EP0779376A1 - Plasma carburizing of metallic workpieces - Google Patents

Plasma carburizing of metallic workpieces Download PDF

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Publication number
EP0779376A1
EP0779376A1 EP96118592A EP96118592A EP0779376A1 EP 0779376 A1 EP0779376 A1 EP 0779376A1 EP 96118592 A EP96118592 A EP 96118592A EP 96118592 A EP96118592 A EP 96118592A EP 0779376 A1 EP0779376 A1 EP 0779376A1
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Prior art keywords
propane
methane
carbon
plasma
carburizing
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German (de)
French (fr)
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EP0779376B2 (en
EP0779376B1 (en
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Winfried Dipl.-Phys. Gräfen
Bernd Dr. Mont. Edenhofer
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Ipsen International GmbH
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    • 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
    • C23C8/00Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals
    • C23C8/06Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases
    • C23C8/36Solid state diffusion of only non-metal elements into metallic material surfaces; Chemical surface treatment of metallic material by reaction of the surface with a reactive gas, leaving reaction products of surface material in the coating, e.g. conversion coatings, passivation of metals using gases using ionised gases, e.g. ionitriding
    • C23C8/38Treatment of ferrous surfaces

Definitions

  • the invention relates to a process for the plasma carburization of metallic workpieces in a furnace, the furnace atmosphere containing a carbon carrier which is split under the process conditions of the plasma carburization with the release of pure carbon.
  • propane (C 3 H 8 ) is generally used as the carbon carrier, which is split in the course of the so-called propane pyrolysis according to the following reaction equations: C. 3rd H 8th ⁇ CH 4th + C 2nd H 4th C. 2nd H 4th ⁇ 2C + 2H 2nd CH 4th ⁇ C + 2H 2nd
  • methane (CH 4 ) is mostly used as the carbon carrier, which is obtained by methane pyrolysis according to the equation CH 4th ⁇ C + 2H 2nd is split.
  • propane instead of methane.
  • propane is a more effective carbon carrier than methane due to its larger number of carbon atoms - 3 carbon atoms for propane versus 1 carbon atom for methane.
  • propane has the disadvantage that propane is thermally split in the temperature range above 600 ° C., as a result of which carburization takes place in the furnace, which leads to sooting of the furnace.
  • Methane on the other hand, has only one carbon atom, but the methane molecule is so stable that it is not already split at the necessary carburizing temperature. Rather, the splitting takes place only in the plasma and therefore really only on the workpiece surface. Since the carbon mass flow density is only very low when splitting methane, large-scale batches are very difficult to carburize evenly with methane.
  • the invention has for its object to provide a method for the plasma carburizing of metal workpieces, which ensures carburizing with a high carbon mass flow density, without at the same time the risk of sooting the furnace.
  • the achievement of the high carbon mass flow density on the one hand and the avoidance of sooting on the other hand is due to the fact that propane can provide much more carbon than methane due to its three carbon atoms during thermal and electrical splitting in the plasma.
  • the methane on the other hand hardly splits at carburizing temperatures between 800 ° C and 1000 ° C.
  • the methane is only split in the plasma, ie really only on the workpiece surface, so that these released carbon atoms can only contribute to carburizing the workpieces, but not to sooting the furnace.
  • the gas pressure in the furnace atmosphere is below 10 mbar, since thermal splitting of the methane is almost impossible in this pressure range.
  • the furnace atmosphere can also contain other gases, in particular hydrogen and / or argon, which, as inert gases, are also intended to prevent oxidation of the workpieces.
  • the drawing shows the hardness curve for the material 27 CrMo 4 according to the plasma carburizing process with a methane-propane mixture as a carbon carrier.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Mechanical Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Solid-Phase Diffusion Into Metallic Material Surfaces (AREA)
  • Arc Welding In General (AREA)

Abstract

In plasma carburisation of metal work pieces in a furnace containing an atmosphere of carbon carrier under plasma carburisation conditions to produce pure C, a mixture of methane and propane is used as C carrier.

Description

Die Erfindung betrifft ein Verfahren zur Plasmaaufkohlung metallischer Werkstücke in einem Ofen, wobei die Ofenatmosphäre einen Kohlenstoff-Träger enthält, der unter den Prozeßbedingungen der Plasmaaufkohlung unter Abgabe von reinem Kohlenstoff gespalten wird.The invention relates to a process for the plasma carburization of metallic workpieces in a furnace, the furnace atmosphere containing a carbon carrier which is split under the process conditions of the plasma carburization with the release of pure carbon.

Unter den thermochemischen Behandlungsverfahren zur Einsatzhärtung metallischer Werkstücke haben sich in den letzten Jahren neben der konventionellen Gasaufkohlung immer mehr die Aufkohlungsprozesse in Vakuumanlagen durchgesetzt, da nur mit diesen Verfahren eine randoxidationsfreie Aufkohlung realisierbar ist. Bei diesen Aufkohlungsprozessen in Vakuumanlagen handelt es sich um die Niederdruck- und die Plasmaaufkohlung. Da bei diesen Aufkohlungsverfahren ohne sauerstoffhaltige Reaktionsgase gearbeitet wird, kann keine C-Pegelregelung erfolgen; die entscheidende Kenngröße für den Kohlenstoffübergang ist bei diesen Verfahren die Kohlenstoff-Massenstromdichte, die als Kohlenstoffmenge definiert ist, die pro Zeit- und Flächeneinheit in den Werkstoff übergeht. Dieser zur Aufkohlung benötigte Kohlenstoff wird von einem in der Ofenatmosphäre befindlichen Kohlenstoff-Träger - meist einem Kohlenwasserstoff - zur Verfügung gestellt, der bei den gegebenen Prozeßbedingungen unter Abgabe von reinem Kohlenstoff gespalten wird.In addition to conventional gas carburizing, the carburizing processes in vacuum systems have become more and more common among thermochemical treatment processes for case hardening of metallic workpieces, since only these processes can be used to carry out carburizing without edge oxidation. These carburizing processes in vacuum plants are low pressure and plasma carburizing. Since these carburizing processes work without oxygen-containing reaction gases, no C level control can take place; The decisive parameter for the carbon transition in these processes is the carbon mass flow density, which is defined as the amount of carbon that passes into the material per unit of time and area. This carbon required for the carburization is made available by a carbon carrier in the furnace atmosphere - usually a hydrocarbon - which is split under the given process conditions with the release of pure carbon.

Bei den bekannten Niederdruck-Aufkohlungsverfahren wird als Kohlenstoff-Träger in der Regel Propan (C3H8) verwendet, welches im Laufe der sogenannten Propanpyrolyse nach folgenden Reaktionsgleichungen gespalten wird: C 3 H 8 → CH 4 + C 2 H 4

Figure imgb0001
C 2 H 4 → 2C + 2H 2
Figure imgb0002
CH 4 → C + 2H 2
Figure imgb0003
In the known low-pressure carburizing processes, propane (C 3 H 8 ) is generally used as the carbon carrier, which is split in the course of the so-called propane pyrolysis according to the following reaction equations: C. 3rd H 8th → CH 4th + C 2nd H 4th
Figure imgb0001
C. 2nd H 4th → 2C + 2H 2nd
Figure imgb0002
CH 4th → C + 2H 2nd
Figure imgb0003

Bei der Plasmaaufkohlung wird als Kohlenstoff-Träger meist Methan (CH4) verwendet, welches im Wege der Methanpyrolyse nach der Gleichung CH 4 → C + 2H 2

Figure imgb0004
gespalten wird. Bei der Plasmaaufkohlung ist es jedoch auch möglich, anstelle von Methan Propan zu verwenden.In plasma carburizing, methane (CH 4 ) is mostly used as the carbon carrier, which is obtained by methane pyrolysis according to the equation CH 4th → C + 2H 2nd
Figure imgb0004
is split. In plasma carburizing, however, it is also possible to use propane instead of methane.

Die Verwendung von Methan oder Propan als Kohlenstoff-Träger ist jeweils mit verschiedenen Vor- und Nachteilen verbunden. So ist beispielsweise Propan aufgrund seiner größeren Anzahl von Kohlenstoffatomen - 3 C-Atome beim Propan gegenüber 1 C-Atom beim Methan - ein wirksamerer Kohlenstoff-Träger als Methan. Andererseits weist Propan jedoch den Nachteil auf, daß Propan bereits im Temperaturbereich über 600°C thermisch gespalten wird, wodurch bereits im Ofen eine Aufkohlung stattfindet, die zum Verrußen des Ofens führt. Methan hingegen weist zwar nur ein C-Atom auf, jedoch ist das Methan-Molekül so stabil, daß es nicht bereits bei der notwendigen Aufkohlungstemperatur gespalten wird. Die Spaltung erfolgt vielmehr erst im Plasma und somit wirklich nur an der Werkstückoberfläche. Da die Kohlenstoff-Massenstromdichte bei der Spaltung von Methan nur sehr gering ist, lassen sich großflächige Chargen nur sehr schwer gleichmäßig mit Methan aufkohlen.The use of methane or propane as a carbon carrier has various advantages and disadvantages. For example, propane is a more effective carbon carrier than methane due to its larger number of carbon atoms - 3 carbon atoms for propane versus 1 carbon atom for methane. On the other hand, however, propane has the disadvantage that propane is thermally split in the temperature range above 600 ° C., as a result of which carburization takes place in the furnace, which leads to sooting of the furnace. Methane, on the other hand, has only one carbon atom, but the methane molecule is so stable that it is not already split at the necessary carburizing temperature. Rather, the splitting takes place only in the plasma and therefore really only on the workpiece surface. Since the carbon mass flow density is only very low when splitting methane, large-scale batches are very difficult to carburize evenly with methane.

In Anbetracht des voranstehend geschilderten Standes der Technik liegt der Erfindung die Aufgabe zugrunde, ein Verfahren zur Plasmaaufkohlung metallischer Werkstücke bereitzustellen, das eine Aufkohlung mit einer hohen Kohlenstoff-Massenstromdichte gewährleistet, ohne daß gleichzeitig die Gefahr der Verrußung des Ofens besteht.In view of the prior art described above, the invention has for its object to provide a method for the plasma carburizing of metal workpieces, which ensures carburizing with a high carbon mass flow density, without at the same time the risk of sooting the furnace.

Überraschenderweise hat sich im Laufe der Versuche herausgestellt, daß diese Aufgabe erfindungsgemäß dadurch gelöst wird, daß als Kohlenstoff-Träger ein Gemisch aus Methan und Propan verwendet wird.Surprisingly, the experiments has been found in the course that this object is inventively achieved in that a mixture of methane and propane is used as carbon support.

Das Erreichen der hohen Kohlenstoff-Massenstromdichte einerseits und das Vermeiden der Verrußung des Ofens andererseits kommt dabei dadurch zustande, daß Propan aufgrund seiner drei C-Atome bei der thermischen und elektrischen Spaltung im Plasma viel mehr Kohlenstoff zur Verfügung stellen kann als Methan. Das Methan auf der anderen Seite spaltet sich bei den Aufkohlungstemperaturen zwischen 800°C und 1000°C fast gar nicht. Die Spaltung des Methans findet erst im Plasma, also wirklich nur an der Werkstückoberfläche statt, so daß diese frei werdenden Kohlenstoff-Atome nur zum Aufkohlen der Werkstücke, nicht jedoch zur Verrußung des Ofens beitragen können.The achievement of the high carbon mass flow density on the one hand and the avoidance of sooting on the other hand is due to the fact that propane can provide much more carbon than methane due to its three carbon atoms during thermal and electrical splitting in the plasma. The methane on the other hand hardly splits at carburizing temperatures between 800 ° C and 1000 ° C. The methane is only split in the plasma, ie really only on the workpiece surface, so that these released carbon atoms can only contribute to carburizing the workpieces, but not to sooting the furnace.

Bei den Versuchen hat sich herausgestellt, daß ein Methan-Propan-Gemisch mit bis zu 60 Vol.-% Propan, insbesondere einem Propan-Anteil von 5 bis 50 Vol.-% besonders geeignet ist, um ohne Rußbildung eine hohe Kohlenstoff-Massenstromdichte bzw. Kohlenstoff-Übertragungsrate zu erhalten.The tests have shown that a methane / propane mixture with up to 60 vol.% Propane, in particular a propane fraction of 5 to 50 vol.%, Is particularly suitable for achieving a high carbon mass flow density or soot formation without soot formation To get carbon transfer rate.

Gemäß einer bevorzugten Ausführungsform des erfindungsgemäßen Verfahrens beträgt der Gasdruck in der Ofenatmosphäre unter 10 mbar, da in diesem Druckbereich eine thermische Spaltung des Methans nahezu unmöglich ist.According to a preferred embodiment of the method according to the invention, the gas pressure in the furnace atmosphere is below 10 mbar, since thermal splitting of the methane is almost impossible in this pressure range.

Neben dem Methan-Propan-Gemisch kann die Ofenatmosphäre zusätzlich noch weitere Gase, insbesondere Wasserstoff und/oder Argon enthalten, welche als Inertgase zusätzlich die Oxidation der Werkstücke verhindern sollen.In addition to the methane-propane mixture, the furnace atmosphere can also contain other gases, in particular hydrogen and / or argon, which, as inert gases, are also intended to prevent oxidation of the workpieces.

In der Zeichnung ist für den Werkstoff 27 CrMo 4 der Härteverlauf nach dem Plasmaaufkohlungsverfahren mit einem Methan-Propan-Gemisch als Kohlenstoff-Träger dargestellt.The drawing shows the hardness curve for the material 27 CrMo 4 according to the plasma carburizing process with a methane-propane mixture as a carbon carrier.

Die Prozeßparameter für den in der Abbildung dargestellten Plasmaaufkohlungsprozeß waren:

  • zehnminütiges Aufkohlen bei einer Aufkohlungstemperatur von 940°C.
  • Die anschließende Diffusionsphase betrug 51 Minuten,
  • woran anschließend nach dem Absenken auf die Härtetemperatur von 860°C die Charge mittels Hochdruckgasabschreckung abgeschreckt wurde.
The process parameters for the plasma carburizing process shown in the figure were:
  • carburizing for ten minutes at a carburizing temperature of 940 ° C.
  • The subsequent diffusion phase was 51 minutes,
  • after which the charge was quenched by high-pressure gas quenching after lowering to the hardening temperature of 860 ° C.

Als Ergebnis dieses Prozesses wurde eine Einsatzhärtungstiefe (550 HV 1) von 0,7 mm auf der Zahnflanke erzielt.As a result of this process, a case hardening depth (550 HV 1) of 0.7 mm was achieved on the tooth flank.

Mit dem voranstehend dargestellten Verfahren ist es somit möglich, durch die Verwendung des Methan-Propan-Gemisches als Kohlenstoff-Träger die Kohlenstoff-Massenstromdichte bei der Plasmaaufkohlung deutlich zu erhöhen, ohne daß die Gefahr der Verrußung des Ofens besteht.With the method described above, it is thus possible, by using the methane-propane mixture as the carbon carrier, to significantly increase the carbon mass flow density in the plasma carburizing, without the risk of sooting the furnace.

Claims (6)

Verfahren zur Plasmaaufkohlung metallischer Werkstücke in einem Ofen, wobei die Ofenatmosphäre einen Kohlenstoff-Träger enthält, der unter den Prozeßbedingungen der Plasmaaufkohlung unter Abgabe von reinem Kohlenstoff gespalten wird,
dadurch gekennzeichnet,
daß als Kohlenstoff-Träger ein Gemisch aus Methan und Propan verwendet wird.
Process for plasma carburizing metallic workpieces in a furnace, the furnace atmosphere containing a carbon carrier which is split under the process conditions of plasma carburization with the release of pure carbon,
characterized,
that a mixture of methane and propane is used as the carbon carrier.
Verfahren nach Anspruch 1, dadurch gekennzeichnet, daß das Methan-Propan-Gemisch bis zu 60 Vol.-% Propan enthält.A method according to claim 1, characterized in that the methane-propane mixture contains up to 60 vol .-% propane. Verfahren nach Anspruch 1 oder 2, dadurch gekennzeichnet, daß der Propan-Anteil in dem Methan-Propan-Gemisch 5 bis 50 Vol.-% beträgt.A method according to claim 1 or 2, characterized in that the propane content in the methane-propane mixture is 5 to 50% by volume. Verfahren nach einem der Ansprüche 1 bis 3, dadurch gekennzeichnet, daß der Gasdruck der Ofenatmosphäre unter 10 mbar beträgt.Method according to one of claims 1 to 3, characterized in that the gas pressure of the furnace atmosphere is below 10 mbar. Verfahren nach einem der Ansprüche 1 bis 4, dadurch gekennzeichnet, daß in der Ofenatmosphäre neben dem Kohlenstoff-Träger noch andere Gase enthalten sind.Method according to one of claims 1 to 4, characterized in that other gases are contained in the furnace atmosphere in addition to the carbon carrier. Verfahren nach Anspruch 5, dadurch gekennzeichnet, daß die Ofenatmosphäre zusätzlich noch Wasserstoff und/oder Argon enthält.A method according to claim 5, characterized in that the furnace atmosphere additionally contains hydrogen and / or argon.
EP96118592A 1995-12-16 1996-11-20 Plasma carburizing of metallic workpieces Expired - Lifetime EP0779376B2 (en)

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DE19815233A1 (en) * 1998-04-04 1999-10-07 Ald Vacuum Techn Gmbh Process for vacuum carburizing under treatment gas
WO2008025344A1 (en) * 2006-08-31 2008-03-06 Schaeffler Kg Process for producing a highly case-hardenable roller bearing component

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US20050016831A1 (en) * 2003-07-24 2005-01-27 Paganessi Joseph E. Generation of acetylene for on-site use in carburization and other processes
DE102004053935B4 (en) * 2004-11-09 2015-04-09 Schaeffler Technologies AG & Co. KG Process for the heat treatment of a component made of a thermosetting heat-resistant steel and a component made of a thermosetting, heat-resistant steel
KR101622306B1 (en) * 2009-10-29 2016-05-19 삼성전자주식회사 Graphene sheet, substrate comprising graphene sheet and process for preparing these materials

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE19815233A1 (en) * 1998-04-04 1999-10-07 Ald Vacuum Techn Gmbh Process for vacuum carburizing under treatment gas
WO2008025344A1 (en) * 2006-08-31 2008-03-06 Schaeffler Kg Process for producing a highly case-hardenable roller bearing component

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DE19547131A1 (en) 1997-06-19
ATE189271T1 (en) 2000-02-15
US5851314A (en) 1998-12-22
DE59604291D1 (en) 2000-03-02
EP0779376B2 (en) 2002-12-18
EP0779376B1 (en) 2000-01-26

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