METHOD AND APPARATUS FOR REMOVING COATINGS
20200055615 ยท 2020-02-20
Assignee
Inventors
Cpc classification
B64F5/40
PERFORMING OPERATIONS; TRANSPORTING
C25F7/00
CHEMISTRY; METALLURGY
B23K1/20
PERFORMING OPERATIONS; TRANSPORTING
International classification
B64F5/40
PERFORMING OPERATIONS; TRANSPORTING
B23K1/00
PERFORMING OPERATIONS; TRANSPORTING
C25F7/00
CHEMISTRY; METALLURGY
Abstract
A method and apparatus for removing a coating from a gas turbine engine component enabling repair of the component, including application of a braze alloy, without fluoride ion cleaning uses electrolytic stripping of the component in an alkaline bath with the component acting as an anode and current passing to a conformal cathode.
Claims
1.-25. (canceled)
26. A method of removing a coating from an engine run gas turbine engine component, comprising a substrate and a coating on at least a portion of the substrate, the component having stress corrosion cracks including spinels in the substrate, the method comprising: providing a bath with a conformal cathode and an electrolyte solution having a pH that is basic; placing the component in the bath, wherein the component is electrically connected to a power source enabling the component to act as an anode; agitating the solution while passing an electric current through the solution between the component and the conformal cathode effective to remove the coating from the substrate and to remove the spinels from the cracks.
27. The method of claim 26 further comprising: removal of the component from the bath, rinsing the component, and application of a braze alloy to the cracks without use of fluoride ion cleaning to effect a repair to the stress corrosion cracks in the substrate.
28. The method of claim 26 wherein the gas turbine engine component is selected from the group consisting of vanes, nozzles, blades, buckets, combustion liners, transition ducts and end caps.
29. The method of claim 26 wherein the gas turbine engine component is selected from the group consisting of shrouds and tiles.
30. The method of claim 26 further comprising: removing the component from the bath; and subjecting the component to a high temperature, hot vacuum cycle in a heat treat furnace.
31. The method of claim 30 wherein the high hot vacuum cycle comprises a temperature of about 1975 F. for about two hours at a vacuum pressure range of 10.sup.4 or 10.sup.5 Torr.
32. A method of removing a coating from a gas turbine engine component, the component comprising a substrate and a coating on at least a portion of the substrate, the method comprising: providing a bath with a conformal cathode and an electrolyte solution, wherein the electrolyte solution has a pH between about 9 and about 12; placing the component in the bath, wherein the component is electrically connected to a power source enabling the component to act as an anode; agitating the solution while passing an electric current through the solution between the component and the conformal cathode effective to remove the coating from the substrate.
33. The method of claim 26 wherein the pH of the electrolyte solution is between about 9 and about 10.
34. The method of claim 32 wherein the electrolyte solution has a chemical composition comprising at least one of sodium citrate, sodium percarbonate, sodium bicarbonate, and sodium phosphate.
35. The method of claim 34 wherein the electrolyte solution has a chemical composition comprising about one third molar sodium citrate and about one third molar sodium percarbonate.
36. The method of claim 26 wherein the power source is a rectifier with a voltage controlled to not exceed 5 volts.
37. The method of claim 36 wherein the electrical current is between 0 and 4000 amperes.
38. The method of claim 26 wherein the conformal cathode comprises an electrically conductive material having a which is inert when immersed in a solution with a pH in a range of about 9 to about 11.
39. The method of claim 26 wherein the temperature of the electrolyte solution is between about 48 C. to about 75 C.
40. The method of claim 26 wherein the component comprises at least one of a cobalt based substrate, a cobalt containing coating, a CoCrAlY, coating, and a CrCoNiCr coating.
41. The method of claim 26 wherein the coating comprises at least one of the elements selected from the group consisting of cobalt, chromium, aluminum and yttrium.
42. Apparatus for enabling a stripping process to strip a coating from a gas turbine engine component comprising; a bath holding an electrolyte solution that has a pH that is basic; a conformal cathode placed in the bath and shaped to conform to the component being stripped; Page 7 means for heating the solution comprising a heater controlled by a thermocouple; a rectifier for providing a direct current between the components acting as an anode when in the bath and the conformal cathode; and an agitator for agitating the electrolyte solution during a stripping process.
43. The apparatus of claim 42 wherein: the rectifier is capable of providing up to about 4000 A in a range of about 3.75 volts to 4.25 volts; and the conformal cathode comprises an electrically conductive material which is inert when immersed in a solution with a pH in a range of about 9 to about 11 and is formed in a thickness capable of conducting up to about 4000 A in a range of about 3.75 volts to 4.25 volts without loss of material.
44. The apparatus of claim 42 wherein the electrolyte solution a chemical composition including at least one of sodium citrate, sodium percarbonate, sodium bicarbonate, and sodium phosphate.
45. The apparatus of claim 42 wherein the agitator is a pump selected from the group consisting of a direct in the tank agitation pump and an external pump for flowing the solution into the tank through a sparger.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0013] The accompanying drawings, which are incorporated in and constitute a part of this specification, illustrate embodiments of the invention and together with the detailed description given below, serve to explain various aspects of the invention.
[0014]
[0015]
[0016]
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[0019]
DETAILED DESCRIPTION
[0020] As previously discussed,
[0021]
[0022]
[0023]
[0024] Tile/shroud samples from components that had been run in an engine and had stress corrosion cracks with spinels were tested using the method and apparatus described above. The substrate was a cobalt based superalloy, GE FSX414 having an environmental coating. Coatings were removed from a tile/shroud sample using a method including the steps of providing the bath with a conformal cathode and an electrolyte solution, placing the tile/shroud sample in the bath and electrically connecting tile/shroud sample to a rectifier power source which enabled the tile/shroud sample to act as an anode while passing an electric current through the solution between the tile/shroud sample and the conformal cathode. Surprisingly coatings were stripped so effectively that it was determined that it was not necessary to perform the conventional FIC cleaning prior to application of the braze alloy. The tiles came out of the stripping process clean enough that they could be brazed directly, although it may be advantageous to run the parts in a high hot vacuum cycle, like 1975 F. for two hours at a range of 10.sup.4 or 10.sup.5 Torr. Coming out of this cycle the braze can be applied directly to the part. The recipe for the chemical solution was rd molar sodium citrate and rd molar sodium percarbonate. The pH of the solution was around 9-10. Voltage was applied through the rectifier between the parts (as an anode) and a conformal cathode. This voltage was controlled to be around 4 volts and restricted so as to never permit it to exceed, five volts.
[0025] The conformal cathodes were made from SS 304. The thickness of these cathodes must be adequate to carrying the current load. In one bath a rectifier 42 capable of 4000 amperes was used, so the cathodes were large and thick to carry this current. While ability to carry such a high current would suggest copper being better than SS 304, copper is a metal which would deleteriously affect the substrate of the desired part or component by incipient melting and thus should not be used. Copper, silver or other such metals should be avoided for use as cathodes, and metals like titanium are not conductive enough and would need to be very thick to be effective.
[0026] The baths can be run from 48 C. as a standard but can be up to 75 C. Higher temperatures of the bath begins to drive off the percarbonate portion and the cost of the operation increases substantially.
[0027] It has been determined that the electrolyte solution must be agitated. In one embodiment, direct in the tank agitation can be accomplished by a pump such a Flo-King Pump. In another embodiment the solution can exit the tank for filtering the solution and reentering the tank via a sparger. Ventilation is not necessary.
[0028] When percarbonate is used, a portion of the molecule, that portion which is a peroxide ion is eventually consumed and driven off. The remainder of the molecule is a carbonate, really a carbon and a number of oxygens. When this occurs the chemical reaction will continue to work just at a slower rate.
[0029] There is some deep chemistry which is behind the excellent performance of this bath. First, Aluminum, yttrium and chromium can all be stripped in a solution wherein the pH is 9-10 regardless of the chemical method whereby it was contrived. Sodium hydroxide might therefore be an alternative except that it is very high pH. A typical 1 molar solution would be around pH 12. When such a solution was attempted in the same manner in a laboratory large holes developed in the substrate much more dramatically than typical Hydrochloric acid pitting. Therefore, gentle dilute basic solution like those proposed are the likely best candidate for this operation, with a preferred solution being generally basic and one embodiment having an electrolyte solution with a pH of between about 9 and about 12, and another embodiment with a pH of between about 9 and about 10. It has been determined acidic electrolytic solutions such as using oxalic acid would cause significant loss of substrate material when a current is applied. Alternative alkaline compositions such as sodium phosphate could be used. The electrolyte solution can be optimized based on the component materials and coatings involved, the current and the conformal cathode.
[0030] While the present invention has been illustrated by a description of various embodiments and while these embodiments have been described in some detail, it is not the intention of the inventor to restrict or in any way limit the scope of the appended claims to such detail. Thus, additional advantages and modifications will readily appear to those of ordinary skill in the art. The various features of the invention may be used alone or in any combination depending on the needs and preferences of the user.