EP2098314B1 - Method and apparatus for producing metallic casting moulds using the lost wax casting method - Google Patents
Method and apparatus for producing metallic casting moulds using the lost wax casting method Download PDFInfo
- Publication number
- EP2098314B1 EP2098314B1 EP08004045A EP08004045A EP2098314B1 EP 2098314 B1 EP2098314 B1 EP 2098314B1 EP 08004045 A EP08004045 A EP 08004045A EP 08004045 A EP08004045 A EP 08004045A EP 2098314 B1 EP2098314 B1 EP 2098314B1
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- Prior art keywords
- heating mantle
- gas
- heat transfer
- burners
- transfer gas
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- 238000000034 method Methods 0.000 title claims description 30
- 238000005266 casting Methods 0.000 title claims description 22
- 238000005495 investment casting Methods 0.000 title claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 88
- 239000007789 gas Substances 0.000 claims description 85
- 239000002826 coolant Substances 0.000 claims description 32
- 238000012546 transfer Methods 0.000 claims description 21
- 238000002485 combustion reaction Methods 0.000 claims description 16
- 229910052751 metal Inorganic materials 0.000 claims description 16
- 239000002184 metal Substances 0.000 claims description 16
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- 238000002156 mixing Methods 0.000 claims description 7
- 238000004519 manufacturing process Methods 0.000 claims description 6
- 229910045601 alloy Inorganic materials 0.000 claims description 5
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- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 5
- 239000001301 oxygen Substances 0.000 claims description 5
- 229910052760 oxygen Inorganic materials 0.000 claims description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims description 4
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 4
- 239000011261 inert gas Substances 0.000 claims description 4
- 238000009826 distribution Methods 0.000 claims description 3
- 239000001257 hydrogen Substances 0.000 claims description 3
- 229910052739 hydrogen Inorganic materials 0.000 claims description 3
- 239000007788 liquid Substances 0.000 claims description 3
- 230000003647 oxidation Effects 0.000 claims description 3
- 238000007254 oxidation reaction Methods 0.000 claims description 3
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 2
- 229910021529 ammonia Inorganic materials 0.000 claims description 2
- 239000001569 carbon dioxide Substances 0.000 claims description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 2
- 150000008282 halocarbons Chemical class 0.000 claims description 2
- 229930195733 hydrocarbon Natural products 0.000 claims description 2
- 150000002430 hydrocarbons Chemical class 0.000 claims description 2
- 150000002431 hydrogen Chemical class 0.000 claims description 2
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- 239000005864 Sulphur Substances 0.000 claims 1
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- -1 sulphur halides Chemical class 0.000 claims 1
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- 241001156002 Anthonomus pomorum Species 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 230000035515 penetration Effects 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 241000196324 Embryophyta Species 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
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 235000009754 Vitis X bourquina Nutrition 0.000 description 1
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- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 1
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- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- 230000017525 heat dissipation Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 229910001338 liquidmetal Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
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- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
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- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Images
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B22—CASTING; POWDER METALLURGY
- B22D—CASTING OF METALS; CASTING OF OTHER SUBSTANCES BY THE SAME PROCESSES OR DEVICES
- B22D27/00—Treating the metal in the mould while it is molten or ductile ; Pressure or vacuum casting
- B22D27/04—Influencing the temperature of the metal, e.g. by heating or cooling the mould
- B22D27/045—Directionally solidified castings
Definitions
- the present invention relates to a method according to claim 1 and a device according to claim 6 for the production of metal castings by precision casting, in particular cast aluminum or aluminum-containing alloys.
- Advantageous developments are specified in the subclaims.
- a wax model is usually produced by an object to be cast, which is then coated with a ceramic shell. This can be done, for example, by immersing the wax model in suitable ceramic slip. In this case, different slips can be applied successively. Subsequently, the wax model is melted out, and fired the ceramic form. As a result, a porous mold is obtained, in which metallic melts can be cast. After solidification of the metallic melt, the mold is destroyed and the casting can be removed.
- the method described above also allows the production of complex castings.
- a disadvantage of the casting technique described is that the ceramic casting molds produced have a poor thermal conductivity and thus contribute to a relatively long and unregulated solidification time of the molten metal in the casting mold.
- a relatively coarse-grained microstructure arises, which can lead to reduced mechanical properties.
- the EP 1 076 118 A discloses a method and apparatus for producing directionally cured castings. It is envisaged to lower the cast body in a cooling bath to achieve a directional curing. The located above the cooling bath part of the mold is tempered with a heating chamber, which has electrical heating elements.
- the casting mold and thus also the melt introduced into the casting mold are heated above the cooling liquid level by means of an electrical resistance heater in order to keep the filled molten metal liquid above the cooling liquid level.
- an electrical resistance heater in order to keep the filled molten metal liquid above the cooling liquid level.
- the system is flushed by means of a protective gas at overpressure. This requires a suitably closed container.
- the method known from the prior art has drawbacks such that in the electrical resistance heating based on radiation, the desired temperature level for securely holding the molten metal above the level of the cooling liquid can be kept difficult or even not achieved if the plant dimensions go beyond a critical limit measure or the grape geometry is such that radiation dead inner areas arise, ie those areas of the mold, which are shielded by other mold areas of the radiated by the electrical resistance heating radiant heat.
- This is a significant limitation of the process in terms of the size of the castings to be cast and their geometry given.
- the injection of inert gas leads to an additional cooling effect.
- This object is achieved with respect to the method by a method for producing a metal casting by the investment casting method, wherein the casting metal or alloy to be cast is poured into a ceramic mold with porous walls and the mold for cooling and solidification of the melt from one end Starting from constantly immersed in such a way in a coolant, that as the interface between the melt and already solidified metal solidifying front lags the coolant level, which is characterized in that the lying still above the coolant level region of the mold by means of a heat transfer gas to a temperature above the Solidus temperature of the metal or alloy to be cast is heated.
- the heat transfer gas to be used in this case contains an exothermically oxidizable gas and oxygen.
- Suitable exothermic oxidizable gases are, for example, hydrogen, gaseous hydrocarbons such as methane, ethane, propane, butane, ethene, acetylene, or else carbon monoxide, and mixtures of these.
- the heat transfer gas may contain other gases such as noble gases, halogenated hydrocarbons, ammonia, nitrogen, carbon dioxide, sulfur halides or mixtures thereof.
- the further gases containing the heat gas can serve as protective or inert gases in order to prevent diffusion of hydrogen into the molten metal or the cast body.
- the exothermic oxidizable gas contained in the heat transfer gas is directly oxidized within a heating hood, whereby the region of the casting mold located above the cooling liquid level is heated.
- the heat carrier gas is removed from the heating hood together with possibly evaporated coolant constituents and fed to afterburning.
- the exhaust gases resulting from the afterburning are fed to a heat exchanger which preheats at least part of the heat transfer gas to be supplied fresh to the heating hood.
- the temperature is determined within the heating hood and used as a controlled variable for the content of exothermally oxidizable gas in the heat carrier gas or the content of other gases in the heat transfer gas.
- the exothermic oxidizable gas is burned by burners in the course of a direct oxidation within the heating hood.
- a heating hood has at least two burners or burner levels arranged one above the other. The individual burners can be controlled separately and can be clocked depending on the operating state of the heating hood. In addition, the combustion ratio (lambda) of the individual burners can be set differently.
- the combustion ratio lambda a lower burner level ⁇ 1.0, the burners are thus operated with a substoichiometric gas / oxygen ratio, whereas the combustion ratio lambda the upper burner level> 1.0, ie the burner with be operated at a superstoichiometric gas / air ratio.
- Such an embodiment of the method according to the invention makes it possible to dispense with afterburning of the exhaust gases discharged from the heating hood since, on the one hand, the surface of the coolant passing into contact with the heating hood is not oxidized due to the substoichiometric gas / oxygen ratio and, on the other hand, evaporating oxidizable constituents of the coolant bath in the Area of the upper, with a superstoichiometric gas / air ratio operated burner level directly oxidized in the course of combustion.
- the exhaust gases discharged from the heating hood for further thermal utilization of a heat exchanger for preheating the heat transfer gas can be supplied.
- a heating hood for carrying out a method according to the invention, which has an outer jacket, an insulating layer, burner and at least one outlet, wherein the burners burn a heat carrier gas containing exothermic oxidizable gas and the resulting exhaust gases are dissipatable via the at least one outlet, wherein the burners are arranged within the heating hood so that a substantially uniform heat distribution is ensured within the heating hood.
- the burners are arranged in at least two levels within the heating hood.
- the burners are each individually controllable.
- individually controllable means that the burners can be switched on and off individually as well as with regard to the composition and the volume flow of the gas mixture supplied to them.
- this is designed so that it can be integrated in a known from the prior art container for receiving a coolant in a precision casting process, for example by integration of the heating hood in the lid of such a container.
- the heating hood according to the invention may have a post-combustion zone in which unburned constituents of the exothermically oxidizable gas reacted in the burners and / or any other gaseous constituents of the exhaust gas discharged from the heating hood are after-burned.
- the post-combustion zone can either be located directly inside the heating hood or a separate post-combustion zone can be provided outside the heating hood.
- gas inlets can be provided within the heating hood, via which further gases such as protective or inert gases can be introduced into the heating hood.
- the exhaust gas for transmitting at least a portion of the thermal energy contained can be performed via a heat exchanger in one embodiment.
- the waste heat can serve both for preheating the combustion air required in the burners, the exothermic oxidizable gas or the additional heating gas optionally supplied via the additional gas inlets further gases.
- the entire gas flow does not necessarily have to be heated, but instead a bypass line can be provided for bypassing the heat exchanger.
- the heating hood on mixing valves for adjusting a ratio between the gas passed through the heat exchanger and cold gas.
- the heating hood according to the invention may also have temperature sensors for detecting the temperature within the heating hood.
- the temperature sensor can pass a measurement signal corresponding to the temperature to a control device which controls the burners and / or the mixing valves for mixing cold and preheated gas as a function of the temperature determined in the heating hood.
- Fig. 1 shows a heating hood 1 according to the invention for use in a precision casting process of the type described above.
- the heating hood 1 has an outer jacket 2, which is equipped on the inside with a refractory insulating layer.
- the outer shell 2 may be made of steel or other sufficiently temperature-resistant materials.
- the refractory insulating layer 3 may be formed, for example, of a ceramic coating or Schamottausmautation.
- the heating hood 1 according to the invention has burners 4, with which an exothermic oxidizable gas can be burned.
- the burners 4 can in this case be arranged in two superimposed planes. In such an embodiment, the burners in the different levels can be operated with different combustion ratios lambda.
- Fig. 2 shows a heating hood according to the invention, which is arranged within a coolant tank 13.
- the heating hood is integrated into the lid 18 of the coolant tank.
- the coolant tank 13 contains a coolant 15, which can be supplied or removed via inlet 14 and outlet 16.
- the coolant tank 13 can have auxiliary connections 17, through which, for example, protective gas can be introduced into the coolant tank 13, or which can serve to ventilate the coolant tank 13.
- the liquid level of the coolant 15 within the coolant tank 13 may be in the in Fig. 2 shown configuration through inlet 14 and outlet 16 are set so that the coolant level is flush with the lower edge of the heating hood.
- Fig. 3 shows a further embodiment of a heating hood 1 according to the invention, which in addition to the burners 4 gas inlets 9, through which additional gases such as inert or protective gases can be introduced into the heating hood.
- a post-combustion zone 5 is provided, to which a heat exchanger 7 is connected.
- the gas mixture supplied to the burners 4 and / or the gas which can be introduced into the heating hood via the gas inlets 7 can be preheated.
- the in Fig. 3 shown heating hood 1 temperature sensor 20, by means of which the temperature prevailing in the heating hood temperature can be determined.
- a plurality of temperature sensors 20 are provided in different areas of the heating hood 1.
- the temperature sensor 20 can be connected to a control unit which controls the burner 4 and / or mixing valves for adjusting the ratio of preheated by the heat exchanger 7 gas and cold gas and / or control valves for controlling the additional gas input depending on the temperature prevailing in the heating hood , As a result, an exact temperature control within the heating hood 1 according to the invention is possible.
- the mold to be arranged in the heating hood is heated uniformly by means of a heat transfer gas, so that radiation-dead spaces are heated sufficiently.
- the adjustable gas flow within the heating hood according to the invention ensures that any evaporating constituents of the coolant, which optionally have a reaction potential to the still liquid metal in the mold, are discharged as quickly as possible.
- FIGS. 4 and 5 show further embodiments of the heating hood according to the invention in which the burner 4 can be aligned in a deviating from the horizontal orientation angle of 3 to 10 °. Likewise, it may be provided according to the invention, to arrange the burner tangentially to the hood center. Such a design of the heating hood according to the invention, a flow of the heat transfer gas is achieved within the heating hood, which contributes to a uniform heat distribution.
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Furnace Details (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
Description
Die vorliegende Erfindung betrifft ein Verfahren gemäß Anspruch 1 sowie eine Vorrichtung gemäß Anspruch 6 zur Herstellung metallischer Gusskörper nach dem Feingussverfahren, insbesondere Gusskörper aus Aluminium oder aluminium-haltigen Legierungen. Vorteilhafte Weiterbildungen sind in den Unteransprüchen angegeben.The present invention relates to a method according to
Verfahren zur Herstellung metallischer Gusskörper nach dem Feingussverfahren sind aus dem Stand der Technik bekannt. Zur Herstellung von Gusskörpern mittels des Feingussverfahrens wird in der Regel von einem zu gießenden Objekt ein Wachsmodell gefertigt, welches anschließend mit einer keramischen Schale umhüllt wird. Dies kann beispielsweise durch Eintauchen des Wachsmodells in geeignete keramische Schlicker erfolgen. Hierbei können auch nacheinander unterschiedliche Schlicker aufgetragen werden. Anschließend wird das Wachsmodell ausgeschmolzen, und die keramische Form gebrannt. Hierdurch wird eine poröse Gießform erhalten, in welche metallische Schmelzen vergossen werden können. Nach Erstarren der metallischen Schmelze wird die Gießform zerstört und der Gusskörper kann entnommen werden. Das zuvor beschriebene Verfahren ermöglicht auch die Herstellung komplexer Gusskörper.Methods for producing metal castings by the precision casting method are known from the prior art. For the production of castings by means of the investment casting process, a wax model is usually produced by an object to be cast, which is then coated with a ceramic shell. This can be done, for example, by immersing the wax model in suitable ceramic slip. In this case, different slips can be applied successively. Subsequently, the wax model is melted out, and fired the ceramic form. As a result, a porous mold is obtained, in which metallic melts can be cast. After solidification of the metallic melt, the mold is destroyed and the casting can be removed. The method described above also allows the production of complex castings.
Ein Nachteil der beschriebenen Gusstechnik ist, dass die hergestellten keramischen Gießformen eine schlechte Wärmeleitfähigkeit besitzen und so zu einer relativ langen und ungeregelten Erstarrungszeit der Metallschmelze in der Gießform beitragen. Durch langsames Erstarren und Abkühlen entsteht jedoch in Abhängigkeit vom zu vergießenden Metall ein relativ grobkörniges Gefüge, welches zu verminderten mechanischen Eigenschaften führen kann.A disadvantage of the casting technique described is that the ceramic casting molds produced have a poor thermal conductivity and thus contribute to a relatively long and unregulated solidification time of the molten metal in the casting mold. However, due to slow solidification and cooling, depending on the metal to be cast, a relatively coarse-grained microstructure arises, which can lead to reduced mechanical properties.
Zur Verbesserung der geringen Wärmeleitfähigkeit der keramischen Gießformen wird mit der
Die
Mit der
Es ist daher die Aufgabe der vorliegenden Erfindung, ein Verfahren sowie eine Vorrichtung bereitzustellen, mit welchem die aus dem Stand der Technik bekannten Nachteile bei der Herstellung von metallischen Gusskörpern nach dem Feingussverfahren insbesondere hinsichtlich der Größe sowie der Gussteilgeometrie überwunden werden.It is therefore the object of the present invention to provide a method and a device with which known from the prior art Disadvantages in the production of metal castings after the investment casting process, especially in terms of size and the casting geometry to be overcome.
Gelöst wird diese Aufgabe hinsichtlich des Verfahrens durch ein Verfahren zur Herstellung eines metallischen Gusskörpers nach dem Feingussverfahren, wobei das zu gießende Metall oder die zu gießende Legierung in eine keramische Gießform mit porösen Wänden gegossen wird und die Gießform zur Abkühlung und Erstarrung der Schmelze von einem Ende aus beginnend stetig derart in ein Kühlmittel eingetaucht wird, dass die als Grenzfläche zwischen Schmelze und bereits erstarrtem Metall sich bildende Erstarrungsfront dem Kühlmittelspiegel nacheilt, welches dadurch gekennzeichnet ist, dass der noch oberhalb des Kühlmittelspiegels liegende Bereich der Gießform mittels eines Wärmeträgergases auf eine Temperatur oberhalb der Solidustemperatur des zu vergießenden Metalls oder der Legierung erwärmt wird. This object is achieved with respect to the method by a method for producing a metal casting by the investment casting method, wherein the casting metal or alloy to be cast is poured into a ceramic mold with porous walls and the mold for cooling and solidification of the melt from one end Starting from constantly immersed in such a way in a coolant, that as the interface between the melt and already solidified metal solidifying front lags the coolant level, which is characterized in that the lying still above the coolant level region of the mold by means of a heat transfer gas to a temperature above the Solidus temperature of the metal or alloy to be cast is heated.
Das hierbei einzusetzende Wärmeträgergas enthält ein exotherm oxidierbares Gas sowie Sauerstoff. Geeignete exotherm oxidierbare Gase sind beispielsweise Wasserstoff, gasförmige Kohlenwasserstoffe wie Methan, Ethan, Propan, Butan, Ethen, Acetylen, oder auch Kohlenmonoxid sowie Mischungen dieser.The heat transfer gas to be used in this case contains an exothermically oxidizable gas and oxygen. Suitable exothermic oxidizable gases are, for example, hydrogen, gaseous hydrocarbons such as methane, ethane, propane, butane, ethene, acetylene, or else carbon monoxide, and mixtures of these.
Zusätzlich kann das Wärmeträgergas weitere Gase wie beispielsweise Edelgase, Halogenkohlenwasserstoffe, Ammoniak, Stickstoff, Kohlendioxid, Schwefelhalogenide oder Mischungen dieser enthalten. Hierbei können die weiteren im Wärmegas enthaltenden Gase als Schutz- oder Inertgase dienen, um eine Diffusion von Wasserstoff in die Metallschmelze bzw. den Gusskörper zu vermeiden.In addition, the heat transfer gas may contain other gases such as noble gases, halogenated hydrocarbons, ammonia, nitrogen, carbon dioxide, sulfur halides or mixtures thereof. In this case, the further gases containing the heat gas can serve as protective or inert gases in order to prevent diffusion of hydrogen into the molten metal or the cast body.
Das im Wärmeträgergas enthaltene exotherm oxidierbare Gas wird innerhalb einer Heizhaube direkt oxidiert, wodurch der über dem Kühlflüssigkeitsspiegel liegende Bereich der Gießform beheizt wird.The exothermic oxidizable gas contained in the heat transfer gas is directly oxidized within a heating hood, whereby the region of the casting mold located above the cooling liquid level is heated.
Erfindungsgemäß ist es vorgesehen, dass das Wärmeträgergas nach der exothermen Oxidierung des im Wärmeträgergas enthaltenen exotherm oxidierbaren Gases aus der Heizhaube zusammen mit eventuell verdampften Kühlmittelbestandteilen abgeführt und einer Nachverbrennung zugeführt wird. Hierbei kann es vorgesehen sein, dass die aus der Nachverbrennung entstehenden Abgase einem Wärmetauscher zugeführt werden, welcher zumindest einen Teil des frisch der Heizhaube zuzuführenden Wärmeträgergases vorwärmt. Hierdurch wird die thermische Nutzung des Energiegehaltes des exotherm oxidierbaren Gases maximiert, wodurch sich der Bedarf an exotherm oxidierbaren Gas im Wärmeträgergas reduziert.According to the invention, it is provided that after the exothermic oxidation of the exothermic oxidizable gas contained in the heat carrier gas, the heat carrier gas is removed from the heating hood together with possibly evaporated coolant constituents and fed to afterburning. In this case, it may be provided that the exhaust gases resulting from the afterburning are fed to a heat exchanger which preheats at least part of the heat transfer gas to be supplied fresh to the heating hood. As a result, the thermal utilization of the energy content of the exothermic oxidizable gas is maximized, thereby the need for exothermic oxidizable gas in the heat transfer gas is reduced.
In der Nachverbrennung selbst werden noch nicht vollständig oxidierte Reste des exotherm oxidierbaren Gases im Wärmeträgergas zusammen mit eventuell verdampften Bestandteilen des Kühlmittels verbrannt, um einen Austrag von noch nicht oxidierten Gas bzw. Kühlmittelbestandteilen zu vermeiden. Die Abgase der Nachverbrennung können nach thermischer Ausnutzung des Energiegehaltes im Wärmetauscher einer geeigneten Abgasreinigung zugeführt werden.In the afterburning itself not completely oxidized residues of the exothermic oxidizable gas are burned in the heat carrier gas together with any evaporated components of the coolant to avoid discharge of not yet oxidized gas or coolant components. After the thermal utilization of the energy content in the heat exchanger, the exhaust gases of the afterburning can be supplied to a suitable exhaust gas purification system.
Erfindungsgemäß kann es vorgesehen sein, dass die Temperatur innerhalb der Heizhaube bestimmt und als Regelgröße für den Gehalt an exotherm oxidierbaren Gas im Wärmeträgergas oder auch des Gehaltes an weiteren Gasen im Wärmeträgergas genutzt wird.According to the invention it can be provided that the temperature is determined within the heating hood and used as a controlled variable for the content of exothermally oxidizable gas in the heat carrier gas or the content of other gases in the heat transfer gas.
In einer Ausgestaltung des erfindungsgemäßen Verfahrens wird das exotherm oxidierbare Gas mittels Brennern im Zuge einer Direktoxidation innerhalb der Heizhaube verbrannt. In einer weiteren Ausgestaltung der Erfindung weist eine Heizhaube wenigstens zwei übereinander angeordnete Brenner bzw. Brennerebenen auf. Die einzelnen Brenner sind getrennt steuerbar und können in Abhängigkeit des Betriebszustandes der Heizhaube getaktet werden. Darüber hinaus kann das Verbrennungsverhältnis (Lambda) der einzelnen Brenner unterschiedlich eingestellt sein. In einer weiteren Ausgestaltung des erfindungsgemäßen Verfahrens ist das Verbrennungsverhältnis Lambda einer unteren Brennerebene < 1,0, die Brenner werden also mit einem unterstöchiometrischen Gas/Sauerstoff-Verhältnis betrieben, wohingegen das Verbrennungsverhältnis Lambda der oberen Brennerebene > 1,0 ist, also die Brenner mit einem überstöchiometrischen Gas/Luft-Verhältnis betrieben werden.In one embodiment of the method according to the invention, the exothermic oxidizable gas is burned by burners in the course of a direct oxidation within the heating hood. In a further embodiment of the invention, a heating hood has at least two burners or burner levels arranged one above the other. The individual burners can be controlled separately and can be clocked depending on the operating state of the heating hood. In addition, the combustion ratio (lambda) of the individual burners can be set differently. In a further embodiment of the method according to the invention, the combustion ratio lambda a lower burner level <1.0, the burners are thus operated with a substoichiometric gas / oxygen ratio, whereas the combustion ratio lambda the upper burner level> 1.0, ie the burner with be operated at a superstoichiometric gas / air ratio.
Durch eine solche Ausgestaltung des erfindungsgemäßen Verfahrens kann auf eine Nachverbrennung der aus der Heizhaube abgeführten Abgase verzichtet werden, da einerseits die mit der Heizhaube gegebenenfalls in Kontakt tretende Oberfläche des Kühlmittels aufgrund des unterstöchiometrischen Gas/Sauerstoffverhältnisses nicht oxidiert wird und andererseits verdampfende oxidationsfähige Bestandteile des Kühlmittelbades im Bereich der oberen, mit einem überstöchiometrischen Gas/LuftVerhältnis betriebenen Brennerebene direkt im Zuge einer Verbrennung oxidiert werden.Such an embodiment of the method according to the invention makes it possible to dispense with afterburning of the exhaust gases discharged from the heating hood since, on the one hand, the surface of the coolant passing into contact with the heating hood is not oxidized due to the substoichiometric gas / oxygen ratio and, on the other hand, evaporating oxidizable constituents of the coolant bath in the Area of the upper, with a superstoichiometric gas / air ratio operated burner level directly oxidized in the course of combustion.
Auch bei der zuvor beschriebenen Ausgestaltung des erfindungsgemäßen Verfahrens kann es vorgesehen sein, dass die aus der Heizhaube abgeführten Abgase zur weiteren thermischen Ausnutzung einem Wärmetauscher zur Vorwärmung des Wärmeträgergases zugeführt werden.Also in the above-described embodiment of the method according to the invention, it may be provided that the exhaust gases discharged from the heating hood for further thermal utilization of a heat exchanger for preheating the heat transfer gas can be supplied.
Erfindungsgemäß ist es vorgesehen, die Kühlmittelzusammensetzung so zu wählen, dass die Gefahr von Brandüberschlägen oder Verpuffungen ausgeschlossen ist.According to the invention it is provided to select the coolant composition so that the risk of fire flashovers or deflagration is excluded.
Hinsichtlich der Vorrichtung wird die der Erfindung zugrunde liegende Aufgabe durch eine Heizhaube zur Durchführung eines erfindungsgemäßen Verfahrens gelöst, welche einen äußeren Mantel, eine Isolierschicht, Brenner und wenigstens einen Auslass aufweist, wobei die Brenner ein exotherm oxidierbares Gas enthaltendes Wärmeträgergas verbrennen und die dabei entstehenden Abgase über den wenigstens einen Auslass abführbar sind, wobei die Brenner innerhalb der Heizhaube so angeordnet sind, dass eine im Wesentlichen gleichmäßige Wärmeverteilung innerhalb der Heizhaube gewährleistet ist.With regard to the device, the object underlying the invention is achieved by a heating hood for carrying out a method according to the invention, which has an outer jacket, an insulating layer, burner and at least one outlet, wherein the burners burn a heat carrier gas containing exothermic oxidizable gas and the resulting exhaust gases are dissipatable via the at least one outlet, wherein the burners are arranged within the heating hood so that a substantially uniform heat distribution is ensured within the heating hood.
In einer Ausgestaltung der erfindungsgemäßen Heizhaube sind die Brenner in wenigstens zwei Ebenen innerhalb der Heizhaube angeordnet. Die Brenner sind jeweils einzeln steuerbar. Hierbei ist unter einzeln steuerbar zu verstehen, dass die Brenner sowohl einzeln ein- und ausschaltbar sind, als auch hinsichtlich der Zusammensetzung und des Volumenstromes des ihnen zugeführten Gasgemisches steuerbar sind.In one embodiment of the heating hood according to the invention, the burners are arranged in at least two levels within the heating hood. The burners are each individually controllable. In this case, individually controllable means that the burners can be switched on and off individually as well as with regard to the composition and the volume flow of the gas mixture supplied to them.
In einer weiteren Ausgestaltung der erfindungsgemäßen Heizhaube ist diese so gestaltet, dass sie in einen aus dem Stand der Technik bekannten Behälter zur Aufnahme eines Kühlmittels in einem Feingussverfahren integrierbar ist, beispielsweise durch Integration der Heizhaube in den Deckel eines solchen Behälters.In a further embodiment of the heating hood according to the invention, this is designed so that it can be integrated in a known from the prior art container for receiving a coolant in a precision casting process, for example by integration of the heating hood in the lid of such a container.
Die erfindungsgemäße Heizhaube kann eine Nachverbrennungszone aufweisen, in welcher nicht verbrannte Bestandteile des in den Brennern umgesetzten exotherm oxidierbaren Gases und/oder etwaige andere gasförmige Bestandteile des aus der Heizhaube abgeführten Abgases nachverbrannt werden. Hierbei kann die Nachverbrennungszone entweder sich direkt innerhalb der Heizhaube befinden, oder es kann eine separate Nachverbrennungszone außerhalb der Heizhaube vorgesehen sein.The heating hood according to the invention may have a post-combustion zone in which unburned constituents of the exothermically oxidizable gas reacted in the burners and / or any other gaseous constituents of the exhaust gas discharged from the heating hood are after-burned. In this case, the post-combustion zone can either be located directly inside the heating hood or a separate post-combustion zone can be provided outside the heating hood.
Des Weiteren können innerhalb der Heizhaube Gaseinlässe vorgesehen sein, über welche weitere Gase wie beispielsweise Schutz- oder Inertgase in die Heizhaube eingeleitet werden können.Furthermore, gas inlets can be provided within the heating hood, via which further gases such as protective or inert gases can be introduced into the heating hood.
Bei der erfindungsgemäßen Heizhaube kann in einer Ausgestaltung das Abgas zur Übertragung zumindest eines Teils der enthaltenen thermischen Energie über einen Wärmetauscher geführt werden. Die Abwärme kann sowohl zum Vorwärmen der in den Brennern benötigten Verbrennungsluft, des exotherm oxidierbaren Gases oder der der Heizhaube über die zusätzlichen Gaseinlässe gegebenenfalls zugeführten weiteren Gase dienen. Hierbei muss nicht zwangsläufig der gesamte Gasstrom erwärmt werden, sondern es kann eine Bypassleitung zur Umgehung des Wärmetauschers vorgesehen sein. In einer solchen Ausgestaltung weist die Heizhaube Mischventile zur Einstellung eines Verhältnisses zwischen über den Wärmetauscher geleiteten Gas und kaltem Gas auf.In the heating hood according to the invention, the exhaust gas for transmitting at least a portion of the thermal energy contained can be performed via a heat exchanger in one embodiment. The waste heat can serve both for preheating the combustion air required in the burners, the exothermic oxidizable gas or the additional heating gas optionally supplied via the additional gas inlets further gases. In this case, the entire gas flow does not necessarily have to be heated, but instead a bypass line can be provided for bypassing the heat exchanger. In such an embodiment, the heating hood on mixing valves for adjusting a ratio between the gas passed through the heat exchanger and cold gas.
Die erfindungsgemäße Heizhaube kann darüber hinaus Temperaturfühler zur Erfassung der Temperatur innerhalb der Heizhaube aufweisen. Die Temperaturfühler können ein der Temperatur entsprechendes Messsignal an eine Steuereinrichtung weitergeben, welche in Abhängigkeit der in der Heizhaube bestimmten Temperatur die Brenner und/oder die Mischventile zur Mischung von kalten und vorgewärmten Gas steuert.The heating hood according to the invention may also have temperature sensors for detecting the temperature within the heating hood. The temperature sensor can pass a measurement signal corresponding to the temperature to a control device which controls the burners and / or the mixing valves for mixing cold and preheated gas as a function of the temperature determined in the heating hood.
Darüber hinaus können erfindungsgemäß weitere Messeinrichtungen wie beispielsweise eine Lambda-Sonde zur Bestimmung der Zusammensetzung der aus der erfindungsgemäßen Heizhaube abgeführten Abgase vorgesehen sein, welche ebenfalls mit der Steuereinrichtung verbunden ist, so dass die durch diese Messeinrichtungen ermittelten Messwerte als Steuergröße für die Steuerung der Brenner und/oder der Mischventile dienen können.
- Fig. 1:
- zeigt einen Querschnitt durch eine erfindungsgemäße Heizhaube.
- Fig. 2:
- zeigt einen Querschnitt durch eine in einen Kühlmittelbehälter integrierte erfindungsgemäße Heizhaube.
- Fig. 3:
- zeigt einen Querschnitt einer erfindungsgemäßen Heizhaube, welche eine außerhalb der Heizhaube angeordnete Nachverbrennungszone sowie einen Wärmetauscher aufweist.
- Fig. 4:
- zeigt eine erfindungsgemäße Heizhaube im Querschnitt, in welcher die Brenner in einem von der horizontalen Ausrichtung abweichenden Winkel ausgerichtet sind.
- Fig. 5:
- zeigt den Querschnitt in horizontaler Ebene einer erfindungsgemäßen
- Fig. 1:
- shows a cross section through a heating hood according to the invention.
- Fig. 2:
- shows a cross section through an integrated into a coolant tank inventive heating hood.
- 3:
- shows a cross section of a heating hood according to the invention, which has a arranged outside the heating hood post-combustion zone and a heat exchanger.
- 4:
- shows a heating hood according to the invention in cross section, in which the burners are aligned at an angle deviating from the horizontal orientation.
- Fig. 5:
- shows the cross section in the horizontal plane of an inventive
Darüber hinaus weist die in
Durch die erfindungsgemäße Ausgestaltung einer Heizhaube wird die in der Heizhaube anzuordnende Gießform mittels eines Wärmeträgergases gleichmäßig aufgeheizt, so dass auch strahlungstote Räume hinreichend erwärmt werden. Darüber hinaus stellt die innerhalb der erfindungsgemäßen Heizhaube einstellbare Gasführung sicher, dass eventuell abdampfende Bestandteile des Kühlmittels, welche gegebenenfalls ein Reaktionspotential zu dem noch flüssigen Metall in der Gießform aufweisen, schnellstmöglich ausgetragen werden.Due to the inventive design of a heating hood, the mold to be arranged in the heating hood is heated uniformly by means of a heat transfer gas, so that radiation-dead spaces are heated sufficiently. In addition, the adjustable gas flow within the heating hood according to the invention ensures that any evaporating constituents of the coolant, which optionally have a reaction potential to the still liquid metal in the mold, are discharged as quickly as possible.
Die
- 11
- Heizhaubeheating cover
- 22
- äußerer Mantelouter coat
- 33
- Isolierschichtinsulating
- 44
- Brennerburner
- 55
- Nachverbrennungafterburning
- 66
- Auslassoutlet
- 77
- Wärmetauscherheat exchangers
- 99
- Gaseinlässegas inlets
- 1313
- Behältercontainer
- 1414
- ZulaufIntake
- 1515
- Kühlmittelcoolant
- 1616
- Ablaufprocedure
- 1717
- Nebenanschlussshunt
- 2020
- Temperaturfühlertemperature sensor
Claims (15)
- A method for producing a metallic casting in accordance with the lost-wax casting process, wherein the metal to be cast or the alloy to be cast is poured into a ceramic casting mould with porous walls and the casting mould is from one end onward steadily immersed in a cooling medium in order to cool and solidify the molten metal, namely in such a way that the solid-liquid interface being formed as boundary surface between the molten metal and the already solidified metal lags the cooling medium level, characterized in that the region of the casting mould that still lies above the cooling medium level is heated to a temperature above the solidus temperature of the metal or the alloy to be cast within a heating mantle by means of a heat transfer gas, wherein the heat transfer gas contains oxygen, as well as an exothermally oxidizable gas.
- The method according to Claim 1, wherein the heat transfer gas contains an exothermally oxidizable gas in the form of a gas that is selected from the group consisting of hydrogen, gaseous hydrocarbons, carbon monoxide or mixtures thereof.
- The method according to one of Claims 1 or 2, wherein the heat transfer gas contains at least one other gas of the group consisting of noble gases, halogenated hydrocarbons, ammonia, nitrogen, carbon dioxide, sulphur halides or mixtures thereof.
- The method according to Claim 1, wherein the region of the casting mould that still lies above the cooling medium level is heated by means of a heating mantle, in which the exothermally oxidizable gas in the heat transfer gas is exothermally oxidized.
- The method according to Claim 4, wherein the gaseous reaction products created due to the exothermal oxidation are withdrawn from the heating mantle and fed to a post-combustion.
- A heating mantle for carrying out the method according to one of Claims 1 to 5, featuring an outer mantle (2), an insulating layer (3), burners (4) and at least one outlet (6), wherein a heat transfer gas that contains an exothermally oxidizable gas can be burned in the burners (4) and the waste gases created during this process can be discharged through the outlet (6), wherein the burners (4) are arranged within the heating mantle (1) in such a way that a uniform heat distribution within the heating mantle is ensured, and wherein this heating mantle features a post-combustion zone (5) for the post-combustion of the waste gases discharged from the heating mantle (1).
- The heating mantle according to Claim 6, wherein the burners (4) are arranged within the heating mantle (1) on at least two levels.
- The heating mantle according to one of Claims 6 or 7, wherein the burners (4) can be individually controlled.
- The heating mantle according to one of Claims 6 to 8, wherein the heating mantle is integrated into the cover of a container (13) for accommodating a cooling medium (15).
- The heating mantle according to one of Claims 6 to 9, wherein gas inlets (9) are provided within the heating mantle and inert gas can be introduced into the heating mantle through these gas inlets.
- The heating mantle according to one of Claims 6 to 10, featuring a heat exchanger (7) for transferring at least part of the thermal energy contained in the waste gases discharged from the heating mantle (1) to the heat transfer gas.
- The heating mantle according to Claim 11, wherein a bypass line is provided for bypassing the heat exchanger.
- The heating mantle according to Claim 12, wherein mixing valves are provided that make it possible to adjust the ratio between heat transfer gas conveyed through the heat exchanger (9) and cold heat transfer gas.
- The heating mantle according to one of Claims 6 to 13, featuring temperature sensors (20) for measuring the temperature within the heating mantle (1).
- The heating mantle according to Claim 14, wherein the temperature sensors (20) are connected to a control unit that controls the burners (4), as well as the mixing valves for adjusting the ratio between heat transfer gas conveyed through the heat exchanger (9) and cold heat transfer gas, in dependence on the temperature measured within the heating mantle (1) by the temperature sensors (4).
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
ES08004045T ES2393415T3 (en) | 2008-03-05 | 2008-03-05 | Procedure and device for the manufacture of metal foundries according to the precision casting procedure |
PL08004045T PL2098314T3 (en) | 2008-03-05 | 2008-03-05 | Method and apparatus for producing metallic casting moulds using the lost wax casting method |
PT08004045T PT2098314E (en) | 2008-03-05 | 2008-03-05 | Method and apparatus for producing metallic casting moulds using the lost wax casting method |
EP08004045A EP2098314B1 (en) | 2008-03-05 | 2008-03-05 | Method and apparatus for producing metallic casting moulds using the lost wax casting method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP08004045A EP2098314B1 (en) | 2008-03-05 | 2008-03-05 | Method and apparatus for producing metallic casting moulds using the lost wax casting method |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2098314A1 EP2098314A1 (en) | 2009-09-09 |
EP2098314B1 true EP2098314B1 (en) | 2012-09-19 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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EP08004045A Active EP2098314B1 (en) | 2008-03-05 | 2008-03-05 | Method and apparatus for producing metallic casting moulds using the lost wax casting method |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP2098314B1 (en) |
ES (1) | ES2393415T3 (en) |
PL (1) | PL2098314T3 (en) |
PT (1) | PT2098314E (en) |
Family Cites Families (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE3629079A1 (en) | 1986-08-27 | 1988-03-03 | Thyssen Industrie | Method for the precision casting of castings in a ceramic shell mould |
DE4216870C2 (en) | 1992-05-22 | 1994-08-11 | Titan Aluminium Feingus Gmbh | Process for the production of a metallic casting by the precision casting process |
US6311760B1 (en) * | 1999-08-13 | 2001-11-06 | Asea Brown Boveri Ag | Method and apparatus for casting directionally solidified article |
US7448428B2 (en) * | 2005-10-14 | 2008-11-11 | Pcc Airfoils, Inc. | Method of casting |
-
2008
- 2008-03-05 EP EP08004045A patent/EP2098314B1/en active Active
- 2008-03-05 ES ES08004045T patent/ES2393415T3/en active Active
- 2008-03-05 PT PT08004045T patent/PT2098314E/en unknown
- 2008-03-05 PL PL08004045T patent/PL2098314T3/en unknown
Also Published As
Publication number | Publication date |
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PL2098314T3 (en) | 2013-02-28 |
PT2098314E (en) | 2012-10-04 |
EP2098314A1 (en) | 2009-09-09 |
ES2393415T3 (en) | 2012-12-21 |
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