CASTING CORE REMOVAL THROUGH THERMAL CYCLING

Abstract

A method of removing a core of a cast component includes providing a casting that includes a silica based ceramic core in a temperature controlled closed volume; cycling temperature between a first temperature and a second temperature within the temperature controlled closed volume that repeatedly subjects the silica based ceramic core to a beta-to-alpha cristobalite transition that induces microfractures in the silica based ceramic core; and after the cycling temperature, chemically dissolving the silica based ceramic core from the casting.

Claims

1. A method of removing a core of a cast component, comprising: providing a casting that includes a silica based ceramic core in a temperature controlled closed volume; cycling temperature between a first temperature and a second temperature within the temperature controlled closed volume that repeatedly subjects the silica based ceramic core to a beta-to-alpha cristobalite transition that induces microfractures in the silica based ceramic core; and after the cycling temperature, in a volume different than the temperature controlled closed volume chemically dissolving the silica based ceramic core from the casting.

2. The method of claim 1 where the temperature controlled closed volume comprises at least one of an autoclave, a gas fired kiln or a resistively heated furnace box.

3. The method of claim 1 where the temperature controlled closed volume comprises a temperature controlled closed pressure volume.

4. The method of claim 1, where the first temperature is 175 degrees C. and the second temperature is 300 degrees C.

5. The method of claim 1, where the first temperature is less than 200 degrees C. and the second temperature is at least 275 degrees C.

6. A method of removing a core of an airfoil cast component, comprising: inserting the airfoil cast component, which includes a silica based ceramic core, into a temperature controlled vessel; cycling temperature, within the temperature controlled vessel, between a first temperature and a second temperature a plurality of times that repeatedly subjects the silica based ceramic core to at least one phase transition that induces microfractures in the silica based ceramic core; and after the cycling temperature, in a vessel different than the temperature controlled vessel chemically dissolving the silica based ceramic core from the airfoil cast component.

7. The method of claim 6, where the temperature controlled vessel comprises an autoclave.

8. The method of claim 6, where the first temperature is less than 200 degrees C. and the second temperature is at least 275 degrees C.

9. The method of claim 8, where the plurality of times is at least five.

10. The method of claim 8, where the plurality of times is at least ten.

11. The method of claim 9, where repeatedly cycling between the second temperature, where the core is transitioned to beta cristobalite phase, and the first temperature, where the core is transitioned to alpha cristobalite phase, repeatedly subjects the core to beta-to-alpha transitions that induce the microfractures in the core.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0020] FIG. 1A illustrates a cross-section through a prior art airfoil.

[0021] FIG. 1B illustrates a cross-section through a prior art core used to fabricate the airfoil illustrated in FIG. 1A.

[0022] FIG. 1C illustrates a cross section through a casting core as shown in FIG. 1B along with a surrounding prior art integral shell mold.

[0023] FIG. 2 illustrates an exemplary method for removal/dissolution of the casting core.

[0024] FIG. 3 is a plot of temperature versus time associated with the exemplary method illustrated in FIG. 2.

DETAILED DESCRIPTION

[0025] It is noted that various connections and steps are set forth between elements in the following description and in the drawings (the contents of which are incorporated in this specification by way of reference). It is noted that these connections and steps are general and, unless specified otherwise, may be direct or indirect and that this specification is not intended to be limiting in this respect. A coupling between two or more entities may refer to a direct connection or an indirect connection. An indirect connection may incorporate one or more intervening entities or a space/gap between the entities that are being coupled to one another.

[0026] Aspects of the disclosure may be applied in connection with a gas turbine engine.

[0027] FIG. 2 illustrates an exemplary method 100 for removal/dissolution of casting cores, for example during the manufacturing of an airfoil such as a gas turbine engine turbine blade, U.S. Patent Application Publication No. 2005/0258577 entitled Method of Producing Unitary Multi-Element Ceramic Casting Cores and Integral Core/Shell System, assigned to the assignee of the present application, is hereby incorporated by reference. The method 100 includes a step 102 of forming a cast component (e.g., an airfoil such as a turbine blade) that includes a ceramic core. The component may be the core assembly 70 illustrated in FIG. 1B surrounded by the ceramic mold 80, where the shape of the cavity 81 corresponds to the airfoil illustrated in FIG. 1A.

[0028] Step 102 includes forming a cast component that includes a ceramic core. Silica based cores undergo a phase transformation during the casting process from amorphous silica to the crystalline phase cristobalite. Subsequent to this phase transformation, in step 104 the cast component (FIG. 1C) containing the core 70 (FIG. 1C) is placed in a temperature controlled volume (e.g., a heated pressure vessel, an autoclave, gas fired kiln, resistively heated box furnace etc.). The temperature within the volume is brought from ambient temperature T.sub.0 to a first temperature T.sub.1 (e.g., 175-200 degrees C.). T.sub.1 is defined as a temperature such that the equilibrium phase of cristobalite is alpha cristobalite. T.sub.1 can be equal to ambient temperature T.sub.0; however this is not the preferred method as it requires an inefficiently wide transition range. In step 106 the temperature is then increased to a second temperature T.sub.2 (e.g., 275-300 degrees C.). T.sub.2 is defined as a temperature such that the equilibrium phase of cristobalite is beta cristobalite. The heating from ambient temperature T.sub.0 to T.sub.2 can be done continuously and does not require a dwell at T.sub.1. As T.sub.2 is higher than T.sub.1 the temperature will inherently pass T.sub.1 on heating from T.sub.0 to T.sub.2. FIG. 3 illustrates a plot of temperature versus time of the temperature cycling illustrated in FIG. 2. In step 108 the temperature within the volume is then decreased to the first temperature T.sub.1. A pyrometer may be used to monitor the surface temperature of the cast component. The decrease in temperature from the second temperature T.sub.2 to the first temperature T.sub.1 induces fractures in the ceramic core because of the volume change caused by the temperature change. Cristobalite undergoes a displacive phase transformation on cooling between the second temperature T.sub.2 and the first temperature T.sub.1. This beta-to-alpha cristobalite transition is accompanied by approximately a 4% volume change. Repeated thermally cycling between T.sub.2 and T.sub.1 subjects the casting core material 70 (FIGS. 1B and 1C) to repeated beta-to-alpha transitions that induce fractures in the casting core from the volume change. This micro fracturing of the core accelerates core removal/dissolution by caustic attack by opening paths in the core for caustic infiltration, thus reducing the time for core removal/dissolution.

[0029] The process of repeatedly increasing and decreasing the temperature within the volume as set forth in steps 106 and 108 may be repeated a number of times (e.g., 2-20 times times) to induce fractures from the volume change. Step 110 asks if the temperature cycling should be repeated. If yes, then the method 100 returns to step 106 to increase temperature in the vessel to the second temperature T.sub.2. Once the process of repeatedly increasing and decreasing the temperature within the volume has been performed the desired number of times and step 110 determines the cycling does not need to be repeated, then the method 100 terminates and proceeds onto chemically remove/dissolve the core. The test performed in step 100 may use a simple counter based upon the number of times the steps 106 and 108 have been performed in succession. Alternatively, visual assessment of the cast component may be made to determine if the silica core has largely been reduced from solid ceramic to loose powder. Alternatively, parts may be rotated or agitated after each cycle and progress may monitored by mass loss from loose core material falling from the casting.

[0030] The fracturing caused by the repeated cycling of temperature set forth in step 106 and 108 helps to reduce the amount of time required to chemically remove/dissolve the core.

[0031] In one exemplary method, an oven was heated to 650 degrees F. (343 degrees C.) and the cast component containing the core was placed in the oven until heated to at least 290 degrees C. The cast component containing the core was removed and allowed to cool. When the temperature on the surface of the cast component was below 190 degrees C. the component was returned to the heated oven and heated to at least 290 degrees C. The heated component was removed again from the oven and allowed to air cool. The process of heating to above 290 degrees C. and then allowing to cool to below 190 degrees C. was performed for ten (10) cycles before caustic core removal.

[0032] The higher and lower temperature bound can be varied significantly so long as the upper temperature, T.sub.0, results in the core predominantly transitioning to the beta cristobalite phase and the lower temperature, T.sub.1, results in the core predominantly transitioning to the alpha cristobalite phase. The exact temperatures will be dependent on the precise core formulation and thermal history. The beta-to-alpha cristobalite transition temperature may vary over a wide range (e.g., 200-250 degrees C.) depending on impurity content and thermal history of the base silica material. Any selection of T.sub.2 above this transition point and T.sub.1 below this transition point would be effective.

[0033] Although the different non-limiting embodiments have specific illustrated components, the embodiments of this invention are of limited to those particular combinations. It is possible to use some of the components or features from any of the non-limiting embodiments in combination with features or components from any of the other non-limiting embodiments. For example, it is contemplated that the dirt separator for internally cooled components disclosed herein it not limited to use in vanes and blades, but rather may also be used in combustor components or anywhere there may be dirt within an internal flowing passage.

[0034] It should be understood that like reference numerals identify corresponding or similar elements throughout the several drawings. It should also be understood that although a particular component arrangement is disclosed in the illustrated embodiment, other arrangements will benefit herefrom.

[0035] The foregoing description is exemplary rather than defined by the features within. Various non-limiting embodiments are disclosed herein, however, one of ordinary skill in the art would recognize that various modifications and variations in light of the above teachings will fall within the scope of the appended claims. It is therefore to be understood that within the scope of the appended claims, the disclosure may be practiced other than as specifically described. For that reason the appended claims should be studied to determine true scope and content.