Apparatus for removing dust accretions from a smelting furnace

Information

  • Patent Grant
  • 6797229
  • Patent Number
    6,797,229
  • Date Filed
    Wednesday, December 18, 2002
    22 years ago
  • Date Issued
    Tuesday, September 28, 2004
    20 years ago
Abstract
The invention relates to an apparatus for mechanically breaking up and detaching dust accretions created by process gases and accumulated on the inner walls of a suspension smelting furnace and/or a waste heat boiler permanently connected to the suspension smelting furnace. According to the invention, on the outer surface (7,13) of the wall of a suspension smelting furnace (1) and/or a waste heat boiler (6), in the vicinity of the connecting point (5) of the suspension smelting furnace and the waste heat boiler, there is installed at least one striker device (8,14), whereby there can be created a mechanical impact effect and mechanical contact between the apparatus (8,14) and at least one of the dust accretions (12,19).
Description




The present invention relates to an apparatus for removing dust accretions from a suspension smelting furnace used in the smelting of sulfidic raw materials, such as ores or concentrates, containing useful metals, such as copper, nickel or lead.




In order to recover metals, such as copper, nickel or lead, from sulfidic raw materials containing said materials, for instance from ores or concentrates, there is generally applied the suspension smelting method, where the heat amounts contained by finely divided sulfidic raw materials are made use of. In addition to sulfidic raw materials, into the reaction space of the suspension smelting furnace there is fed oxygen-containing gas, such as air, oxygen-enriched air or oxygen. In addition, to the reaction space there is fed for instance flue dust recovered and recirculated from the exhaust gases of the suspension smelting furnace, as well as metallurgic slag-forming agent, flux. In the reaction space of the suspension smelting furnace, the solid and gaseous feed materials react with each other, so that in the bottom part of the suspension smelting furnace, there are formed at least two molten phases, a slag phase and a matte phase contained by the metal to be utilized. The molten phases that are formed in the bottom part of the suspension smelting furnace, i.e. in the settler, are removed from the suspension smelting furnace at regular intervals. The sulfur dioxide bearing process gases created in the reaction space of the suspension smelting furnace are conducted, via the settler, to the uptake shaft of the suspension smelting furnace, and from the uptake shaft further to a waste heat boiler connected to the suspension smelting furnace, where the exhaust gases from the suspension smelting furnace are cooled, and at the same time the solids, i.e. flue dust, contained by the gas are removed.




When the suspension smelting furnace exhaust gases are transferred from the uptake shaft of the suspension smelting furnace to the waste heat boiler, the flowing direction of the gases is changed from an essentially vertical direction to an essentially horizontal direction. Moreover, when the flowing area of the connecting aperture between the uptake shaft and the waste heat boiler is made essentially smaller than that of the uptake shaft in order to reduce the heat losses from the suspension smelting furnace, contacts of sulfur dioxide bearing exhaust gases with the walls of the suspension smelting furnace cannot be avoided. Further, because the temperature of the exhaust gases is dropped towards the top part of the uptake shaft of the suspension smelting furnace, the molten particles contained in the exhaust gases start to be solidified, and when touching the uptake shaft walls, they are attached to the wall, particularly in the vicinity of the connecting aperture between the uptake shaft and the waste heat boiler. Thus, in the vicinity of the connecting aperture, there are accumulated dust accretions that obstruct the flowing of the exhaust gases and must therefore be broken apart.




It is an object of the invention to achieve an improved apparatus for breaking up dust accretions created in the vicinity of the connecting point between the uptake shaft and successive waste heat boiler, in the inner parts of the uptake shaft and/or the waste heat boiler, so that the dust accretions do not essentially obstruct the flowing of the exhaust gases from the uptake shaft to the waste heat boiler.




According to the invention, in the vicinity of the connecting point between the uptake shaft of a suspension smelting furnace and the waste heat boiler connected to the uptake shaft, there is installed at least one apparatus, whereby the dust accretions created in the vicinity of the connecting aperture of the uptake shaft and the waste heat boiler can be subjected to an impact effect in order to break up the dust accretions and to drop them back to the bottom part of the uptake shaft of the suspension smelting furnace and/or to the bottom part of the waste heat boiler. The apparatus according to the invention is attached to the wall of the suspension smelting furnace and/or of the waste heat boiler, so that the impact effect achieved by means of the apparatus can be conducted, through the wall of the suspension smelting furnace uptake shaft and/or of the waste heat boiler to at least one dust accretion located inside the uptake shaft and/or waste heat boiler.




In order to break up dust accretions from the inside of the suspension smelting furnace uptake shaft and/or the waste heat boiler, in the vicinity of the connecting point between the suspension smelting furnace uptake shaft and the waste heat boiler, by means of an apparatus according to the invention, in the wall of the uptake shaft and/or the waste heat boiler, on the outer wall surface, in a location corresponding to the spot where the dust accretions are accumulated, there is installed at least one striker device. By means of the striker device, strokes are directed through the wall to the counterpart of the striker device that serves as an anvil. In that end of the counterpart of the striker device, installed through the wall, that is placed inside the uptake shaft and/or the waste heat boiler, which end at the same time is the opposite end with respect to the striker device, there is further installed a striker element whereby a mechanical contact can be achieved between the striker element and the dust accretions to be broken up. The force of the stroke hit by the striker element makes the dust accretions to be broken up and detached from the wall of the uptake shaft and/or the waste heat boiler, so that they are dropped down, to the bottom part of the uptake shaft on the uptake shaft side, and to the bottom part of the waste heat boiler on the waste heat boiler side.




Advantageously the striker device meant for breaking up dust accretions operates pneumatically, hydraulically or in some other advantageous manner. The striker device may advantageously be arranged to operate so that it hits the striker counterpart, serving as the anvil, at essentially regular intervals. Naturally the striker device can also be arranged to operate so that strokes are placed only in cycles, at essentially regular intervals, or so that single strokes are hit according to the need for breaking up the dust accretions, with respect to their degree of accumulation. In addition, the impact force of the striker device provided in the apparatus according to the invention can advantageously be adjusted, in which case the hardness and adhesion caused by the composition of the dust accretions can be taken into account.











The invention is explained more detail with reference to the appended drawing, where





FIG. 1

is a schematical side-view illustration of a preferred embodiment of the invention, seen in a partial cross-section, and





FIG. 2

is a schematical side-view illustration of another preferred embodiment of the invention, seen in a partial cross-section.











According to

FIG. 1

, the sulfur dioxide bearing gases that are created during the smelting that takes place in the reaction space


2


of a suspension smelting furnace


1


are exhausted through the settler


3


to the uptake shaft


4


of the suspension smelting furnace. The uptake shaft


4


is, via the aperture


5


, connected to the waste heat boiler


6


in order to cool down the sulfur dioxide bearing exhaust gases and in order to recover the solids that are exhausted along with the gases. In the vicinity of the aperture


5


between the uptake shaft


4


and the waste heat boiler


6


, on the outer surface


7


of the wall of the uptake shaft


4


, there is installed striker device


8


. In order to enable the desired operation of the striker device


8


, in an aperture arranged in the wall


9


of the uptake shaft


4


, there is installed a counterpart


10


of the striker device


8


, which counterpart serves as the anvil. At that end of the counterpart


10


that is left inside the uptake shaft


4


, there is further installed an impact plate


11


.




When the striker device


8


is used for breaking up the dust accretions


12


accumulated inside the uptake shaft


4


, the striker device


8


hits the counterpart


10


, which moves in parallel to the aperture arranged in the wall of the uptake shaft


4


. The counterpart


10


further moves the impact plate


11


, which directs an impact to the dust accretions


12


. Owing to the force of the impact, the dust accretions


12


are broken up and dropped downwardly in the uptake shaft


4


.




According to

FIG. 2

, on the outer surface


13


of a waste heat boiler


6


connected to the uptake shaft


4


of a suspension smelting furnace


1


via an aperture


5


, there is installed striker device


14


. In order to enable the desired operation of the striker device


14


, in an aperture arranged in the wall


15


of the waste heat boiler


6


, there is installed a counterpart


17


for the striker device


14


, said counterpart serving as the anvil. Moreover, at the end of the counterpart


17


that is left inside the waste heat boiler


6


, there also is installed an impact element


18


.




The striker device


14


operates in a similar way as the striker device


8


, so that a stroke hit by the striker device


14


to the counterpart


17


moves the counterpart


17


so that the impact element


18


gets into contact with the dust accretions


19


and breaks up the dust accretions


19


attached on the wall of the waste heat boiler


6


.



Claims
  • 1. An apparatus for mechanically breaking up and detaching dust accretions created by process gases and accumulated on the inner walls of a suspension smelting furnace and/or a waste heat boiler permanently connected to the suspension smelting furnace, the apparatus comprising:at least one linearly-acting striker device utilizing a single linear actuator, the striker device being mounted on the outer surface of the wall of the suspension smelting furnace and/or waste heat boiler, in the vicinity of the connecting point of the suspension smelting furnace and the waste heat boiler, the at least one striker device, creating a mechanical impact effect and mechanical contact between the apparatus and at least one of the dust accretions; and a counterpart for the at least one linearly-acting striker device movably installed in an aperture provided in the wall of the suspension smelting furnace and/or the waste heat boiler to receive strokes caused by the striker device and in order to direct the strokes to the dust accretions accumulated in the suspension smelting furnace and/or waste heat boiler, the counter part for the striker device being installed through the wall of the suspension smelting furnace and/or the waste heat boiler in an aperture provided in the wall, an impact plate attached to the counterpart, the impact plate being installed on an inner side of the wall, aligned with the direction of the wall.
  • 2. An apparatus according to claim 1, wherein the counterpart of the striker device is, at the end that is opposite to the striker device, provided with an impact element.
  • 3. An apparatus according to claim 1, wherein the striker device is arranged to operate pneumatically.
  • 4. An apparatus according to claim 1, wherein the striker device is arranged to operate hydraulically.
  • 5. An apparatus according to claim 1, wherein the striker device is arranged to operate electrically.
Priority Claims (1)
Number Date Country Kind
20001547 Jun 2000 FI
PCT Information
Filing Document Filing Date Country Kind
PCT/FI01/00590 WO 00
Publishing Document Publishing Date Country Kind
WO02/01131 1/3/2002 WO A
US Referenced Citations (4)
Number Name Date Kind
3721217 Willach et al. Mar 1973 A
3737554 Horibe et al. Jun 1973 A
4475947 Andersson Oct 1984 A
4878654 Carminati et al. Nov 1989 A
Foreign Referenced Citations (6)
Number Date Country
27 10 153 Sep 1978 DE
0 254 379 Jan 1988 EP
58-009945 Jan 1983 JP
59-093180 May 1984 JP
63-058100 Mar 1988 JP
04-292787 Oct 1992 JP