US20020053306A1 - Shredder dust feeding facilities and reverberatory furnace provided with this feeding facilities - Google Patents
Shredder dust feeding facilities and reverberatory furnace provided with this feeding facilities Download PDFInfo
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- US20020053306A1 US20020053306A1 US09/896,203 US89620301A US2002053306A1 US 20020053306 A1 US20020053306 A1 US 20020053306A1 US 89620301 A US89620301 A US 89620301A US 2002053306 A1 US2002053306 A1 US 2002053306A1
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- Prior art keywords
- feeding
- reverberatory furnace
- facilities
- shredder dusts
- shredder
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/003—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals for used articles
- F23G7/005—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals for used articles cars, vehicles
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- C—CHEMISTRY; METALLURGY
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B15/00—Obtaining copper
- C22B15/0026—Pyrometallurgy
- C22B15/0056—Scrap treating
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/442—Waste feed arrangements
- F23G5/444—Waste feed arrangements for solid waste
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L7/00—Supplying non-combustible liquids or gases, other than air, to the fire, e.g. oxygen, steam
- F23L7/007—Supplying oxygen or oxygen-enriched air
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2205/00—Waste feed arrangements
- F23G2205/16—Waste feed arrangements using chute
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
- F27B3/00—Hearth-type furnaces, e.g. of reverberatory type; Tank furnaces
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D3/00—Charging; Discharging; Manipulation of charge
- F27D3/0033—Charging; Discharging; Manipulation of charge charging of particulate material
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F27—FURNACES; KILNS; OVENS; RETORTS
- F27D—DETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
- F27D3/00—Charging; Discharging; Manipulation of charge
- F27D3/10—Charging directly from hoppers or shoots
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Definitions
- the present invention relates to a feeding facilities for shredder dusts for performing an incinerating process by burning shredder dusts comprising various shredded waste materials by feeding the shredder dusts to a reverberatory furnace for non-ferrous smelting and to a reverberatory furnace provided with this feeding facilities.
- FIG. 9 A schematic flow chart of the processing of automobile shredder dusts in a reverberatory furnace is shown in FIG. 9.
- the reverberatory furnace 1 is a green charge type (wet charge type) reverberatory furnace used for non-ferrous smelting and in particular for smelting copper concentrates.
- Industrial waste materials such as automobile shredder dusts are stored in the stockyard 2 , then transported to the reverberatory furnace 1 by conveyors 4 from the feed hopper 3 and fed into the inside of the reverberatory furnace 1 by a feeding chute composed by such as a steel pipe.
- the industrial waste materials are then processing in the reverberatory furnace 1 together with copper concentrates.
- Oxygen enriched air is also supplied to the reverberatory furnace 1 from an oxygen plant 5 .
- the off-gas from the reverberatory furnace 1 is cooled through a waste heat boiler 6 for recovering heat and, then the dust in the off-gas has been collected by an electrostatic precipitator 7 , SO 2 in the gas is fixed as gypsum by a gypsum plant 8 .
- SO 2 in the gas is fixed as gypsum by a gypsum plant 8 .
- the steam generated in the waste heat boiler 6 is used to electrical power in a turbine generator 9 , however, the amount of generated power corresponds to approximately half of the total amount of power consumption at the smelter.
- dried copper concentrates and oxygen from the oxygen plant 5 are fed into the converter 10 and the off-gas is fed to the sulfuric acid plant 13 via the boiler 11 and the electrostatic precipitator 12 .
- an anode produced from the converter 10 via an anode furnace 14 is changed to electrolytic copper in a tank house (electro-refining plant) 15 .
- a tank house 15 gold, silver, and palladium are collected as anode slime.
- the shredder dusts is stored the stockyard 2 of the smelter, transported by the conveyor 4 from the feed hopper 3 , then fed to the inside of the reverberatory furnace 1 via a feeding chute.
- the feeding chute is simply installed in the ceiling of the reverberatory furnace 1 and the shredder dusts simply fed into this chute, the off-gases increase and in cases in which it is not possible to maintain a sufficient negative draft inside the reverberatory furnace 1 , there is the concern that the off-gas inside the furnace and the gas from the burning will leak out by the feeding chute.
- the present invention was achieved on the basis of these circumstances and it is an object thereof to provide an facilities for feeding shredder dusts to a reverberatory furnace capable of securing the sealing of a feeding chute when shredder dusts is fed to a reverberatory furnace used for non-ferrous smelting as described above and for ensuring that the shredder dusts is burnt properly and thereby achieving an increase in the amount of this processing that can be performed.
- a further aim of the present invention is to provide a reverberatory furnace in which the formation of large piles the reverberatory furnace caused by unburnt of shredder dusts is prevented, and in which the blocking of the propagation of burning heat from the burner is prevented, and also in which hot gas is prevented from leaking from inside the furnace.
- the present invention relates to facilities for feeding shredder dusts to a reverberatory furnace in which shredder dusts is fed to a reverberatory furnace for non-ferrous smelting, and in particular, to facilities for feeding shredder dusts to a reverberatory furnace in which a feeding chute that passes to the inside of the reverberatory furnace is fitted to the ceiling of the reverberatory furnace and shredder dusts can be fed from this feeding chute, and which also allows oxygen enriched air to be supplied to the feeding chute and fed to the inside of the reverberatory furnace.
- the feeding chute is branched partway along its length and it is desirable that the shredder dusts is fed from one end thereof while the oxygen enriched air is supplied in from the other end thereof.
- an air supply nozzle that has a smaller diameter than the feeding chute is inserted in the other end of the branched feeding pipe and the distal end of the air supply nozzle is positioned adjacent to the branched portion of the feeding chute and that the oxygen enriched air is supplied in from the air supply nozzle.
- the present invention relates to a reverberatory furnace for non-ferrous smelting provided with the shredder dust feeding facilities, and in particular, to a reverberatory furnace for non-ferrous smelting in which a burner is able to be installed in a wall portion of one end side thereof and a plurality of feeding ports to which are connected the feeding chutes of the shredder dusts feeding facilities are provided at the one end side at a ceiling portion forming a plurality of staggered rows facing another end side.
- the one end side where the feeding ports are provided is raised above the other end side.
- a feeding chute of the feeding facilities is connected to each one of the plurality of feeding ports and the positions at which shredder dusts is fed to the feeding hoppers are arranged in a single row.
- FIG. 1 is a plan view showing the schematic structure of a reverberatory furnace according to the present invention.
- FIG. 2 is a side view as seen from the direction of the arrow A in FIG. 1 showing the schematic structure of the feeding facilities according to the present invention.
- FIG. 3 is a side cross sectional view showing in detail a portion of the reverberatory furnace according to the present invention.
- FIG. 4 is a horizontal cross sectional view of the reverberatory furnace shown in FIG. 3 (wherein below the center line O shows the cross section along the line B-B in FIG. 3).
- FIG. 5 is a half sectional view taken along the line C-C in FIG. 3.
- FIG. 6 is a plan view showing in detail a portion of the feeding facilities according to the present invention.
- FIG. 7 is a cross sectional view taken along the line D-D in FIG. 6.
- FIG. 8 is a cross sectional view taken along the line E-E in FIG. 6.
- FIG. 9 is a flow chart for when shredder dusts is fed to a reverberatory furnace used for smelting copper concentrates.
- FIGS. 1 through 8 show an embodiment of the present invention.
- the present invention is applied to a green charge type (wet charge type) of reverberatory furnace 21 used for smelting copper concentrates.
- reverberatory furnaces 21 and 21 are provided in parallel and eight feeding ports 22 . . . are provided in each ceiling portion 21 a of the reverberatory furnaces 21 and 21 .
- a shredder dusts feeding facilities 23 is provided for each of the feeding ports 22 . . .
- the reverberatory furnaces 21 are formed in a substantially elongated schematic box shape and one end side in the longitudinal direction thereof (i.e. the bottom side in FIG. 1 and the right side in FIGS. 3 and 4) is the side where the burner is provided.
- a plurality of window portions 21 c for burner installation are formed in the wall portion 21 b of the one end side in the longitudinal direction, and two waste heat boilers 24 and 24 are connected to each reverberatory furnace 21 at the wall portion 21 d of the other end side in the longitudinal direction (i.e. at the top side in FIG. 1 and the left side in FIGS. 3 and 4).
- a plurality of unillustrated hoppers used for inserting copper concentrates are provided at the burner side of the ceiling portions 21 a of the reverberatory furnaces 21 in a line along the wall portions 21 e and 21 e that extend in the longitudinal direction of the reverberatory furnace 21 .
- each ceiling portion 21 a of the reverberatory furnaces 21 at the one end side in the longitudinal direction where the burner is situated is formed slightly raised above the other end side, as is shown in FIG. 3, and the above eight feeding ports 22 . . . are provided at this raised portion at the one end side.
- These feeding ports 22 . . . are arranged in two rows as seen in plan view in the vicinity of the center line O in the transverse direction of the reverberatory furnace 21 (i.e. in the horizontal direction in FIGS. 1 and 5 and in the vertical direction in FIG. 4) such that the same number (four) thereof are placed on either side of this center line O and in rows parallel thereto.
- the distance from each row of feeding ports 22 A . . . and 22 B . . . to the center line O is equal.
- the four feeding ports 22 A . . . and 22 B . . . in each row are arranged equidistantly in the direction of the center line O, namely, in the aforementioned longitudinal direction.
- the distance between adjacent feeding ports 22 and 22 in the direction of the center line O is set equal to each other in the same row.
- the feeding ports of the other row are positioned at the center of adjacent feeding ports 22 and 22 in the direction of the center line of one row.
- the feeding ports 22 A and the feeding ports 22 B are arranged so as to alternate in a staggered (i.e. zigzag) pattern along the direction of the center line O.
- the portion of the ceiling portion 21 a where these feeding ports 22 . . . are provided is constructed as a water cooled copper jacket.
- the bottom ends of the feeding facilities 23 provided for each of the feeding ports 22 . . . arranged in this way are connected to the feeding ports 22 and open onto the inside of the reverberatory furnace 21 .
- the feeding facilities 23 are provided with feeding chute 25 that are provided at the ceiling portion 21 a so as to extend vertically upwards. More specifically, as is shown in FIGS. 6 to 8 , branch pipes 26 having the same diameter as the feeding chute 25 branch out extending in a diagonally upward direction from partway along the vertically extending feeding chutes 25 .
- air supply nozzles 27 having a smaller diameter than the feeding chutes 25 are inserted coaxially with the feeding chutes 25 into the feeding chutes 25 from the top end thereof.
- Hoppers 28 are provided via a freely removable insertion damper at the top end portion of the branch pipes 26 , namely, at the position where shredder dusts is fed to the feeding chutes 25 .
- the peripheries of the air supply nozzles 27 are sealed by lid bodies 29 .
- An observation window 29 a manufactured from heat resistant glass and an inspection opening 29 b that is normally closed are provided in each lid body 29 .
- short branch pipes 26 branch from a position in the upper end portion of the feeding chutes 25 diagonally upwards in a direction away from the center line O along a plane that intersects the center line O.
- long branch pipes 26 branch from a position in the bottom end portion of the feeding chutes 25 diagonally upwards at a sloping angle equal to that of the above branch pipes 26 of the feeding facilities 23 A along a plane that intersects the center line O. Furthermore, as seen in plan view, these branch pipes 26 extend beyond the center line O to the side of the one feeding facilities 23 A . . . (note that, for this description, in FIG. 2, the sloping angles of the branch pipes 26 in both feeding facilities 23 A and 23 B are shown as being different).
- the hoppers 28 are provided on a straight line parallel with the center line O such that the positions of the hoppers 28 , namely, the positions at which the shredder dust is fed to the feeding chutes 25 , have the same height and match each other in the transverse direction, as is shown in FIG. 6. Furthermore, a shuttle conveyor 30 is provided extending parallel to the center line O directly above the hoppers 28 . . .
- each feeding facility 23 A . . . and 23 B . . . are bent in a horizontal direction at the point where they protrude from the lid bodies 29 and are then connected with larger diameter air supply pipes 33 .
- Each air supply pipe 33 is connected to an unillustrated oxygen enriched air supply source such as, for example, the oxygen plant 5 shown in FIG. 9.
- Oxygen enriched air having a predetermined density and pressure is expelled from the air supply nozzles via the air supply pipes 33 and is able to be supplied into the reverberatory furnace 21 together with shredder dust fed through the branch pipes 26 .
- an operation floor 34 is placed at a distance above the ceiling portion 21 a of the reverberatory furnace 21 .
- the operation floor 34 is provided with a water cooled plate to insulate it from the heat from the reverberatory furnace 21 and the top end portions of the feeding chutes 25 and the branch pipes 26 protrude above this operation floor 34 .
- the shredder dusts is inserted into the reverberatory furnace 21 while being burnt by the oxygen enriched air that is supplied together with it. Accordingly, even if the atmosphere inside the reverberatory furnace 21 becomes insufficient in oxygen, it is possible to ensure that the fed shredder dust is incinerated at a high temperature.
- shredder dust from scrapped automobiles and the like can be reliably processed without generating harmful materials such as dioxin, and also that the heat from the combustion can be used effectively for the smelting of (for example copper concentrates). Moreover, it is possible to suppress the actual formation of the aforementioned piles caused by unburnt shredder dust.
- the branch pipes 26 are provided branching off from partway along the feeding chutes 25 and shredder dusts is fed from these branch pipes 26 while oxygen enriched air is supplied from the top end portion of the feeding chutes 25 . Accordingly, even if the shredder dusts becomes blocked inside the branch pipes 26 , the supply of the oxygen enriched air is not cut off and, at the least, the sealing performance can be ensured due to the oxygen enriched air and it is possible to reliably prevent high temperature gas from leaking from inside the reverberatory furnace 21 .
- the small diameter air supply nozzles 27 are inserted into the feeding chutes 25 and the distal end (i.e. the bottom end) thereof is positioned at the connecting portion of the branch pipes 26 with the feeding chutes 25 , and oxygen enriched air is supplied from the air supply nozzles 27 at a predetermined pressure into the feeding chutes 25 and fed into the reverberatory furnace 21 .
- the shredder dusts inserted into the branch pipes 26 from the hoppers 28 is fed by being sucked into the feeding chutes 25 .
- the plurality of feeding ports 22 in which the above feeding facilities 23 are provided are placed in a staggered arrangement running from the wall portion 21 b of the reverberatory furnace 21 in which the burners are placed in the longitudinal direction of the reverberatory furnace 21 , namely, in the direction of the burning by the burners.
- the distance between each of the feeding ports 22 and 22 is increased compared with if, for example, they were placed in a lattice arrangement. Therefore, even if the piles are formed, they can be prevented from becoming too large.
- the result of this is that, as described above, the gap to the ceiling 21 a is maintained and flames are prevented from escaping.
- the portion at one end side of the ceiling portion 21 a in the longitudinal direction of the reverberatory furnace 21 where the burner is situated is formed slightly raised above the other end side, and the feeding ports 22 . . . are provided in a staggered arrangement in this raised portion. Accordingly, even if the above described piles do become formed, it is possible to ensure that a sufficient clearance is maintained between the piles and the ceiling portion 21 a , therefore, it is possible to even more reliably prevent flames from leaking.
- the feeding ports 22 . . . are arranged in two rows in a staggered pattern, however, it is also possible for the feeding ports 22 . . . to be arranged in three or more rows in the above staggered pattern depending on the size and the like of the reverberatory furnace 21 .
- the branch pipes 26 instead of forming the branch pipes 26 all at an equal slope angle branching out from different positions of the feeding chutes 25 , as described above, it is possible, as is shown in FIG. 2, to provide branch pipes 26 having different slope angles and to make both the branch position and the slope angle different.
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Abstract
The present invention relates to facilities for feeding shredder dusts to a reverberatory furnace in which shredder dusts is fed to a reverberatory furnace for non-ferrous smelting, and in particular, to facilities for feeding shredder dusts to a reverberatory furnace in which a feeding chute that passes to the inside of the reverberatory furnace is fitted to the ceiling of the reverberatory furnace and shredder dusts can be fed from this feeding chute, and which also allows oxygen enriched air to be supplied to the feeding chute and fed to the inside of the reverberatory furnace. Further, the present invention relates to a reverberatory furnace for non-ferrous smelting in which a burner is able to be installed in a wall portion of one end side thereof, and in particular, to a reverberatory furnace for non-ferrous smelting in which a plurality of feeding ports to which are connected the feeding chutes of the shredder dusts feeding facilities are provided at the one end side in the ceiling portion thereof forming a plurality of staggered rows facing the other end side.
Description
- 1. Field of the Invention
- The present invention relates to a feeding facilities for shredder dusts for performing an incinerating process by burning shredder dusts comprising various shredded waste materials by feeding the shredder dusts to a reverberatory furnace for non-ferrous smelting and to a reverberatory furnace provided with this feeding facilities.
- 2. Description of the Related Art
- In recent years the processing of industrial waste materials has become a problem for society. Currently, the landfilling of waste materials is severely restricted and incineration methods are also regulated so as to prevent dioxin from being generated. In this situation, in order to recover various metals such as copper, gold, silver, and palladium without generating dioxin, the inventors of the present invention attempted the processing of automobile shredder dusts in a reverberatory furnace. Here, the term shredder dusts is used to refer generally to fluff materials coming out when scrapped vehicles are crushed in order to recover steel and aluminum. Shredder dusts is more easily burnt than chipped tires and also contains valuable metals; therefore, the processing ratio of such attempts is continually improving.
- A schematic flow chart of the processing of automobile shredder dusts in a reverberatory furnace is shown in FIG. 9. In this flow chart, the reverberatory furnace1 is a green charge type (wet charge type) reverberatory furnace used for non-ferrous smelting and in particular for smelting copper concentrates. Industrial waste materials such as automobile shredder dusts are stored in the
stockyard 2, then transported to the reverberatory furnace 1 byconveyors 4 from the feed hopper 3 and fed into the inside of the reverberatory furnace 1 by a feeding chute composed by such as a steel pipe. The industrial waste materials are then processing in the reverberatory furnace 1 together with copper concentrates. Oxygen enriched air is also supplied to the reverberatory furnace 1 from anoxygen plant 5. - Moreover, the off-gas from the reverberatory furnace1 is cooled through a
waste heat boiler 6 for recovering heat and, then the dust in the off-gas has been collected by an electrostatic precipitator 7, SO2 in the gas is fixed as gypsum by agypsum plant 8. Note that the steam generated in thewaste heat boiler 6 is used to electrical power in aturbine generator 9, however, the amount of generated power corresponds to approximately half of the total amount of power consumption at the smelter. On the other hand, in the period when the converter is operating, dried copper concentrates and oxygen from theoxygen plant 5 are fed into theconverter 10 and the off-gas is fed to thesulfuric acid plant 13 via theboiler 11 and theelectrostatic precipitator 12. Moreover, an anode produced from theconverter 10 via ananode furnace 14 is changed to electrolytic copper in a tank house (electro-refining plant) 15. In thistank house 15, gold, silver, and palladium are collected as anode slime. - As the present inventors were continuing the above described attempts, they noticed that there were several problems that needed to be resolved arising from the burning of shredder dusts in the reverberatory furnace1 in the above described manner. One of these problems was that the amount of shredder dusts to be processed in the reverberatory furnace 1 was limited by the volume of off-gas expelled from the reverberatory furnace 1. Namely, if the atmosphere inside the reverberatory furnace 1 becomes insufficient in oxygen due to the off-gas generated in the burning of the shredder dusts previously supplied or to the burning off-gases caused by fuel directly fed from the burner into the reverberatory furnace 1 and burnt therein, then even if new shredder dusts is fed into the reverberatory furnace 1, this cannot be easily burnt and simply accumulates in an unprocessed state inside the reverberatory furnace 1.
- Moreover, as described above, the shredder dusts is stored the
stockyard 2 of the smelter, transported by theconveyor 4 from the feed hopper 3, then fed to the inside of the reverberatory furnace 1 via a feeding chute. However, for example, if the feeding chute is simply installed in the ceiling of the reverberatory furnace 1 and the shredder dusts simply fed into this chute, the off-gases increase and in cases in which it is not possible to maintain a sufficient negative draft inside the reverberatory furnace 1, there is the concern that the off-gas inside the furnace and the gas from the burning will leak out by the feeding chute. Since the sealing needs to be so secure that the gas inside the furnace does not leak even when the shredder dusts is being fed, it is necessary to provide a double damper, for example, which results, of course, in the operation of feeding the shredder dusts becoming complicated, but also means that continuous feeding is difficult. The ultimate result is that restrictions are placed on the amount of shredder dusts that can be processed. - Another problem is that if shredder dusts remains as unburnt condition when the shredder dusts is charged to the reverberatory furnace1, this unburnt shredder dusts piles up in the reverberatory furnace 1 forming small hills (piles) in the furnace. If the dimension of these piles increases, the clearance between them and the ceiling of the reverberating furnace 1 becomes smaller. As a result, when new shredder dusts is fed to the top of the pile, the hot-gas goes out of the reverberatory furnace 1 through the feeding chute positioned directly above the flames, creating the concern that the conveyor belt used for transporting the shredder dusts may be burnt. Moreover, particularly if these large piles are formed nearby the burners inside the reverberatory furnace 1, then the burning condition of the burners is disturbed which naturally results in the burning of the shredder dusts not being possible, and also results in the burner combustion heat not being able to be used effectively for the melting of the copper concentrates.
- The present invention was achieved on the basis of these circumstances and it is an object thereof to provide an facilities for feeding shredder dusts to a reverberatory furnace capable of securing the sealing of a feeding chute when shredder dusts is fed to a reverberatory furnace used for non-ferrous smelting as described above and for ensuring that the shredder dusts is burnt properly and thereby achieving an increase in the amount of this processing that can be performed.
- In addition, a further aim of the present invention is to provide a reverberatory furnace in which the formation of large piles the reverberatory furnace caused by unburnt of shredder dusts is prevented, and in which the blocking of the propagation of burning heat from the burner is prevented, and also in which hot gas is prevented from leaking from inside the furnace.
- In order to solve the above problems and achieve these objects, the structure described below has been employed in the present invention. Namely, the present invention relates to facilities for feeding shredder dusts to a reverberatory furnace in which shredder dusts is fed to a reverberatory furnace for non-ferrous smelting, and in particular, to facilities for feeding shredder dusts to a reverberatory furnace in which a feeding chute that passes to the inside of the reverberatory furnace is fitted to the ceiling of the reverberatory furnace and shredder dusts can be fed from this feeding chute, and which also allows oxygen enriched air to be supplied to the feeding chute and fed to the inside of the reverberatory furnace.
- In this case, the feeding chute is branched partway along its length and it is desirable that the shredder dusts is fed from one end thereof while the oxygen enriched air is supplied in from the other end thereof.
- It is also desirable that an air supply nozzle that has a smaller diameter than the feeding chute is inserted in the other end of the branched feeding pipe and the distal end of the air supply nozzle is positioned adjacent to the branched portion of the feeding chute and that the oxygen enriched air is supplied in from the air supply nozzle.
- Furthermore, the present invention relates to a reverberatory furnace for non-ferrous smelting provided with the shredder dust feeding facilities, and in particular, to a reverberatory furnace for non-ferrous smelting in which a burner is able to be installed in a wall portion of one end side thereof and a plurality of feeding ports to which are connected the feeding chutes of the shredder dusts feeding facilities are provided at the one end side at a ceiling portion forming a plurality of staggered rows facing another end side.
- In this case, it is desirable that, in the ceiling portion, the one end side where the feeding ports are provided is raised above the other end side.
- Moreover, it is desirable that a feeding chute of the feeding facilities is connected to each one of the plurality of feeding ports and the positions at which shredder dusts is fed to the feeding hoppers are arranged in a single row.
- FIG. 1 is a plan view showing the schematic structure of a reverberatory furnace according to the present invention.
- FIG. 2 is a side view as seen from the direction of the arrow A in FIG. 1 showing the schematic structure of the feeding facilities according to the present invention.
- FIG. 3 is a side cross sectional view showing in detail a portion of the reverberatory furnace according to the present invention.
- FIG. 4 is a horizontal cross sectional view of the reverberatory furnace shown in FIG. 3 (wherein below the center line O shows the cross section along the line B-B in FIG. 3).
- FIG. 5 is a half sectional view taken along the line C-C in FIG. 3.
- FIG. 6 is a plan view showing in detail a portion of the feeding facilities according to the present invention.
- FIG. 7 is a cross sectional view taken along the line D-D in FIG. 6.
- FIG. 8 is a cross sectional view taken along the line E-E in FIG. 6.
- FIG. 9 is a flow chart for when shredder dusts is fed to a reverberatory furnace used for smelting copper concentrates.
- FIGS. 1 through 8 show an embodiment of the present invention. In this embodiment, the present invention is applied to a green charge type (wet charge type) of
reverberatory furnace 21 used for smelting copper concentrates. In the present embodiment, as is shown in FIG. 1,reverberatory furnaces feeding ports 22 . . . are provided in eachceiling portion 21 a of thereverberatory furnaces dusts feeding facilities 23 is provided for each of thefeeding ports 22 . . . As is shown in FIG. 1 and in FIGS. 3 to 5, as seen in plan view, thereverberatory furnaces 21 are formed in a substantially elongated schematic box shape and one end side in the longitudinal direction thereof (i.e. the bottom side in FIG. 1 and the right side in FIGS. 3 and 4) is the side where the burner is provided. A plurality ofwindow portions 21 c for burner installation are formed in thewall portion 21 b of the one end side in the longitudinal direction, and twowaste heat boilers reverberatory furnace 21 at thewall portion 21 d of the other end side in the longitudinal direction (i.e. at the top side in FIG. 1 and the left side in FIGS. 3 and 4). Note that a plurality of unillustrated hoppers used for inserting copper concentrates are provided at the burner side of theceiling portions 21 a of thereverberatory furnaces 21 in a line along thewall portions reverberatory furnace 21. - Approximately half of each
ceiling portion 21 a of thereverberatory furnaces 21 at the one end side in the longitudinal direction where the burner is situated is formed slightly raised above the other end side, as is shown in FIG. 3, and the above eightfeeding ports 22 . . . are provided at this raised portion at the one end side. Thesefeeding ports 22 . . . are arranged in two rows as seen in plan view in the vicinity of the center line O in the transverse direction of the reverberatory furnace 21 (i.e. in the horizontal direction in FIGS. 1 and 5 and in the vertical direction in FIG. 4) such that the same number (four) thereof are placed on either side of this center line O and in rows parallel thereto. In addition, the distance from each row offeeding ports 22A . . . and 22B . . . to the center line O is equal. - In addition, the four
feeding ports 22A . . . and 22B . . . in each row are arranged equidistantly in the direction of the center line O, namely, in the aforementioned longitudinal direction. Moreover, the distance betweenadjacent feeding ports adjacent feeding ports ports 22A and the feedingports 22B are arranged so as to alternate in a staggered (i.e. zigzag) pattern along the direction of the center line O. Note that the portion of theceiling portion 21 a where these feedingports 22 . . . are provided is constructed as a water cooled copper jacket. - As is shown in FIG. 2, the bottom ends of the
feeding facilities 23 provided for each of the feedingports 22 . . . arranged in this way are connected to the feedingports 22 and open onto the inside of thereverberatory furnace 21. In addition, thefeeding facilities 23 are provided with feedingchute 25 that are provided at theceiling portion 21 a so as to extend vertically upwards. More specifically, as is shown in FIGS. 6 to 8,branch pipes 26 having the same diameter as the feedingchute 25 branch out extending in a diagonally upward direction from partway along the vertically extendingfeeding chutes 25. In addition,air supply nozzles 27 having a smaller diameter than the feedingchutes 25 are inserted coaxially with the feedingchutes 25 into the feedingchutes 25 from the top end thereof.Hoppers 28 are provided via a freely removable insertion damper at the top end portion of thebranch pipes 26, namely, at the position where shredder dusts is fed to thefeeding chutes 25. At the top end portion of the feedingchutes 25 into which theair supply nozzles 27 are inserted, the peripheries of theair supply nozzles 27 are sealed bylid bodies 29. Anobservation window 29 a manufactured from heat resistant glass and aninspection opening 29 b that is normally closed are provided in eachlid body 29. - Here, as is shown in FIG. 7, in the
feeding facilities 23A . . . attached to the fourfeeding ports 22A . . . forming the aforementioned one row from out of thefeeding facilities 23 attached to the feedingports 22 . . . ,short branch pipes 26 branch from a position in the upper end portion of the feedingchutes 25 diagonally upwards in a direction away from the center line O along a plane that intersects the center line O. In contrast, as is shown in FIG. 8, in thefeeding facilities 23B . . . attached to the feedingports 22B . . . forming the other row and positioned on the opposite side of the center line O from the one row of feedingports 22A . . . ,long branch pipes 26 branch from a position in the bottom end portion of the feedingchutes 25 diagonally upwards at a sloping angle equal to that of theabove branch pipes 26 of thefeeding facilities 23A along a plane that intersects the center line O. Furthermore, as seen in plan view, thesebranch pipes 26 extend beyond the center line O to the side of the onefeeding facilities 23A . . . (note that, for this description, in FIG. 2, the sloping angles of thebranch pipes 26 in bothfeeding facilities - By making the length and the positions where the
branch pipes 26 branch from the feedingchutes 25 different, regardless of whether or not the positions of the feedingports feeding facilities 23A . . . and 23B . . . are different, namely, regardless of whether or not the positions of the feedingchutes 25 are different, thehoppers 28 are provided on a straight line parallel with the center line O such that the positions of thehoppers 28, namely, the positions at which the shredder dust is fed to thefeeding chutes 25, have the same height and match each other in the transverse direction, as is shown in FIG. 6. Furthermore, ashuttle conveyor 30 is provided extending parallel to the center line O directly above thehoppers 28 . . . of thefeeding facilities 23A . . . and 23B . . . arranged thus in a straight line. As a result, when the insertion dampers are removed to thebranch pipes 26, as is shown in FIG. 1, by loading the shredder dust that has been transported via the conveyor belt 32 (corresponding to theconveyor belt 4 in FIG. 9) from the feed hopper 31 (corresponding to the feed hopper 3 in FIG. 9) into thehoppers 28 of eachfeed facilities 23 . . . from theshuttle conveyor 30, it is possible to feed the shredder dust into thereverberatory furnace 21 through thefeed chutes 25 via thebranch pipes 26. - The bottom ends of the
air supply nozzles 27 that are inserted into thefeed chutes 25 through thelid portions 29 from the top end portion of the feedingchutes 25 reach as far as the branch portion of thebranch pipes 26 with thefeeding chutes 25. Accordingly, in thefeeding facilities 23A in which thebranch pipes 26 branch from the top end portion of the feedingchutes 25, while the insertion depth of theair supply nozzles 27 from the top end portion of the feedingchutes 25 is shallow, in the feeding facilities 23 b in which thebranch pipes 26 branch from the bottom end portion of the feedingchutes 25, the insertion depth of theair supply nozzles 27 is deep. In this case, the bottom ends of all of theair supply nozzles 27 are positioned substantially in the center in the vertical direction of the opening formed at the branch portion of thebranch pipes 26 with thefeeding chutes 25. In contrast, the top end portion of theair supply nozzles 27 of eachfeeding facilities 23A . . . and 23B . . . are bent in a horizontal direction at the point where they protrude from thelid bodies 29 and are then connected with larger diameterair supply pipes 33. Eachair supply pipe 33 is connected to an unillustrated oxygen enriched air supply source such as, for example, theoxygen plant 5 shown in FIG. 9. Oxygen enriched air having a predetermined density and pressure is expelled from the air supply nozzles via theair supply pipes 33 and is able to be supplied into thereverberatory furnace 21 together with shredder dust fed through thebranch pipes 26. Note that anoperation floor 34 is placed at a distance above theceiling portion 21 a of thereverberatory furnace 21. In the present embodiment, theoperation floor 34 is provided with a water cooled plate to insulate it from the heat from thereverberatory furnace 21 and the top end portions of the feedingchutes 25 and thebranch pipes 26 protrude above thisoperation floor 34. - In the
facilities 23 for feeding shredder dusts to thereverberatory furnace 21 having the structure described above, in order to feed shredder dust that is inserted via thebranch pipes 26 from the feeding chutes installed via the feedingports 22 in theceiling portion 21 a of thereverberatory furnace 21 together with oxygen enriched air supplied in through theair supply nozzles 27 to thereverberatory furnace 21, the shredder dusts is inserted into thereverberatory furnace 21 while being burnt by the oxygen enriched air that is supplied together with it. Accordingly, even if the atmosphere inside thereverberatory furnace 21 becomes insufficient in oxygen, it is possible to ensure that the fed shredder dust is incinerated at a high temperature. The result of this is that shredder dust from scrapped automobiles and the like can be reliably processed without generating harmful materials such as dioxin, and also that the heat from the combustion can be used effectively for the smelting of (for example copper concentrates). Moreover, it is possible to suppress the actual formation of the aforementioned piles caused by unburnt shredder dust. - In addition, by feeding shredder dust together with oxygen enriched air to the inside of the
reverberatory furnace 21 in this way, the feedingchutes 25 and the feedingports 22 in theceiling 21 a of thereverberatory furnace 21 to which the shredder dusts is fed can be sealed by the pressure of the supplying of the oxygen enriched air. Accordingly, even if the furnace pressure inside thereverberatory furnace 21 changes and a sufficient negative pressure state cannot be maintained inside thereverberatory furnace 21, it is possible to prevent the high temperature gas inside thereverberatory furnace 21 from leaking from the feedingports 22 through thefeeding chutes 25. As a result, without providing a double damper as in a conventional chute pipe, for example, it is possible to prevent a state in which the conveyor belt of theshuttle conveyor 30 is burned from occurring, and a continuous feed of the shredder dusts becomes possible. Namely, according to thefeeding facilities 23 having the above described structure, the sealing performance is secured and it is possible to reliably burn the shredder dusts and stable, efficient processing of shredder dust can be promoted. - It should be noted that if oxygen enriched air and shredder dusts are fed in this way via the
feeding chutes 25 to the interior of thereverberatory furnace 21, it is also possible to consider, for example, a means in which thebranch pipes 26 as they are in the present embodiment are not provided, and shredder dusts is fed to a single feed pipe and is then pressure supplied by oxygen enriched air. However, in a means such as this, the risk of the shredder dusts becoming blocked inside this single feed pipe and the supply of the oxygen enriched air being obstructed and the oxygen enriched air then damaging the sealing performance described above must be considered. In contrast to this, in thefeeding facilities 23 of the present embodiment, thebranch pipes 26 are provided branching off from partway along the feedingchutes 25 and shredder dusts is fed from thesebranch pipes 26 while oxygen enriched air is supplied from the top end portion of thefeeding chutes 25. Accordingly, even if the shredder dusts becomes blocked inside thebranch pipes 26, the supply of the oxygen enriched air is not cut off and, at the least, the sealing performance can be ensured due to the oxygen enriched air and it is possible to reliably prevent high temperature gas from leaking from inside thereverberatory furnace 21. - Furthermore, in the
feeding facilities 23 of the present embodiment, when oxygen enriched air is supplied from the top end portion of the feedingchutes 25, the small diameterair supply nozzles 27 are inserted into the feedingchutes 25 and the distal end (i.e. the bottom end) thereof is positioned at the connecting portion of thebranch pipes 26 with the feedingchutes 25, and oxygen enriched air is supplied from theair supply nozzles 27 at a predetermined pressure into the feedingchutes 25 and fed into thereverberatory furnace 21. Accordingly, because the portions inside thebranch pipes 26 where they connect to thefeeding chutes 25 are placed in a negative pressure condition by the oxygen enriched air supplied in via theair supply nozzles 27, the shredder dusts inserted into thebranch pipes 26 from thehoppers 28 is fed by being sucked into thefeeding chutes 25. As a result, it is possible to prevent the shredder dusts from becoming blocked and to achieve a reliable and smooth feed of shredder dusts. - In addition, in the
reverberatory furnace 21 of the present embodiment, in theceiling portion 21 a, the plurality of feedingports 22 in which theabove feeding facilities 23 are provided are placed in a staggered arrangement running from thewall portion 21 b of thereverberatory furnace 21 in which the burners are placed in the longitudinal direction of thereverberatory furnace 21, namely, in the direction of the burning by the burners. As a result, it is possible to prevent the formation of the above described large piles inside thereverberatory furnace 21 and to prevent flames from escaping out from the feedingports 22 . . . and the burning of the burner being obstructed. Namely, by placing the feedingports 22 . . . in a staggered arrangement, the distance between each of the feedingports ceiling 21 a is maintained and flames are prevented from escaping. In addition, it is possible to spread the burning of the burner over the whole interior of the reverberatory furnace 21 (i.e. as far as the other side) and to melt the copper concentrates, and also to effectively use the heat of the burning of the fed shredder dust. - Furthermore, in the
reverberatory furnace 21 of the present embodiment, the portion at one end side of theceiling portion 21 a in the longitudinal direction of thereverberatory furnace 21 where the burner is situated is formed slightly raised above the other end side, and the feedingports 22 . . . are provided in a staggered arrangement in this raised portion. Accordingly, even if the above described piles do become formed, it is possible to ensure that a sufficient clearance is maintained between the piles and theceiling portion 21 a, therefore, it is possible to even more reliably prevent flames from leaking. - It should be noted that when the feeding
ports 22 . . . are arranged in two rows in a staggered arrangement in this manner, if the feedingchutes 25 . . . of thefeeding facilities 23 . . . connected to the feedingports 22 . . . are only provided in theceiling portion 21 a extending vertically, then the feed positions where shredder dusts is fed to these feedingpipes 25 . . . , namely, the positions of thehoppers 28 . . . also end up being arranged in two staggered rows. Accordingly, in order to insert the shredder dusts into this type ofhopper 28 . . . , it is necessary to provide two rows of shuttle conveyors for transporting the shredder dusts from theconveyor belt 32 to asingle reverberatory furnace 21. - In contrast, in the case of the
reverberatory furnace 21 of the present embodiment, in thefeeding facilities 23A . . . attached to the feedingports 22A . . . forming the one row parallel to the center line O in thereverberatory furnace 21 from out of the feedingports 22 . . . arranged in a staggered pattern,short branch pipes 26 branch from a position in the upper end portion of the feedingpipes 25 while, in thefeeding facilities 23B . . . attached to the feedingports 22B . . . forming the other row,long branch pipes 26 branch from a position in the bottom end portion of the feedingchutes 25 parallel to thebranch pipes 26 of thefeeding facilities 23A. Furthermore, the top end positions of thebranch pipes 26 . . . to which the shredder dusts is fed match each other in height and in their positions in the transverse direction and a single row of thehoppers 28 . . . is provided at the top end thereof. Accordingly, in thisreverberatory furnace 21, there only needs to be a single row of theshuttle conveyor 30 for feeding the shredder dust from thehoppers 28 . . . to thefeed chutes 25 . . . of each of thefeed facilities 23A . . . and 23B . . . via thebranch pipes 26 . . . As a result, even if there are a plurality of rows of the feedingports 22 . . . arranged in a staggered pattern, there does not need to be a plurality of rows ofshuttle conveyors 30, which is economical as well as efficient. - Note that, in this
reverberatory furnace 21, the feedingports 22 . . . are arranged in two rows in a staggered pattern, however, it is also possible for the feedingports 22 . . . to be arranged in three or more rows in the above staggered pattern depending on the size and the like of thereverberatory furnace 21. Moreover, in each row of thefeeding facilities 23A . . . and 23B . . . , instead of forming thebranch pipes 26 all at an equal slope angle branching out from different positions of the feedingchutes 25, as described above, it is possible, as is shown in FIG. 2, to providebranch pipes 26 having different slope angles and to make both the branch position and the slope angle different. In these examples, in the same way as in the present embodiment, it is also possible to make the positions (the positions of thehoppers 28 . . . in the present embodiment) from which the shredder dusts is fed to thefeed chutes 25 . . . in one row.
Claims (6)
1. Facilities for feeding shredder dusts to a reverberatory furnace in which shredder dusts is fed to a reverberatory furnace for non-ferrous smelting and is burned, wherein a feeding chute that passes to the inside of the reverberatory furnace is fitted to a ceiling of the reverberatory furnace and shredder dusts can be fed from the feeding pipe, and wherein oxygen enriched air can also be supplied to the feeding nozzle and fed to the inside of the reverberatory furnace.
2. The facilities for feeding shredder dusts according to claim 1 , wherein the feeding chute is branched partway along its length and the shredder dusts is fed from one end of the branched pipe while the oxygen enriched air is supplied in from the other end of the branched pipe.
3. The facilities for feeding shredder dusts according to claim 1 or 2, wherein an air supply nozzle that has a smaller diameter than the feeding chute is inserted in the other end of the branched feeding chute and the distal end of the air supply nozzle is positioned adjacent to the branched portion of the feeding chute and the oxygen enriched air is supplied in from the air supply nozzle.
4. A reverberatory furnace for non-ferrous smelting provided with the shredder dusts feeding facilities, wherein a burner is able to be installed in a wall portion of one end side of the reverberatory furnace and a plurality of feeding ports to which are connected the feeding chutes of the shredder dusts feeding facilities are provided at the one end side in a ceiling portion forming a plurality of staggered rows facing the other end side.
5. The reverberatory furnace according to claim 4 , wherein in the ceiling portion, the one end side where the feeding ports are provided is raised above the other end side.
6. The reverberatory furnace according to claim 4 or 5, wherein a feed chute of the feed facilities is connected to each one of the plurality of feeding ports and the positions at which shredder dusts is fed to the feeding hoppers are arranged in a single row.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/075,162 US6764642B2 (en) | 2001-06-26 | 2002-02-14 | Shredder dust feeding device, reverberatory furnace provided with this feeding device, and furnace for burning shredder dust |
US10/869,528 US20040222575A1 (en) | 2001-06-26 | 2004-06-16 | Shredder dust feeding device, reverberatory furnace provided with this feeding device, and furnace for burning shredder dust |
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JPP2000-247039 | 2000-08-16 | ||
JP2000247040A JP2002061817A (en) | 2000-08-16 | 2000-08-16 | Reverberatory furnace provided with shredder dust feeder |
JPP2000-247040 | 2000-08-16 | ||
JP2000247039A JP4549500B2 (en) | 2000-08-16 | 2000-08-16 | Equipment for supplying shredder dust to a reverberatory furnace |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/075,162 Continuation-In-Part US6764642B2 (en) | 2001-06-26 | 2002-02-14 | Shredder dust feeding device, reverberatory furnace provided with this feeding device, and furnace for burning shredder dust |
Publications (1)
Publication Number | Publication Date |
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US20020053306A1 true US20020053306A1 (en) | 2002-05-09 |
Family
ID=26598020
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US09/896,203 Abandoned US20020053306A1 (en) | 2000-08-16 | 2001-06-29 | Shredder dust feeding facilities and reverberatory furnace provided with this feeding facilities |
Country Status (3)
Country | Link |
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US (1) | US20020053306A1 (en) |
CA (1) | CA2340271A1 (en) |
SG (1) | SG89381A1 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20020195754A1 (en) * | 2001-06-26 | 2002-12-26 | Onahama Smelting And Refining Co., Ltd | Shredder dust feeding device, reverberatory furnace provided with this feeding device, and furnace for burning shredder dust |
EP1457270A1 (en) * | 2003-03-12 | 2004-09-15 | Voest-Alpine Industrieanlagenbau GmbH & Co. | Process for the utilisation of coarse shredder-residue in a fusion cyclone |
US20150176102A1 (en) * | 2013-06-21 | 2015-06-25 | Mitsubishi Materials Corportion | Method for treating combustible material and installation |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5839214B2 (en) * | 1977-12-30 | 1983-08-29 | 三菱マテリアル株式会社 | Non-ferrous metal smelting method |
US4274870A (en) * | 1979-04-25 | 1981-06-23 | Newmont Exploration Limited | Smelting of copper concentrates by oxygen injection in conventional reverberatory furnaces |
JPS57210931A (en) * | 1981-06-18 | 1982-12-24 | Onahama Smelt & Refining Co Ltd | Automatic charging method for ore into copper smelting reverberatory furnace |
-
2001
- 2001-03-09 SG SG200101454A patent/SG89381A1/en unknown
- 2001-03-09 CA CA 2340271 patent/CA2340271A1/en not_active Abandoned
- 2001-06-29 US US09/896,203 patent/US20020053306A1/en not_active Abandoned
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20020195754A1 (en) * | 2001-06-26 | 2002-12-26 | Onahama Smelting And Refining Co., Ltd | Shredder dust feeding device, reverberatory furnace provided with this feeding device, and furnace for burning shredder dust |
US6764642B2 (en) * | 2001-06-26 | 2004-07-20 | Onahama Smelting And Refining Co., Ltd. | Shredder dust feeding device, reverberatory furnace provided with this feeding device, and furnace for burning shredder dust |
US20040222575A1 (en) * | 2001-06-26 | 2004-11-11 | Onahama Smelting And Refining Co., Ltd. | Shredder dust feeding device, reverberatory furnace provided with this feeding device, and furnace for burning shredder dust |
EP1457270A1 (en) * | 2003-03-12 | 2004-09-15 | Voest-Alpine Industrieanlagenbau GmbH & Co. | Process for the utilisation of coarse shredder-residue in a fusion cyclone |
US20150176102A1 (en) * | 2013-06-21 | 2015-06-25 | Mitsubishi Materials Corportion | Method for treating combustible material and installation |
US9745643B2 (en) * | 2013-06-21 | 2017-08-29 | Mitsubishi Materials Corporation | Method for treating combustible material and installation |
Also Published As
Publication number | Publication date |
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SG89381A1 (en) | 2002-06-18 |
CA2340271A1 (en) | 2002-02-16 |
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Owner name: ONAHAMA SMELTING AND REFINING CO., LTD., JAPAN Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:NISHIWAKI, MICHIO;TOBE, KIYOMI;SATO, TAKAYUKI;REEL/FRAME:012334/0066 Effective date: 20011001 |
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STCB | Information on status: application discontinuation |
Free format text: EXPRESSLY ABANDONED -- DURING EXAMINATION |