The present invention relates to furnaces suitable for metallurgical processes, and particularly to furnaces having refractory brick side walls, or a refractory brick, hearth or roof, and gaseous media cooling systems.
The furnaces used in metallurgical processes typically have a crucible consisting of a refractory lining, composed of either bricks, blocks or monolithic refractories, with an adjacent outer shell or some other means of support for the refractory lining. Such furnaces hold a bath of molten metal or matte, usually with an overlying slag layer.
Due to the aggressive nature of many slags produced in metallurgical processes, cooling is required to freeze a layer of slag on the inner surface of the vessel to maintain a stable side wall. As discussed in Voermann et al., Furnace Cooling Design for Modern High Intensity Pyrometallurgical Processes (Proceedings at the Copper 99—Cobre 99 International Conference, Phoenix, Ariz., U.S.A.), the cooling required is dictated by the process conditions in the vessel. To keep the crucible lining in equilibrium, the process heat flux imposed by the process must be matched by the cooling system's heat removal capacity.
In practice, a wide range of heat fluxes are encountered in various metallurgical furnaces. Heat fluxes are dependent on the intensity of the process and whether the containment is for slag or metal. Heat fluxes can typically range from a low value of about 5 kW/m2, which can be removed by natural air cooling, to over 2,500 kW/m2, which requires intense forced water cooling. Generally, for heat fluxes in the lower range, about 15 kW/m2 or less, forced air cooling of the furnace shell plate can be used. For heat fluxes above about 15 kW/m2, some type of water cooling is generally adopted to avoid overheating of the furnace shell plate and structural members.
Due to the potential risk of an explosion in the event that molten material from inside the furnace contacts water in the cooling system, it is desirable to avoid using water as the cooling medium wherever possible. For this reason it may be desirable to use a furnace cooling system which does not use water as a cooling fluid. Although typical air cooling systems cannot match the heat removal capacity of water cooling systems, they have a wider operating temperature range and hence offer significant advantages in cooling applications where adjustable heat removal rates are required.
A number of furnace cooling systems are known in which gaseous media is used as the cooling fluid. For example, U.S. Pat. No. 5,230,617 (Klein et al.) discloses a cooling arrangement in which a number of metal shrouds encircle a cylindrical furnace. Each shroud forms a hollow cooling chamber through which air is circulated, and into which water is atomized to enhance the cooling effect. However, the introduction of water vapour into the system will complicate the cooling air supply system, and create corrosion problems that will impact material selection. Both of these issues will increase complexity and cost.
U.S. Pat. No. 1,674,422 to Allen, Jr. et al. discloses an air-cooled furnace wall in which cast hangers support refractory walls separated by air circulation spaces. U.S. Pat. No. 3,315,950 to Potocnik et al. discloses a heating chamber wall for a furnace, in which the wall has an interior space through which air is allowed to circulate. U.S. Pat. No. 3,777,043 (O'Neill) discloses an annular air circulation channel formed within the refractory furnace wall. U.S. Pat. No. 4,199,652 (Longenecker) discloses J-shaped channels formed between the refractory side wall and the metal outer shell of a furnace. U.S. Pat. No. 6,251,237 (Bos) discloses localized jets blowing directly onto the shell with variable flow for Hall-Heroult aluminum electrolytic pots.
In the above-mentioned patent to O'Neill, and in U.S. Pat. No. 1,751,008 (La France), the structure of the refractory furnace side wall is modified to provide increased surface area for enhanced cooling. In La France, this is accomplished by forming vertical ribs and channels in the outer surfaces of the blocks making up the refractory walls. In O'Neill, the annular cooling channels can be made in the form of “tortuous paths” by using bricks of varying lengths. While these techniques can help to enable increased heat removal capacity, it is extremely difficult to distribute the air evenly over the wall, a problem which worsens as the furnace ages due to shifting and movement of the brickwork. Also, the addition of air into the brickwork behind the shell plate would not be feasible in many furnaces since air would react with the furnace products, e.g. CO gas, metals, etc. For some applications this method is of limited value as it does not provide sufficient cooling capacity.
Thus, known gaseous media-cooling arrangements for metallurgical furnaces generally provide insufficient cooling and/or are unduly complex, requiring specially constructed furnace side walls. Such systems are also relatively expensive and cannot be practically adapted to existing furnace installations.
The following summary is intended to introduce the reader to the more detailed description that follows and not to define or limit the claimed subject matter.
In accordance with a first aspect of the present subject matter, a furnace is provided suitable for metallurgical processes, comprising at least one section comprised of refractory bricks with an outer shell plate adjacent to the refractory bricks, including exterior bricks whose external faces adjacent the shell plate define gaseous media cooling channels extending along the exterior of the refractory bricks between them and the shell plate. The furnace further comprises cooling plates within the cooling channels and joints between the successive courses of bricks. Advantageously, the conductivity of the cooling plates is at least 5 times the conductivity of the refractory lining into which it is inserted. Suitable materials include copper and copper-based alloys, brasses, bronzes, cast irons, aluminum alloys, silver, high-temperature steels, refractory metals and their alloys, graphite, silicon carbide, and aluminum nitride.
Advantageously, the gaseous media cooling channels are aligned with the joints between successive courses of brick of the refractory brick section. More advantageously, the channels are defined by complimentary recesses along adjacent upper and lower portions respectively of the successive courses of exterior bricks. In some examples, the refractory brick section is a side wall of the furnace.
In certain embodiments, the exterior bricks are tapered at their external faces such that successive courses of the exterior bricks together define gaseous media cooling channels between the side wall and the shell plate that have a generally triangular cross section. In some embodiments, the gaseous cooling media is air. In other embodiments the gas may be nitrogen, carbon dioxide, argon, or a combination, or other suitable gases.
In some embodiments, the furnace also includes inlets in the outer shell plate through which gaseous cooling media can enter the channels and outlets through which the gas is exhausted from the cooling channels. In some examples, the furnace includes a fan for blowing gas into the inlets and through the cooling channels.
According to another aspect of the present subject matter, there is provided a set of refractory bricks for use on the exterior of a refractory side wall of a metallurgical furnace having an outer shell plate adjacent to and supporting such a side wall, each of the bricks comprising an external face to be oriented adjacent the outer shell plate, the external faces of the bricks having profiles such that in use on the exterior of a refractory side wall, they define gaseous media cooling channels that extend generally along the exterior of such side wall, between such side wall and such shell plate.
In order that the claimed subject matter may be more fully understood, reference will be made to the accompanying drawings, in which:
a is a schematic isometric view, partially cut away, of another embodiment;
b is a cross sectional view of the embodiment of
a is a schematic isometric view, partially cut away, of another embodiment;
b is a cross section view of the embodiment of
c is a detailed view of a portion of the embodiment of
In the following description, specific details are set out to provide examples of the claimed subject matter. However, the embodiments described below are not intended to define or limit the claimed subject matter. It will apparent to those skilled in the art that many variations of the specific embodiments may be possible within the scope of the claimed subject matter.
As shown in the drawings, the furnace 12 has rectangular side walls 14 extending between an upper portion 15 and a lower portion 16 of the furnace 12, the lower portion 16 comprising a hearth 18 and a base 20. Both the hearth 18 and side wall 14 are formed of a refractory material, preferably refractory bricks 30. Surrounding the refractory side wall, hearth and base of the furnace is a structural metal shell 22, which has an inner surface 24 in contact with the side wall 14, hearth 18 and base 20, and an opposed outer surface 26 in contact with support columns 28.
The refractory bricks 30 of side wall 14 are of two types: regular bricks 32 (which have a conventional rectangular prism or cuboid shape), and specially shaped channel bricks 34 which have tapered outer edges 36. In the embodiments of
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There are a number of possible inlet and outlet configuration which can be applied to an gaseous media cooling system in a circular furnace. For example, one or more inlets may be provided at one end of the wall, and one or more outlets may be provided at the other end of the wall, such that the gaseous media circulation paths 62, 64 extend horizontally along the wall between the inlet(s) and the outlet(s). Alternatively, each end of the wall may be provided with one or more inlets, with the gaseous media flowing toward one or more outlets located centrally between the ends of the wall. It will be appreciated that other inlet/outlet configurations are possible.
When applied to a rectangular furnace, a separate cover member is preferably applied to each wall being cooled, with each wall preferably being provided with at least one inlet and at least one outlet. It will be appreciated that the cooling system can also be applied to circular or oval furnaces.
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The present subject matter can be applied such that the cooling channels are shaped as circular, rectangular, or any shape which can be readily formed or cut into a refractory brick or cast refractory. The cooling channels may be oriented horizontally, vertically, or diagonally.
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While the gaseous cooling media is typically air, in some embodiments, the cooling media may be nitrogen, carbon dioxide or an inert gas to prevent oxidation of the cooling channels, conductive plates or unwanted reactions in the process vessel.
It will be appreciated by those skilled in the art that many variations are possible within the scope of the claimed subject matter. The embodiments that have been described above are intended to be illustrative and not defining or limiting.
For example, while the embodiments above refer to furnace walls, the present subject matter could also be applied to hearths or roofs formed from refractory bricks mounted by an outer shell.
Filing Document | Filing Date | Country | Kind | 371c Date |
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PCT/CA2012/000917 | 10/1/2012 | WO | 00 | 3/31/2014 |
Number | Date | Country | |
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61540896 | Sep 2011 | US |