EP0054962A1 - Non polluting process for carburizing steel in a molten salt bath - Google Patents

Non polluting process for carburizing steel in a molten salt bath Download PDF

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Publication number
EP0054962A1
EP0054962A1 EP81110690A EP81110690A EP0054962A1 EP 0054962 A1 EP0054962 A1 EP 0054962A1 EP 81110690 A EP81110690 A EP 81110690A EP 81110690 A EP81110690 A EP 81110690A EP 0054962 A1 EP0054962 A1 EP 0054962A1
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EP
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Prior art keywords
salt
carburizing
bath
alkaline earth
steel
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Granted
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EP81110690A
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German (de)
French (fr)
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EP0054962B1 (en
Inventor
Heinrich Dipl.-Ing. Michel
Alexander Pralea
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Evonik Operations GmbH
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Goerig & Co & Co KG GmbH
Goerig & Co & Co KG GmbH
Degussa GmbH
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Priority to AT81110690T priority Critical patent/ATE12951T1/en
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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
    • C23C8/40Solid 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 liquids, e.g. salt baths, liquid suspensions
    • C23C8/52Solid 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 liquids, e.g. salt baths, liquid suspensions more than one element being applied in one step
    • C23C8/54Carbo-nitriding
    • C23C8/56Carbo-nitriding of ferrous surfaces
    • 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
    • C23C8/40Solid 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 liquids, e.g. salt baths, liquid suspensions
    • C23C8/42Solid 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 liquids, e.g. salt baths, liquid suspensions only one element being applied
    • C23C8/44Carburising
    • C23C8/46Carburising of ferrous surfaces

Definitions

  • the present invention relates to a method for carburizing steel in a salt bath, whereby a high cyanide content in the bath is progressively avoided.
  • Carburization processes for steel in a salt bath are available in various versions in the prior art, however the processes in the prior art generally have the disadvantage of having a high cyanide content in the salt bath.
  • This high cyanide content in the baths is questionable for environmental reasons.
  • a steel crucible with a capacity of 80 l is filled with 50 kg of preparation salt, which consists of 60% barium chloride, 20% sodium chloride and 20% potassium chloride.
  • This filling is brought to a temperature of 800 ° C by means of a heating system operated with natural gas, whereby a completely homogeneous melt is created.
  • the steel crucible filling is then heated to 900 ° C and then the workpieces, namely gearwheels (consisting of case hardening steel from alloy 20 MnCr 5) with a unit weight of 1 kg, are suspended from a steel wire in the aforementioned melt and carburized within 4 hours.
  • gearwheels consisting of case hardening steel from alloy 20 MnCr 5
  • the case hardening depth is 0.83 mm.
  • FIG. 1 shows the C content of the workpiece as a function of the edge distance; the C content is given in% by weight; the carburizing depth of the C is measured in mm.
  • Figure 2 shows the hardness curve of the workpiece depending on the edge distance.
  • the hardness is given in hardness HV1 and the edge distance in mm.
  • the cyanide content is checked by sampling and titration with nickel sulfate and murexide as an indicator.

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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)
  • Heat Treatment Of Articles (AREA)
  • Cleaning And De-Greasing Of Metallic Materials By Chemical Methods (AREA)
  • Solid-Phase Diffusion Into Metallic Material Surfaces (AREA)
  • Treatment Of Steel In Its Molten State (AREA)

Abstract

1. Process for carburizing steel in a salt bath, characterised by the following process steps : a) the process container is charged with a first salt which consists of a mixture of an alkali halide and an alkaline earth halide ; b) the first salt is brought to a molten state ; c) an additional salt is added which consists of a mixture of an alkaline earth halide, an alkali ferrocyanide and an alkali cyanate, wherein the alkaline earth halide of the additional salt corresponds chemically to the alkaline earth halide of the first salt ; d) the container charge is heated to its operating temperature ; e) the workpiece to be treated is immersed in the charge in the carburizing bath and is left therein until the desired depth of carburizing is attained ; f) the workpiece is removed from the carburizing bath and, according to the type of material, is quenched in an appropriate quenching medium.

Description

Die vorliegende Erfindung betrifft ein Verfahren zum Aufkohlen von Stahl im Salzbad, wobei fortschrittlicherweise ein hoher Cyanidgehalt im Bad vermieden wird.The present invention relates to a method for carburizing steel in a salt bath, whereby a high cyanide content in the bath is progressively avoided.

Aufkohlungsverfahren von Stahl im Salzbad stehen dem Stand der Technik in verschiedenen Varianten zur Verfügung, jedoch sind die Verfahren des Standes der Technik generell mit dem Nachteil behaftet, im Salzbad einen hohen Cyanidgehalt aufzuweisen. Dieser hohe Cyanidgehalt der Bäder ist aus Umweltschutzgründen bedenklich. Es ist ferner bei solchen Bädern mit hohem Cyanidgehalt nur bedingt möglich, die aus den Bädern kommenden Werkstücke direkt in einem Abschrecksalzbad abzuschrecken, da der hohe Cyanidgehalt sehr heftige explosionsartige Reaktionen zwischen flüssigem Nitrit-Nitrat einerseits und dem Cyanid andererseits auslösen kann.Carburization processes for steel in a salt bath are available in various versions in the prior art, however the processes in the prior art generally have the disadvantage of having a high cyanide content in the salt bath. This high cyanide content in the baths is questionable for environmental reasons. In such baths with a high cyanide content, it is also only possible to quench the workpieces coming from the baths directly in a quenching salt bath, since the high cyanide content can trigger very violent explosive reactions between liquid nitrite nitrate on the one hand and the cyanide on the other hand.

Alle diese Nachteile des Standes der Technik werden bei dem erfindungsgemäßen Verfahren zum Aufkohlen der eingangs genannten Gattung unter Erreichung von Vorteilen überwunden; insbesondere wird mit dem erfindungsgemäßen Verfahren eine umweltfreundliche Aufkohlungsmöglichkeit von Stahl im Salzbad geschaffen. Ein weiterer großer Vorteil des erfindungsgemäßen Verfahrens besteht darin, daß sämtliche verwendete Salzmischungen alkali-cyanidfrei sind.All of these disadvantages of the prior art are overcome in the process according to the invention for carburizing the type mentioned at the outset, with advantages being achieved; in particular, the method according to the invention creates an environmentally friendly possibility of carburizing steel in a salt bath. Another great advantage of the process according to the invention is that all of the salt mixtures used are alkali-cyanide-free.

Ferner ist es nach dem erfindungsgemäßen Verfahren möglich, die aus dem Bad kommenden Werkstücke unmittelbar anschließend in nitritnitrathaltigen Salzbädern abzuschrecken ohne daß unerwünschte Nebenreaktionen wie beispielsweise explosionsartige Oxidationsreaktionen stattfinden. Das erfindungsgemäße Verfahren zum Aufkohlen von Stahl im Salzbad ist durch die folgenden Verfahrensschritte gekennzeichnet:

  • a) der Verfahrensbehälter wird mit einem Ansatzsalz gefüllt, das aus einem Gemisch aus Alkalihalogenid und Erdalkalihalogenid besteht;
  • b) das Ansatzsalz wird zum Schmelzen gebracht;
  • c) es wird Zugabesalz hinzugegeben, das aus einem Gemisch von Erdalkalihalogenid, Alkaliferrocyanid und Alkalicyanat besteht, wobei das Erdalkalihalogenid des Zugabesalzes chemisch mit dem Erdalkalihalogenid des Ansatzsalzes übereinstimmt;
  • d) die Verfahrensbehälterfüllung wird auf die Anwendungstemperatur erhitzt;
  • e) das zu behandelnde Werkstück wird in .die Verfahrensbehälterfüllung, nämlich in das Aufkohlungsbad getaucht und dort bis zur Erreichung der gewünschten Aufkohlungstiefe belassen;
  • f) das Werkstück wird aus dem Aufkohlungsbad entnommen und je nach Werkstoffart im entsprechenden Abschreck-Medium abgeschreckt.
Furthermore, according to the method according to the invention, it is possible to quench the workpieces coming from the bath immediately afterwards in salt baths containing nitrite nitrate without undesired side reactions such as explosive oxidation reactions taking place. The process according to the invention for carburizing steel in a salt bath is characterized by the following process steps:
  • a) the process container is filled with a preparation salt, which consists of a mixture of alkali halide and alkaline earth metal halide;
  • b) the starting salt is melted;
  • c) addition salt is added, which consists of a mixture of alkaline earth metal halide, alkali ferrocyanide and alkali metal cyanate, the alkaline earth metal halide of the addition salt chemically corresponding to the alkaline earth metal halide of the preparation salt;
  • d) the process container filling is heated to the application temperature;
  • e) the workpiece to be treated is immersed in the process tank filling, namely in the carburizing bath and left there until the desired carburizing depth is reached;
  • f) the workpiece is removed from the carburizing bath and, depending on the type of material, quenched in the appropriate quenching medium.

Das Wesen vorliegender Erfindung wird nun anhand eines Ausführungsbeispiels weiterhin erläutert:The essence of the present invention will now be further explained using an exemplary embodiment:

Ausführungsbeispiel:Design example:

Ein Stahltiegel eines Fassungsvermögens von 80 1 wird mit 50 kg Ansatzsalz gefüllt, das zu 60 % aus Bariumchlorid, zu 20 % aus Natriumchlorid und zu 20 % aus Kaliumchlorid besteht.A steel crucible with a capacity of 80 l is filled with 50 kg of preparation salt, which consists of 60% barium chloride, 20% sodium chloride and 20% potassium chloride.

Diese Füllung wird mittels einer mit Erdgas betriebenen Heizung auf eine Temperatur von 800°C gebracht, wobei eine völlig homogene Schmelze entsteht.This filling is brought to a temperature of 800 ° C by means of a heating system operated with natural gas, whereby a completely homogeneous melt is created.

Sodann werden 10 kg Zugabesalz hinzugefügt, das zu 60 % aus Bariumchlorid, zu 20 % aus Kaliumferrocyanid ( = gelbes Blutlaugensalz ) und zu 20 % aus Kaliumcyanat besteht.Then 10 kg of addition salt are added, which consists of 60% barium chloride, 20% potassium ferrocyanide (= yellow blood-lye salt) and 20% potassium cyanate.

Die Stahltiegelfüllung wird nun auf 900°C aufgeheizt und sodann die Werkstücke, nämlich Zahnräder (bestehend aus Einsatzstahl aus Legierung 20 MnCr 5) mit einem Stückgewicht von 1 kg, an einem Stahldraht hängend in die vorgenannte Schmelze eingebracht und innerhalb von 4 Stunden aufgekohlt.The steel crucible filling is then heated to 900 ° C and then the workpieces, namely gearwheels (consisting of case hardening steel from alloy 20 MnCr 5) with a unit weight of 1 kg, are suspended from a steel wire in the aforementioned melt and carburized within 4 hours.

Sodann entnimmt man diese Werkstücke aus der Schmelze und gibt sie unmittelbar danach in ein Warmbad ein, das zu 50 % aus Kaliumnitrat und zu 50 % aus Natriumnitrit besteht; die Abschrecktemperatur beträgt 200°C.Then these workpieces are removed from the melt and immediately put into a warm bath which consists of 50% potassium nitrate and 50% sodium nitrite; the quenching temperature is 200 ° C.

ErgebnissenResults

Es wurde ein Rand-Kohlenstoffgehalt von 0,955 % C erreicht.An edge carbon content of 0.955% C was reached.

Die Einsatzhärtungstiefe beträgt 0,83 mm.The case hardening depth is 0.83 mm.

Der Kohlenstoffverlauf und der Härteverlauf dieser Werkstücke (Zahnräder) sind in der beiliegenden Figur 1 und der beiliegenden Figur 2 angegeben.The carbon profile and the hardness profile of these workpieces (gear wheels) are given in the attached FIG. 1 and the attached FIG. 2.

Die Figur 1 zeigt den C-Gehalt des Werkstückes in Abhängigkeit vom Randabstand; der C-Gehalt ist in Gew.-% angegeben; die Aufkohlungstiefe des C ist in mm gemessen.FIG. 1 shows the C content of the workpiece as a function of the edge distance; the C content is given in% by weight; the carburizing depth of the C is measured in mm.

Figur 2 zeigt den Härteverlauf des Werkstückes in Abhängigkeit vom Randabstand.Figure 2 shows the hardness curve of the workpiece depending on the edge distance.

Die Härte ist in Härte HV1 und der Randabstand in mm angegeben.The hardness is given in hardness HV1 and the edge distance in mm.

Im kontinuierlichen Betrieb erfolgt die Kontrolle des Cyanidgehaltes durch Probenahmen und Titration mit Nickelsulfat und Murexid als Indikator.In continuous operation, the cyanide content is checked by sampling and titration with nickel sulfate and murexide as an indicator.

Alle 3 Stunden wurde 0,5 kg Zugabesalz zugegeben, wobei sich ein Cyanidgehalt von etwa 1,5 % einstellt.0.5 kg of addition salt was added every 3 hours, resulting in a cyanide content of about 1.5%.

Innerhalb einer Zeitdauer von 3 Monaten wurden 30 Probebolzen der Stahlqualität 20 MnCr 5, ferner 30 Probebolzen aus der Legierung C 15 und schließlich 18 Probebolzen aus der Legierung 18 Cr Ni 8 getestet und zwar jeweils 4 Stunden bei Temperaturen von 900°C.Within a period of 3 months, 30 steel M 20 Cr 5 test bolts, 30 C 15 alloy bolts and finally 18 18 Cr Ni 8 alloy bolts were tested, each for 4 hours at temperatures of 900 ° C.

Dabei ergaben sich Rand-Kohlenstoffwerte zwischen 0,9 und 0,98 Gew.-% C.This resulted in marginal carbon values between 0.9 and 0.98% by weight of C.

Damit ist die ständige Reproduzierbarkeit des erfindungsgemäßen Verfahrens sichergestellt.This ensures the constant reproducibility of the method according to the invention.

Aufgrund des ständigen Badgebrauches ist auch eine ständige Kontrolle des geringen Cyanidgehalts möglich. Die Regulierung des Cyanidgehalts d.h. die Sicherstellung des gleichbleibenden geringen Cyanidgehaltes wird fortschrittlicherweise nicht etwa durch Zugabe an Cyanid erreicht. bzw. geregelt, sondern lediglich durch Einbringen des Zugabesalzes gemäß den Angaben im Merkmal c) des Hauptpatentanspruchs 1.Due to the constant use of the bath, a constant control of the low cyanide content is possible. The regulation of the cyanide content i.e. progressively, ensuring the constant low cyanide content is not achieved by adding cyanide, for example. or regulated, but only by introducing the addition salt according to the information in feature c) of the main patent claim 1.

Gegebenenfalls kann man ferner beispielsweise nach Entstehen der kompletten Schmelze, also nach Beendigung der Verfahrensstufe c) des Hauptpatentanspruchs 1 zur Erreichung einer sogenannten künstlichen Alterung des Bades geringe Mengen an Soda, beispielsweise 1 Gew.-% bezogen auf die Badmenge hinzugeben.If necessary, it is also possible to add small amounts of soda, for example 1% by weight, based on the amount of bath, for example after the complete melt has formed, that is to say after process step c) of main patent claim 1 has ended, in order to achieve what is known as artificial aging of the bath.

Alle %-Angaben der vorliegenden Offenbarung sind Gew.-%.All percentages of the present disclosure are percentages by weight.

Claims (9)

1. Umweltfreundliches Verfahren zum Aufkohlen von Stahl im Salzbadgekennzeichnet durch folgende Verfahrensschritte: a) der Verfahrensbehälter wird mit einem Ansatzsalz gefüllt, das aus einem Gemisch von Alkalihalogenid und Erdalkalihalogenid besteht; b) das Ansatzsalz wird zum Schmelzen gebracht; c) es wird Zugabesalz hinzugegeben, das aus einem Gemisch von Erdalkalihalogenid, Alkaliferrocyanid und Alkalicyanat besteht, wobei das Erdalkalihalogenid des Zugabesalzes chemisch mit dem Erdalkalihalogenid des Ansatzsalzes übereinstimmt; d) die VerfahrensbehälterfÜllung wird auf die Anwendungstemperatur erhitzt; e) das zu behandelnde Werkstück wird in die Verfahrensbehälterfüllung, nämlich in das Aufkohlungsbad getaucht und dort bis zur Erreichung der gewünschten Aufkohlungstiefe belassen; f) das Werkstück wird aus dem Aufkohlungsbad entnommen und je nach Werkstoffart im entsprechenden Abschreck-Medium abgeschreckt. 1. Environmentally friendly process for carburizing steel in a salt bath characterized by the following process steps: a) the process container is filled with a preparation salt, which consists of a mixture of alkali halide and alkaline earth metal halide; b) the starting salt is melted; c) addition salt is added, which consists of a mixture of alkaline earth metal halide, alkali ferrocyanide and alkali metal cyanate, the alkaline earth metal halide of the addition salt chemically corresponding to the alkaline earth metal halide of the preparation salt; d) the process tank filling is heated to the application temperature; e) the workpiece to be treated is immersed in the process tank filling, namely in the carburizing bath and left there until the desired carburizing depth is reached; f) the workpiece is removed from the carburizing bath and, depending on the type of material, quenched in the appropriate quenching medium. 2. Verfahren zum Aufkohlen von Stahl im Salzbad, dadurch gekennzeichnet,
daß in der Verfahrensstufe a) bei normaler Temperatur der Verfahrensbehälter zu 80 % der gewünschten Gesamtfüllmenge mit Ansatzsalz gefüllt wird.
2. Process for carburizing steel in a salt bath, characterized in that
that in process step a) the process container is filled to 80% of the desired total filling quantity with starting salt at normal temperature.
3. Verfahren zum Aufkohlen von Stahl im Salzbad nach Anspruch 1,
dadurch gekennzeichnet,
daß man in der Verfahrensstufe b) das Ansatzsalz auf eine Temperatur von ca. 800°C erhitzt, wobei Schmelzfluß eintritt.
3. A method for carburizing steel in a salt bath according to claim 1,
characterized,
that the process salt is heated to a temperature of about 800 ° C. in process step b), melt flow occurring.
4. Verfahren zum Aufkohlen von Stahl im Salzbad nach Anspruch 1,
dadurch gekennzeichnet,
daß in der Verfahrensstufe c) 20 % Zugabesalz hinzugegeben wird , das aus Erdalkalihalogenid, Kaliumferrocyanid oder Natriumferrocyanid sowie aus Kaliumcyanat oder Natriumcyanat besteht.
4. A method for carburizing steel in a salt bath according to claim 1,
characterized,
that in process step c) 20% addition salt is added, which consists of alkaline earth metal halide, potassium ferrocyanide or sodium ferrocyanide and potassium cyanate or sodium cyanate.
5. Verfahren zum Aufkohlen von Stahl im Salzbad nach Anspruch 1,
dadurch gekennzeichnet,
daß man das Bad auf eine Anwendungstemperatur von etwa 880°C bis 1020°C erhitzt.
5. A method for carburizing steel in a salt bath according to claim 1,
characterized,
that the bath is heated to an application temperature of about 880 ° C to 1020 ° C.
6. Verfahren zum Aufkohlen von Stahl im Salzbad nach Anspruch 1,
dadurch gekennzeichnet,
daß man das zu behandelnde Werkstück wie beispielsweise eine aus Stahl bestehende Kurbelwelle oder ein Zahnrad in das Aufkohlungsbad eintaucht und dort je nach der gewünschten Aufkohlungstiefe beläBt.
6. A method for carburizing steel in a salt bath according to claim 1,
characterized,
that the workpiece to be treated, such as a steel crankshaft or a gearwheel, is immersed in the carburizing bath and left there depending on the desired carburizing depth.
7. Verfahren zum Aufkohlen von Stahl im Salzbad nach mindestens einem der Ansprüche 1 bis 6, dadurch gekennzeichnet,
daß die Aufkohlungstemperatur kontrolliert und/oder geregelt wird.
7. A method for carburizing steel in a salt bath according to at least one of claims 1 to 6, characterized in that
that the carburizing temperature is checked and / or regulated.
8. Verfahren zum Aufkohlen von Stahl im Salzbad nach Anspruch 1,
dadurch gekennzeichnet,
daß man in der Verfahrensstufe f) das aus dem Bad entnommene Werkstück in Wasser, Öl oder im Abschrecksalzbad abschreckt.
8. A method for carburizing steel in a salt bath according to claim 1,
characterized,
that in process step f) the workpiece removed from the bath is quenched in water, oil or in the quenching salt bath.
9. Verfahren zum Aufkohlen von Stahl im Salzbad nach mindestens einem der Ansprüche 1 bis 8, dadurch gekennzeichnet,
daß die Regelung des geringen Cyanidgehalts des Bades durch Einbringen des Zugabesalzes durchgeführt wird.
9. A method for carburizing steel in a salt bath according to at least one of claims 1 to 8, characterized in that
that the control of the low cyanide content of the bath is carried out by introducing the addition salt.
EP81110690A 1980-12-23 1981-12-22 Non polluting process for carburizing steel in a molten salt bath Expired EP0054962B1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT81110690T ATE12951T1 (en) 1980-12-23 1981-12-22 ECO-FRIENDLY SALT BATH CARBURIZING PROCESS FOR STEEL.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE3048607 1980-12-23
DE3048607A DE3048607C2 (en) 1980-12-23 1980-12-23 Cyanide-free process for carburizing steel and adding salt to carry out the process

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EP0054962A1 true EP0054962A1 (en) 1982-06-30
EP0054962B1 EP0054962B1 (en) 1985-04-24

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Cited By (4)

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US6461448B1 (en) 1998-08-12 2002-10-08 Swagelok Company Low temperature case hardening processes
US6547888B1 (en) 2000-01-28 2003-04-15 Swagelok Company Modified low temperature case hardening processes
DE102006026883B3 (en) * 2006-06-09 2007-08-16 Durferrit Gmbh Hardening of stainless steel comprises submerging in hot bath of molten salts
EP2055801A1 (en) * 2007-10-31 2009-05-06 Durferrit GmbH Method for hardening stainless steel surfaces on workpieces and fused salt for performing the method

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US6165597A (en) * 1998-08-12 2000-12-26 Swagelok Company Selective case hardening processes at low temperature

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6461448B1 (en) 1998-08-12 2002-10-08 Swagelok Company Low temperature case hardening processes
US6547888B1 (en) 2000-01-28 2003-04-15 Swagelok Company Modified low temperature case hardening processes
DE102006026883B3 (en) * 2006-06-09 2007-08-16 Durferrit Gmbh Hardening of stainless steel comprises submerging in hot bath of molten salts
DE102006026883B8 (en) * 2006-06-09 2007-10-04 Durferrit Gmbh Process for hardening stainless steel and molten salt for carrying out the process
US7909943B2 (en) 2006-06-09 2011-03-22 Durferrit Gmbh Method for hardening stainless steel and molten salt bath for realizing said process
EP2055801A1 (en) * 2007-10-31 2009-05-06 Durferrit GmbH Method for hardening stainless steel surfaces on workpieces and fused salt for performing the method
US8083866B2 (en) 2007-10-31 2011-12-27 Durferrit Gmbh Method for hardening the surfaces of work pieces made of stainless steel, and a molten salt bath for realizing the method

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CH647002A5 (en) 1984-12-28
EP0054962B1 (en) 1985-04-24
DE3170212D1 (en) 1985-05-30
DE3048607A1 (en) 1982-07-01
DE3048607C2 (en) 1983-07-07
ATE12951T1 (en) 1985-05-15

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