US20070068606A1 - Single-chamber vacuum furnace with hydrogen quenching - Google Patents
Single-chamber vacuum furnace with hydrogen quenching Download PDFInfo
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- US20070068606A1 US20070068606A1 US11/526,209 US52620906A US2007068606A1 US 20070068606 A1 US20070068606 A1 US 20070068606A1 US 52620906 A US52620906 A US 52620906A US 2007068606 A1 US2007068606 A1 US 2007068606A1
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- furnace
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- hydrogen
- filling
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- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 33
- 239000001257 hydrogen Substances 0.000 title claims abstract description 32
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 32
- 238000010791 quenching Methods 0.000 title description 21
- 230000000171 quenching effect Effects 0.000 title description 21
- 238000000034 method Methods 0.000 claims abstract description 42
- 238000010438 heat treatment Methods 0.000 claims abstract description 24
- 238000001816 cooling Methods 0.000 claims abstract description 21
- 238000011049 filling Methods 0.000 claims abstract description 15
- 238000007789 sealing Methods 0.000 claims abstract description 6
- 239000011261 inert gas Substances 0.000 claims abstract 7
- 239000007789 gas Substances 0.000 claims description 32
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 22
- 229910052757 nitrogen Inorganic materials 0.000 claims description 11
- 229910052799 carbon Inorganic materials 0.000 claims description 9
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 8
- 150000002431 hydrogen Chemical class 0.000 claims description 4
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims description 3
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 claims description 3
- 230000001105 regulatory effect Effects 0.000 claims description 2
- 239000012159 carrier gas Substances 0.000 claims 1
- 230000008569 process Effects 0.000 description 8
- 229910000831 Steel Inorganic materials 0.000 description 5
- 239000000112 cooling gas Substances 0.000 description 5
- 239000010959 steel Substances 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 238000004880 explosion Methods 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 238000003860 storage Methods 0.000 description 4
- 229910045601 alloy Inorganic materials 0.000 description 3
- 239000000956 alloy Substances 0.000 description 3
- 239000012298 atmosphere Substances 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000001681 protective effect Effects 0.000 description 3
- 230000007704 transition Effects 0.000 description 3
- 229910000746 Structural steel Inorganic materials 0.000 description 2
- 238000007872 degassing Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910000997 High-speed steel Inorganic materials 0.000 description 1
- 238000000137 annealing Methods 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 150000001721 carbon Chemical class 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000004320 controlled atmosphere Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000002360 explosive Substances 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 238000013383 initial experiment Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229910000734 martensite Inorganic materials 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000002093 peripheral effect Effects 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 238000005476 soldering Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000010561 standard procedure Methods 0.000 description 1
- 238000005482 strain hardening Methods 0.000 description 1
- 238000005496 tempering Methods 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
Images
Classifications
-
- 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
Definitions
- This invention relates to a method for operating a heat treatment plant with a single-chamber vacuum furnace, and to a single-chamber vacuum furnace.
- Low alloy steels have hitherto mainly been hardened in controlled atmosphere furnaces with oil quenching (so-called sealed quenching).
- the vacuum gas carburization is carried out in special multi-chamber systems in which oil baths or high pressure quenching stations with nitrogen or helium are used for quenching.
- Gas quenching is preferred because there is less distortion on the hardened material when quenching in gas, and because no subsequent cleaning is required.
- the multi-chamber furnaces normally used for this, in the prior art, are very expensive and have been developed specially for the mass production of automotive supplier parts or similar parts. They lack the flexibility to be adaptable to changing objectives and tasks imposed on them. Moreover, the process must be controlled and monitored much better in the case of single chamber furnaces because during the process the workpieces must not be moved and it must therefore be possible to arrange measurement sensors directly on or in the workpiece capable of recording its actual temperature.
- Lambda 0.35 for bolts 20 mm ⁇ 40 mm long
- Lambda 0.65 for bolts 40 mm ⁇ 80 mm long
- Lambda 1.50 for bolts 80 mm ⁇ 160 mm long
- Lambda 2.35 for bolts 120 mm ⁇ 240 mm long
- lambda value is the cooling time from 800° C. to 500° C., measured in seconds, divided by 100. These values for the cooling rate are much slower than those that can be achieved when quenching in the oil bath.
- This object is realized by a method for operating a single-chamber vacuum hardening furnace, including the steps of filling the interior of the furnace with workpieces, sealing the interior of the furnace and evacuating the same, heating the workpieces and maintaining a theoretical temperature, filling the interior of the furnace with hydrogen under high pressure, switching off the heating and circulating the hydrogen for cooling the workpieces, discharging the hydrogen and evacuating the interior of the furnace, filling the interior of the furnace with an inert protective gas up to approximately atmospheric pressure, and opening the furnace and unloading the workpieces.
- a single-chamber vacuum furnace for carrying out such method, and including a safety zone that surrounds the furnace and which prevents walking or travelling in the immediate vicinity of the furnace, with the exception of the front side thereof, which is adapted to be opened by mechanical or electrical means.
- FIG. 1 shows the basic time curve of temperature and pressure, and the type of gas supplied in the gas carburization of workpieces
- FIG. 2 shows the spatial arrangement of the essential plant components in an operation in a diagrammatic representation
- FIG. 3 shows a hardening furnace suitable for the method according to FIG. 1 in a cross-section from the side.
- FIG. 1 the time curve of the temperature inside a hardening furnace when a method according to the invention is carried out is plotted in curve 1 .
- Curve 2 shows the progress of the pressure inside the hardening furnace over the time during which the method is carried out.
- the time scale which generally represents a period of five hours from the beginning to the end of the process, is arranged on the horizontal X-axis.
- the temperature scale covers a temperature range from 0° C. to 1,200° C.
- the pressure scale is arranged on the right-hand side of the graph and indicates the pressure in bars absolute, going from 0 bar to 10 bars, 0 bar being the vacuum.
- Curve 1 commences at room temperature, which is section 1 a on temperature curve 1 .
- the heating is then switched on and brings the furnace to a temperature of approx. 1,050° along section 1 b .
- the required temperature range in the different carburization applications for which the furnace will be suitable is 800° C. to 1,100° C.
- the furnace temperature is kept constant in section 1 c.
- Section 1 c is approximately one hour long.
- the furnace is cooled quickly, approximately within 20 minutes, from 1,050° to room temperature. There the temperature is then kept constant until the end of the process, i.e. until the workpieces are unloaded. This section is denoted by 1 e.
- the pressure curve which is illustrated in curve 2 , initially commences at 1 bar, i.e. at ambient pressure. This corresponds to the air which is present inside the furnace when the hardening furnace is loaded.
- section 2 a of the graph the furnace space is evacuated for a period of approx. 20 minutes. The air in the furnace space is removed before the heating is switched on so that no oxidation can take place. Instead the furnace space is flooded with approx. 2 bars of nitrogen, as protective gas, when the heating is switched on, i.e. in the transition from 1 a to 1 b on the temperature curve. The pressure is maintained for a period of approx. 2 hours, which corresponds to section 2 b on the pressure curve.
- the nitrogen filling of the furnace is maintained up to a temperature of 700° C. Up to this temperature range the workpieces in the furnace are heated by convection heating. The furnace interior is then evacuated by the application of vacuum. The associated pressure reduction from 2 bars to 0 bar is identified by section 2 c . Further heating of the workpieces from 700° to the final temperature of 1,050° is achieved by radiant heating.
- a gas containing carbon is repeatedly introduced into the furnace space at a pressure of approx. 30 mbars for a short time.
- This gas e.g. acetylene
- This carbon diffuses from the surface into the workpiece.
- so-called diffusion phases 2 f are provided between carburization phases 2 e , in which diffusion phases the gas is removed from the furnace space by applying vacuum. Carbon absorbed by the workpiece surface until that time can then diffuse into the workpiece without additional carbon.
- Phases 2 e and 2 f can be repeated according to the desired carbon distribution.
- This exemplary embodiment contains process steps that would be suitable for thin-walled workpieces, where a relatively small carburization depth is aimed for.
- the interior is flooded with nitrogen from 0 bar to ambient pressure to unload the inner furnace space, which is illustrated by curve section 2 i . If the furnace is then opened, air enters the inner space, and the pressure is set to atmospheric pressure. This section of the pressure curve is denoted by 2 k.
- the method described offers the possibility, in a single chamber vacuum furnace, to achieve cooling rates which otherwise would only be attainable during oil quenching or water quenching.
- the cooling rate depends on the slope steepness of curve 1 in section 1 d .
- section 2 g If in section 2 g the hydrogen is then fed into the interior, there will no longer be any oxygen there. This therefore totally eliminates the risk of explosion. No oxygen enters the furnace interior during the cooling phase either.
- the hydrogen is then discharged off into the flue by means of discharge valves, and when atmospheric pressure is reached the remaining hydrogen is pumped out of the furnace interior by means of vacuum pumps (section 2 h ). Any residual hydrogen present is then diluted by flooding with nitrogen in section 2 i until no further ignitable mixture can be formed in any case. At that time there is also an absence of ignition source in the furnace interior because the entire content of the furnace has been cooled to approximately room temperature.
- the drive motors of the fans and the heating are without power.
- the opening of the furnace in section 2 k for unloading the inventory contained in it, is then entirely non-critical. The air entering during opening finds neither an ignition source nor an adequate concentration of hydrogen to create explosive conditions.
- the hydrogen pumped off in section 2 h is discharged through gas tight pipes and vacuum pipes via a flue into the atmosphere outside the operating building. After the hydrogen is pumped off, flue 17 ( FIG. 2 ) is fully flushed with nitrogen to ensure that no hydrogen that could form an ignitable mixture remains in it.
- the operating building is shown in more detail in FIG. 2 .
- FIG. 2 shows, in a diagrammatic representation, an operating building 10 for carrying out the method described above.
- the operating building is designed as a shop in which a hardening furnace 11 is installed by an intrinsically known method.
- a storage tank 12 for hydrogen is provided outside the building.
- a storage tank 13 for gaseous nitrogen is arranged next to a further storage tank 14 for liquid nitrogen. Both storage tanks 12 and 13 for the gaseous supply are connected by connecting pipes 15 , 16 to hardening furnace 11 .
- Hardening furnace 11 is also provided with a flue 17 , which leads from the building into the atmosphere. Flue 17 is in this case designed higher than the ridge line of building 10 .
- hardening furnace 11 On its left front side, hardening furnace 11 has a sealing or closure cover 18 which can be opened for loading and unloading hardening furnace 11 .
- a shaded region 20 in which special precautions are taken against mechanical damage to the outer added components and the pipes, is illustrated behind the plane of sealing cover 18 .
- This region 20 is mechanically protected so that it is not possible to pass through this region in the vicinity of hardening furnace 11 with machines such as fork lift trucks and the like. It is also not possible to pass through region 20 with a gantry crane due to the installation of suitable mechanical devices or electrical precautionary measures which influence the control of the crane. Barriers, guide planks, or even a cage may be provided for this purpose. These safety precautions prevent pipes 15 carrying hydrogen, the associated valve means and pumps, and the hardening furnace itself, from being damaged so that hydrogen can escape inside operating building 10 .
- Sealing cover 18 of hardening furnace 11 is also provided with a peripheral seal which is sealed safely and hermetically by excess pressure from a protective gas during operation. This prevents leakages from occurring during the transition from vacuum to excess pressure that takes place during operation, as illustrated in curve 2 of FIG. 1 .
- FIG. 3 shows hardening furnace 11 in an enlarged representation.
- the furnace is designed as a single-chamber vacuum furnace with a fan whose axis of rotation is identical to the central axis of the furnace.
- Furnace door or cover 18 is specially equipped to protect against leaks occurring during the transition between vacuum and excess pressure. This is described in more detail in laid-open specification WO 2004/096427A1, which originates from the same applicant. It should also be mentioned that vertical single-chamber furnaces are being built and that the cooling fan and heat exchanger can also be installed in an external housing which is then connected to the furnace housing.
- Lambda 0.10 for bolts 20 mm ⁇ 40 mm long
- Lambda 0.26 for bolts 40 mm ⁇ 80 mm long
- Lambda 0.72 for bolts 80 mm ⁇ 160 mm long
- Lambda 1.30 for bolts 120 mm ⁇ 240 mm long
- a cold water store of several cubic meters of cooling water may be kept at a low temperature of approx. 3° C. - 5° C. for feeding into the heat exchanger for the first 30-60 seconds of the cooling process.
- This favorably influences the extremely critical time phase of initial quenching from holding temperature 1 c.
- the quality of the workpieces is also determined by the distortion that takes place during the hardening process.
- the gas flow has been introduced successfully in vacuum furnaces several years ago. Now, this invention provides a new, supplementary solution to this problem.
- the full hydrogen gas pressure is introduced into the furnace for quenching.
- this pressure may be 10 bars but may also be 20 bars or 40 bars.
- the cooling rate which must be set to achieve a certain lambda value is controlled by the gas flow rate and ultimately by the rate of circulation inside the furnace.
- the circulating fan is speed controlled, a control range of 10% of the maximum speed being provided until the full maximum speed is reached.
- the technical effect of this means that there are three factors of influence for the cooling rate, namely the type of gas, the gas pressure and the gas flow rate. Hitherto, the technical world was of the opinion that these three components were of equal importance. This may be true in terms of the hardness that can be achieved.
- the type of cooling gas used affects all surfaces of the workpieces exposed to the cooling gas. The same applies to the gas pressure, which is the same throughout the treatment area of the furnace. However, the flow rate of the cooling gas has different effects on the workpiece surfaces according to how the gas flow is obtained.
- a twist throttle or similar means may also be used to influence the flow rate.
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Abstract
A method for operating a hardening furnace with hydrogen cooling, including filling the interior of the furnace with workpieces, sealing the interior of the furnace and evacuating it, filling the interior of the furnace with an inert gas, convective heating the workpieces with circulation of the inert gas, evacuating the interior of the furnace, further heating the workpieces by radiant heating and maintaining a theoretical temperature, switching off the heating, filling the interior of the furnace with hydrogen under high pressure, and circulating the hydrogen for cooling the workpieces, evacuating the interior of the furnace and filling it with an inert gas up to approximately atmospheric pressure, and opening the furnace and unloading the workpieces.
Description
- The instant application should be granted the priority date of Sep. 23, 2005 the filing date of the corresponding
German patent application 10 2005 045 783.5. - This invention relates to a method for operating a heat treatment plant with a single-chamber vacuum furnace, and to a single-chamber vacuum furnace.
- In conventional single-chamber vacuum furnaces with gas quenching, different heat treatment methods have hitherto been carried out. These methods include annealing, soldering, sintering, degassing, hardening of tool steels, high speed steels, hot and cold working steels, as well as sub-zero refrigeration and tempering.
- In the future, methods for hardening low alloy steels and vacuum gas carburization will also be added to these heat treatment methods. The need to expand the range of application results from the sharp rise in the cost of heat treatment operations. The most significant factor influencing production costs is the number of operating hours of the furnace plants per year. A heat treatment operation may use special furnaces for both of the last-mentioned methods if long-term contracts have been signed with customers. For the remaining business, for which there are only short-term contractual obligations, considerable flexibility is required. This means that both of the last-mentioned methods should, if possible, be carried out using the same furnaces as those used in the standard methods already mentioned.
- Low alloy steels have hitherto mainly been hardened in controlled atmosphere furnaces with oil quenching (so-called sealed quenching). The vacuum gas carburization is carried out in special multi-chamber systems in which oil baths or high pressure quenching stations with nitrogen or helium are used for quenching.
- Gas quenching is preferred because there is less distortion on the hardened material when quenching in gas, and because no subsequent cleaning is required. The multi-chamber furnaces normally used for this, in the prior art, are very expensive and have been developed specially for the mass production of automotive supplier parts or similar parts. They lack the flexibility to be adaptable to changing objectives and tasks imposed on them. Moreover, the process must be controlled and monitored much better in the case of single chamber furnaces because during the process the workpieces must not be moved and it must therefore be possible to arrange measurement sensors directly on or in the workpiece capable of recording its actual temperature.
- Standard single chamber vacuum furnaces currently operate at 10 bars of nitrogen for quenching, and attain the following lambda values in the material core of structural steel bolts:
Lambda =0.35 forbolts 20 mm ø×40 mm long
Lambda =0.65 for bolts 40 mm ø×80 mm long
Lambda =1.50 for bolts 80 mm ø×160 mm long
Lambda =2.35 for bolts 120 mm ø×240 mm long - Here the lambda value is the cooling time from 800° C. to 500° C., measured in seconds, divided by 100. These values for the cooling rate are much slower than those that can be achieved when quenching in the oil bath.
- The current prior art is described in the periodical article by R. Hoffmann, H. Steinmann and D. Uschkoreit: Possibilities and limitations of gas cooling—HTM 47-1992, p. 2 ff. For hardening low alloy steels and for vacuum gas carburization the quenching rate must be considerably increased to values which have so far not been regarded as attainable in a single-chamber furnace.
- In order to expand the range of application of single-chamber vacuum furnaces in the manner described above, it is therefore the object of this invention to obtain quenching rates which correspond to quenching in the oil bath.
- This object is realized by a method for operating a single-chamber vacuum hardening furnace, including the steps of filling the interior of the furnace with workpieces, sealing the interior of the furnace and evacuating the same, heating the workpieces and maintaining a theoretical temperature, filling the interior of the furnace with hydrogen under high pressure, switching off the heating and circulating the hydrogen for cooling the workpieces, discharging the hydrogen and evacuating the interior of the furnace, filling the interior of the furnace with an inert protective gas up to approximately atmospheric pressure, and opening the furnace and unloading the workpieces. This object is also realized by a single-chamber vacuum furnace for carrying out such method, and including a safety zone that surrounds the furnace and which prevents walking or travelling in the immediate vicinity of the furnace, with the exception of the front side thereof, which is adapted to be opened by mechanical or electrical means.
- The invention is described in the following with reference to an exemplary embodiment and the drawing, in which:
-
FIG. 1 : shows the basic time curve of temperature and pressure, and the type of gas supplied in the gas carburization of workpieces; -
FIG. 2 : shows the spatial arrangement of the essential plant components in an operation in a diagrammatic representation; and -
FIG. 3 : shows a hardening furnace suitable for the method according toFIG. 1 in a cross-section from the side. - In
FIG. 1 the time curve of the temperature inside a hardening furnace when a method according to the invention is carried out is plotted incurve 1.Curve 2 shows the progress of the pressure inside the hardening furnace over the time during which the method is carried out. Here the time scale, which generally represents a period of five hours from the beginning to the end of the process, is arranged on the horizontal X-axis. The temperature scale covers a temperature range from 0° C. to 1,200° C. The pressure scale is arranged on the right-hand side of the graph and indicates the pressure in bars absolute, going from 0 bar to 10 bars, 0 bar being the vacuum. - Underneath the graph it is illustrated which gases are conducted at what times into the device, and when vacuum is applied. This representation is described later in detail.
- The temperature curve is first described over the process time of 5 hours.
Curve 1 commences at room temperature, which issection 1 a ontemperature curve 1. The heating is then switched on and brings the furnace to a temperature of approx. 1,050° alongsection 1 b. The required temperature range in the different carburization applications for which the furnace will be suitable is 800° C. to 1,100° C. - At the target temperature of 1,050° C. predetermined in this exemplary embodiment the furnace temperature is kept constant in
section 1 c.Section 1 c is approximately one hour long. Insection 1 d the furnace is cooled quickly, approximately within 20 minutes, from 1,050° to room temperature. There the temperature is then kept constant until the end of the process, i.e. until the workpieces are unloaded. This section is denoted by 1 e. - The pressure curve, which is illustrated in
curve 2, initially commences at 1 bar, i.e. at ambient pressure. This corresponds to the air which is present inside the furnace when the hardening furnace is loaded. Insection 2 a of the graph the furnace space is evacuated for a period of approx. 20 minutes. The air in the furnace space is removed before the heating is switched on so that no oxidation can take place. Instead the furnace space is flooded with approx. 2 bars of nitrogen, as protective gas, when the heating is switched on, i.e. in the transition from 1 a to 1 b on the temperature curve. The pressure is maintained for a period of approx. 2 hours, which corresponds tosection 2 b on the pressure curve. The nitrogen filling of the furnace is maintained up to a temperature of 700° C. Up to this temperature range the workpieces in the furnace are heated by convection heating. The furnace interior is then evacuated by the application of vacuum. The associated pressure reduction from 2 bars to 0 bar is identified by section 2 c. Further heating of the workpieces from 700° to the final temperature of 1,050° is achieved by radiant heating. - After the vacuum has been achieved in the furnace space, denoted by 2 d, a gas containing carbon is repeatedly introduced into the furnace space at a pressure of approx. 30 mbars for a short time. This gas, e.g. acetylene, loads the surface with carbon by thermal decomposition on the surface of the workpieces during
time intervals 2 e. This carbon diffuses from the surface into the workpiece. In order to obtain a more uniform carbon concentration over the thickness of the carburized layer, so-calleddiffusion phases 2 f are provided between carburization phases 2 e, in which diffusion phases the gas is removed from the furnace space by applying vacuum. Carbon absorbed by the workpiece surface until that time can then diffuse into the workpiece without additional carbon. 2 e and 2 f can be repeated according to the desired carbon distribution. In this exemplary embodiment there are a total of fourPhases carburization phases 2 e. This exemplary embodiment contains process steps that would be suitable for thin-walled workpieces, where a relatively small carburization depth is aimed for. - After completion of the
last diffusion phase 2 f the inner furnace space evacuated until that point is flooded with hydrogen gas up to an absolute pressure of 10 bars. At the same time the heating is switched off, which has up until then kept the temperature incurve section 1 c constant. Due to hydrogen cooling alongcurve 1 d the temperature drops rapidly to the ambient temperature. The hydrogen cooling phase is denoted by 2 g. Circulation of the hydrogen gas with an efficient fan inside the furnace assists the heat dissipation. For uniform cooling, which minimizes the displacement of the workpieces during cooling, the hydrogen flow inside the furnace space is deflected several times so that the workpieces are loaded from several sides with the cooling gas. When cooling to almost room temperature is completed, the hydrogen gas insection 2 h is removed from the furnace space until vacuum is achieved. The interior is flooded with nitrogen from 0 bar to ambient pressure to unload the inner furnace space, which is illustrated bycurve section 2 i. If the furnace is then opened, air enters the inner space, and the pressure is set to atmospheric pressure. This section of the pressure curve is denoted by 2 k. - In the case of more solid or larger workpieces provision may also be made for quenching to take place initially to a point above the martensite start line, and the temperature is maintained there until the edge temperature and the core temperature of the workpiece have equalized. Further quenching may then be carried out until room temperature is approximately reached.
- The method described offers the possibility, in a single chamber vacuum furnace, to achieve cooling rates which otherwise would only be attainable during oil quenching or water quenching. The cooling rate depends on the slope steepness of
curve 1 insection 1 d. Although a method is known for cooling workpieces in the hardening shop with hydrogen, this method is not used in practice in single chamber vacuum furnaces because it is considered that the safety problems cannot be solved economically. - Here a new solution for the safety problems is found with the method described. The risk of explosion when filling the interior of the furnace with hydrogen arises because on the one hand ignition sources are present in the furnace, namely the workpieces kept at over 1,000° C., and on the other the hydrogen is present as an oxidizable gas. To eliminate a risk of explosion all oxygen must therefore be kept away from the furnace interior. This is achieved in the method according to the invention in that the air present after the furnace is loaded is almost completely removed, initially in
section 2 a, by evacuation. A nitrogen atmosphere is then built up (2 b), which is later also pumped away in the course of the process. Any residual oxygen remaining from the atmosphere or due to degassing the workpieces is then flushed out with the nitrogen. Finally the carburization gas, which does not react with hydrogen, is fed into the furnace. This gas is pumped away repeatedly, which is equivalent to further flushing of the furnace interior. - If in section 2 g the hydrogen is then fed into the interior, there will no longer be any oxygen there. This therefore totally eliminates the risk of explosion. No oxygen enters the furnace interior during the cooling phase either. The hydrogen is then discharged off into the flue by means of discharge valves, and when atmospheric pressure is reached the remaining hydrogen is pumped out of the furnace interior by means of vacuum pumps (
section 2 h). Any residual hydrogen present is then diluted by flooding with nitrogen insection 2 i until no further ignitable mixture can be formed in any case. At that time there is also an absence of ignition source in the furnace interior because the entire content of the furnace has been cooled to approximately room temperature. The drive motors of the fans and the heating are without power. The opening of the furnace insection 2 k, for unloading the inventory contained in it, is then entirely non-critical. The air entering during opening finds neither an ignition source nor an adequate concentration of hydrogen to create explosive conditions. - The hydrogen pumped off in
section 2 h is discharged through gas tight pipes and vacuum pipes via a flue into the atmosphere outside the operating building. After the hydrogen is pumped off, flue 17 (FIG. 2 ) is fully flushed with nitrogen to ensure that no hydrogen that could form an ignitable mixture remains in it. - The operating building is shown in more detail in
FIG. 2 . -
FIG. 2 shows, in a diagrammatic representation, an operatingbuilding 10 for carrying out the method described above. The operating building is designed as a shop in which a hardeningfurnace 11 is installed by an intrinsically known method. Astorage tank 12 for hydrogen is provided outside the building. Furthermore, astorage tank 13 for gaseous nitrogen is arranged next to afurther storage tank 14 for liquid nitrogen. Both 12 and 13 for the gaseous supply are connected by connectingstorage tanks 15, 16 to hardeningpipes furnace 11. - Hardening
furnace 11 is also provided with aflue 17, which leads from the building into the atmosphere.Flue 17 is in this case designed higher than the ridge line ofbuilding 10. - On its left front side, hardening
furnace 11 has a sealing or closure cover 18 which can be opened for loading and unloading hardeningfurnace 11. A shadedregion 20, in which special precautions are taken against mechanical damage to the outer added components and the pipes, is illustrated behind the plane of sealingcover 18. Thisregion 20 is mechanically protected so that it is not possible to pass through this region in the vicinity of hardeningfurnace 11 with machines such as fork lift trucks and the like. It is also not possible to pass throughregion 20 with a gantry crane due to the installation of suitable mechanical devices or electrical precautionary measures which influence the control of the crane. Barriers, guide planks, or even a cage may be provided for this purpose. These safety precautions preventpipes 15 carrying hydrogen, the associated valve means and pumps, and the hardening furnace itself, from being damaged so that hydrogen can escape inside operatingbuilding 10. - Sealing
cover 18 of hardeningfurnace 11 is also provided with a peripheral seal which is sealed safely and hermetically by excess pressure from a protective gas during operation. This prevents leakages from occurring during the transition from vacuum to excess pressure that takes place during operation, as illustrated incurve 2 ofFIG. 1 . - Because of the safety precautions described it is not necessary to design
region 20 so that it is protected from explosions. This results in a reduction in plant and operating costs relative to the concepts of the prior art for hydrogen cooling in the hardening operation. - Finally,
FIG. 3 shows hardening furnace 11 in an enlarged representation. The furnace is designed as a single-chamber vacuum furnace with a fan whose axis of rotation is identical to the central axis of the furnace. Furnace door or cover 18 is specially equipped to protect against leaks occurring during the transition between vacuum and excess pressure. This is described in more detail in laid-open specification WO 2004/096427A1, which originates from the same applicant. It should also be mentioned that vertical single-chamber furnaces are being built and that the cooling fan and heat exchanger can also be installed in an external housing which is then connected to the furnace housing. - Initial experiments with the plant and method described have shown that the following lambda values can be achieved in the material core of structural steel bolts:
Lambda=0.10 forbolts 20 mm ø×40 mm long
Lambda=0.26 for bolts 40 mm ø×80 mm long
Lambda=0.72 for bolts 80 mm ø×160 mm long
Lambda=1.30 for bolts 120 mm ø×240 mm long - These are values which correspond to quenching in oil.
- For a further improvement in the attainable cooling rates provision may be made for a cold water store of several cubic meters of cooling water to be kept at a low temperature of approx. 3° C. - 5° C. for feeding into the heat exchanger for the first 30-60 seconds of the cooling process. This favorably influences the extremely critical time phase of initial quenching from holding
temperature 1 c. - The quality of the workpieces is also determined by the distortion that takes place during the hardening process. In order to reduce the distortion problems that still remain in furnaces with gas quenching, the gas flow, with frequent reversals of direction, has been introduced successfully in vacuum furnaces several years ago. Now, this invention provides a new, supplementary solution to this problem.
- In the method and with the device according to the invention it is possible to achieve certain specific lambda values. Here the full hydrogen gas pressure is introduced into the furnace for quenching. Depending on the furnace, this pressure may be 10 bars but may also be 20 bars or 40 bars. The cooling rate which must be set to achieve a certain lambda value is controlled by the gas flow rate and ultimately by the rate of circulation inside the furnace. The circulating fan is speed controlled, a control range of 10% of the maximum speed being provided until the full maximum speed is reached. The technical effect of this means that there are three factors of influence for the cooling rate, namely the type of gas, the gas pressure and the gas flow rate. Hitherto, the technical world was of the opinion that these three components were of equal importance. This may be true in terms of the hardness that can be achieved. Because of the distortion of the workpieces, however, differences have been found. For example, the type of cooling gas used affects all surfaces of the workpieces exposed to the cooling gas. The same applies to the gas pressure, which is the same throughout the treatment area of the furnace. However, the flow rate of the cooling gas has different effects on the workpiece surfaces according to how the gas flow is obtained.
- The use of hydrogen gas at very high pressure establishes both of the first mentioned points. Now, when lower lambda values than would be possible at full fan power are aimed for, the power of the circulating fan is reduced and the parameter “flow rate of the cooling gas” is adapted to requirements. Due to the gas circulation, which is then slower, a lower distortion of the processed workpiece is obtained than if the fan were to be operated at full power and one of the other parameters were to be changed.
- As an alterative to regulating the fan power, a twist throttle or similar means may also be used to influence the flow rate.
- The specification incorporates by reference the disclosure of
German priority document 10 2005 045 783.5 filed Sep. 23, 2005. - The present invention is, of course, in no way restricted to the specific disclosure of the specification and drawings, but also encompasses any modifications within the scope of the appended claims.
Claims (11)
1. A method for operating a single-chamber vacuum hardening furnace, including the steps of:
filling an interior of the furnace with workpieces;
sealing the interior of the furnace;
evacuating the interior of the furnace;
heating the workpieces and maintaining a theoretical temperature;
filling the interior of the furnace with hydrogen under high pressure, switching off the heating and circulating the hydrogen for cooling the workpieces;
discharging the hydrogen and evacuating the interior of the furnace;
filling the interior of the furnace with an inert gas up to approximately atmospheric pressure; and
opening the furnace and unloading the workpieces.
2. A method according to claim 1 , which, between the evacuating and heating steps, includes the further steps of:
filling the interior of the furnace with an inert gas;
convective heating the workpieces with circulation of the inert gas; and
evacuating the interior of the furnace.
3. A method according to claim 2 , wherein the inert gas of at least one of said filling steps is nitrogen.
4. A method according to claim 1 , wherein said discharging step comprises conveying the hydrogen out of an operating building via a flue.
5. A method according to claim 4 , wherein said flue is higher than a roof height of the operating building.
6. A method according to claim 1 , wherein during and/or after said step of heating the workpieces and maintaining a theoretical temperature, a gas containing carbon is conveyed at least one time into the interior of the furnace.
7. A method according to claim 6 , wherein said gas containing carbon is pumped out of the interior of the furnace prior to said step of filling the interior of the furnace with hydrogen under high pressure.
8. A method according to claim 6 , wherein said gas is a acetylene.
9. A method according to claim 8 , wherein a carrier gas is added to said acetylene.
10. A method according to claim 1 , wherein a fan is provided for circulating the hydrogen, and wherein the speed of the fan is adapted to be regulated.
11. A device for carrying out the method of claim 1 , and comprising a safety zone that surrounds the hardening furnace, wherein the safety zone is adapted to prevent walking or travelling in the immediate vicinity of the furnace, with the exception of a front side of the furnace that is adapted to be opened by mechanical or electrical means.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102005045783A DE102005045783A1 (en) | 2005-09-23 | 2005-09-23 | Single-chamber vacuum furnace with hydrogen quenching |
| DE102005045783.5 | 2005-09-23 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US20070068606A1 true US20070068606A1 (en) | 2007-03-29 |
Family
ID=37492110
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US11/526,209 Abandoned US20070068606A1 (en) | 2005-09-23 | 2006-09-22 | Single-chamber vacuum furnace with hydrogen quenching |
Country Status (5)
| Country | Link |
|---|---|
| US (1) | US20070068606A1 (en) |
| EP (1) | EP1767660B1 (en) |
| CN (1) | CN1936030A (en) |
| AT (1) | ATE504664T1 (en) |
| DE (2) | DE102005045783A1 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8820098B2 (en) | 2011-05-17 | 2014-09-02 | Air Products And Chemicals, Inc. | Method and apparatus for quenching of materials in vacuum furnace |
| US20180187284A1 (en) * | 2016-12-30 | 2018-07-05 | Shanghai Yibai Industrial Furnaces Co., Ltd. | High-pressure liquid-state or supercritical-state quenching apparatus |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE102007029038A1 (en) * | 2007-06-21 | 2009-01-02 | Eliog-Kelvitherm Industrieofenbau Gmbh | Vacuum furnace for heat treatment of metallic workpieces and method for its operation |
| CN107560425A (en) * | 2017-09-30 | 2018-01-09 | 志圣科技(广州)有限公司 | Vacuum pressure baking box |
| CN111785445A (en) * | 2020-07-31 | 2020-10-16 | 浙江佳伟新材料科技有限责任公司 | Tensile strength control process of copper-clad steel coaxial cable |
| CN112853072A (en) * | 2020-12-31 | 2021-05-28 | 江苏华苏工业炉制造有限公司 | Horizontal multizone heating high vacuum tempering furnace of square single chamber |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4278421A (en) * | 1978-10-14 | 1981-07-14 | Ipsen Industries International Gesellschaft Mit Beschrankter Haftung | Industrial furnaces for the heat treatment of metallic workpieces |
| US4867808A (en) * | 1987-10-28 | 1989-09-19 | Degussa Aktiengesellschaft | Heat treating a metallic workpiece by quenching under cooling gas under above atmospheric pressure and specified circulation rate |
| US20060180961A1 (en) * | 2001-07-27 | 2006-08-17 | Surface Combustion, Inc. | Furnace for vacuum carburizing with unsaturated aromatic hydrocarbons |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3416902A1 (en) * | 1984-05-08 | 1985-11-14 | Schmetz Industrieofenbau und Vakuum-Hartlöttechnik KG, 5750 Menden | METHOD AND VACUUM OVEN FOR HEAT TREATING A BATCH |
| DE3819803C1 (en) * | 1988-06-10 | 1989-12-14 | Ulrich 5810 Witten De Wingens | |
| DE4034085C1 (en) * | 1990-10-26 | 1991-11-14 | Degussa Ag, 6000 Frankfurt, De | |
| DE4100989A1 (en) * | 1991-01-15 | 1992-07-16 | Linde Ag | PROCESS FOR HEAT TREATMENT IN VACUUM OVENS |
| DE4121277C2 (en) * | 1991-06-27 | 2000-08-03 | Ald Vacuum Techn Ag | Device and method for the automatic monitoring of operational safety and for controlling the process sequence in a vacuum heat treatment furnace |
| DE4312627A1 (en) * | 1993-04-19 | 1994-10-20 | Hauzer Holding | Method and device for heat treatment of objects |
| FR2810340B1 (en) * | 2000-06-20 | 2003-03-14 | Etudes Const Mecaniques | GAS QUENCHING CELL |
| DE10108057A1 (en) * | 2001-02-20 | 2002-08-22 | Linde Ag | Process for quenching metallic workpieces |
| DE602004006984T2 (en) * | 2003-04-30 | 2008-02-21 | Sistem Teknik Endustriyel Elektronik Sis.San. Ve Tic. Ltd. Sti., Dudullu | QUICK-CLOSING DOOR FOR PRESSURE TANK |
-
2005
- 2005-09-23 DE DE102005045783A patent/DE102005045783A1/en not_active Withdrawn
-
2006
- 2006-09-06 AT AT06018641T patent/ATE504664T1/en active
- 2006-09-06 DE DE502006009240T patent/DE502006009240D1/en active Active
- 2006-09-06 EP EP06018641A patent/EP1767660B1/en not_active Not-in-force
- 2006-09-19 CN CNA2006101270056A patent/CN1936030A/en active Pending
- 2006-09-22 US US11/526,209 patent/US20070068606A1/en not_active Abandoned
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4278421A (en) * | 1978-10-14 | 1981-07-14 | Ipsen Industries International Gesellschaft Mit Beschrankter Haftung | Industrial furnaces for the heat treatment of metallic workpieces |
| US4867808A (en) * | 1987-10-28 | 1989-09-19 | Degussa Aktiengesellschaft | Heat treating a metallic workpiece by quenching under cooling gas under above atmospheric pressure and specified circulation rate |
| US4867808B1 (en) * | 1987-10-28 | 1994-02-22 | Leybold Durferrit Gmbh | |
| US20060180961A1 (en) * | 2001-07-27 | 2006-08-17 | Surface Combustion, Inc. | Furnace for vacuum carburizing with unsaturated aromatic hydrocarbons |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8820098B2 (en) | 2011-05-17 | 2014-09-02 | Air Products And Chemicals, Inc. | Method and apparatus for quenching of materials in vacuum furnace |
| US20180187284A1 (en) * | 2016-12-30 | 2018-07-05 | Shanghai Yibai Industrial Furnaces Co., Ltd. | High-pressure liquid-state or supercritical-state quenching apparatus |
| US10640845B2 (en) * | 2016-12-30 | 2020-05-05 | Shanghai Yibai Industrial Furnaces Co., Ltd. | High-pressure liquid-state or supercritical-state quenching apparatus |
Also Published As
| Publication number | Publication date |
|---|---|
| EP1767660A1 (en) | 2007-03-28 |
| ATE504664T1 (en) | 2011-04-15 |
| DE102005045783A1 (en) | 2007-03-29 |
| EP1767660B1 (en) | 2011-04-06 |
| DE502006009240D1 (en) | 2011-05-19 |
| CN1936030A (en) | 2007-03-28 |
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