The present invention relates to an arrangement for treatment of articles by hot pressing and in particular by hot isostatic pressing.
Hot isostatic pressing (HIP) is a technology that finds more and more widespread use. Hot isostatic pressing is for instance used in achieving elimination of porosity in castings, such as for instance turbine blades, in order to substantially increase their service life and strength, in particular the fatigue strength. Another field of application is the manufacture of products, which are required to be fully dense and to have pore-free surfaces, by means of compressing powder.
In hot isostatic pressing, an article to be subjected to treatment by pressing is positioned in a load compartment of an insulated pressure vessel. A cycle, or treatment cycle, comprises the steps of: loading, treatment and unloading of articles, and the overall duration of the cycle is herein referred to as the cycle time. The treatment may, in turn, be divided into several portions, or states, such as a pressing state, a heating state, and a cooling state.
After loading, the vessel is sealed off and a pressure medium is introduced into the pressure vessel and the load compartment thereof. The pressure and temperature of the pressure medium is then increased, such that the article is subjected to an increased pressure and an increased temperature during a selected period of time. The temperature increase of the pressure medium, and thereby of the articles, is provided by means of a heating element or furnace arranged in a furnace chamber of the pressure vessel. The pressures, temperatures and treatment times are of course dependent on many factors, such as the material properties of the treated article, the field of application, and required quality of the treated article. The pressures and temperatures in hot isostatic pressing may typically range from 200 to 5000 bars, and preferably 800 to 200 bars, and from 300° C. to 3000° C., and preferably from 800° C. to 2000° C., respectively.
When the pressing of the articles is finished, the articles often need to be cooled before being removed, or unloaded, from the pressure vessel. In many kinds of metallurgical treatment, the cooling rate will affect the metallurgical properties. For example, thermal stress (or temperature stress) and grain growth should be minimized in order to obtain a high quality material. Thus, it is desired to cool the material homogeneously and, if possible, to control the cooling rate. Many presses known in the art suffer from slow cooling of the articles and efforts have therefore been made to reduce the cooling time of the articles.
In U.S. Pat. No. 5,118,289, there is provided a hot isostatic press adapted to rapidly cool the articles after completed pressing and heating treatment. This is achieved by using a heat exchanger, which is located above the hot zone. Thereby, the pressure medium will be cooled by the heat exchanger before it makes contact with the pressure vessel wall. Consequently, the heat exchanger allows for an increased cooling capacity without the risk of, for example, overheating the wall of the pressure vessel. However, since the heat exchanger is located close to the top closure of the pressure vessel there is a risk that the cooling capability of the heat exchanges is impaired due to undesired heating of the heat exchanges caused by ascending thermal energy within the pressure vessel. Therefore, it may be desirable to enhance the cooling capability of the heat exchanger. It is well known within the art that an increased flow rate of the pressure medium entails an enhanced cooling due to an increased heat transfer coefficient. In U.S. Pat. No. 5,118,289, an increased flow rate is achieved by allowing the circulating gas (pressure medium) to pass the heat exchanger via a pump of fan or the like. This solution may, on the other hand, add complexity to the construction of the pressing arrangement as well as it may increase maintenance requirements and needs.
Hence, there is still a need within the art of an improved pressing arrangement for hot isostatic pressing that is capable of controlled rapid cooling of articles and of pressure medium.
A general object of the present invention is to provide an improved pressing arrangement, which is capable of a controlled and rapid cooling of articles being treated in the pressing arrangement and of the pressure medium during hot isostatic pressing.
A further object of the present invention is to provide an improved pressing arrangement, which is capable of such controlled rapid cooling without special purpose equipment such as fans or pumps for the cooling.
Another object of the present invention is to provide an improved pressing arrangement with reduced maintenance requirements.
Yet another object of the present invention is to provide an improved pressing arrangement, which is capable of high temperature uniformity during, for example, the pressing state and the steady-state.
Still another object of the present invention is to provide an improved pressing arrangement in which the risk of overheating the pressure vessel is significantly reduced in comparison to prior art pressing arrangements for hot isostatic pressing.
These and other objects of the present invention are achieved by means of a pressing arrangement having the features defined in the independent claims. Embodiments of the present invention are characterized in the dependent claims.
In the context of the present invention, the term “heat exchanging unit” refers to a unit capable of storing thermal energy and exchanging thermal energy with the surrounding environment.
Furthermore, in the context of the present invention, the terms “cold” and “hot” or “warm” (e.g. cold and warm or hot pressure medium or cold and warm or hot temperature) should be interpreted in a sense of average temperature within the pressure vessel. Similarly, the term “low” and high” temperature should also be interpreted in a sense of average temperature within the pressure vessel.
According to a main aspect of the present invention, there is provided a pressing arrangement for hot pressing, comprising a pressure vessel including a pressure cylinder provided with top and bottom end closures. A furnace chamber adapted to hold articles is provided inside the pressure vessel and is at least party enclosed by a heat insulated casing. At least one guiding passage communicating with the furnace chamber forms an outer cooling loop, wherein the pressure medium in a part of the outer cooling loop is guided in proximity to pressure vessel walls and the top end closure before it re-enters into the furnace chamber. Further, a guiding channel element is located in the at least one guiding passage forming the outer cooling loop is arranged with at least one pressure medium channel for guiding the pressure medium from a central opening of the heat insulated casing radially and circumferentially towards a lateral wall of the pressure cylinder. The at least one pressure medium channel has a substantially constant cross-sectional area in a flow direction of the pressure medium over its entire length.
Generally, the present invention is based on the idea of utilizing passages and spaces of an outer cooling loop for the pressure medium which cannot be used for carrying load to enhance the cooling capabilities of the pressing arrangement.
According to a main aspect of the present invention, this is achieved by providing a guiding channel element in the outer cooling loop above the furnace chamber close to or in contact with the top end closure. The guiding channel element is arranged with pressure medium channels designed with a cross-section area and a curvature in a radial and circumferential direction such that a high and substantially constant speed of the pressure medium is obtained during its passage through the guiding channel element. Due to the high and constant speed of the pressure medium during its passage close to the top end closure, the heat transfer ratio can be maintained at a high rate during the entire passage through the guiding channel element and thereby, in turn, the thermal energy that can be transmitted from the pressure medium during its passage of the guiding channel element to the top end closure.
An even further improved cooling capability can be achieved by arranging heat exchanging or heat sink elements in passages or spaces in the outer cooling loop, for example, in connection with the guiding channel element or in proximity to the lateral wall of the pressure vessel. Thereby, an enhanced cooling capability can be achieved at the same time as no additional space is occupied by the heat exchanging elements. That is, the space occupied by the heat exchanging elements does not compete with load carrying space. In conventional pressure arrangements these passages and spaces are only used for guiding or passing pressure medium. The present invention therefore provides an enhanced cooling capability without having to use valuable load space.
In preferred embodiments, the guiding channel element itself is made of a material having heat exchanging or heat sink capabilities.
The amount of thermal energy transferred via the top end closure depends inter alia on:
Features from two or more embodiments outlined above can be combined, unless they are clearly complementary, in further embodiments. Likewise, the fact that two features are recited in different claim does not preclude that they can be combined to advantage.
The different embodiments of the present invention described herein can be combined, alone or in different combinations, with embodiments in different combinations described in the patent applications “Non-uniform cylinder” and “Pressing arrangement” filed on the same day as the present application by the same applicant. The content of the patent applications “Non-uniform cylinder” and “Pressing arrangement”, respectively, are included herein by reference.
Embodiments of the present invention will now be described with reference to the accompanying drawings, on which:
The following is a description of exemplifying embodiments of the present invention. This description is intended for the purpose of explanation only and is not to be taken in a limiting sense. It should be noted that the drawings are schematic and that the pressing arrangements of the described embodiments comprise features and elements that are, for the sake of simplicity, not indicated in the drawings.
Embodiments of the pressing arrangement according to the present invention may be used to treat articles made from a number of different possible materials by pressing, in particular by hot isostatic pressing.
With reference first to
The pressure medium may be a liquid or gaseous medium with low chemical affinity in relation to the articles to be treated. The pressure vessel 1 includes a furnace chamber 18, which comprises a furnace (or heater) 36, or heating elements, for heating of the pressure medium during the pressing state of the treatment cycle. The furnace 36 may, as shown in for example
The furnace chamber 18 further includes a load compartment 19 for receiving and holding articles 5 to be treated. The furnace chamber 18 is surrounded by a heat insulated casing 3, which is likely to save energy during the heating state. It may also ensure that convection takes place in a more ordered manner. In particular, because of the vertically elongated shape of the furnace chamber 18, the heat insulated casing 3 may prevent forming of horizontal temperature gradients, which are difficult to monitor and control. The bottom of the heat insulated casing 3 comprises a bottom heat insulating portion 7b. Fittings inside the pressure vessel 1—including the load compartment 19, casing 3, heat insulating portion 7b, any apertures between the furnace chamber 18 and the first guiding passage 10 and even adjustable valves—will form guiding flow channels or otherwise play the role as guiding means for streams of pressure medium when such arise as a consequence of convective or forced flow. It should be noted, that the disclosed layout of the fittings may be varied in a number of ways, e.g., to satisfy specific needs.
Furthermore, the pressure vessel 1 may be provided with one or more cooling circuits including channels or tubes, in which a coolant for cooling may be provided. In this manner, the vessel wall may be cooled in order to protect it from detrimental heat. The flow of coolant is indicated in
The heat-insulated casing 3 of the furnace chamber 18 is accompanied by a housing 2, which includes a top aperture 13, for adding another layer to the circulation loop. A guiding passage 11 is formed between the housing 2 of the furnace chamber 18 and the heat insulating portion 7 of the furnace chamber 18. The second guiding passage 11 is used to guide the pressure medium towards the top end closure 8 of the pressure vessel (or alternatively towards the pressure vessel wall, which is not shown herein) via the top aperture 3. Thus, in addition to the internal circulation inside the furnace chamber 18, the pressure medium is guided substantially upwards in the guiding passage 11 formed between the casing 3 and the housing 2, and substantially downwards in the first guiding passage 10, between the housing and the outer wall of the pressure vessel 1 in an outer cooling loop. It is noted that one portion of the internal circulation is guided back into the furnace chamber 18, whereas a second portion joins the upward flow between the housing 2 and the casing 3, and a third portion flows directly into the intermediate space 10. The proportion of these three flows can be adjusted by varying the spacing between a bottom heat insulating portion 7b, the housing 2 and the casing 3.
A guiding channel element 40 is arranged in the space 22 a above the housing 2 and below the upper lid 8. The guiding channel element 40 is arranged with at least one channel 50 (see
However, it is also conceivable that each channel 50 has a specific cross-sectional area being constant over the length of the channel, i.e. it is not necessary that all the channels have the same cross-sectional area.
By securing that the guiding channel element 40 is pressed against the upper lid 8, an efficient transfer of thermal energy from the pressure medium to the upper lid 8 can be achieved. In the embodiment shown in
In
With reference now to
The upper part 61 includes at least one channel 68, see
In
In
In
The channel area A1 and the channel area A2 do not have to be the same but may differ in some embodiments. Furthermore, the channels 65 and 68 are shown in
With reference to
The heat exchanging elements 91 and 92 are arranged in spaces and/or passages of the outer cooling loop 10, 11 that cannot be used for other purposes such as loading articles 5. Thereby, by utilizing these otherwise unused spaces and/or passages for locating heat exchanging elements the cooling capabilities of the pressure arrangement 100 can be improved at the same time as the loading capabilities of the pressure arrangement 100 can be maintained.
The arrows indicate the flow of pressure medium during, for example, a cooling phase. A first heat exchanging element 92 is arranged in the first guiding passage 10, between the housing 2 and the outer wall of the pressure vessel 1. Further, a second heat exchanging element 91 is arranged in the second guiding passage 11 formed between the housing 2 of the furnace chamber 18 and the heat insulating portion 7 of the furnace chamber 18. The second guiding passage 11 is used to guide the pressure medium towards the top of the pressure vessel (or alternatively towards the pressure vessel wall, which is not shown herein). Further heat exchanging elements (not shown) may be arranged in a space 19 below the housing 2.
The heat exchanging elements or heat sink elements 91 and 92 are arranged completely inside the pressure vessel and is not supplied with any external cooling medium. Hence, the heat exchanging elements 91 and 92 have no physical connection with the environment outside the pressure vessel 1.
Because the heat exchanging element 91 and 92 are arranged in the outer cooling loop 10, 11, the cooling can be enhanced since thermal energy is transferred to the heat exchanging elements 91 and 92 from the pressure medium passing through and/or by the heat exchanging elements 91 and 92 in addition to the transmission of thermal energy from the pressure medium descending through the guiding passage 10 through the vessel wall into the cooling circuit (not shown) outside the vessel wall.
The amount of thermal energy transferred to a heat exchanging element depends inter alia on the following:
With reference now to
As the skilled person realizes, the number of heat exchanging elements, their respective placements and their relative sizes of the elements illustrated in
Even though the present description and drawings disclose embodiments and examples, including selections of components, materials, temperature ranges, pressure ranges, etc., the invention is not restricted to these specific examples. Numerous modifications and variations can be made without departing from the scope of the present invention, which is defined by the accompanying claims.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/EP2011/050026 | 1/3/2011 | WO | 00 | 1/6/2014 |
Publishing Document | Publishing Date | Country | Kind |
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WO2012/092959 | 7/12/2012 | WO | A |
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4349333 | Bowles | Sep 1982 | A |
5118289 | Bergman et al. | Jun 1992 | A |
7011510 | Nakai | Mar 2006 | B2 |
20050039896 | Laine | Feb 2005 | A1 |
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2349490 | Nov 1999 | CN |
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Number | Date | Country | |
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20140127637 A1 | May 2014 | US |