996-12-18 1998-06-25 Messer Griesheim Gmbh Process for glue-free annealing of non-ferrous metal parts
EP0949348A1 (en) * 1998-04-09 1999-10-13 Alusuisse Technology & Management AG Process for controlled cooling of aluminium alloy strips and profiles
US6228187B1 (en) 1998-08-19 2001-05-08 Air Liquide America Corp. Apparatus and methods for generating an artificial atmosphere for the heat treating of materials
DE10054765A1 (en) * 2000-11-04 2002-05-16 Messer Griesheim Gmbh Heat treatment furnace used for heat treating steel comprises a housing containing a heating chamber with a treatment chamber having a deep cooling system
DE102004054627A1 (en) * 2004-11-11 2006-05-18 Linde Ag Device for cooling long objects
US20060266793A1 (en) * 2005-05-24 2006-11-30 Caterpillar Inc. Purging system having workpiece movement device

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE671046C (en) * 1934-08-30 1939-01-30 Aeg Process for the cooling of metallic goods heated in electrically heated bright annealing continuous furnaces
FR845086A (en) * 1938-02-18 1939-08-10 Method and device for the heat treatment of metallic objects
DE2652943A1 (en) * 1975-12-05 1977-06-16 Fagersta Ab PROCESS AND SYSTEM FOR THE PRODUCTION OF FLAT, HORIZONTAL LYING STEEL BLOCKS WITH LARGER WIDTH THAN HEIGHT
FR2379607A1 (en) * 1977-02-03 1978-09-01 Vide & Traitement Sa Thermal or thermochemical treatment process of metals - involves a cooling step using a jet of liquid nitrogen

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3036825A (en) * 1957-05-17 1962-05-29 Eisenmenger Friedrich Process and apparatus for the continuous heat treating of elongated material
US3189490A (en) * 1962-11-05 1965-06-15 United States Steel Corp Method and apparatus for quenching pipe
US3407099A (en) * 1965-10-22 1968-10-22 United States Steel Corp Method and apparatus for spraying liquids on the surface of cylindrical articles
US3507712A (en) * 1967-09-08 1970-04-21 United States Steel Corp Method and apparatus for quenching pipe

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE671046C (en) * 1934-08-30 1939-01-30 Aeg Process for the cooling of metallic goods heated in electrically heated bright annealing continuous furnaces
FR845086A (en) * 1938-02-18 1939-08-10 Method and device for the heat treatment of metallic objects
DE2652943A1 (en) * 1975-12-05 1977-06-16 Fagersta Ab PROCESS AND SYSTEM FOR THE PRODUCTION OF FLAT, HORIZONTAL LYING STEEL BLOCKS WITH LARGER WIDTH THAN HEIGHT
FR2379607A1 (en) * 1977-02-03 1978-09-01 Vide & Traitement Sa Thermal or thermochemical treatment process of metals - involves a cooling step using a jet of liquid nitrogen

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0189759A1 (en) * 1985-01-17 1986-08-06 Linde Aktiengesellschaft Method and apparatus for heat treating work pieces
EP2227570B1 (en) 2007-11-29 2017-01-25 Benteler Automobiltechnik GmbH Method for producing a shaped component comprising at least two joining areas having different ductility

Also Published As

Publication number Publication date
ATE23197T1 (en) 1986-11-15
US4515645A (en) 1985-05-07
EP0106113B1 (en) 1986-10-29
ZA836972B (en) 1984-05-30
DE3234863C2 (en) 1986-04-10
DE3234863A1 (en) 1984-03-22

Similar Documents

Publication Publication Date Title
EP0106113B1 (en) Process and apparatus for the bright annealing of metallic parts using nitrogen as the protective atmosphere
DE102005012296A1 (en) Method and device for descaling a metal strip
DE102014101159A1 (en) Process for the surface treatment of workpieces
WO2017178200A1 (en) Method and furnace installation for heat treating metal strip
DE69931063T2 (en) METHOD AND DEVICE FOR CONTINUOUS REMOVAL OF OXIDES FROM METALS
WO2006105899A1 (en) Method and device for gas quenching
EP1203106B1 (en) Method and installation for hot dip galvanizing hot rolled steel strip
DE3819803C1 (en)
EP2389260A2 (en) Method and device for annealing and descaling strips of stainless steel
DE102014003473A1 (en) Method for operating a galvanizing plant
DE4208208A1 (en) METHOD AND DEVICE FOR REDUCING IGNITION FORMING HOT METAL, IN PARTICULAR STEEL
DE3109499C2 (en)
EP0449030A2 (en) Process for annealing steel material
DE2757694A1 (en) PROCESS AND DEVICE FOR COOLING THE STRAND DURING CONTINUOUS CASTING OF METALS
EP1838892B1 (en) Method and device for hot-dip coating a metal strip
EP1518004B1 (en) Use of separation gas in continuous hot dip metal finishing
EP1430162B1 (en) Method for hot-dip finishing
DE1452106A1 (en) Device for partial cooling of wide flange carriers in carrier pockets
DE2529518B1 (en) METHOD AND DEVICE FOR LARGE PIPE QUARING
DE102022110647A1 (en) Process for tempering steel strips
DE2412391A1 (en) METHOD AND APPARATUS FOR TEMPERING HARDENABLE ALLOYS
DE928717C (en) Device and method for direct, continuous hardening of bare strips and wires made of steel
DE2347248A1 (en) PROCESS FOR PRODUCING TIN COATINGS ON WIRE FROM COPPER OR COPPER ALLOYS BY HOT TIN PLATING
WO2023198634A1 (en) Heat treatment line for a hot strip
DE102012007292A1 (en) Method and treatment section for partially refining a metal product

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

AK Designated contracting states

Designated state(s): AT BE FR IT NL

17P Request for examination filed

Effective date: 19840519

GRAA (expected) grant

Free format text: ORIGINAL CODE: 0009210

AK Designated contracting states

Kind code of ref document: B1

Designated state(s): AT BE FR IT NL

REF Corresponds to:

Ref document number: 23197

Country of ref document: AT

Date of ref document: 19861115

Kind code of ref document: T

ITF It: translation for a ep patent filed
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
ITTA It: last paid annual fee
PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: FR

Payment date: 20020910

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: AT

Payment date: 20020911

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: NL

Payment date: 20020930

Year of fee payment: 20

PGFP Annual fee paid to national office [announced via postgrant information from national office to epo]

Ref country code: BE

Payment date: 20021129

Year of fee payment: 20

PG25 Lapsed in a contracting state [announced via postgrant information from national office to epo]

Ref country code: NL

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20030907

Ref country code: AT

Free format text: LAPSE BECAUSE OF EXPIRATION OF PROTECTION

Effective date: 20030907

BE20 Be: patent expired

Owner name: *MESSER GRIESHEIM G.M.B.H.

Effective date: 20030907

NLV7 Nl: ceased due to reaching the maximum lifetime of a patent

Effective date: 20030907