Industrial electric heating furnaces – Arc furnace device – Indirect
Reexamination Certificate
2001-04-04
2002-12-03
Hoang, Tu Ba (Department: 3742)
Industrial electric heating furnaces
Arc furnace device
Indirect
C373S009000, C373S108000
Reexamination Certificate
active
06490312
ABSTRACT:
BACKGROUND OF THE INVENTION
1. Field of the Invention
The invention relates to a direct-current arc furnace for producing steel, comprising a smelting vessel with at least two electrodes for producing arcs as well as tapping openings for the molten mass and the slag. It further concerns a method therefor.
2. Description of the Related Art
Several methods for producing steel are known. Essentially, two process routes are primarily in use: on the one hand, the steel production according to the conventional blast furnace-Bessemer converter route and, on the other hand, the production in an electric steel furnace.
An electric steel furnace is conventionally a flat-cylindrical or oval vessel for melting down scrap metal or directly reduced iron (sponge iron). In the case of electric arc furnaces, the furnace is usually filled with the lid being pivoted out of the way, and the batch is melted down with the arc of the electrodes which penetrate through the lid into the furnace. Emptying of the furnace is realized, depending on the type of furnace, via a tapping launder or an eccentric bottom tapping opening. Electric arc furnaces of the AC (alternating current) as well as DC (direct current) type are known.
Conventional direct-current arc furnaces have a graphite electrode and a bottom electrode. The resulting arc extends vertically downwardly onto the steel bath. Recently, direct-current arc furnaces with two graphite electrodes have also become known.
Conventional direct-current arc furnaces have the following disadvantages.
During the melting-down process an arc deflection results which causes an increased stress on the refractory material. In the shallow bath phase it is therefore required to provide a high foamed slag for covering the arc and for protecting the walls of the vessel.
During the charging process, the resulting exhaust gas or dust cannot be controlled. Also, it is impossible to control in the hot gases the iron oxidation of the scrap metal to be melted down.
Moreover, electrode breakage can result when the scrap metal drops.
Moreover, the temperatures of the exiting gases is too low so that they must be reheated in order to prevent dioxin formation. This requires additional burners in the exhaust gas system.
In direct-current arc furnaces with two electrodes, there is a great heat loading between the two electrodes in the furnace lid area.
SUMMARY OF THE INVENTION
The present invention has the object to propose a direct-current arc furnace and a method for producing steel wherein a reduced loading of the furnace and the environment will result despite an increase of productivity.
This object is solved according to the invention in regard to the furnace in that adjacent to the shaft openings are provided in the upper part of the smelting vessel for receiving suction devices for dust and/or gases which result during the charging process of the melt-down material, and in that the shaft suction device and the vessel suction device are connected to a common device and in that switching elements are provided for actuating only one suction device, respectively, and/or for adjusting a combination of the exhaust gas flows dependent on the charging and smelting process as well as in regard to the method in that during the charging the resulting gases and dust are removed by a furnace vessel suction device connected to openings in the upper part of the smelting vessel, wherein the exhaust gases are removed from the furnace vessel suction device and the shaft suction device into a common device.
The invention suggests that two electrodes and at least one bottom electrode are arranged in the furnace vessel such that two slanted arcs are generated which extend toward the center of the bottom of the smelting furnace and that the smelting vessel is extended in the upward direction by a centrally arranged shaft for introducing melt-down material into the vessel as well as for forming a column of melt-down material.
As a result of the features according to the invention it is achieved that two arcs will burn in a controlled fashion underneath the melt-down material column. With this directed arc deflection and the provided charging shaft, a controlled uniform feeding of the melt-down material into the furnace vessel and a high-capacity melting process are ensured. When using scrap metal, an improved scrap metal cutting and faster cutting are realizable.
With this solution a doubling of the previous capacity of a conventional graphite electrode of 140 kVA or 110 MW can be achieved, and a reduction of the diameter of the two electrodes and thus of the electrode consumption is possible.
It is conceivable, aside from the arrangement of two electrodes (cathodes) and a (common) bottom electrode (anode), to also arrange two cathodes and two anodes. The anodes are bottom electrodes and are arranged such at the center of the bottom that two arcs extending slantedly relative to the bottom center will result. Finally, it is also proposed to provide all embodiments with a larger number of electrodes wherein the feature of the slanted arc is always fulfilled.
It is also advantageous that as a result of the charging shaft the dropping of the scrap metal and thus electrode breakage can be prevented.
According to the invention, the electrodes are arranged such that the arcs no longer extend vertically but at a slant. Therefore, a reduced slag height for covering the arc is required.
For a simultaneous control of the exhaust gases it is proposed that, adjacent to the shaft, openings are provided in the upper part of the smelting vessel for receiving a suction device for dust and/or gases which are produced during the charging process of the melt-down material and that a suction device is provided as an extension of the shaft for sucking away the exhaust gases during the smelting process.
In this way, an exhaust gas control is possible already during the charging process. Simply by means of the removal action of the gases by means of the vessel suction device an iron oxidation of the melt-down material can be mostly avoided.
The directed exhaust gas control has at the same time the advantage that the suction removal of the exhaust gases through the shaft during the smelting process can be used for preheating the scrap metal. The scrap metal preheating is carried out only during the suction removal phase of the gases through the shaft. By doing so, the preheating time can be controlled and thus the iron oxidation of the melt-down material.
It is preferably suggested that the shaft suction device and the vessel suction device are designed such that they end in a common suction pipe and that means are provided for switching between the shaft suction device and the vessel suction device in order to change between the two suction devices and the two exhaust gas flows for the charging and smelting processes. The two suction devices are thus combined to a common device. As a result of the proposed switching elements, it is possible to actuate only one exhaust gas device or to adjust a combination of exhaust gas flows. A control of the exhaust gas flows as well as of the exhaust gas quantities can be realized. This advantageous embodiment of the exhaust gas devices represents a direct suction removal so that, in combination with the proposed shaft, the catching and thus removal of the flue gases resulting during charging and smelting and tapping are made possible.
By changing the exhaust gas flow direction within the shaft, it is also possible to realize an exhaust gas temperature control. With a controlled mixing of the two exhaust gas flows, a heating of the gases to temperatures above the dioxin formation can be achieved.
According to the invention, the smelting vessel in its upper part has openings for the vessel suction devices adjacent to the shaft and the openings for the electrodes. It is especially recommended to arrange the openings for the electrodes in relation to the shaft such that the shaft or the melt-down material column guided through the shaft serve as a thermal shield between the two elec
Pleschiutschnigg Fritz-Peter
Wu Wei-Ping
Friedrich Kueffner
Hoang Tu Ba
SMS Schloemann--Siemag Aktiengesellschaft
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