METHOD AND APPARATUS FOR PRODUCING CASTING SHELL
20220379370 · 2022-12-01
Inventors
Cpc classification
B22C9/12
PERFORMING OPERATIONS; TRANSPORTING
B22C1/165
PERFORMING OPERATIONS; TRANSPORTING
International classification
B22C9/12
PERFORMING OPERATIONS; TRANSPORTING
B22C1/16
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A ceramic casting shell is formed by a method comprising the steps of coating a wax former with one or more layers of a ceramic slurry; drying the or each layer of ceramic slurry; wherein the dried layer or layers of ceramic slurry form a ceramic shell; applying over the ceramic shell, a coating of a polymer material; heating the formed assembly to melt and remove the wax former, wherein the polymer coating acts as a strengthening layer to the ceramic shell during the wax removal process; and subsequent to removal of the wax former, heating the ceramic shell to melt and remove the polymer coating. The polymer coating is preferably the outer coating of the ceramic shell. The polymer coating may be applied by spraying, dipping or painting onto the ceramic shell.
Claims
1. A method of forming a ceramic casting shell comprising the steps of: coating a wax former with one or more layers of a ceramic slurry; drying each layer of ceramic slurry, thereby forming a ceramic shell; applying a coating of a polymer material over the ceramic shell; heating the ceramic shell to melt and remove the wax former, wherein the polymer coating strengthens the ceramic shell during the wax removal process; following removal of the wax former, heating the ceramic shell to melt and remove the polymer coating.
2. The method of claim 1 wherein the polymer coating defines the outer coating of the ceramic shell.
3. The method of claim 1 wherein the polymer coating is a distinct layer having no or negligible ceramic material therein.
4. The method of claim 1 further including the step of firing the ceramic shell, wherein the polymer coating is removed during or prior to firing of the ceramic shell.
5. The method of claim 1 wherein the polymer coating is applied by one of: spraying, dipping and painting onto the ceramic shell.
6. The method of claim 1 wherein the polymer coating is dried in air or cured by UV curing.
7. The method of claim 1 wherein the polymer material used for the coating has a viscosity at ambient temperature with no shear of one of: at least 0.25 g/cm/s (25 centipoise), at least 2.50 g/cm/s (250 centipoise), and at least 5.0 g/cm/s (500 centipoise).
8. The method of claim 1 wherein the polymer material has one of: less than 35% w/w of refractory material; less than 20% w/w of refractory material; less than 10% w/w; less than 5% w/w; with the balance being water.
9. The method of claim 1 wherein the polymer material includes a polyvinyl alcohol, a styrene butadiene polymer, an acrylic polymer, an epoxy resin, a latex, or any combination thereof.
10. The method of claim 1 wherein the polymer coating is applied to only a portion of the ceramic shell.
11. The method of claim 1 further including the step, following removal of the polymer coating, of producing a cast article by use of the ceramic shell.
12. The method of claim 1 further including the steps of: following removal of the polymer coating, filling the ceramic shell with casting material; following hardening of the casting material, removing the ceramic shell to reveal a cast article.
13. A cast article formed by the method of claim 12.
14. A system for forming a ceramic casting shell comprising: a ceramic shell forming station configured to coat a wax former with one or more layers of a ceramic slurry; a drying station configured to dry each layer of ceramic slurry, thereby forming a ceramic shell; a coating station configured to apply a polymer coating over the ceramic shell; a first heating station configured to heat the coated ceramic shell to melt and remove the wax former, wherein the polymer coating defines a strengthening layer for the ceramic shell during the wax removal process; a second heating station configured to heat the ceramic shell after removal of the wax former to melt and remove the polymer coating.
15. The system of claim 14 wherein the stations are physically separate.
16. The system of claim 14 wherein at least two of the stations are combined in a common unit or chamber.
17. The system of claim 14 wherein the coating station is configured to apply the polymer coating to define an outer layer on the ceramic shell.
18. The system of claim 14 wherein the heating station is configured to heat to a temperature lower than firing temperature to thereby remove the polymer coating.
19. The system of claim 14 wherein the coating station includes one of: a spray device, a dipping bath and a painting device for applying the polymer coating over the ceramic shell.
20. The system of claim 14 further including a polymer coating drying station including an air drier or a UV curing device.
21. The system of claim 14 wherein the polymer coating station comprises a polymer coating source containing at least one polymer material having one of: less than 35% w/w of refractory material, less than 20% w/w of refractory material, less than 10% w/w of refractory material, and less than 5% w/w) of refractory material, with the balance being water; and the polymer material including one of: a polyvinyl alcohol, a styrene butadiene polymer, an acrylic polymer, an epoxy resin, a latex, or any combination thereof.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0074] Embodiments of the present invention are described below, by way of example only, with reference to the accompanying drawings in which:
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TERMINOLOGY
[0099] Green Strength refers to the shell strength prior to elevated heating (>800° C.), in other words at temperatures <180° C. used for dewaxing.
[0100] Hot Strength: refers to the shell strength at elevated temperatures (>500° C.)
[0101] Post Fired strength: refers to the shell strength after pre-cast firing but at a temperature <100° C.
First Example of Testing Method
[0102] To evaluate the capability of the shell to cope with the dewax stage of the process, general shell evaluation has been carried out using a modulus-of-rupture (MoR) test (see
[0103] A disadvantage of the test is that it does not perfectly replicate the conditions during dewax in terms of the loads placed on the shell by the wax expansion. The MoR test places one half of the shell thickness in tension, as the mold experiences at dewax, and the other half is in compression. As ceramics are always stronger in compression than tension then this effectively removes half the thickness from being evaluated during the test as it will never be the site of failure.
[0104] This has led to discussion within the investment casting community about the correct way to test MoR bars as the test either evaluates the capabilities of the face coat or the seal coat to withstand dewax. As the test will never replicate the real situation then it is not clear that this discussion will be resolved.
[0105] Also, the ceramic shell, when it cracks at dewax, predominantly fails from the edges of the wax. These edges act in two ways to enhance failure at dewax; firstly, they concentrate the stress in these areas making them more demanding in terms of the load; and secondly the shell build at edges is usually thinner than in plane sections so there is less material to carry the load.
[0106] In this invention the shell is preferably strengthened at its outer surface. If the MoR test is used in the most common application, whereby the face coat is placed in tension, then the test will not be designed to identify any advantage for the reinforcing coat. If the MoR test is conducted with the outer face in tension then the benefit of the reinforcement can be seen. This is due to the nature of the MoR tests as outlined above rather than any inherent issue with the reinforcement. During the dewax phase of the process the shell mold will be in tension throughout the thickness and as such the reinforcement will be of benefit.
[0107] The MoR test is, however, useful in the design of ceramic molds and in providing an early assessment of the benefits of the teachings herein.
Practical Testing
[0108] In addition to MoR testing, the applicant has carried out sample testing on a variety of shell structures. These are described below in connection with the photographs of
EXAMPLES
[0109] The shell molds used for evaluating the teachings herein were manufactured using a standard investment process with the shell molds being formed on wax patterns allowing modulus of rupture bars to be produced. The process steps are well defined in the literature. The shell molds were made in the following manner:
[0110] Prime coat: polymer enhanced silica binder system (Primcote Plus manufactured by Ransom & Randolph LLC or Remasol Adbond Advantage manufactured by Remet Corp, 80% loading of zirconium silicate flour, zirconium silicate stucco)
[0111] Intermediate coat: polymer enhanced silica binder system, 60% loading of silica flour, 50-100 mesh fused silica
[0112] Three back-up coats: polymer enhanced silica binder system, 60% loading of silica flour, aluminosilicate 47-22S
[0113] Seal coat: polymer enhanced silica binder system, 60% loading of silica flour
[0114] Some of the test bars were treated with the polymeric seal coat to evaluate the performance of this addition.
[0115] The drying times were four hours between coats and 24 hours final dry.
[0116] Following the production of the dried shell molds the edges are removed and the ceramic bars released from the wax.
[0117] MoR tests were undertaken at room temperature on an electric load frame with a cross-head speed of 25.4 mm/min. The dimensions of the bars were measured with digital callipers. Multiple results were taken for each formulation and the results averaged.
[0118] The polymeric seal coats were made up as described below and added to the test bars.
Formulations:
[0119] 1. Baseline shell system with standard seal coat without polymeric seal coat
2. Baseline shell system without standard seal coat without polymeric seal coat
3. 15% by weight poly vinyl alcohol solution seal coat, 85% water, without standard seal
4. Mixture comprising: 24.2 wt % water, 0.8 wt % wetting agent, 0.4 wt % bactericide, 40% styrene butadiene, 29% poly vinyl alcohol, 4% cotton flock, 1.6% antifoam, without standard seal
5. Mixture comprising: 34.97 wt % water, 0.55 wt % a wetting agent, 0.28 wt % bactericide, 27.75% acrylic styrene butadiene, 32.57% poly vinyl alcohol, 2.77% cotton flock, 1.11% antifoam, without standard seal
6. Mixture comprising: 34.97 wt % water, 0.55 wt % a wetting agent, 0.28 wt % bactericide, 27.75% acrylic styrene butadiene, 32.57% poly vinyl alcohol, 2.77% cotton flock, 1.11% antifoam, with standard seal
[0120] The results of the modulus of rupture testing are shown in Table 1.
TABLE-US-00001 TABLE 1 Average Thickness Average MoR Average MoR Formulation (mm) (psi) (MPa) Improvement 1 6.50 897 6.19 — 2 5.93 775 5.34 — 3 6.47 1719 11.86 +121% 4 6.59 1387 9.56 +78% 5 6.29 1422 9.81 +83% 6 6.42 1420 9.79 +58%
[0121] Formulation 2 has no ceramic seal coat and can be seen to be weaker than formulation 1 which has a ceramic seal coat. However, the addition of the polymeric seal coats (Formulations 3, 4 and 5) to the shell build without a ceramic seal coat can be seen to have improved MoR results of at least 78% above the baseline result (formulation 2).
[0122] When the ceramic seal is in place the results show less improvement but are still 58% better (formulations 1 and 6). The results in Table 1 are averages; however, if significance testing is undertaken on the full data sets then it can be shown that the improvements are classed as highly significant.
[0123] Referring now to
[0124] The first part of the preferred method involves the preparation of the ceramic shell, which is typically formed by coating a wax former with a plurality of layers of a ceramic slurry. At step 100, a layer of ceramic slurry is coated over the wax former or over a previous ceramic layer, after which, at step 102, the newly applied ceramic slurry layer is dried. At step 104 it is determined whether the ceramic shell is of a sufficient thickness. This will typically be determined empirically and before the manufacture of the ceramic shell, using knowhow and principles well known in the art. If the ceramic shell is not yet of sufficient thickness, the process repeats step 100 and 102, until the shell is of sufficient thickness. Typically, a ceramic shell will comprise three of four layers, although these could be more in cases where the mold shape is such as to exhibit particularly large expansion forces during dewaxing and other process steps.
[0125] Once it is determined that the ceramic shell is of a sufficient thickness, the process passes to step 106, at which the process applies a polymer layer, as disclosed herein, preferably as the outermost surface of the ceramic shell. The polymer may be of any of the formulations and examples given herein. Optionally, prior to the application of the outer polymer layer, the ceramic shell may be coated with a conventional ceramic seal coat of a type known in the art, which would occur prior to step 106. The polymer layer may be applied in a variety of ways, for example by spraying, dipping or painting. It may be applied as a single layer or as multiple layers to form the final polymer coating. For this purpose, it is preferred that one layer of polymer coating is dried prior to application of any further layer. Drying maybe by air drying or any other suitable method. It is envisaged that UV drying could be particularly advantageous, as it can provide rapid curing of the polymer and as a consequence faster processing at this step.
[0126] The polymer coating material used for the coating preferably has a viscosity with no shear at ambient temperature of 22° C. of at least 0.25 g/cm/s (25 centipoise), more preferably of at least 2.5 g/cm/s (250 centipoise) and most preferably of at least 5.0 g/cm/s (500 centipoise) or greater. The higher the viscosity, the thicker the coat will be and the greater elasticity it will have.
[0127] At step 108 the process removes the was former from within the shell, by a conventional dewaxing process. This is typically carried out at a temperature up to 180° C., which causes the wax to melt and leak out of the surrounding shell. For this purpose, the ceramic shell is typically provided with one or more apertures to allow the wax to flow out of the shell. The dewaxing step 108 may be carried out by any of the methods described above, including by rapid heating of the ceramic shell. As described herein, as a consequence of the provision of the polymer coating, it has been found that the shell structure is much stronger than prior art structures and that there is significantly reduced incident of cracking of the ceramic shell during the dewaxing stage 108. Examples are provided below.
[0128] At step 110 the process removes the polymer outer coating. This is typically removed by heating the ceramic shell to a temperature of around 500° C., although this is dependent upon the melting temperature of the particular polymer used for the outer coating. After step 110, the surrounding shell is formed solely of ceramic layers. In the preferred embodiments, the ceramic layers may have no polymer constituents in them or only modest amounts of polymer, thereby reducing the existence of any voids within the ceramic shell of the type known in the prior art.
[0129] At step 112, the ceramic shell is fired, typically at a temperature of around 800° C., as disclosed herein.
[0130] It is to be understood that steps 110 and 112 could in effect be combined in a two-stage filing process, in which at a first stage of the heating the polymer outer coating is removed, by heating the shell to a lower temperature, and in a second stage, upon increasing heating temperature, the remaining ceramic shell is fired.
[0131] Once completed, the fired ceramic shell can be used for casting, at step 114, typically metal components. The casting can be by any of the well known methods.
[0132] It will be appreciated from the teachings herein that the cast components made by this process are likely to be more precisely manufactured as a result of the avoidance or significant reduction in defects caused during the dewaxing of the ceramic shell. Additionally, as demonstrated below, the process enables the manufacture of ceramic shells that are thinner than prior art shells and yet can still withstand the dewaxing process, and to do so much more effectively than other ceramic shell manufacturing methods. As a consequence of the use of a thinner shell, heat can be transferred faster into the casting. This can significantly speed up the casting process as well as making it more precise. As explained above, the ability to provide thinner shells also reduces the amount of material required for the manufacture of the shells and the time for manufacture, resulting in manufacturing savings and the shell making stage.
[0133] Referring now to
[0134] The apparatus also includes a polymer coating station 210 for applying a polymer outer coating to the formed ceramic shell, as previously described. The polymer coating station 210 may include a UV curing device 212, or other drying device, to dry the polymer coating. Instead of a UV curing device, an air drier or other suitable polymer coating drying device may be used. It is to be understood that the polymer coating station 210 may in some embodiments be a part of the ceramic shell station and in the form of a polymer applicator within the station 200.
[0135] In other embodiments, the polymer coating station may be a separate stage in the apparatus. In accordance with the disclosure herein, the polymer coating could be applied in a single layer or in multiple layers. The coating station 210 may be configured for either or both of these possibilities, such configurations being well within the ability of the skilled person.
[0136] The apparatus also includes a dewaxing station 220, of known form and as described herein. The dewaxing station 220 is configured to heat the formed ceramic shell (with the polymer outer coating) in order to remove the wax former. Dewaxing is typically carried out at temperatures up to 180° C.
[0137] The apparatus also includes a polymer coating removal station and a shell firing station 230. These may be separate units of the apparatus or, as previously described, could be a singular unit configured to operate first to remove polymer and then to fire the shell. The polymer coating removal station 230 is configured to heat the polymer coated ceramic shell to slightly above the melting temperature of the polymer, typically around 500° C., although this is dependent upon the nature of the polymer coating. The shell firing station is configured to fire the ceramic shell (after removal of the outer polymer coating) to a typical firing temperature of around 800° C. or more.
[0138] The apparatus may also include a casting station 240 for casting products using the ceramic shell formed at stations 200-230. It is to be understood that the casting station 240 may not be physically connected to the other parts of the apparatus. It may be a separate station, for example at the third party site.
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[0140] With reference to
[0141] The shells shown in
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[0143] With reference now to
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[0145] Referring now to
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[0148] The embodiment of
[0149] The examples described above and shown in
[0150] It is to be understood that although the above described embodiments of ceramic casting shells comprised an outer ceramic seal coat, such a seal coat is not necessary and other embodiments could be formed of layers of dried ceramic slurry and an outer polymer layer.
[0151] In accordance with the teachings herein, exemplary versions of the invention include the following features:
[0152] Feature 1. A method of forming a ceramic casting shell comprising the steps of:
[0153] coating a wax former with one or more layers of a ceramic slurry;
[0154] drying the or each layer of ceramic slurry;
[0155] wherein the dried layer or layers of ceramic slurry form a ceramic shell;
[0156] applying over the ceramic shell, a coating of a polymer material;
[0157] heating the formed assembly to melt and remove the wax former, wherein the polymer coating acts as a strengthening layer to the ceramic shell during the wax removal process;
[0158] subsequent to removal of the wax former, heating the ceramic shell to melt and remove the polymer coating.
[0159] Feature 2. A method according to feature 1, wherein the polymer coating is the outer coating of the ceramic shell.
[0160] Feature 3. A method according to feature 1 or 2, wherein the polymer coating is a distinct layer of the assembly having no or negligible ceramic material.
[0161] Feature 4. A method according to any preceding feature, wherein the polymer coating is removed during firing of the ceramic shell.
[0162] Feature 5. A method according to any one of features 1 to 3, wherein the polymer coating is removed prior to firing.
[0163] Feature 6. A method according to any preceding feature, wherein the polymer coating is applied by spraying, dipping or painting onto the ceramic shell.
[0164] Feature 7. A method according to any preceding feature, wherein the polymer coating is dried in air or cured by UV curing.
[0165] Feature 8. A method according to any preceding feature, wherein the polymer coating is applied as a single layer of polymer material.
[0166] Feature 9. A method according to any preceding feature, wherein the polymer coating is applied in a plurality of layers or passes.
[0167] Feature 10. A method according to any preceding feature, wherein the polymer material used for the coating has a viscosity at ambient temperature of at least 0.2 g/cm/s (20 centipoise) with no shear.
[0168] Feature 11. A method according to any preceding feature, wherein the polymer material used for the coating has a viscosity at ambient temperature with no shear of at least 0.25 g/cm/s (25 centipoise), preferably of at least 2.50 g/cm/s (250 centipoise), more preferably of at least 5.0 g/cm/s (500 centipoise).
[0169] Feature 12. A method according to any preceding feature, wherein the polymer coating comprises less than 35% w/w of refractory material.
[0170] Feature 13. A method according to any preceding feature, wherein the polymer coating is formed from a formulation including at least one polymer material, wherein the formulation includes less than 35% w/w of refractory material (preferably less than 20% w/w, more preferably less than 10% w/w, most preferably less than 5% w/w), with the balance being water.
[0171] Feature 14. A method according to any preceding feature, wherein the polymer coating is essentially free of refractory material.
[0172] Feature 15. A method according to any preceding feature, wherein the polymer material used for the coating includes a polyvinyl alcohol, a styrene butadiene polymer, an acrylic polymer, an epoxy resin, a latex, or any combination thereof.
[0173] Feature 16. A method according to feature 15, wherein the amount of the at least one polymer is at least 5% w/w, preferably at least 12% w/w, more preferably at least 24% w/w, and most preferably at least 35% w/w.
[0174] Feature 17. A method according to any preceding feature, wherein the polymer coating is applied to a part of the ceramic shell.
[0175] Feature 18. A method according to any one of features 1 to 16, wherein the polymer coating is applied to the whole of the ceramic shell.
[0176] Feature 19. A system for forming a ceramic casting shell comprising:
[0177] a ceramic shell forming station configured to coat a wax former with one or more layers of a ceramic slurry;
[0178] a drying station configured to dry the or each layer of ceramic slurry;
[0179] wherein the dried layer or layers of ceramic slurry form a ceramic shell;
[0180] a coating station configured to apply over the ceramic shell, a coating of a polymer material;
[0181] a heating station configured to heat the formed assembly to melt and remove the wax former, wherein the polymer coating acts as a strengthening layer to the ceramic shell during the wax removal process;
[0182] a heating station configured, subsequent to removal of the wax former, to heat the ceramic shell to melt and remove the polymer coating.
[0183] Feature 20. A system according to feature 19, wherein the system is formed to have physically separate stations.
[0184] Feature 21. A system according to feature 19 or 20, wherein the system comprises stations combined in a common unit or chamber.
[0185] Feature 22. A system according to any one of features 19 to 21, wherein the coating station is configured to apply a polymer coating as the outer layer of the ceramic shell.
[0186] Feature 23. A system according to any one of features 19 to 22, wherein the polymer coat is a distinct layer of the assembly
[0187] Feature 24. A system according to any one of features 19 to 23, wherein the heating station is configured to heat to a temperature lower than firing temperature so as to remove the polymer coating.
[0188] Feature 25. A system according to any one of features 19 to 24, wherein the coating station includes: a spray device, a dipping bath or a painting device for applying the polymer coating onto the ceramic shell.
[0189] Feature 26. A system according to any one of features 19 to 25, wherein the polymer coating drying station is an air drier or a UV curing device.
[0190] Feature 27. A system according to any one of features 19 to 26, wherein the coating station is configured to apply a single layer of polymer material or multiple layers of polymer material.
[0191] Feature 28. A system according to any one of features 19 to 27, wherein the coating station is configured to apply polymer material to the ceramic shell having a viscosity at ambient temperature with no shear of at least 0.2 g/cm/s (20 centipoise), more preferably of at least 0.25 g/cm/s (25 centipoise), preferably of at least 2.50 g/cm/s (250 centipoise), more preferably of at least 5.0 g/cm/s (500 centipoise).
[0192] Feature 29. A system according to any one of features 19 to 28, wherein the wax heating station is configured to heat to a temperature of up to around 180 degrees Centigrade.
[0193] Feature 30. A system according to any one of features 19 to 29, wherein the polymer coating station comprises a source of material for the polymer coating comprising less than 35% w/w of refractory material.
[0194] Feature 31. A system according to any one of features 19 to 30, wherein the polymer coating station comprises a source of material for the polymer coating comprising a formulation including at least one polymer material, wherein the formulation includes less than 35% w/w of refractory material (preferably less than 20% w/w, more preferably less than 10% w/w, most preferably less than 5% w/w), with the balance being water.
[0195] Feature 32. A system according to any one of features 19 to 31, wherein the polymer coating station comprises a source of material for the polymer coating including a polyvinyl alcohol, a styrene butadiene polymer, an acrylic polymer, an epoxy resin, a latex, or any combination thereof.
[0196] Feature 33. A system according to any one of features 19 to 32, wherein the polymer coating station is configured to apply polymer coating to a part of a ceramic shell or to the whole of a ceramic shell.
[0197] Feature 34. A method of casting an article comprising the steps of: filling a ceramic casting shell formed by a method according to any one of claims 1 to 18 with casting material;
[0198] providing for the casting material to harden;
[0199] removing the ceramic shell to reveal the cast article.
[0200] Feature 35. A cast article formed from a ceramic casting shell formed by a method according to any one of features 1 to 18.
[0201] Feature 36. Use of a ceramic casting shell formed by a method according to any one of clauses 1 to 18 in the production of cast articles.
[0202] The disclosures in British patent application number GB21074133.1, from which this application claims priority, and in the abstract accompanying this application are incorporated herein by reference.