JP5770984B2 - Rotary kiln and metal recovery method - Google Patents

Description

  The present invention relates to a rotary kiln capable of recovering metal from an object to be processed and a metal recovery method using the rotary kiln.

  2. Description of the Related Art As a conventional rotary kiln, a rotary kiln having a rotary furnace that performs a combustion process on an object to be processed containing metal is known (for example, see Patent Document 1). This rotary kiln is melted by burning while rotating a substrate of a household appliance or the like in a rotary furnace, and dropping the melt from the outlet of the rotary furnace to a slag cooling device. The slag cooling device forms a crushed mass by cooling and crushing the melt with water. The crushed lump is separated into a metal crushed lump and a slag crushed litter by a magnetic separator or the like.

JP 2008-139209 A

  However, the conventional rotary kiln is inefficient because it is necessary to cool the workpiece once melted, transport the crushed mass to another apparatus, and separate the metal and slag. In addition, it is necessary to cool the workpiece once heated, and there is a need for improvement in terms of energy efficiency. Furthermore, the magnetic beneficiation method as described above has a limit in the metal recovery rate, and the metal may not be sufficiently recovered from the object to be processed. From the above, there has been a demand for efficiently recovering metal from the object to be processed and improving the recovery rate.

  Then, an object of this invention is to provide the rotary kiln which can improve a recovery rate while recovering | recovering a metal efficiently from a to-be-processed object.

  A rotary kiln according to the present invention is electrically connected to a rotary furnace that burns a workpiece containing metal, and a melt of the workpiece that is connected to the rotary furnace via a connecting portion and burned in the rotary furnace. An electric furnace for separating metal by heat treatment, and a reducing agent supply means for supplying a reducing agent to the electric furnace are provided.

  According to the rotary kiln according to the present invention, the electric furnace can further separate the metal from the melt of the object to be processed that has been subjected to the combustion process in the rotary furnace by an electric heat treatment. Thereby, the metal contained in the melt of the object to be processed can be recovered. In addition, since the electric furnace is connected to the rotary furnace via the connecting portion, the object to be processed is subjected to a combustion process in the rotary furnace, and without requiring a cooling process or a process of moving to the next processing apparatus. Immediately charged into the electric furnace as a melt. Therefore, metal recovery from the object to be processed can be performed efficiently. Furthermore, since there is no step for cooling the melt of the workpiece discharged from the rotary furnace, the heat from the combustion process in the rotary furnace can be effectively used for the heat treatment in the electric furnace, improving energy efficiency. be able to. Further, since the reducing agent supply means can supply the reducing agent to the electric furnace, more metal can be recovered by reducing the metal oxide contained in the melt in the electric furnace. . As described above, the metal can be efficiently recovered from the workpiece and the recovery rate can be improved.

  Moreover, in the rotary kiln according to the present invention, it is preferable that the electric furnace is disposed below the outlet of the rotary furnace, and an object to be processed falling in a non-contact manner with the connection portion is input. The melt of the object to be processed, which is burned and processed in the rotary furnace, falls down as it is without being brought into contact with the connecting portion and is put into the electric furnace. For example, when the melt discharged from the rotary furnace is introduced into the electric furnace through the inner wall of the connection portion, the heat of the melt is taken away by the inner wall of the connection portion and solidifies and adheres. On the other hand, according to the rotary kiln according to the present invention, heat related to the combustion process in the rotary furnace can be supplied to the electric furnace without being taken away by other members. This further improves energy efficiency for metal recovery.

  Further, in the rotary kiln according to the present invention, the electric furnace includes an input portion into which the melt of the object to be processed is charged, an electrode that heats the melt of the object to be processed by electricity, and discharges the melt of the object to be processed It is preferable that the charging portion, the electrode, and the discharging port for the electric furnace are arranged in the predetermined direction in the order of the charging portion, the electrode, and the discharging port for the electric furnace. As a result, the melt of the workpiece to be processed that has been input from the input unit into the electric furnace passes through the vicinity of the electrode, is sufficiently heated to separate the metal, and is then discharged from the discharge port for the electric furnace. This improves the metal recovery efficiency.

  Moreover, in the rotary kiln according to the present invention, the electric furnace is preferably disposed below the outlet of the rotary furnace, and is disposed downstream of the rotary furnace in the rotation direction when viewed from the rotation axis direction of the rotary furnace. . Since the melt of the workpiece to be burned is discharged in a state where the rotary furnace is rotated, it falls from the position downstream of the rotational axis to the downstream side at the outlet of the rotary furnace. Since the electric furnace is disposed on the downstream side in the rotation direction, the connecting portion is also configured in accordance with the position of the electric furnace. As a result, the molten material of the object to be processed can be put into the electric furnace without coming into contact with the inner wall or the like of the connection portion, even though the dropping position is shifted by the rotation.

  In the rotary kiln according to the present invention, the rotary furnace preferably has a rotary furnace discharge port for discharging the metal separated from the workpiece by the combustion process through the peripheral wall. As a result, the high-purity metal separated at the stage of the combustion treatment in the rotary furnace can also be recovered from the rotary furnace outlet in the stage before being introduced into the electric furnace.

  The metal recovery method according to the present invention is characterized by using the above-described rotary kiln to recover metal from an object to be processed containing metal. By using the above-described rotary kiln, the metal can be efficiently recovered from the object to be processed, and the recovery rate can be improved.

  In the metal recovery method according to the present invention, specifically, any one of Au, Ag, Cu, Pd, Pb, and Sn is recovered as a metal. Moreover, in the metal recovery method according to the present invention, slag obtained when smelting any one of waste electronic substrates, wire scraps, or copper, gold, and silver is used as a raw material.

  ADVANTAGE OF THE INVENTION According to this invention, while recovering a metal efficiently from a to-be-processed object, a recovery rate can be improved.

It is a schematic sectional drawing which shows the structure of the rotary kiln which concerns on embodiment of this invention. It is sectional drawing which shows the schematic structure of an electric furnace. 3 is a cross-sectional view taken along the line III-III shown in FIG. FIG. 4 is a cross-sectional view taken along the line IV-IV shown in FIG. It is a graph which shows the relationship between the density | concentration of slag in an electric furnace, and a residence time after it inputs from a rotary furnace until it discharges | emits from a slag discharge port. It is a table | surface which concerns on the experimental result which shows the effect of the rotary kiln which concerns on this invention.

  Hereinafter, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings.

  FIG. 1 is a schematic cross-sectional view showing a configuration of a rotary kiln according to an embodiment of the present invention. As shown in FIG. 1, the rotary kiln 1 includes a rotary furnace 2, a secondary combustion chamber 3, a communication chute (connection part) 4, and an electric furnace 6. The rotary kiln 1 separates a workpiece W containing metal into slag and metal using a rotary furnace 2 or an electric furnace 6 and collects the metal. The to-be-processed object W containing a metal is a board | substrate, such as household appliances, a wire scrap, a copper-gold-silver basket, etc., for example. Moreover, the metal contained in these, ie, the metal which can be collect | recovered with the rotary kiln 1 which concerns on this embodiment, is Cu, Au, Ag, Pb, Sn, Pd, etc.

  The rotary furnace 2 melts the workpiece W by burning it. The rotary furnace 2 has a cylindrical shape, and its inner wall is lined with a refractory material. The rotary furnace 2 can burn the workpiece W at 1400 to 1500 ° C. with hot air from the burner 10. The rotary furnace 2 is rotatably supported by a support portion (not shown) fixed on the base and is rotated by a driving device. The rotary furnace 2 is installed with the rotation axis inclined, and thereby flows from the high side inlet 2a to the low side outlet 2b while burning the workpiece W put into the rotary furnace 2. Let On the inlet 2 a side of the rotary furnace 2, a charging chute 7 for loading the workpiece W and a loading pusher 8 for pushing the loaded workpiece W into the rotary furnace 2 are provided. In the rotary kiln 1 according to the present embodiment, it is not necessary to adjust components by adding an additive or the like. Since the component adjustment is not performed, an increase in the slag S is prevented. In order to prevent damage to the refractory, the rotary furnace 2 is protected by water film cooling. The combustion treatment temperature of the rotary kiln 1 according to the present embodiment is as high as 1400 to 1500 ° C., and the refractory is greatly damaged, and the melting point of the workpiece W can be lowered by adjusting the components by adding additives or the like. In this case, the slag S increases. Therefore, it burns without using an additive as much as possible, and the refractory is protected by cooling the rotary furnace 2 with a water film.

  In the rotary furnace 2, the melt of the workpiece W that has been subjected to the combustion process is separated into the slag S and the metal M1 due to the difference in specific gravity. Further, the combustible material in the workpiece W is pyrolyzed and gasified. The metal M1 separated from the workpiece W becomes molten or semi-molten and accumulates on the lower layer side. The surface of the molten metal M1 is covered with a sufficient amount of slag. This prevents the molten metal M1 from being oxidized. The rotary furnace 2 is configured to be able to take out the molten metal M1 through a cylindrical peripheral wall 2c by a tapping method. Specifically, the rotary furnace 2 has a tapping nozzle (discharge port) 9 that can drop and discharge the molten metal M1 accumulated at the bottom of the rotary furnace 2 downward through the peripheral wall 2c. Have. The tapping nozzle 9 is attached to the peripheral wall 2 c of the rotary furnace 2. Specifically, after the melting operation is continued in the rotary furnace 2 for a predetermined time, the rotary furnace 2 is stopped at a timing at which the tapping nozzle 9 is disposed at a predetermined position (position other than the bottom), and the tapping nozzle 9 To open. Thereafter, the rotation of the rotary furnace 2 is resumed, and the tapping nozzle 9 is disposed at the bottom position so as to be immersed in the molten metal M1 portion. Thus, the metal M1 is discharged by its own weight through the tapping nozzle 9, and is cast into an ingot forming apparatus such as a mold and cooled. When the discharge of the metal M1 is completed, the slag S is also discharged from the tapping nozzle 9, so that the rotation of the rotary furnace 2 is restarted at the timing when the discharge of the slag S is confirmed, and the tapping nozzle 9 is closed. By repeating such an operation, the metal M1 separated in the rotary furnace 2 can be selectively recovered. In addition, the molten material thrown into the electric furnace 6 from the rotary furnace 2 may contain not only the slag S but also a part or all of the metal M1 that could not be recovered by the rotary furnace 2.

  The secondary combustion chamber 3 can decompose the gas generated in the rotary furnace 2 to decompose, for example, dioxins and malodorous substances, and supply them to the exhaust gas treatment facility. The secondary combustion chamber 3 is connected to the outlet 2 b of the rotary furnace 2. In the secondary combustion chamber 3, a burner 11 for secondary combustion is installed near the outlet 2 b of the rotary furnace 2, and a supply device and a stirring blower for supplying urea, air, and SCC temperature-controlled water are further installed on the upper side. It has been.

  The communication chute 4 is a communication passage that connects the rotary furnace 2 and the electric furnace 6. The communication chute 4 is provided so as to extend downward from the lower side of the secondary combustion chamber 3 and communicates with the secondary combustion chamber 3. The position of the wall surface portion constituting the communication chute 4 is adjusted so that the slag S discharged from the outlet 2b of the rotary furnace 2 and the inner wall surface do not contact each other. With such a configuration, the slag S is not in contact with the inner wall surface of the communication chute 4 and is vertical in the communication chute 4 (or depending on the rotational force of the rotary furnace 2 and the flow velocity in the rotary furnace 2, It is dropped into the electric furnace 6 with an angle. Since the slag S does not come into contact with the connecting chute 4, the heat of the slag S is supplied into the electric furnace 6 without being taken away by the wall surface portion of the connecting chute 4 or attached and solidified. A burner 12 is attached to the communication chute 4. The burner 12 is an emergency melting means when the slag S is clogged with the communication chute 4 or when the slag S adheres to the wall surface of the communication chute 4. That is, when the slag S is clogged, it is heated and melted and dropped.

  The electric furnace 6 is connected to the rotary furnace 2 through the communication chute 4, and separates the metal from the melt of the workpiece W burned in the rotary furnace 2 by heat treatment using electricity. In the present embodiment, the metal remaining in the slag S separated in the rotary furnace 2 can be recovered. The electric furnace 6 is an electric resistance heating furnace, and includes a tank 20 that retains the melt and separates the metal M2 from the slag S, and electrodes 21A, 21B, and 21C that heat the slag S by electricity. In the tank 20, a molten metal M2 layer is formed on the lower side, and a molten slag S layer is formed on the upper side. The electric furnace 6 is connected with a coke supply device 22A for supplying coke as a reducing agent into the electric furnace 6 via a supply line 22B. In addition to coke, coal and waste carbon can be used as the reducing agent. The electric furnace 6 discharges the metal M2 in the tank 20 through the metal recovery line 23 and discharges the slag S in the tank 20 through the slag recovery line 24. Such an electric furnace 6 can heat the slag S staying with heat efficiency more efficiently than when the slag S is heated with a burner or the like.

  The slag S introduced from the outlet 2b of the rotary furnace 2 contains a metal content of several percent as metal fine particles or metal oxide. The electric furnace 6 melts the metal content in the slag S by Joule heat between the electrodes 21A, 21B, and 21C, and separates it as a molten metal M2. At this time, the metal oxide contained in the slag S is reduced by the reduction effect by the coke supplied from the coke supply device 22A, and can be recovered as the metal M2. By retaining in the tank 20 of the electric furnace 6 for 3 to 6 hours while keeping the temperature at 1400 to 1500 ° C., almost all of the metal components in the slag S can be recovered as the metal M2.

  Next, with reference to FIG.2, FIG3 and FIG.4, the structure of the electric furnace 6 in the rotary kiln 1 and its periphery is demonstrated in detail. FIG. 2 is a cross-sectional view showing a schematic configuration of the electric furnace 6. 3 is a cross-sectional view taken along the line III-III shown in FIG. FIG. 4 is a cross-sectional view taken along the line IV-IV shown in FIG. As shown in FIGS. 2, 3, and 4, the tank 20 of the electric furnace 6 includes a retention portion 31 for retaining the slag S and the metal M <b> 2 and a lid portion 32 that blocks the upper side of the retention portion 31. Yes. The tank 20 has an oval shape when viewed from above, and a portion surrounded by the inner side surface 31b of the staying portion 31 also has an oval shape. Further, the bottom surface 31a of the staying portion 31 is inclined toward the metal discharge port 33 and the slag discharge port 34.

  A top portion 32 a of the lid portion 32 of the tank 20 is formed with an insertion portion 35 that is connected to the communication chute 4. By fixing the charging portion 35 and the lower end portion 4 a of the communication chute 4, the communication chute 4 and the inside of the tank 20 of the electric furnace 6 are communicated. The charging unit 35 and the communication chute 4 are arranged on one end side of the oval shape of the tank 20. That is, the slag S dropped from the rotary furnace 2 is thrown into one end side of the oval shape of the tank 20.

  The retention part 31 of the tank 20 includes a metal discharge port 33 for discharging the metal M2 in the tank 20 and a slag discharge port 34 for discharging the slag S in the tank 20. The metal discharge port 33 and the slag discharge port 34 are arranged on the other end side of the oval shape of the tank 20. That is, the slag S and the metal M2 staying in the tank 20 are discharged from the other end side of the oval shape of the tank 20. The metal discharge port 33 is formed by penetrating the side wall of the staying portion 31 in accordance with the height of the lower metal M2 layer, and is connected to the metal recovery line 23. The slag discharge port 34 is formed by penetrating the side wall of the staying portion 31 at a position higher than the metal discharge port 33 in accordance with the height of the upper slag S layer, and is connected to the slag recovery line 24. In addition, the metal discharge port 33 and the slag discharge port 34 are arranged so as to be shifted from each other when viewed from above.

  Electrodes 21 </ b> A, 21 </ b> B, and 21 </ b> C extending in the vertical direction are inserted into the upper surface wall 32 a of the lid portion 32 of the tank 20. The electrodes 21A, 21B, and 21C are disposed between the insertion portion 35, the metal discharge port 33, and the slag discharge port 34, and are arranged in the direction D1 from the one end side of the tank 20 toward the other end side. 21A, electrode 21B, and electrode 21C are arranged in a straight line in this order (see FIG. 4).

  Here, as shown in FIG. 3, the slag S in the rotary furnace 2 falls while the rotary furnace 2 is rotating. Therefore, the slag S falls at a position on the downstream side in the rotation direction from the position directly below the rotation axis CL at the bottom of the rotary furnace 2. That is, when the rotary furnace 2 rotates counterclockwise in FIG. 3, the slag S falls at a position closer to the right side of the drawing. The position of the electric furnace 6 and the configuration of the connecting chute 4 are set so that the slag S can fall in non-contact with the inner wall surface in accordance with such a shift in the dropping position of the slag S. Specifically, the electric furnace 6 is arranged on the downstream side in the rotation direction of the rotary furnace 2 when viewed from the rotation axis direction CL. In accordance with the position of the electric furnace 6, the lower end portion 4 a of the communication chute 4 is also arranged on the downstream side in the rotation direction of the rotary furnace 2. That is, the electric furnace 6 and the lower end portion 4a of the communication chute 4 are disposed closer to the right side of the drawing in FIG. 3 than the rotation axis CL.

  Next, the flow of the slag and the separated metal in the rotary kiln 1 configured as described above will be described. First, the workpiece W put into the charging chute is pushed into the rotary furnace 2 by the charging pusher 8. The workpiece W is combusted in the rotary furnace by hot air from the burner 10. By the combustion treatment, the workpiece W is melted and separated into a slag S layer and a metal M1 layer. The metal M1 on the lower layer side is recovered from the tapping nozzle 9. The upper layer-side slag S falls from the outlet of the rotary furnace 2 and is charged into the electric furnace 6 via the charging unit 35 without contacting the inner wall of the communication chute 4 or the like. From the slag S staying in the tank 20, the metal M2 is separated by heat treatment with electricity in the electrodes 21A, 21B, and 21C. Further, more metal M2 is separated by the reduction reaction by coke of the metal oxide contained in the slag S. The separated metal M2 accumulates on the bottom side of the tank 20. The separated metal M2 is recovered from the metal recovery line 23, and the slag S from which the metal content has been removed is recovered from the slag recovery line 24. In addition, the residence time in the tank 20 of the slag S thrown in from the injection | throwing-in part 35, ie, the time from when the slag S fell through the injection | throwing-in part 35, to the discharge | emission of the said slag S is 3 to 6 hours It is. This residence time is adjusted by the input amount, the discharge amount, and the volume of the tank 20.

  Next, the operation and effect of the rotary kiln 1 according to this embodiment will be described.

  In the rotary kiln 1 according to the present embodiment, the electric furnace 6 can further separate the metal from the melt of the workpiece W (the slag S in the present embodiment) burned in the rotary furnace 2 by electric heat treatment. it can. Thereby, the metal contained in the slag S that is the melt of the workpiece W can be recovered. Moreover, since the electric furnace 6 is connected to the rotary furnace 2 via the communication chute 4, the workpiece W is burned in the rotary furnace to become the slag S, and then to the cooling process or the next processing apparatus. Immediately, the electric furnace 6 is charged without requiring a moving process. Therefore, metal recovery from the workpiece W can be performed efficiently. Furthermore, since the process of cooling the slag S discharged from the rotary furnace 2 does not enter, the heat from the combustion process in the rotary furnace 2 can be effectively used for the heat treatment in the electric furnace 6, and energy efficiency is improved. Can do. Further, since the coke supply device 22A can supply coke as a reducing agent to the electric furnace 6, more metal can be obtained by reducing the metal oxide contained in the slag S in the electric furnace 6. It can be recovered. As described above, the metal can be efficiently recovered from the workpiece W and the recovery rate can be improved.

  Further, in the rotary kiln 1 according to the present embodiment, the electric furnace 6 is disposed below the outlet 2b of the rotary furnace 2, and slag S that falls in a non-contact manner with the communication chute 4 is introduced. The slag S that is combusted in the rotary furnace 2 and discharged is dropped directly into the electric furnace 6 without contacting the communication chute 4. For example, when the slag S discharged from the rotary furnace 2 is introduced into the electric furnace 6 through the inner wall of the communication chute 4, the heat of the slag S is taken by the inner wall of the communication chute 4 and solidifies and adheres. On the other hand, according to the rotary kiln 1 according to the present embodiment, the heat related to the combustion process in the rotary furnace 2 can be supplied to the electric furnace 6 without being taken away by other members or without trouble due to solidification adhesion. This further improves energy efficiency and availability for metal recovery.

  Further, in the rotary kiln 1 according to the present embodiment, the insertion portion 35, the electrodes 21A, 21B, 21C, the metal discharge port 33, and the slag discharge port 34 are arranged in this order toward the direction D1 shown in FIG. Has been. As a result, the slag S charged into the electric furnace 6 from the charging unit 35 is sufficiently heated by the electrodes 21A, 21B, and 21C to separate the metal M2, and then discharged from the slag discharge port 34. Thereby, the recovery efficiency of the metal M2 is improved.

  Further, in the rotary kiln 1 according to the present embodiment, the electric furnace 6 is disposed below the outlet 2b of the rotary furnace 2, and is downstream in the rotation direction of the rotary furnace 2 when viewed from the rotation axis CL direction of the rotary furnace 2. Arranged on the side. Since the slag S, which is a melt of the workpiece W that has been subjected to the combustion treatment, is discharged in a state in which the rotary furnace 2 is rotated, the rotation direction of the slag S at the outlet 2b of the rotary furnace 2 is less than the position directly below the rotation axis CL. It falls from the downstream position. Since the electric furnace 6 is disposed on the downstream side in the rotation direction, the connecting chute 4 is also configured to match the position of the electric furnace 6. As a result, the slag S can be introduced into the electric furnace 6 without contacting the inner wall of the communication chute 4 or the like, although the drop position is shifted due to the rotation.

  Moreover, in the rotary kiln 1 which concerns on this embodiment, it is preferable that the rotary furnace 2 has the tapping nozzle 9 which discharges | emits the metal isolate | separated from the to-be-processed object W by the combustion process through the surrounding surface wall 2c. As a result, the high-purity metal that is separated at the stage of the combustion treatment in the rotary furnace 2 can be recovered from the tapping nozzle 9 at a stage before being introduced into the electric furnace 6. In the present embodiment, the metal M1 recovered in the rotary furnace 2 has a high precious metal concentration, and the metal M2 separated in the electric furnace 6 also reduces the iron content in the slag S due to the reduction effect, so the precious metal concentration is low. . Therefore, according to the rotary kiln 1 according to the present embodiment, the tapping nozzle 9 collects high-quality metal with few impurities, and the electric furnace 6 collects metal that could not be collected in the rotary furnace 2 as much as possible. It can be used properly as a collection of many.

  Examples of the present invention will be described below. Table 1 shown in FIG. 6A shows the metal concentration and the recovery rate of the metal M1 recovered from the tapping nozzle 9 of the rotary furnace 2 and the metal M2 recovered from the electric furnace 6 from the workpiece W according to the present invention. The experimental result in is shown.

  The values listed in Table 1 are based on the total mass of the product obtained in three days of operation, and were obtained in experiments in the case of recovering metal with the electric furnace 6 of the rotary kiln 1 according to the present invention. Indicates material balance. FIG. 5 is a graph showing the relationship between the concentration of slag S in the electric furnace 6 and the residence time from when it is introduced from the rotary furnace 2 to when it is discharged from the slag discharge port 34. FIG. 5 shows an example of the concentration of Cu among the metals contained in the workpiece W. In FIG. 5, the portion indicated by A indicates the Cu concentration of the slag S that has just dropped from the outlet 2 b of the rotary furnace 2 and has been put into the electric furnace 6. On the other hand, in FIG. 5, a portion indicated by B indicates the Cu concentration of the slag S immediately before being discharged from the electric furnace 6. As shown in FIG. 5, the Cu concentration of the slag S immediately after the addition is about 4 to 5%, whereas the Cu concentration gradually decreases as the residence time elapses (that is, the Cu concentration decrease in the slag S). The Cu concentration is 1% or less after being treated in the furnace for 2 to 4 hours. Table 2 shown in FIG. 6 (b) shows a comparison between the metal main element content and the recovery rate of the conventional method. Table 3 shown in FIG. 6C shows energy consumption in the case of performing an operation for obtaining the same recovery rate as in the example. The case where the slag S on the upper layer falls from the outlet of the rotary furnace 2 and the required energy when it is charged into the furnace via the charging part 35 is changed in the present invention by using an electric furnace and a gas burner. This is a comparison with a case where the slag S discharged in step 1 is cooled and solidified and then remelted in an electric furnace. In this way, by using the electric furnace 6 connected to the rotary furnace 2, it is possible to achieve a higher energy efficiency than before and at the same time greatly improve the metal recovery efficiency. Note that the slag S may be discharged at an earlier stage than the position indicated by B in FIG. 5 by adjusting the input amount and the discharge amount of the slag S.

  The present invention is not limited to the embodiment described above.

  For example, in the above-described embodiment, the metal M1 separated in the rotary furnace 2 is collected by the tapping nozzle 9, but there is no tapping nozzle 9, and all the melt of the workpiece W is put into the electric furnace 6. May be.

  Further, the shape of the electric furnace 6 and the arrangement positions of the charging portion 35, the electrode 21, the electrode 21A, the electrode 21B, the electrode 21C, the slag discharge port 34, and the metal discharge port 33 are not limited to those shown in the embodiment.

  Moreover, in the above-described embodiment, as a particularly preferable example, the melt discharged from the rotary furnace 2 is put into the electric furnace 6 without contacting any inner wall surface in the apparatus. The structure which contacts may be sufficient.

  DESCRIPTION OF SYMBOLS 1 ... Rotary kiln, 2 ... Rotary furnace, 4 ... Communication chute (connection part), 9 ... Tapping nozzle (rotary furnace discharge port), 22A ... Coke supply apparatus (reducing agent supply means), 21A, 21B, 21C ... Electrode , 22B ... supply line (reducing agent supply means), 33 ... metal discharge port (discharge port for electric furnace), 34 ... slag discharge port (discharge port for electric furnace), 35 ... charging part, W ... workpiece, S ... Slag (melt of processed material), M1, M2 ... Metal (melt of processed material).

Claims (6)

A rotary furnace for burning the object to be treated containing metal;
An electric furnace that is connected to the rotary furnace via a connecting portion, and separates the metal from the melt of the object to be processed in the rotary furnace by heat treatment with electricity,
A reducing agent supply means for supplying a reducing agent to the electric furnace,
The electric furnace is
An input that is disposed below the outlet of the rotary furnace and opens so that the melt of the object to be processed that falls out of contact with the connection portion communicates with an opening portion on a lower end side of the connection portion in the vertical direction. From the department ,
When viewed from the rotation axis direction of the rotary furnace,
Arranged on the downstream side in the rotation direction of the rotary furnace ,
The opening width of the opening portion of the charging portion is smaller than the radius of the inner periphery of the rotary furnace, and the upstream end of the opening portion of the charging portion in the rotation direction is the rotation axis of the rotary furnace. It is arrange | positioned in the downstream in the said rotation direction rather than the rotary kiln characterized by the above-mentioned . The electric furnace is
And the closing portion of the melt of the object to be treated is introduced,
An electrode for heat-treating the melt of the object to be processed by electricity;
An electric furnace discharge port for discharging the melt of the workpiece,
The said charging part, the said electrode, and the said outlet for electric furnace are arrange | positioned in the order of the said charging part, the said electrode, and the said outlet for electric furnace in a predetermined direction, The electric furnace of Claim 1 characterized by the above-mentioned. Rotary kiln. The rotary kiln according to claim 1 or 2, wherein the rotary furnace has a rotary furnace discharge port for discharging the metal separated from the object to be processed by a combustion process through a peripheral wall. The metal collection | recovery method which collect | recovers metals from the to-be-processed object containing a metal using the rotary kiln as described in any one of Claims 1-3 . The metal recovery method according to claim 4 , wherein any one of Au, Ag, Cu, Pd, Pb, and Sn is recovered as a metal. The metal recovery method according to claim 4 or 5 , wherein a slag obtained by smelting waste electronic substrates, wire scraps, or copper, gold, or silver as the object to be treated containing metal is used as a raw material.

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