This application claims the priority of German application No. 100 36 620.1, filed Jul. 27, 2000, the disclosure of which is expressly incorporated by reference herein.
The present invention relates to a process and an apparatus for chroming an inner surface, in particular a cavity, of a metallic component.
To save weight or for cooling purposes, metallic components, such as turbine blades of stationary gas turbines or aircraft engines, can be of hollow design and have a cavity with an inner surface. In the case of turbine blades, the inner surface has to be chromed, on account of the risk of corrosion or sulfuration caused by sulphur.
A powder pack process for chroming the inner surface of the cavity of turbine blades is known, in which a powder mixture comprising Al2O3, chromium and an activator, such as NH4Cl, is introduced into the cavity. When the powder mixture is heated while hydrogen is being supplied, chromium is deposited, so as to form a chromium-containing diffusion layer. The introduction and removal of the powder mixture into and from the cavity have proven to be drawbacks of this process. During introduction, the complete covering of the inner surface of the cavity which is required in order to form a continuous diffusion layer causes problems in particular with complicated geometry or sharp edges. After the process, it is difficult to remove the powder pack from the cavities without leaving any residues. Powder residues often adhere to the inner surface of the cavity.
The object of the present invention is to provide a process in which an inner surface which is to be coated does not have to be brought into contact with a powder which forms the coating gas. Furthermore, it is intended to provide an apparatus for chroming an inner surface of a component.
With regard to the process, the solution according to the present invention is characterized by the following steps:
The advantage of the process is that the coating of the inner surface of the cavity takes place in the gas phase. Therefore, the introduction of a powder mixture into the cavity at the start of the process and the removal of the powder pack after the coating has been carried out are eliminated. Moreover, it is impossible for any powder residues to adhere to the coated surface of the cavity. The mixture, which substantially comprises granules, e.g. with a particle size of 5-20 mm, can be processed more rapidly and more economically than a powder mixture comprising a donor powder and a filler powder for preventing sintering. The granules do not cause any blockages which could impede the dissipation of the coating gas. Moreover, the granules are broken down gradually and do not have to be exchanged after each coating process, as is the case with a powder.
The mixture can be prepared using approximately 99% by weight of chromium granules and approximately 1% by weight of activator, it being possible for the activator to be, for example, NH4Cl in powder form.
To form the coating gas, the mixture can be heated at a temperature of approximately 1200° C.
The dissipation of the coating gas from the container and the step of exposing the inner surface of the component which is to be coated may take place automatically under the action of the force of gravity, since the coating gas, which substantially comprises CrCl, has a higher density or weight than the gases of the atmosphere, such as the inert gas. Therefore, the heating continuously generates coating gas without further measures for generating or influencing the flow being required.
The process can be carried out in an inert environment, in which case, by way of example, Ar is used for purging purposes.
The component used may be a hollow turbine blade, the cavity of which serves to save weight or is for cooling purposes and the surface of which has to be protected against corrosion and/or sulfuration. The latter occurs in particular with hollow, uncooled gas turbine components.
To ensure reliable protection against corrosion and sulfuration, the diffusion layer is formed with a layer thickness in the region of 25 μm and a chromium content in the range from 17% to 20%.
Furthermore, according to the present invention an apparatus is provided having a container for accommodating a mixture of chromium granules and an activator, such as NH4Cl in powder form. At the bottom of the container, there is at least one outlet for a coating gas. A device for holding the component in such a way that the outlet of the container is positioned in the region of the inner surface of the component is also provided. It is possible for the apparatus to be arranged in a heatable retort for heating the mixture which is in the container to a temperature at which a coating gas which substantially comprises CrCl is formed.
To ensure advantageous dissipation of the coating gas, the base of the container may slope downwards towards the outlet or, for example, may also be of funnel-shaped design.
Furthermore, the shape of the outlet may be matched to the shape of a cavity in the component which has the inner surface, so as to ensure that the inner surface is completely exposed, without losses, to the coating gas.
To create an inert atmosphere, the retort may have a gas-feed device and a gas-discharge device for an inert gas, such as for example Ar, which is supplied and removed again for the purpose of purging the apparatus.
For relatively long coating times in the pulverulent activator, such as NH4Cl, is initially present in the mixture in an insufficient amount, the container may have a feed line 1b as shown in
To improve the economic viability, a multiplicity of apparatuses may be arranged in the retort, in order to allow the simultaneous coating of a plurality of components. For this purpose, the apparatus may also have a plurality of outlets at the base.
Other objects, advantages and novel features of the present invention will become apparent from the following detailed description of the invention when considered in conjunction with the accompanying drawings.
Approximately 99% by weight of the mixture 4 consists of chromium granules with a particle size of between 5-20 mm, and approximately 1% by weight of the mixture 4 consists of the activator in powder form. The apparatus is inserted into a retort 14 and is purged with 1000 l/h of Ar in order to create an inert atmosphere. There are spaces between the particles of the granules.
The turbine blade 1 is positioned in a holding device 15 in such a way that the outlet 7 of the container 5 is arranged in the region of an opening 9 in the cavity 2 of the turbine blade 1. In an embodiment, the shape of the outlet 7 of the opening 9 is matched to the cavity 2 such that the outlet 7 projects into the cavity 2, thus ensuring optimum flow of the coating gas 8 through the cavity 2 and optimum exposure of the inner surface 3 of the turbine blade 1 to the coating gas. The retort 14 has a heater (not shown), which the mixture 4 in the container 5 is heated at a temperature at which the coating gas 8, which substantially comprises CrCl, is formed.
In the gas-phase chroming process, the mixture 4 of chromium granules and NH4Cl as activator which is provided in the container 5 is heated, by a heater arrangement, to a temperature of approximately 1200° C., so that coating gas which substantially comprises gaseous CrCl is formed. The coating gas 8 has a greater density or weight than the surrounding Ar or H2 and, on account of the force of gravity, automatically and continuously flows through the outlet 7 at the base 6 of the container 5, in this way is passed to the cavity 2 of the turbine blade 1 and then acts on the surface 2 of this blade so as to form a chromium-containing diffusion layer, which is indicated by a dotted line in FIG. 1.
On account of the coating gas 8 being formed continuously and flowing downwards through the outlet 7 under the force of gravity, the process proceeds automatically. The coating temperature is maintained for a period which is to be varied as a function of the desired layer thickness. In the present configuration of the process, the coating temperature is maintained for 10 h. In this case, a chromium-containing diffusion layer 12 with a layer thickness of 25 μm and a chromium content of 17% is formed.
Liquid CrCl can be deposited at the base 6 of the container 5, as indicated by a thick line denoted by 13.
The modification of the container 5′ consists in the funnel-shaped base 6′, which slopes downwards towards the outlet 7 provided in the center of the funnel. In the same way as in the embodiment illustrated in
For the simultaneous coating of a plurality of components 1, the containers 5 shown in FIG. 1 and
The foregoing disclosure has been set forth merely to illustrate the invention and is not intended to be limiting. Since modifications of the disclosed embodiments incorporating the spirit and substance of the invention may occur to persons skilled in the art, the invention should be construed to include everything within the scope of the appended claims and equivalents thereof.
Number | Date | Country | Kind |
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100 36 620 | Jul 2000 | DE | national |
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4132816 | Benden et al. | Jan 1979 | A |
4148275 | Benden et al. | Apr 1979 | A |
6120843 | Pillhoefer et al. | Sep 2000 | A |
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349420 | Jan 1990 | EP |
696649 | Feb 1996 | EP |
84334416 | Apr 1938 | FR |
2024463 | Aug 1970 | FR |
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363954 | May 1930 | GB |
783953 | Oct 1957 | GB |
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Number | Date | Country | |
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20020025376 A1 | Feb 2002 | US |