EP2881492B1 - Method for carburising metal deep drawn article or a bent pressed article made of austenitic stainless steel - Google Patents
Method for carburising metal deep drawn article or a bent pressed article made of austenitic stainless steel Download PDFInfo
- Publication number
- EP2881492B1 EP2881492B1 EP13196076.7A EP13196076A EP2881492B1 EP 2881492 B1 EP2881492 B1 EP 2881492B1 EP 13196076 A EP13196076 A EP 13196076A EP 2881492 B1 EP2881492 B1 EP 2881492B1
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- gas
- gas mixture
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- process step
- temperature
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- 238000000034 method Methods 0.000 title claims description 62
- 229910052751 metal Inorganic materials 0.000 title description 4
- 239000002184 metal Substances 0.000 title description 4
- 229910000963 austenitic stainless steel Inorganic materials 0.000 title description 2
- 239000007789 gas Substances 0.000 claims description 72
- 239000000203 mixture Substances 0.000 claims description 39
- 238000005255 carburizing Methods 0.000 claims description 17
- IJGRMHOSHXDMSA-UHFFFAOYSA-N nitrogen Substances N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 15
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical group [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 10
- 239000001301 oxygen Substances 0.000 claims description 10
- 229910052760 oxygen Inorganic materials 0.000 claims description 10
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 9
- 230000008569 process Effects 0.000 claims description 9
- 229910052757 nitrogen Inorganic materials 0.000 claims description 8
- 229910052739 hydrogen Inorganic materials 0.000 claims description 7
- 229910001220 stainless steel Inorganic materials 0.000 claims description 7
- 239000001257 hydrogen Substances 0.000 claims description 6
- 239000010935 stainless steel Substances 0.000 claims description 6
- 238000011282 treatment Methods 0.000 claims description 6
- 229930195735 unsaturated hydrocarbon Natural products 0.000 claims description 5
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 claims description 3
- -1 salt compound Chemical class 0.000 claims description 2
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims 1
- 229910000831 Steel Inorganic materials 0.000 description 19
- 239000010410 layer Substances 0.000 description 19
- 239000010959 steel Substances 0.000 description 19
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 16
- 229910052799 carbon Inorganic materials 0.000 description 16
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 10
- 239000002344 surface layer Substances 0.000 description 10
- 230000015572 biosynthetic process Effects 0.000 description 9
- 238000010438 heat treatment Methods 0.000 description 8
- 230000007797 corrosion Effects 0.000 description 7
- 238000005260 corrosion Methods 0.000 description 7
- WGLPBDUCMAPZCE-UHFFFAOYSA-N Trioxochromium Chemical compound O=[Cr](=O)=O WGLPBDUCMAPZCE-UHFFFAOYSA-N 0.000 description 6
- 229910000423 chromium oxide Inorganic materials 0.000 description 6
- 238000003856 thermoforming Methods 0.000 description 6
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 5
- 230000004913 activation Effects 0.000 description 5
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 5
- 229910021529 ammonia Inorganic materials 0.000 description 5
- 229910052731 fluorine Inorganic materials 0.000 description 5
- 239000011737 fluorine Substances 0.000 description 5
- 238000009792 diffusion process Methods 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 230000007547 defect Effects 0.000 description 3
- 239000011261 inert gas Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical group O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 238000005452 bending Methods 0.000 description 2
- 239000001569 carbon dioxide Substances 0.000 description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 description 2
- 229910052804 chromium Inorganic materials 0.000 description 2
- 239000011651 chromium Substances 0.000 description 2
- 239000000470 constituent Substances 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- QDOXWKRWXJOMAK-UHFFFAOYSA-N dichromium trioxide Chemical compound O=[Cr]O[Cr]=O QDOXWKRWXJOMAK-UHFFFAOYSA-N 0.000 description 2
- 229910052736 halogen Inorganic materials 0.000 description 2
- 150000002367 halogens Chemical class 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000004886 process control Methods 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 230000001603 reducing effect Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 229910000640 Fe alloy Inorganic materials 0.000 description 1
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 238000005275 alloying Methods 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000012999 compression bending Methods 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- 229910021385 hard carbon Inorganic materials 0.000 description 1
- 231100001261 hazardous Toxicity 0.000 description 1
- 239000000383 hazardous chemical Substances 0.000 description 1
- 231100000086 high toxicity Toxicity 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 230000002427 irreversible effect Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 238000009736 wetting Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C8/00—Solid 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
- C23C8/06—Solid 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
- C23C8/08—Solid 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 only one element being applied
- C23C8/20—Carburising
- C23C8/22—Carburising of ferrous surfaces
-
- C—CHEMISTRY; METALLURGY
- C21—METALLURGY OF IRON
- C21D—MODIFYING 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
- C21D1/00—General methods or devices for heat treatment, e.g. annealing, hardening, quenching or tempering
- C21D1/74—Methods of treatment in inert gas, controlled atmosphere, vacuum or pulverulent material
-
- C—CHEMISTRY; METALLURGY
- C23—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; CHEMICAL SURFACE TREATMENT; DIFFUSION TREATMENT OF METALLIC MATERIAL; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL; INHIBITING CORROSION OF METALLIC MATERIAL OR INCRUSTATION IN GENERAL
- C23C—COATING METALLIC MATERIAL; COATING MATERIAL WITH METALLIC MATERIAL; SURFACE TREATMENT OF METALLIC MATERIAL BY DIFFUSION INTO THE SURFACE, BY CHEMICAL CONVERSION OR SUBSTITUTION; COATING BY VACUUM EVAPORATION, BY SPUTTERING, BY ION IMPLANTATION OR BY CHEMICAL VAPOUR DEPOSITION, IN GENERAL
- C23C8/00—Solid 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
- C23C8/02—Pretreatment of the material to be coated
Definitions
- the invention relates to a method for carburizing a thermoformed article or a stamped and bent article made of austenitic stainless steel with a wall thickness which is at least partially suitable for such articles.
- customary low wall thicknesses are below 2000 ⁇ m.
- Such stainless steel articles are made of very thin sheets by tensile or compression bending and sometimes take on very filigree structures.
- articles with varying or constant wall thickness can be produced, whereby they then have a wall thickness of less than 2000 ⁇ m, at least in regions or as a whole.
- filigree articles are used in a variety of fields of technology such. used as bearing covers in gearboxes, valve seats in ABS systems or as sample carriers for hazardous substances in high-precision measurements where they are exposed to extreme mechanical, thermal and chemical stresses.
- the demand for high hardness corrosion resistant materials is therefore correspondingly high.
- the US 6,461,448 shows a method for carburizing a steel article, wherein said steel article is treated in a Schmelzalkalibad.
- Such an aggressive type of treatment leads to filigree articles in the context of the invention due to the small wall thickness sometimes severe corrosion phenomena, which has a highly inhomogeneous edge layer result.
- liquid treatments in filigree articles due to incomplete surface wetting lead to unsatisfactory results.
- the EP 0 678 589 B1 discloses in this context a method of carburizing an austenitic metal.
- the metal is exposed to a fluorine-containing gas.
- Fluorine-containing gases are highly corrosive due to their reactivity and, as a result, aggressively affect the surface of the metal. While the resulting removal of surface is even desirable for articles with high wall thickness due to a corresponding material wealth, it can not be compensated for thin-walled thermoforming and stamping bending articles and leads to the irreversible destruction of the article.
- the gases used there due to their high toxicity, their high corrosiveness and their highly environmentally hazardous properties enormous demands on the reactor to be used, storage and work safety.
- the EP 1 553 204 A1 discloses a method of edge hardening an austenitic steel part.
- the method is characterized in that the steel part is heated in a first process step to a temperature between 200 ° C and 500 ° C for a time between 10 minutes and 3 hours.
- the heating takes place in an atmosphere consisting of between 0.5 to 20% by volume of a halogen gas or a halide gas and the balance of nitrogen, hydrogen or an inert gas to activate the steel surface.
- the surface of the steel part is nitrocarburized in a second process step. This is done within a temperature range of 430 ° C to 600 ° C for 20 minutes or more within a mixed atmosphere comprising ammonia for nitrification and carbon monoxide and / or methane for carburizing.
- D3 discloses a method for carburizing a steel part.
- the steel part is heated in a first process step to a temperature between 500 ° F and 600 ° F in a halogenated hydrogen atmosphere, preferably HCL or HF.
- a halogenated hydrogen atmosphere preferably HCL or HF.
- the activation with strong bases the coating with iron or a treatment in the cyanide melt bath can be used for the activation.
- the thus activated steel part is then initially heated to a temperature of 1125 ° C.
- Said initial carburizing temperature is cooled to 925 ° F in the course of the carburizing process.
- hydrocarbon gases such as methane, ethane and propane, oxygen-containing gases such as carbon monoxide and carbon dioxide or mixtures of these gases such as synthesis gases can be used as the carburizing gas.
- the EP 1 193 413 A1 discloses a method for carburizing an austenitic steel roller bearing.
- said roller bearing is activated at a temperature between 200 ° C and 400 ° C a fluorine-containing gas, preferably NF3 in the nitrogen.
- the activated rolling bearing is treated at a temperature between 460 ° C and 520 ° C with a carburizing gas.
- Said carburizing gas may consist of either RX gas or a gas containing an unsaturated hydrocarbon, preferably acetylene or ethylene.
- the EP 0 497 409 A2 discloses a method of edge hardening an austenitic steel part.
- the steel part is either at a temperature between 250 ° C and 400 ° C in a fluoride-containing gas atmosphere or at a temperature between 100 ° C. and heated at 250 ° C in a fluorine-containing atmosphere.
- the steel part activated in the first step would be heated in a second process step to a temperature of 530 ° C and treated in an atmosphere consisting of nitrogen and hydrogen over a period of 30 minutes.
- the activated steel part is then nitrocarborated in an ammonia-containing gas mixture at a temperature of 480 ° C to 700 ° C over a period of three to five hours.
- the ammonia-containing atmosphere may be formed in particular of ammonia and RX gas or ammonia, carbon dioxide and RX gas.
- thermoforming and stamping bending articles With the invention, a method with mild conditions is proposed in an advantageous manner, which are tailored to the specifics of thin-walled thermoforming and stamping bending articles.
- the article is introduced into an oven for carrying out the method. It has been shown that in particular oxygen and water residues interfere with the surface hardening. To exclude these disturbing factors, the article is heated to a temperature which is above the boiling point of water. Preference is given here to a temperature of 110 ° C to 140 ° C, more preferably 120 ° C.
- the oxygen-containing atmosphere in the furnace is replaced in accordance with the invention by a first gas mixture.
- the furnace therefore advantageously has gas inlets and gas outlets.
- the furnace may be provided to flood the furnace with an inert gas before the introduction of the first gas mixture.
- the oxygen displacement is accelerated in an advantageous manner and a potentially existing hazard potential, resulting from the contact of the oxygen-containing normal atmosphere with the first gas mixture is lowered.
- the inert gas it is preferable to use known chemically unreactive gases such as, in particular, nitrogen or argon.
- Stainless steels include, among others, chromium as an alloying constituent. Upon contact with atmospheric oxygen, a passivating and corrosion-resistant chromium (III) oxide layer is formed on the surface of the material.
- the first gas mixture has reducing properties in order to avoid further oxidation of the chromium.
- this gas mixture already initiated the depassivation of the surface.
- the first gas mixture consists of H2 and N2. It has been found that this gas mixture, in particular in conjunction with the mild temperature of the first process step, exerts a particularly mild and advantageous effect on the chromium oxide layer without adversely affecting the morphology of the surface of the filigree articles.
- the oxygen concentration is measured continuously or at intervals by means of a sensor.
- a control unit connected to the sensor checks the actual value here continuously or at intervals with a freely selectable desired value and releases the furnace in the case of an identity between the actual and desired value for a second method step.
- the inventive method is thereby greatly simplified in an advantageous manner and minimizes in this way possible user-side sources of error.
- a second method step in which the article is heated to the target temperature, the second temperature, for the carburization.
- the second temperature is chosen so that it is well below the recrystallization temperature of strongly cold-worked iron alloys (680 ° C). A possible change in the morphology of the surface is thereby effectively prevented, whereby the formation of a homogeneous surface layer is promoted.
- the second temperature is 450 ° C to 550 ° C and preferably 500 ° C.
- the heating phase serves in particular the careful and complete depassivation of the chromium oxide layer.
- the heating rate in a certain temperature range between 0.5 and 1 ° C / min, more preferably between 0.5 and 0.7 ° C / min and more preferably 0.5 ° C / min.
- the temperature range in which this low heating rate is selected is preferably 420 ° C to 550 ° C, more preferably 450 ° C to 500 ° C, and most preferably 480 ° C to 500 ° C.
- the first gas mixture is replaced by a second gas mixture in the second method step. It has been found that mild depassivation of the thin-walled deep-drawn parts takes place during the heating phase to the second temperature by a gas mixture consisting of H 2 , N 2 and a carbon-containing gas from an unsaturated hydrocarbon.
- a gas mixture consisting of H 2 , N 2 and a carbon-containing gas from an unsaturated hydrocarbon.
- the low heating rate may preferably be a particularly slow and therefore mild and easy to control Depassivation of the chromium oxide layer can be achieved.
- the article is treated with additives which selectively or completely dissolve the passive layer.
- additives which selectively or completely dissolve the passive layer.
- it means salt compounds and / or organic substances and acid generators, which are applied in solid or liquid form to the product or in the oven.
- the application is preferably carried out before the article is placed in the oven or during the second process step.
- solids and / or liquids are used which form acid reaction products in conjunction with the reaction gases, which would give a pH ⁇ 7 when introduced into water, as the application of the substances has proven particularly advantageous directly on or in the article surface , As a result, local depassivation processes, which initiate and promote uniform depassivation earlier, already occur at low temperatures.
- an unsaturated hydrocarbon in particular ethyne used.
- elemental nitrogen is used in the second gas mixture.
- the temperature is measured continuously or at intervals by means of a sensor.
- the control unit connected to the sensor checks the actual value here continuously or at intervals with a freely selectable setpoint value for the second temperature and releases the oven in the case of an identity between the actual and setpoint values for a third method step.
- the inventive method is thereby greatly simplified in an advantageous manner and minimizes in this way possible user-side sources of error.
- a third method step is provided in which the deep-drawn part is kept constant at the second temperature.
- the third step in this context serves to carburize the thin-walled deep-drawn part. It has been found that the second temperature advantageously allows a careful construction of the surface layer to be hardened. The diffusion of the carbon into the edge region of the deep-drawn part takes place slowly at these temperatures, is therefore easy to control and causes the formation of a homogeneous carbon-rich surface layer. Too high a temperature is to avoid in any case, as it comes to the formation of irregular layers and the formation of carbide particles due to the high diffusion rate and the high kinetic energy of the molecules involved.
- the second gas mixture is replaced by a third gas mixture, which is particularly suitable for gentle carburizing under mild conditions.
- a gas mixture which is composed of a hydrogen-containing gas, a nitrogen-containing gas and a carbon-containing gas. It is further provided according to the invention to add a further carbon-containing component to this gas mixture, whereby the formation of a homogeneous carbon-rich surface layer is promoted by the two different carbon components in a synergetic manner.
- the carbon-containing component of the second gas mixture according to the invention an unsaturated hydrocarbon, in particular ethyne, is used .
- the second gas mixture contains elemental nitrogen.
- the individual concentrations of the gas components are measured continuously or at intervals by means of respective sensors.
- the control unit connected to the sensors checks the respective actual values here continuously or at intervals with freely selectable desired values for the respective concentration of the gas component and compensates for changes within a fault tolerance continuously or at intervals.
- the process control is advantageously simplified and allows the provision of constant process conditions, which is for the construction of a homogeneous carbon-rich surface layer of crucial importance.
- the layer thickness of the carbon-rich surface layer can be adjusted over the gassing time.
- a period of 2 to 10 hours is required to generate a 10-40 microns thick edge layer.
- control unit which has a corresponding device for time recording, releases the furnace for the fourth method step after the expiration of a freely selectable carburizing time.
- the inventive method is thereby greatly simplified in an advantageous manner and minimizes in this way possible user-side sources of error.
- a fourth method step is provided in which the deep-drawn part is cooled to a third temperature. It is provided here, the deep-drawn part to a temperature of 50 ° C to 80 ° C and more preferably cool to 60 ° C.
- the choice of atmosphere in the cooled is crucial for the formation of a homogeneous surface layer. It is therefore provided according to the invention to replace the third gas mixture by a fourth gas mixture.
- the fourth gas mixture consists of a hydrogen-containing gas and a nitrogen-containing gas. It is envisaged here that the fourth gas mixture is formed from H2 and N2.
- the composition of the fourth gas mixture advantageously from 5% to 25% H2 and 75% to 95% N2, more preferably 5% to 10% H2 and 90% to 95% N2 and more preferably 5% H2 and 95% N2. It has been found that the cooling according to the invention of the thin-walled deep-drawn part effectively prevents the escape of the carbon from the hardened edge layer.
- the invention relates to an edge-hardened thermoforming article with very small wall thicknesses.
- the deep-drawing article produced by the method according to the invention has a soft, elastic core with a hardness of 350 to 400 HV1 and a hard carbon-rich surface layer.
- the edge layer is free of defects and / or particles, circumferentially completely closed and has a substantially planar surface.
- the thin-walled thermoforming article produced by the method according to the invention has mechanical properties of unprecedented quality.
- thermoforming article produced by means of the method according to the invention has in its edge region a carbon-rich layer with a hardness of 700 to 1000 HV0.01 and with a layer thickness of 10 to 40 ⁇ m.
- the corrosion and abrasion resistance of the thermoforming article is better than that of the starting material.
- the former in particular, is surprising in that carburizing generally worsens the corrosion properties of a steel product.
Description
Die Erfindung betrifft ein Verfahren zur Aufkohlung eines Tiefziehartikels oder eines Stanzbiegeartikels aus austenitischem nichtrostendem Edelstahl mit einer wenigstens bereichsweise für solche Artikel üblichen geringen Wandstärke.The invention relates to a method for carburizing a thermoformed article or a stamped and bent article made of austenitic stainless steel with a wall thickness which is at least partially suitable for such articles.
Bei Tiefziehartikeln und Stanzbiegeartikeln im Sinne der Erfindung liegen übliche geringe Wandstärken unterhalb von 2000 µm. Solche Edelstahlartikel werden aus sehr dünnen Blechen durch Zugdruckumformen oder Stanzbiegen hergestellt und nehmen mitunter sehr filigrane Strukturen an. Je nach verwendetem Verfahren können Artikel mit variierender oder konstanter Wandstärke hergestellt werden, wodurch diese dann wenigstens bereichsweise oder in Gänze eine Wandstärke von weniger als 2000 µm aufweisen.For deep-drawing articles and stamped-bent articles in the context of the invention, customary low wall thicknesses are below 2000 μm. Such stainless steel articles are made of very thin sheets by tensile or compression bending and sometimes take on very filigree structures. Depending on the method used, articles with varying or constant wall thickness can be produced, whereby they then have a wall thickness of less than 2000 μm, at least in regions or as a whole.
Diese filigranen Artikel werden in den unterschiedlichsten Bereichen der Technik wie z.B. als Lagerabdeckung in Getrieben, Ventilsitze in ABS-Systemen oder als Probenträger für Gefahrstoffe bei Hochpräzisionsmessungen eingesetzt und sind dort extremen mechanischen, thermischen und chemischen Belastungen ausgesetzt. Der Bedarf an korrosionsbeständigen Materialien mit hoher Härte ist daher dementsprechend hoch.These filigree articles are used in a variety of fields of technology such. used as bearing covers in gearboxes, valve seats in ABS systems or as sample carriers for hazardous substances in high-precision measurements where they are exposed to extreme mechanical, thermal and chemical stresses. The demand for high hardness corrosion resistant materials is therefore correspondingly high.
Die Qualität solcher gehärteten Artikel, insbesondere bei solchen Teilen, die ein hohes Verhältnis von Länge zu Durchmesser besitzen (Aspektverhältnis) und/oder die Stickstoff enthalten, lässt allerdings bislang sowohl hinsichtlich der mechanischen Beständigkeit, der Schweißeignung als auch der Korrosionsbeständigkeit zu wünschen übrig. Abhilfe liefern hier Verfahren auf Kohlenstoffbasis. Diese eignen sich jedoch nur eingeschränkt für schöpfende Tiefzieh- oder Stanzbiegeartikel. Es entstehen durch das Randschichthärten mit Kohlenstoff Verschmutzungen, die sich gemäß dem aktuellen industriellen Standard bei schöpfenden Teilen nicht mehr wirtschaftlich entfernen lassen. Wendet man aus dem Stand der Technik bekannte und etablierte Verfahren zur Randschichthärtung auf Artikel mit sehr dünner Wandstärke und hohem Aspektverhältnis an, so lassen sich keine industriell reproduzierbaren und den Qualitätsansprüchen genügende Randschichten herstellen.However, the quality of such cured articles, especially those parts having a high aspect ratio (aspect ratio) and / or containing nitrogen, has been poor both in mechanical resistance, weldability and corrosion resistance. Provide remedy here carbon-based process. However, these are only partially suitable for scooping deep-drawn or stamped-bent articles. It is caused by the surface hardening with carbon contaminants that can no longer be economically removed according to the current industrial standard in scooping parts. If one uses known and established methods for surface hardening on articles having a very thin wall thickness and a high aspect ratio, it is not possible to produce edge-layers that are industrially reproducible and meet the quality requirements.
Der Grund für diese Ergebnisse ist vor allem in den zum Teil extremen Behandlungsbedingungen der etablierten Verfahren zu suchen.The reason for these results is to be found above all in the sometimes extreme treatment conditions of the established methods.
So zeigt zum Beispiel die
Die
Die
Die
Die D3 offenbart ein Verfahren zur Aufkohlung eines Stahlteils. Zur initialen Aktivierung der Stahloberfläche wird das Stahlteil in einem ersten Verfahrensschritt auf eine Temperatur zwischen 500°F und 600°F in einer halogenen Wasserstoffatmosphäre, vorzugsweise HCL oder HF, erhitzt. Anstelle besagter Gasbehandlung kann zur Aktivierung auch die Kontaktierung mit starken Basen, die Beschichtung mit Eisen oder eine Behandlung im Cyanidschmelzbad genutzt werden. Zur Aufkohlung wird das derart aktivierte Stahlteil dann initial auf eine Temperatur von 1125°C erhitzt. Besagte initiale Aufkohlungstemperatur wird im Laufe des Aufkohlungsprozesses auf 925°F abgekühlt. Als Aufkohlungsgas können insbesondere Kohlenwasserstoffgase wie Methan, Ethan und Propan, sauerstoffhaltige Gase wie Kohlenstoffmonoxid und Kohlenstoffdioxid oder Mischungen dieser Gase wie Synthesegase eingesetzt werden.D3 discloses a method for carburizing a steel part. For the initial activation of the steel surface, the steel part is heated in a first process step to a temperature between 500 ° F and 600 ° F in a halogenated hydrogen atmosphere, preferably HCL or HF. Instead of said gas treatment, the activation with strong bases, the coating with iron or a treatment in the cyanide melt bath can be used for the activation. For carburization, the thus activated steel part is then initially heated to a temperature of 1125 ° C. Said initial carburizing temperature is cooled to 925 ° F in the course of the carburizing process. In particular, hydrocarbon gases such as methane, ethane and propane, oxygen-containing gases such as carbon monoxide and carbon dioxide or mixtures of these gases such as synthesis gases can be used as the carburizing gas.
Die
Die
Allen vorgenannten Verfahren ist gemein, dass sie zur Depassivierung bzw. Aktivierung der Randschicht des Stahlteils auf aggressive Verfahrensschritte aufweisend halogenhaltige, insbesondere fluorhaltige Gase setzen. Wie bereits ausgeführt wurde, sind diese Verfahrensbedingungen allerdings für Tiefziehteile mit geringen Wandstärken unterhalb von 2000 µm nicht geeignet.All of the above-mentioned methods have in common that they use for depassivation or activation of the surface layer of the steel part to aggressive process steps containing halogen-containing, in particular fluorine-containing gases. As already stated, however, these process conditions are not suitable for deep-drawn parts with small wall thicknesses below 2000 μm.
Es ist daher die Aufgabe der Erfindung ein wirksames Verfahren zur Aufkohlung von dünnwandigen tiefgezogenen oder stanzgebogenen Edelstahlartikeln bereitzustellen.It is therefore the object of the invention to provide an effective method for carburizing thin-walled deep-drawn or stamped bent stainless steel articles.
Zur Lösung dieser Aufgabe wird eine Erfindung mit den Merkmalen gemäß Anspruch 1 vorgeschlagen. Weitere Vorteile und Merkmale ergeben sich aus den Unteransprüchen.To solve this problem, an invention with the features of claim 1 is proposed. Further advantages and features emerge from the subclaims.
Mit der Erfindung wird in vorteilhafterweise ein Verfahren mit milden Bedingungen vorgeschlagen, welche auf die Besonderheiten von dünnwandigen Tiefzieh- und Stanzbiegeartikeln abgestimmt sind.With the invention, a method with mild conditions is proposed in an advantageous manner, which are tailored to the specifics of thin-walled thermoforming and stamping bending articles.
In erfindungsgemäßer Weise wird der Artikel zur Durchführung des Verfahrens in einen Ofen eingebracht. Es hat sich gezeigt, dass insbesondere Sauerstoff- und Wasserreste die Randschichthärtung stören. Zum Ausschluss dieser Störfaktoren wird der Artikel auf eine Temperatur erwärmt, die Oberhalb des Siedepunktes von Wasser liegt. Bevorzugt ist hierbei eine Temperatur von 110 °C bis 140 °C, besonders bevorzugt 120 °C.In accordance with the invention, the article is introduced into an oven for carrying out the method. It has been shown that in particular oxygen and water residues interfere with the surface hardening. To exclude these disturbing factors, the article is heated to a temperature which is above the boiling point of water. Preference is given here to a temperature of 110 ° C to 140 ° C, more preferably 120 ° C.
Darüber hinaus wird die sich im Ofen befindliche sauerstoffhaltige Atmosphäre in erfindungsgemäßer Weise durch ein erstes Gasgemisch ersetzt. Der Ofen verfügt daher vorteilhafterweise über Gaseinlässe und Gasauslässe.In addition, the oxygen-containing atmosphere in the furnace is replaced in accordance with the invention by a first gas mixture. The furnace therefore advantageously has gas inlets and gas outlets.
Gemäß einer bevorzugten Verfahrensführung kann es vorgesehen sein, den Ofen vor der Einleitung des ersten Gasgemisches mit einem Inertgas zu fluten. Die Sauerstoffverdrängung wird hierbei in vorteilhafter Weise beschleunigt und ein möglicherweise bestehendes Gefahrenpotential, resultierend aus dem Kontakt der sauerstoffhaltigen Normalatmosphäre mit dem ersten Gasgemisch gesenkt. Als Inertgas werden bevorzugterweise bekannte chemisch unreaktive Gase wie insbesondere Stickstoff oder Argon verwendet.According to a preferred process control, it may be provided to flood the furnace with an inert gas before the introduction of the first gas mixture. In this case, the oxygen displacement is accelerated in an advantageous manner and a potentially existing hazard potential, resulting from the contact of the oxygen-containing normal atmosphere with the first gas mixture is lowered. As the inert gas, it is preferable to use known chemically unreactive gases such as, in particular, nitrogen or argon.
Nichtrostende Edelstähle beinhalten unter anderem Chrom als Legierungsbestandteil. An der Materialoberfläche bildet sich durch den Kontakt mit Luftsauerstoff eine passivierende und korrosionsbeständige Chrom-(III)-Oxidschicht aus.Stainless steels include, among others, chromium as an alloying constituent. Upon contact with atmospheric oxygen, a passivating and corrosion-resistant chromium (III) oxide layer is formed on the surface of the material.
Bei der Aufkohlung ist es von enormer Bedeutung, diese passivierende Chrom-Oxidschicht zu entfernen bzw. zu depassivieren, um eine homogene Diffusion des Kohlenstoffs in den Randbereich des Edelstahls zu ermöglichen. Ist dies durch mangelnde Depassivierung nicht gewährleistet, ist die Eindiffusion in Bereichen mit intakter Chrom-Oxidschicht gehemmt und es kommt in der Konsequenz zu einer inhomogenen Härteverteilung der resultierenden Randschicht. Darüber hinaus fördert eine mangelnde Depassivierung in Bereichen mit intakter Chrom-Oxidschicht die Ausbildung von Defektstellen im Randbereich. Diese Defektstellen führen in der Konsequenz zu einer unerwünschten, verminderten Korrosionsbeständigkeit des Stahls.During carburization, it is of utmost importance to remove or depassivate this passivating chromium oxide layer in order to allow homogeneous diffusion of the carbon into the edge area of the stainless steel. If this is not ensured by a lack of depassivation, the diffusion into regions with an intact chromium oxide layer is inhibited and, as a consequence, an inhomogeneous hardness distribution of the resulting surface layer occurs. In addition, a lack of depassivation in areas with intact chromium oxide layer promotes the formation of defects in the edge area. As a consequence, these defects lead to an undesirable, reduced corrosion resistance of the steel.
Das erste Gasgemisch hat daher gemäß einem Merkmal der Erfindung reduzierende Eigenschaften, um eine weitere Oxidation des Chroms zu vermeiden. Darüber hinaus wird mit dieser Gasmischung bereits die Depassivierung der Oberfläche eingeleitet. Gemäß einem weiteren Merkmal der Erfindung besteht das erste Gasgemisch aus H2 und N2. Es hat sich gezeigt, dass dieses Gasgemisch insbesondere in Verbindung mit der milden Temperatur des ersten Verfahrensschrittes eine besonders milde und vorteilhafte Wirkung auf die Chromoxidschicht ausübt, ohne die Morphologie der Oberfläche der filigranen Artikel nachteilig zu verändern.Thus, according to one feature of the invention, the first gas mixture has reducing properties in order to avoid further oxidation of the chromium. In addition, this gas mixture already initiated the depassivation of the surface. According to a further feature of the invention, the first gas mixture consists of H2 and N2. It has been found that this gas mixture, in particular in conjunction with the mild temperature of the first process step, exerts a particularly mild and advantageous effect on the chromium oxide layer without adversely affecting the morphology of the surface of the filigree articles.
Gemäß einem bevorzugten Merkmal der Erfindung wird die Sauerstoffkonzentration mittels eines Sensors stetig oder intervallweise gemessen. Eine mit dem Sensor verbundene Steuerungseinheit überprüft den Ist-Wert hierbei stetig oder intervallweise mit einem frei wählbaren Soll-Wert und gibt den Ofen im Falle einer Identität zwischen Ist- und Soll-Wert für einen zweiten Verfahrensschritt frei. Das erfindungsgemäße Verfahren ist hierdurch in vorteilhafterweise stark vereinfacht und minimiert auf diese Weise mögliche benutzerseitige Fehlerquellen.According to a preferred feature of the invention, the oxygen concentration is measured continuously or at intervals by means of a sensor. A control unit connected to the sensor checks the actual value here continuously or at intervals with a freely selectable desired value and releases the furnace in the case of an identity between the actual and desired value for a second method step. The inventive method is thereby greatly simplified in an advantageous manner and minimizes in this way possible user-side sources of error.
Erfindungsgemäß ist ein zweiter Verfahrensschritt vorgesehen, in welchem der Artikel auf die Zieltemperatur, die zweite Temperatur, für die Aufkohlung erwärmt wird. Die zweite Temperatur ist so gewählt, dass diese deutlich unterhalb der Rekristallisationstemperatur von stark kaltverformten Eisenlegierungen (680 °C) liegt. Eine mögliche Änderung der Morphologie der Oberfläche ist hierbei wirkungsvoll unterbunden, wodurch die Ausbildung einer homogenen Randschicht gefördert wird. Erfindungsgemäß liegt die zweite Temperatur bei 450 °C bis 550 °C und bevorzugt bei 500 °C. Die Aufheizphase dient hierbei insbesondere der behutsamen und vollständigen Depassivierung der Chromoxidschicht.According to the invention, a second method step is provided, in which the article is heated to the target temperature, the second temperature, for the carburization. The second temperature is chosen so that it is well below the recrystallization temperature of strongly cold-worked iron alloys (680 ° C). A possible change in the morphology of the surface is thereby effectively prevented, whereby the formation of a homogeneous surface layer is promoted. According to the invention, the second temperature is 450 ° C to 550 ° C and preferably 500 ° C. The heating phase serves in particular the careful and complete depassivation of the chromium oxide layer.
Es ist vorteilhaft, die Aufheizrate wenigstens in bestimmten Temperaturbereichen möglichst niedrig zu wählen, um eine gleichmäßige Depassivierung zur gewährleisten. Der Anmelder hat in diesem Zusammenhang herausgefunden, dass die Qualität der resultierenden Randschicht von dünnwandigen Tiefziehteilen in besonderer Weise unter einer hohen Aufheizrate leidet. Bevorzugterweise beträgt die Aufheizrate in einem bestimmten Temperaturbereich zwischen 0,5 und 1 °C/min, weiter bevorzugt zwischen 0,5 und 0,7 °C/min und besonders bevorzugt 0,5 °C/min. Der Temperaturbereich in dem diese niedrige Aufheizrate gewählt wird, beträgt bevorzugterweise 420 °C bis 550 °C, weiter bevorzugt 450 °C bis 500 °C und besonders bevorzugt 480 °C bis 500 °C.It is advantageous to select the heating rate as low as possible, at least in certain temperature ranges, in order to ensure uniform depassivation. The Applicant has found in this context that the quality of the resulting edge layer of thin-walled deep-drawn parts suffers in a special way under a high heating rate. Preferably, the heating rate in a certain temperature range between 0.5 and 1 ° C / min, more preferably between 0.5 and 0.7 ° C / min and more preferably 0.5 ° C / min. The temperature range in which this low heating rate is selected is preferably 420 ° C to 550 ° C, more preferably 450 ° C to 500 ° C, and most preferably 480 ° C to 500 ° C.
Gemäß einem Merkmal der Erfindung wird das erste Gasgemisch im zweiten Verfahrensschritt durch ein zweites Gasgemisch ersetzt. Es hat sich hierbei herausgestellt, dass eine milde Depassivierung der dünnwandigen Tiefziehteile während der Aufheizphase auf die zweite Temperatur durch ein Gasgemisch bestehend aus H2, N2 und einem kohlenstoffhaltigen Gas aus einem ungesättigten Kohlenwasserstoff erfolgt. Insbesondere in Verbindung mit der niedrigen Aufheizrate kann bevorzugterweise eine besonders langsame und daher milde und gut steuerbare Depassivierung der Chromoxidschicht erreicht werden.According to a feature of the invention, the first gas mixture is replaced by a second gas mixture in the second method step. It has been found that mild depassivation of the thin-walled deep-drawn parts takes place during the heating phase to the second temperature by a gas mixture consisting of H 2 , N 2 and a carbon-containing gas from an unsaturated hydrocarbon. In particular, in connection with the low heating rate may preferably be a particularly slow and therefore mild and easy to control Depassivation of the chromium oxide layer can be achieved.
Gemäß einem bevorzugten Merkmal der Erfindung wird der Artikel mit Zusätzen behandelt, die die Passivschicht selektiv oder in Gänze auflösen. Insbesondere sind damit Salzverbindungen und/oder organische Stoffe und Säurebildner gemeint, die in fester oder flüssiger Form auf der Ware oder im Ofen appliziert werden. Die Applikation erfolgt hierbei bevorzugt vor der Verbringung des Artikels in den Ofen oder während des zweiten Verfahrensschritts. Hierfür werden Feststoff und/oder Flüssigkeiten verwendet, die in Verbindung mit den Reaktionsgasen saure Reaktionsprodukte bilden, die bei Einleitung in Wasser einen pH-Wert < 7 ergeben würden, als besonders vorteilhaft hat sich dabei die Applizierung der Stoffe direkt auf oder in der Artikeloberfläche erwiesen. Hierdurch entstehen bereits bei niedrigen Temperaturen lokale Depassivierungsvorgänge, die eine gleichmäßige Depassivierung früher einleiten und fördern.According to a preferred feature of the invention, the article is treated with additives which selectively or completely dissolve the passive layer. In particular, it means salt compounds and / or organic substances and acid generators, which are applied in solid or liquid form to the product or in the oven. The application is preferably carried out before the article is placed in the oven or during the second process step. For this purpose, solids and / or liquids are used which form acid reaction products in conjunction with the reaction gases, which would give a pH <7 when introduced into water, as the application of the substances has proven particularly advantageous directly on or in the article surface , As a result, local depassivation processes, which initiate and promote uniform depassivation earlier, already occur at low temperatures.
Als kohlenstoffhaltige Komponente wird dem zweiten Gasgemisch erfindungsgemäß ein ungesättigter Kohlenwasserstoff, wie insbesondere Ethin, eingesetzt.As the carbon-containing component of the second gas mixture according to the invention, an unsaturated hydrocarbon, in particular ethyne used.
Erfindungsgemäß wird dem zweiten Gasgemisch elementarer Stickstoff eingesetzt.According to the invention, elemental nitrogen is used in the second gas mixture.
Es hat sich darüber hinaus herausgestellt, dass der Einsatz von elementarem Wasserstoff als Bestandteil des zweiten Gasgemisches, insbesondere in Verbindung mit den Depassivierungszusätzen, zur Ausbildung besonders homogener Randschichten führt.In addition, it has been found that the use of elemental hydrogen as a constituent of the second gas mixture, in particular in conjunction with the depassivation additives, leads to the formation of particularly homogeneous boundary layers.
Gemäß einem bevorzugten Merkmal der Erfindung wird die Temperatur mittels eines Sensors stetig oder intervallweise gemessen. Die mit dem Sensor verbundene Steuerungseinheit überprüft den Ist-Wert hierbei stetig oder intervallweise mit einem frei wählbaren Soll-Wert für die zweite Temperatur und gibt den Ofen im Falle einer Identität zwischen Ist- und Soll-Wert für einen dritten Verfahrensschritt frei. Das erfindungsgemäße Verfahren ist hierdurch in vorteilhafterweise stark vereinfacht und minimiert auf diese Weise mögliche benutzerseitige Fehlerquellen.According to a preferred feature of the invention, the temperature is measured continuously or at intervals by means of a sensor. The control unit connected to the sensor checks the actual value here continuously or at intervals with a freely selectable setpoint value for the second temperature and releases the oven in the case of an identity between the actual and setpoint values for a third method step. The inventive method is thereby greatly simplified in an advantageous manner and minimizes in this way possible user-side sources of error.
Erfindungsgemäß ist ein dritter Verfahrensschritt vorgesehen, bei dem das Tiefziehteil konstant auf der zweiten Temperatur gehalten wird. Der dritte Verfahrensschritt dient in diesem Zusammenhang der Aufkohlung des dünnwandigen Tiefziehteils. Es hat sich gezeigt, dass die zweite Temperatur in vorteilhafterweise einen behutsamen Aufbau der zu härtenden Randschicht ermöglicht. Die Diffusion des Kohlenstoffes in den Randbereich des Tiefziehteils erfolgt bei diesen Temperaturen langsam, ist infolgedessen gut steuerbar und bewirkt den Aufbau einer homogenen kohlenstoffreichen Randschicht. Eine zu hohe Temperatur ist in jedem Fall zu vermeiden, da es infolge der hohen Diffusionsgeschwindigkeit und der hohen kinetischen Energie der beteiligten Moleküle zur Ausbildung unregelmäßiger Schichten und zur Bildung von Carbid-Partikeln kommt.According to the invention, a third method step is provided in which the deep-drawn part is kept constant at the second temperature. The third step in this context serves to carburize the thin-walled deep-drawn part. It has been found that the second temperature advantageously allows a careful construction of the surface layer to be hardened. The diffusion of the carbon into the edge region of the deep-drawn part takes place slowly at these temperatures, is therefore easy to control and causes the formation of a homogeneous carbon-rich surface layer. Too high a temperature is to avoid in any case, as it comes to the formation of irregular layers and the formation of carbide particles due to the high diffusion rate and the high kinetic energy of the molecules involved.
In erfindungsgemäße Weise wird das zweite Gasgemisch durch ein drittes Gasgemisch ersetzt, welches sich insbesondere für eine behutsame Aufkohlung unter milden Bedingungen eignet. Als besonders Vorteilhaft hat sich in diesem Zusammenhang die Verwendung eines Gasgemisches bewährt, welches aus einem wasserstoffhaltigen Gas, einem stickstoffhaltigen Gas sowie einem kohlenstoffhaltigen Gas zusammengesetzt ist. Es ist weiterhin erfindungsgemäß vorgesehen, dieser Gasmischung noch eine weitere kohlenstoffhaltige Komponente beizufügen, wodurch die Ausbildung einer homogenen kohlenstoffreichen Randschicht durch die beiden verschiedenen Kohlenstoffkomponenten in synergetischer Weise gefördert wird.Als kohlenstoffhaltige Komponente des zweiten Gasgemisches wird erfindungsgemäß ein ungesättigter Kohlenwasserstoff, wie insbesondere Ethin, eingesetzt. Erfindungsgemäß enthält das zweite Gasgemisch elementaren Stickstoff.In accordance with the invention, the second gas mixture is replaced by a third gas mixture, which is particularly suitable for gentle carburizing under mild conditions. Particularly advantageous in this context, the use of a gas mixture has proven, which is composed of a hydrogen-containing gas, a nitrogen-containing gas and a carbon-containing gas. It is further provided according to the invention to add a further carbon-containing component to this gas mixture, whereby the formation of a homogeneous carbon-rich surface layer is promoted by the two different carbon components in a synergetic manner. As the carbon-containing component of the second gas mixture according to the invention an unsaturated hydrocarbon, in particular ethyne, is used , According to the invention, the second gas mixture contains elemental nitrogen.
Gemäß einem bevorzugten Merkmal der Erfindung werden die einzelnen Konzentrationen der Gaskomponenten mittels jeweiliger Sensoren stetig oder intervallweise gemessen. Die mit den Sensoren verbundene Steuerungseinheit überprüft die jeweiligen Ist-Werte hierbei stetig oder intervallweise mit frei wählbaren Soll-Werten für die jeweilige Konzentration der Gaskomponente und gleicht Änderungen innerhalb einer Fehlertoleranz stetig oder intervallweise aus. Auf diese Weise ist die Verfahrensführung in vorteilhafter Weise vereinfacht und erlaubt die Bereitstellung konstanter Verfahrensbedingungen, was für den Aufbau einer homogenen kohlenstoffreichen Randschicht von entscheidender Bedeutung ist.According to a preferred feature of the invention, the individual concentrations of the gas components are measured continuously or at intervals by means of respective sensors. The control unit connected to the sensors checks the respective actual values here continuously or at intervals with freely selectable desired values for the respective concentration of the gas component and compensates for changes within a fault tolerance continuously or at intervals. In this way, the process control is advantageously simplified and allows the provision of constant process conditions, which is for the construction of a homogeneous carbon-rich surface layer of crucial importance.
Die Schichtdicke der kohlenstoffreichen Randschicht ist hierbei über die Begasungsdauer einstellbar. In vorteilhafter Weise wird zur Generierung einer 10-40 µm dicken Randschicht ein Zeitraum von 2 bis 10 Stunden benötigt.The layer thickness of the carbon-rich surface layer can be adjusted over the gassing time. Advantageously, a period of 2 to 10 hours is required to generate a 10-40 microns thick edge layer.
Gemäß einem bevorzugten Merkmal der Erfindung gibt die Steuereinheit, welche zur Zeiterfassung über eine entsprechende Vorrichtung verfügt, nach Ablauf einer frei wählbaren Aufkohlungszeit den Ofen für den vierten Verfahrensschritt frei. Das erfindungsgemäße Verfahren ist hierdurch in vorteilhafterweise stark vereinfacht und minimiert auf diese Weise mögliche benutzerseitige Fehlerquellen.According to a preferred feature of the invention, the control unit, which has a corresponding device for time recording, releases the furnace for the fourth method step after the expiration of a freely selectable carburizing time. The inventive method is thereby greatly simplified in an advantageous manner and minimizes in this way possible user-side sources of error.
Erfindungsgemäß ist ein vierter Verfahrensschritt vorgesehen, bei dem das Tiefziehteil auf eine dritte Temperatur abgekühlt wird. Es ist hierbei vorgesehen, das Tiefziehteil auf eine Temperatur von 50 °C bis 80 °C und besonders bevorzugt 60 °C abzukühlen.According to the invention, a fourth method step is provided in which the deep-drawn part is cooled to a third temperature. It is provided here, the deep-drawn part to a temperature of 50 ° C to 80 ° C and more preferably cool to 60 ° C.
Es hat sich hierbei herausgestellt, dass die Wahl der Atmosphäre in der abgekühlt wird für die Ausbildung einer homogenen Randschicht von entscheidender Bedeutung ist. Es ist daher gemäß der Erfindung vorgesehen, das dritte Gasgemisch durch ein viertes Gasgemisch zu ersetzen. Insbesondere die Wahl eines leicht reduzierend wirkenden Gasgemisches wird als vorteilhaft angesehen. Gemäß der Erfindung besteht das vierte Gasgemisch aus einem wasserstoffhaltigen Gas und einem stickstoffhaltigen Gas. Vorgesehen ist hierbei, dass das vierte Gasgemisch aus H2 und N2 gebildet ist. Um ein schwaches Reduktionspotential zu gewährleisten, besteht die Zusammensetzung des vierten Gasgemisches vorteilhafterweise aus 5 % bis 25 % H2 und 75 % bis 95 % N2, weiter bevorzugt 5 % bis 10 % H2 und 90 % bis 95 % N2 und besonders bevorzugt 5 % H2 und 95 % N2. Es hat sich gezeigt, dass das erfindungsgemäße Abkühlen des dünnwandigen Tiefziehteils ein Entweichen des Kohlenstoffs aus der gehärteten Randschicht wirkungsvoll unterbindet.It has been found that the choice of atmosphere in the cooled is crucial for the formation of a homogeneous surface layer. It is therefore provided according to the invention to replace the third gas mixture by a fourth gas mixture. In particular, the choice of a slightly reducing gas mixture is considered advantageous. According to the invention, the fourth gas mixture consists of a hydrogen-containing gas and a nitrogen-containing gas. It is envisaged here that the fourth gas mixture is formed from H2 and N2. To ensure a weak reduction potential, the composition of the fourth gas mixture advantageously from 5% to 25% H2 and 75% to 95% N2, more preferably 5% to 10% H2 and 90% to 95% N2 and more preferably 5% H2 and 95% N2. It has been found that the cooling according to the invention of the thin-walled deep-drawn part effectively prevents the escape of the carbon from the hardened edge layer.
Des Weiteren betrifft die Erfindung einen randgehärteten Tiefziehartikel mit sehr geringen Wandstärken.Furthermore, the invention relates to an edge-hardened thermoforming article with very small wall thicknesses.
Mittels des erfindungsgemäßen Verfahrens ist es nun erstmals möglich, dünnwandige Edelstahlartikel, insbesondere Tiefziehartikel, mit einem hohen Längen-Durchmesserverhältnis mit dünner Wandstärke industriell reproduzierbar und in exzellenter Qualität zu härten.By means of the method according to the invention, it is now possible for the first time to harden industrially reproducible thin-walled stainless steel articles, in particular deep-drawn articles, with a high length-diameter ratio with a thin wall thickness and to cure them in excellent quality.
Der mittels des erfindungsgemäßen Verfahrens hergestellte Tiefziehartikel weist einen weichen, elastischen Kern mit einer Härte von 350 bis 400 HV1 und eine harte kohlenstoffreiche Randschicht auf.The deep-drawing article produced by the method according to the invention has a soft, elastic core with a hardness of 350 to 400 HV1 and a hard carbon-rich surface layer.
Gemäß einem Merkmal ist die Randschicht frei von Defektstellen und/oder Partikeln, umlaufend vollständig geschlossen und weist eine im Wesentlichen plan ausgebildete Oberfläche auf.According to one feature, the edge layer is free of defects and / or particles, circumferentially completely closed and has a substantially planar surface.
Der mittels des erfindungsgemäßen Verfahrens hergestellte dünnwandige Tiefziehartikel weist infolgedessen mechanische Eigenschaften bisher unerreichter Qualität auf.As a result, the thin-walled thermoforming article produced by the method according to the invention has mechanical properties of unprecedented quality.
So weist der mittels des erfindungsgemäßen Verfahrens hergestellte Tiefziehartikel in seinem Randbereich eine kohlenstoffreiche Schicht mit einer Härte von 700 bis 1000 HV0.01 und mit einer Schichtdtcke von 10 bis 40 µm auf.Thus, the thermoforming article produced by means of the method according to the invention has in its edge region a carbon-rich layer with a hardness of 700 to 1000 HV0.01 and with a layer thickness of 10 to 40 μm.
Gemäß einem weiteren Merkmal sind die Körrosions- und die Abriebbeständigkeit des Tiefziehartikels besser als die des Ausgangsproduktes. Insbesondere Ersteres ist insofern überraschend, da eine Aufkohlung die Korrosionseigenschaften eines Stahlproduktes in der Regel verschlechtert.According to another feature, the corrosion and abrasion resistance of the thermoforming article is better than that of the starting material. The former, in particular, is surprising in that carburizing generally worsens the corrosion properties of a steel product.
Claims (5)
- A thin wall carburizing process of a deep-drawn article or a bent pressed article made of austenitic rustproof stainless steel,in which the article which comprises a wall thickness of less than 2000 µm at least in some portions, is introduced into an oven in a first process step and heated up to a first temperature comprised between 100°C and 140°C,wherein an oxygen-bearing atmosphere which is present in the oven will be replaced by a first gas mixture, wherein the first gas mixture consists of N2 and H2,and in which the article will be heated up to a second temperature comprised between 450°C and 550°C in a second process step,wherein the first gas mixture will be replaced by a second gas mixture, wherein the second gas mixture consists of H2, N2 and a carbonic gas from an unsaturated hydrocarbon,and in which the article will be held on the second temperature in a third process step,wherein the second gas mixture will be replaced by a third gas mixture, wherein the third gas mixture consists of a hydrogen-bearing gas, nitrogen-bearing gas, a first carbonic gas and a second carbonic gas, wherein the second carbonic gas is a gas different from the first carbonic gas,and in which the article will be cooled down to a third temperature comprised between 50°C and 80°C in a fourth process step,wherein the third gas mixture will be replaced by a fourth gas mixture, wherein the fourth gas mixture consists of N2 and H2.
- A method according to claim 1, characterized in that the residual oxygen content will be measured by means of a sensor during the first process step, and that if a freely selectable residual oxygen value is achieved, the second process step will be initiated.
- A method according to one of the preceding claims 1 or 2, characterized in that if the second temperature is achieved, the third process step will be automatically initiated.
- A method according to one of the preceding claims, characterized in that the article will be treated with at least one depassivating salt compound.
- A method according to one of the preceding claims, characterized in that the fourth process step will be initiated after a freely selectable duration of treatment has come to an end.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
PL13196076T PL2881492T3 (en) | 2013-12-06 | 2013-12-06 | Method for carburising metal deep drawn article or a bent pressed article made of austenitic stainless steel |
EP13196076.7A EP2881492B1 (en) | 2013-12-06 | 2013-12-06 | Method for carburising metal deep drawn article or a bent pressed article made of austenitic stainless steel |
US14/557,574 US9738962B2 (en) | 2013-12-06 | 2014-12-02 | Method for the carburization of a deep-drawn part or a stamped-bent part made of austenitic rustproof stainless steel |
CN201410737053.1A CN104451534B (en) | 2013-12-06 | 2014-12-04 | For the method to the deep-draw part made of austenite anti-rust stainless steel or punching press bending member carburizing |
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EP13196076.7A EP2881492B1 (en) | 2013-12-06 | 2013-12-06 | Method for carburising metal deep drawn article or a bent pressed article made of austenitic stainless steel |
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EP2881492A1 EP2881492A1 (en) | 2015-06-10 |
EP2881492B1 true EP2881492B1 (en) | 2017-05-03 |
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EP13196076.7A Active EP2881492B1 (en) | 2013-12-06 | 2013-12-06 | Method for carburising metal deep drawn article or a bent pressed article made of austenitic stainless steel |
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US (1) | US9738962B2 (en) |
EP (1) | EP2881492B1 (en) |
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DK3175012T3 (en) | 2014-07-31 | 2022-08-08 | Univ Case Western Reserve | IMPROVED ACTIVATION OF SELF-PASSIVATING METALS |
KR20210019435A (en) | 2018-06-11 | 2021-02-22 | 스웨이지락 캄파니 | Chemical activation of self-passivating metals |
US11396692B2 (en) | 2019-02-21 | 2022-07-26 | Fluid Controls Private Limited | Method of heat treating an article |
WO2021222343A1 (en) | 2020-04-29 | 2021-11-04 | Swagelok Company | Activation of self-passivating metals using reagent coatings for low temperature nitrocarburization |
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Publication number | Priority date | Publication date | Assignee | Title |
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JP2633076B2 (en) * | 1990-10-04 | 1997-07-23 | 大同ほくさん株式会社 | Hard austenitic stainless steel screw and its manufacturing method |
DE3933053C1 (en) | 1989-10-04 | 1990-05-03 | Degussa Ag, 6000 Frankfurt, De | |
TW237484B (en) | 1992-09-16 | 1995-01-01 | Daido Oxygen | |
US5536549A (en) * | 1993-08-02 | 1996-07-16 | Tulip Memory Systems, Inc. | Austenitic stainless steel substrate for magnetic-recording media |
EP0678589B1 (en) | 1994-04-18 | 1999-07-14 | Daido Hoxan Inc. | Method of carburizing austenitic metal |
US5556483A (en) * | 1994-04-18 | 1996-09-17 | Daido Hoxan, Inc. | Method of carburizing austenitic metal |
US6093303A (en) | 1998-08-12 | 2000-07-25 | Swagelok Company | Low temperature case hardening processes |
US6547888B1 (en) * | 2000-01-28 | 2003-04-15 | Swagelok Company | Modified low temperature case hardening processes |
JP2001330038A (en) * | 2000-03-17 | 2001-11-30 | Nsk Ltd | Rolling supporting device |
JP3961390B2 (en) * | 2002-10-04 | 2007-08-22 | エア・ウォーター株式会社 | Surface carbonitrided stainless steel parts with excellent wear resistance and manufacturing method thereof |
JP4295350B1 (en) | 2008-09-17 | 2009-07-15 | エア・ウォーター株式会社 | Method of using heat treatment furnace, heat treatment method and heat treatment furnace |
JP5650739B2 (en) * | 2009-08-07 | 2015-01-07 | スウエイジロク・カンパニー | Low temperature carburization under low vacuum |
DE102009056875B4 (en) | 2009-12-03 | 2013-07-11 | Bosch Mahle Turbo Systems Gmbh & Co. Kg | Bearing housing, charging device and method for surface treatment of a bearing housing |
US8696830B2 (en) | 2010-07-21 | 2014-04-15 | Kenneth H. Moyer | Stainless steel carburization process |
EP2627795A1 (en) * | 2010-10-11 | 2013-08-21 | Ipsen International GmbH | Method and arrangement for carburizing and carbonitriding metallic materials |
ITRM20110596A1 (en) * | 2010-11-16 | 2012-05-17 | Selex Sistemi Integrati Spa | ANTENNA RADIANT ELEMENT IN WAVE GUIDE ABLE TO OPERATE IN A WI-FI BAND, AND MEASUREMENT SYSTEM OF THE PERFORMANCE OF A C-BASED ANTENNA USING SUCH A RADIANT ELEMENT. |
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PL2881492T3 (en) | 2017-10-31 |
EP2881492A1 (en) | 2015-06-10 |
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US20150159260A1 (en) | 2015-06-11 |
CN104451534B (en) | 2018-04-27 |
US9738962B2 (en) | 2017-08-22 |
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