Continuous heating device, recovery system for components of solar cell panels

Abstract

The present invention provides a continuous heating device that improves thermal efficiency in heat treatment of a solar cell panel, can reduce energy cost, and improves quality of valuables recovered from a solar cell panel. The present invention also provides a recovery system of a constituent member of a solar cell panel, the recovery system including the continuous heating device.　A continuous heating device (100) is provided with a heating furnace (20). The heating furnace (20) has: a primary treatment unit (13) for obtaining a primary treatment product (2) by heat treating a solar cell panel (1) transported by an endless belt (21) in a non-oxidizing atmosphere; and a secondary treatment unit (15) for obtaining a heat-treated product (3) by heat treating the primary treatment product (2) transported by the endless belt (21) in an oxidizing atmosphere. The primary treatment unit (13) and / or the secondary treatment unit (15) utilizes thermal energy generated by combustion of pyrolysis gas generated when a sealing material of the solar cell panel (1) is heat treated by the primary treatment unit (13) and decomposed.

Description

Technical Field

[0001] The present invention relates to a continuous heating device and a recovery system for components of a photovoltaic panel.

Background Art

[0002] In order to effectively utilize resources, it has been considered to recover cells and glass from used photovoltaic panels. Since an increase in the amount of discarded photovoltaic panels is predicted, the importance of reusing their components is increasing. For example, if the aluminum frame of a photovoltaic panel is removed, an aluminum plate can be recovered. Also, if resins such as adhesives and sealants are removed from a photovoltaic panel, glass, copper wires, and silicon cells can be recovered.

[0003] As a method for removing resins such as sealants from a photovoltaic panel, there are a wet treatment method in which a treatment liquid is used to decompose or separate the resin, and a treatment method in which the resin is vaporized by heat treatment. In terms of continuous treatment, heat treatment is preferable. For example, Patent Document 1 discloses that after heat-treating a photovoltaic panel, glass materials and metal-containing materials are sorted and recovered from the heat-treated product. In the example of Patent Document 1, the organic compounds of the photovoltaic panel are decomposed by performing primary firing in a nitrogen atmosphere and then secondary firing in air.

Prior Art Documents

Patent Documents

[0004]

Patent Document 1

Summary of the Invention

Problems to be Solved by the Invention

[0005] However, in the heating furnace used in the example of Patent Document 1, the solar cell panels are first fired in a nitrogen atmosphere, and then the heated material is cooled once before the second firing. Therefore, the material obtained from the first firing needs to be heated again for the second firing. As a result, there was a problem in that the thermal efficiency of the heat treatment of solar cell panels was poor and the energy cost was high. In addition, soot derived from resin residue may adhere to the heated material, so there is a risk that the quality of valuable materials recovered in the sorting process after heat treatment may vary.

[0006] The present invention provides a continuous heating device that improves the thermal efficiency in the heat treatment of solar cell panels, reduces energy costs, and improves the quality of valuable materials recovered from solar cell panels; and a recovery system for components of solar cell panels equipped with the continuous heating device. [Means for solving the problem]

[0007] The present invention has the following aspects. [1] The heating furnace is equipped with a heating furnace that obtains a heat-treated product by heat-treating solar cell panels while they are being transported by an endless belt, The heating furnace comprises a primary processing unit that obtains a primary processed product by heat-treating the solar cell panel in a non-oxidizing atmosphere while conveying it on the endless belt, and a secondary processing unit that obtains a heat-treated product by heat-treating the primary processed product in an oxidizing atmosphere while conveying it on the endless belt. A continuous heating device in which at least one of the primary processing unit and the secondary processing unit utilizes thermal energy generated by the combustion of pyrolysis gas produced when the sealing material of the solar cell panel is heat-treated and decomposed in the primary processing unit. [2] The continuous heating apparatus according to [1], wherein a flexible seal curtain is suspended in at least one place within the heating furnace, traversing the transport direction of the solar cell panels and in contact with the endless belt. [3] The continuous heating apparatus according to [2], wherein the seal curtain is suspended in the heating furnace between the primary processing unit and the secondary processing unit. [4] The continuous heating apparatus according to [2] or [3], wherein the seal curtain is suspended in the heating furnace upstream of the primary processing unit. [5] The continuous heating apparatus according to any one of [2] to [4], wherein the seal curtain is suspended in the heating furnace downstream of the secondary processing unit. [6] A continuous heating device according to any one of [1] to [5], wherein at least one of the primary processing unit and the secondary processing unit utilizes the thermal energy of the exhaust gas generated after the combustion of the pyrolysis gas. [7] A continuous heating device according to any one of [1] to [6], further comprising a combustion chamber for burning the pyrolysis gas generated when the sealing material of the solar cell panel is heat-treated and decomposed in the primary processing unit. [8] The continuous heating device according to [7], wherein at least one of the primary processing unit and the secondary processing unit utilizes the thermal energy of exhaust gas discharged from the combustion chamber. [9] A continuous heating device according to any one of [1] to [8], wherein a heat exchanger that utilizes the thermal energy generated by the combustion of the pyrolysis gas is arranged in at least one of the primary processing unit and the secondary processing unit.

[10] The continuous heating device according to [9], wherein the heat exchanger utilizes the thermal energy of the exhaust gas generated after the combustion of the pyrolysis gas.

[11] The heating furnace has a muffle that surrounds the endless belt and an outer wall that surrounds the muffle, The continuous heating device according to [9] or

[10] , wherein the heat exchanger is arranged in the space between the muffle and the outer wall.

[12] A continuous heating device according to any one of [9] to

[11] , wherein the heat exchanger is an indirect heat exchanger.

[13] The continuous heating device according to

[11] or

[12] , wherein an electric heater is placed in the space between the muffle and the outer wall.

[14] A continuous heating apparatus according to any one of [1] to

[13] , wherein the amount of soot adhering to the heat-treated product is 100 ppm or less. A continuous heating device as described in any of

[15] [1] to

[14] , A sorting device for separating glass material and valuable metal-containing materials from the heat-treated material, A system for recovering components of solar cell panels, equipped with the following features.

[16] The solar cell panel component recovery system according to

[15] , wherein the sorting device has a sieving section that sieves the heat-treated material into a first valuable metal-containing material including cells and copper wires and a first glass material.

[17] The solar cell panel component recovery system according to

[16] , wherein the sorting device further comprises an air separation unit that separates the first glass material sieved in the sieving unit into a second valuable metal-containing material including cells and a second glass material by air separation.

[18] The solar cell panel component recovery system according to

[17] , further comprising an air table sorting unit for sorting a third glass material from the second glass material using an air table.

[19] A recovery system for components of a solar cell panel according to

[18] , wherein the glass purity of the third glass material after sorting is 99.99% or higher.

[20] A recovery system for components of a solar cell panel according to any one of

[15] to

[19] , wherein the recycling rate of the glass material contained in the heat-treated product is 85% or more.

[21] A recovery system for components of a solar cell panel according to any one of

[15] to

[20] , wherein the recycling rate of cells contained in the heat-treated material is 90% or more.

[22] A recovery system for components of a solar cell panel according to any one of

[15] to

[21] , wherein the recycling rate of the copper wire contained in the heat-treated material is 90% or more. [Effects of the Invention]

[0008] According to the present invention, the thermal efficiency in the heat treatment of solar cell panels is improved, energy costs can be reduced, and the quality of valuable materials recovered from solar cell panels is also improved. [Brief explanation of the drawing]

[0009] [Figure 1]FIG. 1 is a schematic configuration diagram showing an example of a continuous heating device. [Figure 2] FIG. 2 is a schematic view of the continuous heating device of FIG. 1 as seen from the inlet side. [Figure 3] FIG. 3 is a perspective view of the continuous heating device of FIG. 1 with a partial enlargement. [Figure 4] FIG. 4 is a view of the seal curtain as seen from the conveyance direction of the photovoltaic panel. [Figure 5] FIG. 5 is a side view of the state in which the photovoltaic panel is being conveyed while pushing up the seal curtain in the seal chamber of the heating furnace. [Figure 6] FIG. 6 is a view of the state in which the photovoltaic panel is being conveyed while pushing up the seal curtain in the seal chamber of the heating furnace as seen from the rear side in the conveyance direction of the photovoltaic panel. [Figure 7] FIG. 7 is a view of the state in which the photovoltaic panel is being conveyed while pushing up the seal curtain in the seal chamber of the heating furnace as seen from the rear side in the conveyance direction of the photovoltaic panel. [Figure 8] FIG. 8 is a schematic view showing an example of a recovery system for the constituent members of the photovoltaic panel. [Figure 9] FIG. 9 is a schematic view showing another example of a recovery system for the constituent members of the photovoltaic panel. [Figure 10] FIG. 10 shows the glass fragments recovered from the heat-treated product obtained in Example 1. [Figure 11] FIG. 11 shows the glass fragments recovered from the heat-treated product obtained in Comparative Example 1.

MODE FOR CARRYING OUT THE INVENTION

[0010] [TERMS] The term "non-oxidizing atmosphere" refers to an atmosphere that does not contain oxygen gas or an atmosphere that substantially does not contain oxygen gas. The term "oxidizing atmosphere" refers to an atmosphere that contains oxygen gas and is an atmosphere other than a non-oxidizing atmosphere. In this specification and the claims, the "~" indicating a numerical range means that the numbers before and after it are included as the lower and upper limits, respectively.

[0011] [Solar panels] In one example, the photovoltaic panel comprises cells, a glass substrate, and a encapsulant. In another example, the photovoltaic panel may further include wiring electrodes, extraction electrodes, a terminal box, cables, a backsheet, a frame, and the like. It is preferable to heat-treat the solar cell panels after the cables have been removed. From the standpoint of reducing the number of steps involved, it is preferable to perform heat treatment without removing the backsheet, terminal box, and aluminum frame from the solar cell panel.

[0012] Examples of solar cell cells include silicon-based (monocrystalline silicon, polycrystalline silicon, amorphous silicon, etc.) and compound-based (GaAs, CIS, CdTe-CdS). Monocrystalline silicon and polycrystalline silicon are preferred. Examples of glass substrates for solar cell panels include soda-lime glass and alkali-free glass. Examples of encapsulants for solar cell panels include ethylene-vinyl acetate copolymer (EVA) and ethylene-(meth)acrylic acid ester copolymer. Among these, EVA is widely used.

[0013] [Pyrolysis gas] Pyrolysis gases are generated when the encapsulating material of a solar cell panel is thermally decomposed. These gases are produced when the resins in the encapsulating material of a solar cell panel are thermally decomposed. Solar cell panels mainly use various resins and organic compounds such as polymers as encapsulating materials. The constituent elements of these organic compounds include carbon, nitrogen, fluorine, hydrogen, and oxygen. These organic compounds decompose and vaporize when heated, generating pyrolysis gases.

[0014] In the primary treatment, the resin is gasified and carbonized by heat treatment in a non-oxidizing atmosphere. In the secondary treatment, the carbonized material adhering to the heat-treated product after the primary treatment can be oxidized and removed by heat treatment in an oxidizing atmosphere. The pyrolysis gas generated in the primary treatment contains more flammable gases than the oxidizing gas such as CO2 generated in the secondary treatment. The continuous heating device of the present invention is characterized by utilizing the thermal energy generated by the combustion of the pyrolysis gas generated in the primary treatment, which contains more flammable gases, in order to improve the thermal efficiency in heat treatment and to reduce energy costs.

[0015] Several embodiments will be described below with reference to the drawings as appropriate. The following description concerns representative examples of embodiments of the invention, and the present invention is not limited to the following description. Also, the dimensional ratios in each drawing may differ from those of the actual dimensions for the sake of explanation.

[0016] [Continuous heating device] Figure 1 is a schematic diagram showing an example of a continuous heating device. The continuous heating device 100 includes a heating furnace 20 that obtains a heat-treated product by heat-treating a solar cell panel 1 while it is being transported by an endless belt 21; a combustion chamber 40 for burning the pyrolysis gas generated when the sealing material of the solar cell panel 1 is heat-treated and decomposed in the primary processing unit 13 of the heating furnace 20; a first gas supply means (not shown) for supplying an inert gas into the heating furnace 20; and a second gas supply means (not shown) for supplying an oxygen-containing gas into the heating furnace 20.

[0017] The heating furnace 20 has, in order from upstream to downstream, an inlet-side exhaust chamber 11, an inlet-side sealing chamber 12, a primary processing unit 13, a switching unit 14, a secondary processing unit 15, an air-cooling chamber 16, a cooling chamber 17, an outlet-side sealing chamber 18, and an outlet-side exhaust chamber 19.

[0018] Figure 2 is a schematic diagram of the continuous heating device 100 shown in Figure 1, viewed from the entrance 11a side. Figure 3 is a partially enlarged perspective view of the continuous heating device 100. As shown in Figure 2, the heating furnace 20 has a muffle 27 that surrounds the endless belt 21 and an outer wall 28 that surrounds the muffle 27. Although not shown in Figure 3, the muffle 27 and the outer wall 28 each have a structure that extends in the direction of transport by the endless belt 21. Within the muffle 27, a primary processing unit 13, a switching unit 14, and a secondary processing unit 15 are formed, respectively.

[0019] The outer wall 28 covers the muffle 27, a pair of electric heaters 29, the first heat exchanger 31, and the second heat exchanger 32, etc. The outer wall 28 helps to suppress thermal fluctuations, allowing the temperatures of the primary processing unit 13 and the secondary processing unit 15 to be maintained at appropriate heat treatment temperatures. The temperature can be adjusted by controlling the output of each electric heater 29 according to the temperatures of the primary processing unit 13 and the secondary processing unit 15 within the muffle 27.

[0020] The exhaust chamber 11 on the loading side has a loading port 11a for loading the solar cell panel 1 into the heating furnace 20. The exhaust chamber 11 on the loading side is a region for exhausting outside air flowing in from the loading port 11a, along with the inert gas and pyrolysis gas from the loading side sealing chamber 12. In one example, the loading port 11a may be provided with an opening adjustment plate to adjust the degree of opening of the passage (loading port 11a) to the heating furnace 20.

[0021] An exhaust port 11b is formed at the top of the inlet-side exhaust chamber 11 to exhaust outside air flowing in from the inlet 11a along with the inert gas and pyrolysis gas from the inlet-side seal chamber 12. One end of the exhaust pipe 71 is connected to the exhaust port 11b. In one example, the exhaust port 11b may be provided with an opening degree adjustment means for adjusting its opening degree. An example of an opening degree adjustment means is an opening degree adjustment plate.

[0022] The inlet-side sealing chamber 12 is a region designed to prevent outside air from entering the primary processing unit 13 and to suppress the leakage of inert gases and pyrolysis gases from the primary processing unit 13. An inert gas inlet (not shown) is formed at the top of the inlet-side sealing chamber 12 for introducing inert gas supplied from a first gas supply means (not shown) into the inlet-side sealing chamber 12.

[0023] A flexible sealing curtain 22 is suspended in the loading-side sealing chamber 12, traversing the transport direction of the solar cell panel 1 and in contact with the endless belt 21. In one example, the loading-side sealing chamber 12 may be provided with an opening adjustment plate (not shown) upstream of the sealing curtain 22 to adjust the opening of the passage of the heating furnace 20 (the entrance to the loading-side sealing chamber 12).

[0024] The vertical length of the seal curtain 22 should be such that it is in contact with the endless belt 21 inside the heating furnace 20. It is preferable that the lower end of the seal curtain 22 is in contact with the endless belt 21, and it is more preferable that the lower end of the seal curtain 22 is pressed against the endless belt 21 and bent.

[0025] The seal curtain 22 can be flexible and heat-resistant. Examples of the seal curtain 22 include a thin sheet. A thin heat-resistant sheet is preferred, and a thin metal sheet is more preferred.

[0026] Multiple layers of sealing curtains 22 are suspended in the loading-side sealing chamber 12 at intervals in the direction of transport of the solar cell panels 1. The number of layers of the sealing curtains 22 is preferably 2 to 100, more preferably 10 to 85, and even more preferably 20 to 70. If the number of layers of the sealing curtains 22 is above the lower limit of the above range, the intrusion of outside air into the primary processing unit 13 and the leakage of inert gas and pyrolysis gas from the primary processing unit 13 are sufficiently suppressed. If the number of layers of the sealing curtains 22 is below the upper limit of the above range, the solar cell panels 1 can easily pass through the loading-side sealing chamber 12.

[0027] As shown in Figure 4, the seal curtain 22 consists of multiple vertically extending strips 22A arranged without gaps in a direction transverse to the transport direction of the solar cell panel 1. The number of strips 22A per meter in the width direction of the seal curtain 22 is preferably 2 to 50 strips / m, and more preferably 10 to 30 strips / m. If the number of strips 22A is greater than or equal to the lower limit of the above range, the gap between the side surface of the solar cell panel 1 and the strips 22A can be made as small as possible by the mechanism of action described later. As a result, the intrusion of outside air into the primary processing unit 13 and the leakage of inert gas and pyrolysis gas from the primary processing unit 13 are sufficiently suppressed. If the number of strips 22A is less than or equal to the upper limit of the above range, the number of gaps between adjacent strips 22A is suppressed. As a result, the intrusion of outside air into the primary processing unit 13 and the leakage of inert gas and pyrolysis gas from the primary processing unit 13 are sufficiently suppressed.

[0028] The primary processing unit 13 is a region for obtaining a primary processed product by heat-treating the solar cell panel 1 in a non-oxidizing atmosphere while it is being transported by an endless belt 21. An inert gas inlet (not shown) is formed at the top of the primary processing unit 13 for introducing an inert gas supplied from a first gas supply means (not shown) into the primary processing unit 13. As shown in Figure 2, a pair of electric heaters 29 are installed in the space between the muffle 27 and the outer wall 28 in the direction of transport by the endless belt 21. The pair of electric heaters 29 are installed in the primary processing unit 13, flanking the muffle 27 on which the endless belt 21 that transports the solar cell panels 1 is located, in the direction of transport of the solar cell panels 1.

[0029] In the primary processing unit 13, the solar cell panel 1 is heat-treated, causing a portion of the resin contained in the solar cell panel 1 to decompose thermally, resulting in the acquisition of a primary processed product 2. An exhaust port 13a is formed at the top of the primary processing unit 13 to exhaust the pyrolysis gas generated by the thermal decomposition of resins such as encapsulating material contained in the solar cell panel 1, along with an inert gas, from the primary processing unit 13. The pyrolysis gas generated here flows through a pyrolysis gas supply pipe 61 connected to the exhaust port 13a and is supplied to the combustion chamber 40.

[0030] The switching section 14 is a region for switching between primary processing under a non-oxidizing atmosphere and secondary processing under an oxidizing atmosphere. An inert gas inlet (not shown) is formed at the top of the switching section 14 for introducing inert gas supplied from a first gas supply means (not shown) into the switching section 14.

[0031] In the heating furnace 20 of the switching section 14, located between the primary processing section 13 and the secondary processing section 15, multiple layers of sealing curtains 23 are suspended at intervals in the direction of transport of the primary processing material 2. The number of steps in the seal curtain 23 at the switching section 14 is preferably 2 to 50, more preferably 2 to 30, and even more preferably 5 to 20. If the number of steps in the seal curtain 23 is greater than or equal to the lower limit of the above range, leakage of pyrolysis gas and inert gas from the primary processing section 13 to the secondary processing section 15, and leakage of oxidizing gas and oxygen-containing gas from the secondary processing section 15 to the primary processing section 13 can be sufficiently suppressed. If the number of steps in the seal curtain 22 is less than or equal to the upper limit of the above range, the primary processing material 2 can easily pass through the switching section 14. Details and preferred embodiments of the seal curtain 23 are the same as those of the seal curtain 22 in the entrance-side seal chamber 12.

[0032] The secondary processing area 15 is a region for obtaining a heat-treated product 3 by heat-treating the primary processing product 2 in an oxidizing atmosphere while it is being transported by an endless belt 21. An oxygen-containing gas inlet (not shown) is formed at the top of the secondary processing area 15 for introducing oxygen-containing gas supplied from a second gas supply means (not shown) into the secondary processing area 15.

[0033] Within the secondary processing unit 15, a pair of electric heaters 29 (Figure 2) are installed in the direction of transport of the solar cell panel 1, flanking a muffle 27 on which an endless belt 21 for transporting the primary processed material 2 is located. In the secondary processing unit 15, the primary processed material 2 is heat-treated, which oxidizes any remaining resin carbides such as sealant in the primary processed material 2. As a result, the secondary processing unit 15 yields the heat-treated material 3.

[0034] An exhaust port (not shown) is formed at the top of the secondary processing unit 15 to exhaust oxidizing gas, generated by the oxidation of resin carbides such as sealing material remaining in the primary processing material 2, along with oxygen-containing gas, from the secondary processing unit 15. The exhaust port is preferably formed near the switching unit 14 in order to prevent leakage of inert gas and pyrolysis gas from the primary processing unit 13 to the secondary processing unit 15. The oxidizing gas referred to here includes, but is not limited to, carbon dioxide gas, water vapor, nitrogen oxides, sulfur oxides, and their incomplete combustion products.

[0035] The air-cooling chamber 16 and the cooling chamber 17 are areas for cooling the heat-treated object 3. Cooling pipes (not shown) for circulating cooling water are provided inside the cooling chamber 17.

[0036] The outlet-side sealing chamber 18 is a region designed to prevent outside air from entering the cooling chamber 17, the air-cooling chamber 16, and the secondary processing unit 15, as well as to prevent the leakage of oxygen-containing gases and oxidizing gases from the secondary processing unit 15, the air-cooling chamber 16, and the cooling chamber 17. An oxygen-containing gas inlet (not shown) is formed at the top of the outlet-side sealing chamber 18 for introducing oxygen-containing gas supplied from a second gas supply means (not shown) into the outlet-side sealing chamber 18.

[0037] In the discharge-side sealing chamber 18, multiple flexible sealing curtains 24 are suspended at intervals in the direction of transport of the heat-treated material 3, traversing the transport direction of the heat-treated material 3 and in contact with the endless belt 21.

[0038] The number of steps of the sealing curtain 24 in the outlet side sealing chamber 18 is preferably 2 to 100 steps, more preferably 10 to 60 steps, and even more preferably 20 to 40 steps. If the number of steps in the seal curtain 24 is greater than or equal to the lower limit of the range, the intrusion of outside air into the cooling chamber 17 and the secondary processing unit 15, as well as the leakage of oxygen-containing gases and oxidizing gases from the secondary processing unit 15 and the cooling chamber 17, can be sufficiently suppressed. If the number of steps in the seal curtain 24 is less than or equal to the upper limit of the range, the heat-treated material 3 can easily pass through the outlet-side seal chamber 18.

[0039] Details and preferred embodiments of the seal curtain 24 are the same as those of the seal curtain 22 in the entrance-side seal chamber 12. In one example, the outlet-side sealing chamber 18 may be provided with an opening adjustment plate downstream of the sealing curtain 24 to adjust the opening degree of the passage of the heating furnace 20 (the outlet of the outlet-side sealing chamber 18).

[0040] The exhaust chamber 19 on the outlet side has an outlet 19a for discharging the heat-treated material 3 from the heating furnace 20. The exhaust chamber 19 on the outlet side is a region for exhausting outside air flowing in from the outlet 19a, along with oxygen-containing gas and oxidizing gas from the outlet side seal chamber 18. In one example, the outlet 19a may be provided with an opening adjustment plate to adjust the opening of the passage (outlet 19a) of the heating furnace 20.

[0041] An exhaust port 19b is formed at the top of the outlet-side exhaust chamber 19 to exhaust outside air flowing in from the outlet 19a along with oxygen-containing gas and oxidizing gas from the outlet-side seal chamber 18. One end of the exhaust pipe 72 is connected to the exhaust port 19b. In one example, the exhaust port 19b may be provided with an opening adjustment means for adjusting its opening degree. An example of an opening adjustment means is an opening adjustment plate.

[0042] The continuous heating device 100 includes a combustion chamber 40 for burning the pyrolysis gas generated when the resin of the solar cell panel 1 is heat-treated and decomposed in the primary processing unit 13. Connected to the combustion chamber 40 are a pyrolysis gas supply pipe 61 for supplying the pyrolysis gas generated in the primary processing unit 13, an LPG supply pipe 63 for supplying LPG from the LPG tank 64, and an air supply pipe 62 for supplying air. Also connected to the combustion chamber 40 is an exhaust pipe 51 for discharging exhaust gas generated when the pyrolysis gas is burned in the combustion chamber 40. The exhaust pipe 51 is connected to a first reheating line 811 and a second reheating line 821, respectively.

[0043] In the combustion chamber 40, pyrolysis gas supplied from the primary processing unit 13 through the pyrolysis gas supply pipe 61 is mixed with air and combusted. The exhaust gas generated after the combustion of the pyrolysis gas produced in the primary processing unit 13 flows through the exhaust pipe 51 and is discharged outside the combustion chamber 40, and is then used to heat the primary processing unit 13 and the secondary processing unit 15.

[0044] The exhaust gas discharged from the combustion chamber 40 flows through the first reheating line 811 and the second reheating line 821, respectively. Since the exhaust gas discharged from the combustion chamber 40 is at a high temperature, its thermal energy can be utilized by the first heat exchanger 31 and the second heat exchanger 32, which are connected to the first reheating line 811 and the second reheating line 821, respectively.

[0045] The first heat exchanger 31 and the second heat exchanger 32 each utilize the thermal energy generated by the combustion of pyrolysis gas produced when the encapsulating material of the solar cell panel is heat-treated and decomposed in the primary processing unit 13. In the continuous heating device 100, the pyrolysis gas produced when the encapsulating material of the solar cell panel is heat-treated and decomposed in the primary processing unit 13 is converted into high-temperature exhaust gas produced by the combustion reaction in the combustion chamber 40. Therefore, the first heat exchanger 31 and the second heat exchanger 32 can each utilize the thermal energy of the exhaust gas produced after the combustion of this pyrolysis gas.

[0046] The first heat exchanger 31 utilizes the thermal energy of the exhaust gas generated after the combustion of the pyrolysis gas to heat the primary processing unit 13. The second heat exchanger 32 also utilizes the thermal energy of the exhaust gas generated after the combustion of the pyrolysis gas to heat the secondary processing unit 15.

[0047] Here, as shown in Figure 2, the first heat exchanger 31 and the second heat exchanger 32 are installed in the space between the muffle 27 and the outer wall 28. Also, as shown in Figures 1, 2, and 3, the heat exchanger 31 is positioned near the outer wall 28 of the primary processing unit 13 along the conveying direction of the endless belt 21. The heat exchanger 32 is positioned near the outer wall 28 of the secondary processing unit 15 along the conveying direction of the endless belt 21.

[0048] Heating of the primary processing unit 13 using exhaust gas discharged from the combustion chamber 40 is carried out as follows. As shown in Figures 1 and 3, exhaust gas is supplied to the first heat exchanger 31 from the first reheating line 811. The first heat exchanger 31 utilizes the thermal energy of the exhaust gas supplied from the first reheating line 811 to heat the primary processing unit 13. The exhaust gas that has passed through the first heat exchanger 31 flows through the exhaust pipe 813 and exhaust pipe 73 in that order and is supplied to the scrubber 91.

[0049] The heating of the secondary processing unit 15 using the exhaust gas discharged from the combustion chamber 40 is carried out as follows. As shown in Figures 1 and 3, the exhaust gas is supplied to the second heat exchanger 32 from the second reheating line 821. The second heat exchanger 32 utilizes the thermal energy of the exhaust gas supplied from the second reheating line 821 to heat the secondary processing unit 15. The exhaust gas that has passed through the second heat exchanger 32 flows through the exhaust pipe 823 and the exhaust pipe 73 in that order and is supplied to the scrubber 91.

[0050] The first heat exchanger 31 and the second heat exchanger 32 are not particularly limited, but are preferably indirect heat exchangers in that they can suppress corrosion on the outside of the muffle 27 and corrosion on the inside of the outer wall 28. The indirect heat exchangers are not particularly limited, but examples include multi-tube heat exchangers, coiled tube heat exchangers, and heated walls.

[0051] The exhaust gas discharged from the combustion chamber 40 may contain fluorine gas, unburned gas, NOx, etc., which may be corrosive. In particular, depending on the type of resin used in the encapsulation material of the solar cell panel, the airflow within the combustion chamber 40, temperature, and other conditions, unexpected corrosive gases such as fluorine gas, unburned gas, and NOx may remain. If these corrosive gases are directly supplied to the space between the muffle 27 and the outer wall 28, the wall surface may corrode. As a result, complicated maintenance such as replacing and cleaning the entire heating furnace may be required.

[0052] Therefore, with an indirect heat exchanger, by flowing two types of fluids with different temperatures into the space separated by its internal wall, heat can be transferred from the high-temperature fluid to the low-temperature fluid through heat transfer to the wall surface, heat conduction through the wall surface, and heat transfer through the wall surface itself. As a result, the primary processing unit 13 and the secondary processing unit 15 can be heated by heat exchange without directly supplying the exhaust gas discharged from the combustion chamber 40 to the space between the muffle 27 and the outer wall 28. With an indirect heat exchanger, since the exhaust gas passes through its interior, the effects of corrosive gases can be limited to the indirect heat exchanger itself. Even if corrosion occurs, the indirect heat exchanger can be selectively replaced. In addition, corrosion of the outside of the muffle 27 and the inside of the outer wall 28 that constitute the heating furnace 20 can be prevented. As a result, maintenance is easier when affected by corrosive gases with an indirect heat exchanger.

[0053] In the example shown in Figure 1, the pyrolysis gas supply pipe 61 and the air supply pipe 62 supply pyrolysis gas and air to the combustion chamber 40 independently, respectively. However, in other examples, the pyrolysis gas and air may be pre-mixed before supplying the mixture to the combustion chamber 40 in order to improve combustion efficiency or reduce corrosive gases.

[0054] When pre-mixing pyrolysis gas and air, instead of the pyrolysis gas supply pipe 61 and air supply pipe 62 shown in Figure 1, a parallel pipe for pre-mixing pyrolysis gas and air may be used. The parallel pipe has a pyrolysis gas supply pipe and an air supply pipe that are arranged parallel to each other for at least a portion of the pipe. The parallel pipe has openings through which the pyrolysis gas and air flow inside in the portion where the pyrolysis gas supply pipe and the air supply pipe are arranged parallel to each other. Therefore, the mixed gas can be supplied to the combustion chamber 40 after pre-mixing the pyrolysis gas and air. The form of the parallel pipe is not particularly limited, but examples include double pipes in which the pyrolysis gas supply pipe and the air supply pipe are arranged concentrically, and square pipes in which the pyrolysis gas supply pipe and the air supply pipe are arranged adjacent to each other, but is not particularly limited.

[0055] The scrubber 91 is located downstream of exhaust pipes 71, 72, 813, 823, and 73. The scrubber 91 is for removing harmful substances from the gas exhausted from each region within the continuous heating device 100 before it is discharged to the outside.

[0056] A first gas supply means (not shown) supplies inert gas to the primary processing unit 13, the inlet-side seal chamber 12, and the switching unit 14 within the heating furnace 20. Examples of gas sources for the first gas supply means include a membrane separation type nitrogen gas generator, an inert gas cylinder, and an inert gas tank. Examples of inert gases include nitrogen gas, argon gas, helium gas, xenon gas, carbon dioxide gas, and superheated steam. Nitrogen gas is preferred from an economic standpoint.

[0057] A second gas supply means (not shown) supplies oxygen-containing gas to the secondary processing unit 15 and the outlet side seal chamber 18 within the heating furnace 20, respectively. Examples of gas sources for the second gas supply means include oxygen-containing gas cylinders and oxygen-containing gas tanks. Examples of oxygen-containing gases include air and oxygen. From an economic standpoint, air is preferred.

[0058] (Method of manufacturing heat-treated products) A method for manufacturing a heat-treated product 3 using a continuous heating device 100 will be described. First, an inert gas is continuously supplied to the inlet-side sealing chamber 12 and the switching section 14. In addition, an oxygen-containing gas is continuously supplied to the outlet-side sealing chamber 18. A non-oxidizing atmosphere is prepared in the muffle of the primary processing section 13 by continuously supplying an inert gas. An oxidizing atmosphere is prepared in the muffle of the secondary processing section 15 by continuously supplying an oxygen-containing gas.

[0059] Examples of inert gases supplied to the primary processing unit 13 include nitrogen gas, argon gas, helium gas, xenon gas, carbon dioxide gas, and superheated steam. From an economic standpoint, nitrogen gas is preferred.

[0060] Examples of oxygen-containing gases supplied to the secondary processing unit 15 include air and oxygen gas. Air is preferred from an economic standpoint.

[0061] Examples of inert gases supplied for sealing into the inlet-side sealing chamber 12 and the outlet-side sealing chamber 18 include nitrogen gas, argon gas, helium gas, xenon gas, carbon dioxide gas, and superheated steam. From an economic standpoint, nitrogen gas is preferred. Furthermore, it is preferable that the inert gas be heated, as this reduces the amount of gas used due to volume expansion.

[0062] By driving the exhaust fan (not shown), outside air flowing in from the inlet 11a of the heating furnace 20 is constantly exhausted from the exhaust port 11b along with the inert gas and pyrolysis gas from the inlet-side seal chamber 12. To prevent the inert gas and pyrolysis gas from leaking out of the heating furnace 20, the amount of outside air flowing in from the inlet 11a of the heating furnace 20 may be adjusted using an opening adjustment plate.

[0063] Furthermore, outside air flowing in from the outlet 19a of the heating furnace 20 is constantly exhausted from the exhaust port 19b along with oxygen-containing gas and oxidizing gas from the outlet-side seal chamber 18. In one example, to prevent oxygen-containing gas and oxidizing gas from leaking out of the heating furnace 20, the amount of outside air flowing in from the outlet 19a of the heating furnace 20 may be adjusted using an opening adjustment plate. The opening degrees of exhaust port 11b and exhaust port 19b may be adjusted as needed.

[0064] A solar cell panel 1 is placed on an endless belt 21 that moves from the upstream side of the heating furnace 20, through the inside of the heating furnace 20, and toward the downstream side of the heating furnace 20. The solar cell panel 1 is brought in through the entrance 11a of the heating furnace 20 by the endless belt 21 and transported inside the heating furnace 20.

[0065] Inside the loading-side sealing chamber 12, the solar cell panel 1 is transported while pushing up the sealing curtain 22. If necessary, the opening degree of the entrance to the loading-side sealing chamber 12 may be adjusted using the opening degree adjustment plate.

[0066] In the primary processing unit 13, the solar cell panel 1 is transported and heat-treated in a non-oxidizing atmosphere. This thermally decomposes the resin of the encapsulating material contained in the solar cell panel 1 to obtain the primary processed product 2. The oxygen concentration in the primary processing unit 13 is preferably 3.0 volume% or less, more preferably 1.0 volume% or less, and even more preferably 0.1 volume% or less, from the viewpoint of suppressing the formation of detonating gases.

[0067] The ambient temperature inside the primary processing unit 13 is set to, for example, 300 to 550°C, and the heating time is appropriately set in the range of 10 to 180 minutes depending on the heating temperature. The heating temperature may be set in multiple stages. For example, the first stage may be set to 300 to 400°C to decompose and vaporize the acetic acid portion of EVA, and then the second stage may be set to 400 to 550°C to decompose and vaporize the polyethylene portion, which is the main chain of EVA. This promotes the decomposition and vaporization of EVA and suppresses the generation of residues such as charred materials.

[0068] Within the switching section 14, the primary processing material 2 is transported from the primary processing section 13 to the secondary processing section 15 while pushing up the seal curtain 23.

[0069] In the secondary processing unit 15, the primary processed material 2 is heat-treated under an oxidizing atmosphere while being transported. This oxidizes the resin carbides, such as the sealing material, remaining in the primary processed material 2, resulting in the heat-treated product 3. The oxygen concentration in the secondary processing unit 15 is preferably 80% by volume or less, more preferably 50% by volume or less, and even more preferably 25% by volume or less. Furthermore, from the viewpoint of promoting the oxidation of resin carbides (soot) such as the sealing material remaining in the primary processed material 2, it is preferably 5% by volume or more, more preferably 10% by volume or more, and even more preferably 15% by volume or more.

[0070] The ambient temperature inside the secondary processing unit 15 is set to, for example, 300 to 500°C, and the heating time is appropriately set in the range of 10 to 180 minutes depending on the heating temperature.

[0071] In the air-cooling chamber 16, the heat-treated object 3 is slowly cooled to prevent glass breakage due to rapid cooling. Subsequently, in the cooling chamber 17, where cooling water is supplied, the heat-treated object 3 is cooled to a temperature that can be handled by an operator, for example, 100°C or below.

[0072] Within the discharge-side sealing chamber 18, the heat-treated material 3 is transported while pushing up the sealing curtain 24. If necessary, the opening degree of the outlet of the discharge-side sealing chamber 18 may be adjusted using the opening degree adjustment plate. The heat-treated material 3, transported inside the heating furnace 20 by the endless belt 21, is discharged from the outlet 19a of the heating furnace 20. The heat-treated material 3 discharged from the heating furnace 20 mainly consists of cells, glass substrates, etc. A small amount of soot may adhere to it, but the amount is reduced to, for example, 100 ppm or less.

[0073] (Mechanism of action) As described above, the continuous heating apparatus 100 is equipped with a heating furnace 20 that heat-treats the solar cell panels 1 while transporting them to obtain the heat-treated product 3. Therefore, the heat-treated product 3 can be obtained by continuously heat-treating the solar cell panels 1. This allows for a higher processing volume per unit of time compared to batch processing.

[0074] The primary processing unit 13 and the secondary processing unit 15 utilize the thermal energy generated by the combustion of pyrolysis gas produced when the encapsulating material of the solar cell panel 1 is heat-treated and decomposed in the primary processing unit 13. In particular, the pyrolysis gas generated in the primary processing unit 13 contains more flammable gas than the oxidizing gas generated in the secondary processing unit 15. With the continuous heating device 100, the thermal energy generated by the combustion of the pyrolysis gas generated in the primary processing unit 13, which contains more flammable gas, can be used to assist in heating both the primary processing unit 13 and the secondary processing unit 15. More specifically, the pyrolysis gas generated when the encapsulant of the solar cell panel is heat-treated and decomposed in the primary processing unit 13 is converted into high-temperature exhaust gas generated by the combustion reaction in the combustion chamber 40, and then the thermal energy is utilized in the first heat exchanger 31 and the second heat exchanger 32, respectively.

[0075] With the continuous heating device 100 having the characteristic configuration described above, the thermal energy generated by the combustion of pyrolysis gas can be used for each heat treatment in the primary processing unit 13 and the secondary processing unit 15. This improves the thermal efficiency in the heat treatment of the solar cell panel and reduces the energy cost for heating the primary processing unit 13 and the secondary processing unit 15.

[0076] In addition, according to this embodiment, the thermal efficiency in the heat treatment of the solar cell panel is improved, which reduces the amount of soot that adheres to the panel, derived from resin residue. In one example, the amount of soot adhering to the heat-treated material can be reduced to 100 ppm or less. Preferably, the amount of soot adhering to the heat-treated material is 70 ppm or less, more preferably 50 ppm or less, and even more preferably 10 ppm or less. The lower limit of the amount of soot adhering to the heat-treated material is not particularly limited, but may be, for example, 0.1 ppm, 1 ppm, etc.

[0077] In the continuous heating device 100 shown in Figure 1, both the primary processing unit 13 and the secondary processing unit 15 utilize the thermal energy generated by the combustion of pyrolysis gas produced when the resin of the solar cell panel 1 is heat-treated and decomposed in the primary processing unit 13. However, in other examples of continuous heating devices, either the primary processing unit 13 or the secondary processing unit 15 may utilize the thermal energy generated by the combustion of pyrolysis gas produced when the resin of the solar cell panel 1 is heat-treated and decomposed in the primary processing unit 13.

[0078] In the continuous heating device 100, a seal curtain 22 is suspended in the inlet-side seal chamber 12, upstream of the primary processing unit 13 that heats the solar cell panel 1. This seal curtain 22 lies across the transport direction of the solar cell panel 1 and hangs down to a length that contacts the endless belt 21. As a result, outside air and inert gases or pyrolysis gases from the primary processing unit 13 that enter the inlet-side seal chamber 12 have difficulty passing through it. Similarly, a seal curtain 24 is suspended in the outlet-side seal chamber 18, downstream of the secondary processing unit 15. This seal curtain 24 lies across the transport direction of the heat-treated material 3 and hangs down to a length that contacts the endless belt 21. As a result, outside air and oxygen-containing gases or oxidizing gases from the primary processing unit 13 and the cooling chamber 17 that enter the outlet-side seal chamber 18 have difficulty passing through it.

[0079] The seal curtain 22 inside the entrance-side seal chamber 12 is flexible. Therefore, as shown in Figure 5, when the solar cell panel 1 passes through the entrance-side seal chamber 12, the seal curtain 22 is pushed up in a sagging state. At this time, the seal curtain 22 is pressed against the solar cell panel 1 and, as shown in Figures 6 and 7, conforms to the thickness and top surface shape of the solar cell panel 1, making close contact with the surface of the solar cell panel 1. Therefore, the gap between the seal curtain 22 and the top surface of the solar cell panel 1 is minimized. Consequently, outside air and inert gases or pyrolysis gases from the primary processing unit 13 that enter the entrance-side seal chamber 12 have difficulty passing through the entrance-side seal chamber 12 even when the solar cell panel 1 passes through it.

[0080] The seal curtain 23 inside the switching section 14 is also flexible. Therefore, for the same reasons as the seal curtain 22, the gap between the seal curtain 23 and the primary processed material 2 is minimized. Thus, inert gases and pyrolysis gases from the primary processing section 13 that have entered the switching section 14 are less likely to pass through the switching section 14 and enter the secondary processing section 15 when the primary processed material 2 passes through the switching section 14. Similarly, oxygen-containing gases and pyrolysis gases from the secondary processing section 15 that have entered the switching section 14 are less likely to pass through the switching section 14 and enter the primary processing section 13 when the primary processed material 2 passes through the switching section 14.

[0081] The seal curtain 24 inside the outlet-side seal chamber 18 is also flexible. For the same reasons as the seal curtain 22, the gap between the seal curtain 24 and the heat-treated object 3 is minimized. Therefore, outside air that enters the outlet-side seal chamber 18, as well as oxygen-containing gases and oxidizing gases from the secondary processing unit 15 and the cooling chamber 17, have difficulty passing through the outlet-side seal chamber 18 when the heat-treated object 3 passes through it.

[0082] In this way, in the continuous heating device 100, the intrusion of outside air into the primary processing unit 13 and the secondary processing unit 15 is suppressed. Therefore, the oxygen concentration in the primary processing unit 13 is less likely to rise excessively. In addition, the solar cell panel 1 can be continuously heat-treated to obtain the heat-treated product 3 while maintaining a non-oxidizing atmosphere in the primary processing unit 13. As a result, the formation of explosive gases is suppressed. Furthermore, the leakage of inert gases and pyrolysis gases from the heating furnace 20 to the outside is suppressed.

[0083] In the continuous heating device 100 described above, multiple layers of sealing curtains 22 are suspended in the inlet-side sealing chamber 12 at intervals in the direction of transport of the solar cell panel 1. Therefore, outside air that enters the inlet-side sealing chamber 12 and inert gases and pyrolysis gases from the primary processing unit 13 are further prevented from passing through the inlet-side sealing chamber 12. In addition, multiple layers of sealing curtains 24 are suspended in the outlet-side sealing chamber 18 at intervals in the direction of transport of the heat-treated material 3. Therefore, outside air that enters the outlet-side sealing chamber 18 and oxygen-containing gases and oxidizing gases from the secondary processing unit 15 and cooling chamber 17 are further prevented from passing through the outlet-side sealing chamber 18. Thus, the intrusion of outside air into the primary processing unit 13 and the secondary processing unit 15, and the leakage of oxygen-containing gases and oxidizing gases from inside the heating furnace 20 are sufficiently suppressed.

[0084] In the continuous heating device 100 described above, the seal curtain 22 in the inlet-side seal chamber 12 consists of multiple strips 22A arranged without gaps in a direction transverse to the transport direction of the solar cell panel 1; in other words, the seal curtain 22 is finely divided. Therefore, as shown in Figures 6 and 7, only the minimum number of strips 22A are pushed up according to the width of the solar cell panel 1 in the direction transverse to the transport direction of the solar cell panel 1. Therefore, the difference between the total width of the strips 22A pushed up by the solar cell panel 1 and the width of the solar cell panel 1 can be made as small as possible, and the gap between the sides of the solar cell panel 1 and the strips 22A formed on both sides of the solar cell panel 1 in the direction transverse to the transport direction of the solar cell panel 1 can be made as small as possible. Therefore, outside air that enters the inlet-side seal chamber 12 and inert gases and pyrolysis gases from the primary processing unit 13 are even less likely to pass through the inlet-side seal chamber 12. Furthermore, the seal curtain 24 inside the outlet-side seal chamber 18 also consists of multiple strips (not shown) arranged without gaps in a direction that transverses the transport direction of the heat-treated material 3. For the same reasons as the seal curtain 22, outside air that enters the outlet-side seal chamber 18 and oxygen-containing gases and oxidizing gases from the secondary processing unit 15 and cooling chamber 17 are further prevented from passing through the outlet-side seal chamber 18. Thus, the intrusion of outside air into the primary processing unit 13 and the leakage of oxygen-containing gases and oxidizing gases from inside the heating furnace 20 are sufficiently suppressed.

[0085] [System for recovering components of solar cell panels] The solar cell panel component recovery system comprises a continuous heating device and a sorting device for separating glass material and valuable metal-containing materials from the heat-treated material obtained by the continuous heating device. Details and preferred embodiments of the continuous heating device are as described above. Embodiments of the sorting device will be described in detail below.

[0086] Figure 8 is a schematic diagram showing an example of a recovery system for components of a solar cell panel. The recovery system 200 includes a dismantling processing unit 211, a heating processing unit 231, a sieving processing unit 241, a sieving and recovery unit 242, a wind separation unit 251, a light product recovery unit 252, an air table separation unit 261, a waste material recovery unit 621, a retained material recovery unit 622, and a glass recovery unit 623.

[0087] The dismantling processing unit 211 performs pre-processing such as dismantling the aluminum frame of the solar cell panel and removing the backsheet, terminal box, and cables. The dismantling processing unit 211 can first remove the aluminum frame, backsheet, terminal box, and cables from the solar cell panel as needed. After that, it processes the internal structure of the solar cell panel sequentially.

[0088] Tempered glass is preferred for the glass substrate of a solar cell panel. This is because it can be recovered as fine granular glass after heat treatment and is easy to process with sorting equipment. The glass of the solar cell panel may be cracked before heat treatment.

[0089] The heating section 231 produces a heat-treated product by performing a heat treatment using the continuous heating device of the present invention. By performing a heat treatment using the continuous heating device of the present invention, the resin of the encapsulant of the solar cell panel can be removed. When using the continuous heating device 100, the heating section 231 sequentially performs primary processing by the primary processing section 13 and secondary processing by the secondary processing section 15. Details and preferred embodiments of the primary and secondary processing have already been described.

[0090] The sieving section 241 sieves the heat-treated material obtained from the continuous heating device into a first valuable metal-containing material including cells and copper wire, and a first glass material. The sieving section 241 separates the sieved material from the unsieved material. The sieved material is collected in the sieved material recovery section 242. The sieved material contains a first valuable metal-containing material, including cells and copper wires. Examples of the sieved material include linear objects such as copper wires, relatively large objects such as cells, and entanglements of these.

[0091] The material after sieving is processed in the subsequent air separation section 251. The material after sieving may be crushed as needed before being processed in the air separation section 251. The material after sieving contains the first glass material.

[0092] The sieving processing unit 241 has a sieve. The sieve of the sieving processing unit 241 may have one stage or multiple stages. The mesh size of the sieve in the sieving section 241 is preferably 1 to 100 mm. In the case of a multi-stage sieve, the mesh size of the sieve may be changed in stages during the sieving process. For example, a first sieving section may use a first sieve with a large mesh opening, such as 5 mm or more, 8 mm or more, 10 mm or more, 15 mm or more, or 20 mm or more, and a second sieving section may use a second sieve with a smaller mesh opening than the first sieve, such as 15 mm or less, 10 mm or less, 8 mm or less, 5 mm or less, or 3 mm or less. The difference in mesh opening between the first and second sieves may be 1 mm or more, 3 mm or more, 5 mm or more, etc.

[0093] The upper limit of the sieve opening may be 80 mm or less, or 60 mm or less. The shape of the sieve opening used for sieving may be circular or polygonal. A sieve sorting machine may also be used.

[0094] The air separation unit 251 separates the first glass material, which has been sieved in the sieving processing unit 241, into a second valuable metal-containing material including cells and a second glass material by air separation. The second valuable metal-containing material including cells is recovered as a light product in the light product recovery unit 252. The second glass material is processed as a heavy product in the subsequent air table separation unit 261.

[0095] Wind separation is a type of gravity separation technology. Gravity separation is a separation technique that uses the difference in specific gravity between a target substance and other substances to separate them. Wind separation equipment can include vertical wind separators, zigzag separators, horizontal flow separators, inertial force linear separators, and inertial force curve separators.

[0096] For example, a vertical wind separator as shown in Figure 9 of Japanese Patent Publication No. 2023-89446 may be used. With a vertical wind separator, by blowing an upward flow of air from below into a vertically elongated column, low-density particles with a low settling velocity can be moved upward and recovered as light products, and high-density particles with a high settling velocity can be moved downward and recovered as heavy products.

[0097] Light products in wind separation include solar cell cells, etc. Heavy products in wind separation include concentrated coarse-grained glass from solar cell panels, etc. Isotropic glass particles derived from cover glass, etc., are easily distributed as light products when the particles are small. On the other hand, cells are flattened particles and are thought to be more easily exposed to airflow over a wide area, so larger particles are more easily distributed as light products. Since larger particles are easier to classify into light and heavy products, there is little need to excessively crush them before wind separation. The metal can be recycled by refining the second valuable metal-containing material, which includes the cells in the light products.

[0098] In wind separation, the wind speed can be, for example, 4 to 15 m / s, and the airflow can be 20 to 70 L / min. An example of a suitable device for wind separation is the Harada Industries L750SRM wind separator.

[0099] The air table sorting unit 261 uses an air table to separate the third glass material from the second glass material obtained in the wind sorting unit 251. The air table sorting unit 261 can separate the materials into (i) a third glass material containing high-purity glass, (ii) retained light products such as single-edged products containing low-purity glass, etc., and copper wire-derived materials, and (iii) discharged light products such as copper wire-derived materials and cell-derived materials.

[0100] The air table sorting unit 261 collects materials containing valuable metals into the waste collection unit 621 and the retained material collection unit 622, respectively. The third glass material is collected into the glass collection unit 623.

[0101] In the air table sorting section 261, for example, a single-axis air table sorting machine as shown in Figure 10 of Patent Document 1 may be used. With this air table sorting machine, vibrations can be applied to a deck that is angled slightly from the horizontal direction, and air can be blown onto the deck from below in a direction perpendicular to the deck. High-density particles move downward within the powder layer with little effect from the wind and concentrate near the peaks on the deck surface. Their downward movement is suppressed at the peaks, and they move upward on the deck due to the vibrations of the deck and are recovered as heavy products. On the other hand, low-density particles are affected by the wind, move upward within the powder layer, move downward along the slope of the deck and are recovered as light products.

[0102] In air table sorting, materials can be classified into several categories, such as those discharged from the air table's outlet and those that remain on the air table. Taking the air table shown in Figure 10 of Patent Document 1 as an example, light products, mainly copper wire and cells, are discharged from the lower part of the deck. Heavy products, mainly glass, are discharged from the upper part of the deck. In addition, materials that are difficult to move in either direction while the air table is operating may be collected as retained material that remains on the air table's deck. In this retained material, light products such as copper wire are separated on the upper side of the powder layer.

[0103] An example of an air table is the SRM 296P-72N model manufactured by Harada Sangyo. Further sorting methods such as air separation, air table sorting, or sieving may be used to separate light and heavy products with higher precision.

[0104] According to the solar cell panel component recovery system of the present invention, the glass purity of the third glass material after sorting can be 99.99% or higher. Preferably, the glass purity of the third glass material after sorting is 99.995% or higher, more preferably 99.999% or higher, and even more preferably 99.9995% or higher. The upper limit of the glass purity of the third glass material after sorting is not particularly limited, but may be, for example, 99.9999%, 99.9998%, etc.

[0105] The recycling rate of the glass material contained in the heat-treated product is preferably 85% or higher, more preferably 90% or higher, and even more preferably 93% or higher. The recycling rate of glass material contained in heat-treated materials is calculated using the following formula. Recycling rate of glass material contained in heat-treated material = Weight of recycled glass material / Weight of glass material contained in heat-treated material

[0106] The copper wire contained in the heat-treated material can be recycled by metal refining of the first valuable metal-containing material. The recycling rate of the copper wire is preferably 90% or more, more preferably 95% or more, and even more preferably 99% or more. The recycling rate of copper wire contained in heat-treated materials is calculated using the following formula. Recycling rate of copper wire contained in heat-treated material = Weight of recycled copper wire / Weight of copper wire contained in heat-treated material

[0107] Cells contained in the heat-treated material can be recycled by metal refining of the first valuable metal-containing material and the second valuable metal-containing material. The recycling rate of the cells is preferably 90% or more, more preferably 95% or more, and even more preferably 99% or more. The recycling rate of cells contained in heat-treated materials is calculated using the following formula. Recycling rate of cells contained in heat-treated material = Weight of recycled cells / Weight of cells contained in heat-treated material

[0108] Although several embodiments have been described above, the present invention is not limited to the embodiments disclosed herein and can be implemented with appropriate modifications without altering its essence. The embodiments disclosed herein can be implemented in various other forms, and various omissions, substitutions, and modifications are possible without departing from the spirit of the invention.

[0109] For example, Figure 9 is a schematic diagram showing another example of a recovery system for components of a solar cell panel. Recovery system 201 is a modified version of recovery system 200 shown in Figure 8. As in recovery system 201, the order of the dismantling processing unit 211 and the heating processing unit 231 may be reversed. In other words, the dismantling process may be performed after the heating process using the continuous heating device of the present invention. Resin such as backsheets and terminal boxes is removed by the heating process. [Examples]

[0110] The embodiments will be described in more detail below with reference to examples, but the present invention is not limited to the following description.

[0111] [Example 1] A heat-treated product was obtained by processing a solar cell panel using a continuous heating device 100. The aluminum frame was then removed. In the primary treatment, the panel was heated under a nitrogen gas atmosphere, increasing from room temperature to 500°C for 7 minutes, and then at 500°C for 16 minutes. The oxygen concentration in the primary treatment area 13 was controlled to 3% by volume. In the secondary treatment, the panel was heated under an oxidizing atmosphere at 500°C for 16 minutes. The oxygen concentration in the secondary treatment area 15 was controlled to 21% by volume. Next, using the recovery system 200 shown in Figure 8, 273.6 kg of heat-treated material (3.4 kg of copper wire, 13 kg of cells, and 255.5 kg of glass material) was sorted. As a result of the sorting process, 17 kg of a first valuable metal-containing material (the remainder being glass) containing 62.6% copper wire and cells, 14.7 kg of a second valuable metal-containing material (the remainder being glass) containing 39.3% cells, and 239.5 kg of a third glass material (the remainder being cells) with a purity of 99.9997% were recovered. The recycling rates were 100% for copper wire, 99.5% for cells, and 93.7% for glass material, respectively.

[0112] [Comparative Example 1] The solar cell panel was heat-treated using the continuous heating device 100 under the same conditions as in Example 1, except that the heat treatment was performed only by the primary processing unit 13 without operating the secondary processing unit 15.

[0113] As shown by comparing Figures 10 and 11, the amount of soot adhering to the glass fragments was reduced in Example 1 compared to Comparative Example 1. [Industrial applicability]

[0114] According to the present invention, the thermal efficiency in the heat treatment of solar cell panels is improved, energy costs can be reduced, and the quality of valuable materials recovered from solar cell panels is also improved. [Explanation of Symbols]

[0115] 1. Solar cell panel 2. Primary processed materials 3. Heat-treated products 13 Primary Processing Unit 14 Switching section 15 Secondary Processing Unit 20 Furnace 21 Endless belt

Claims

1. The system includes a heating furnace that obtains a heat-treated product by heat-treating solar cell panels while they are being transported by an endless belt. The heating furnace comprises a primary processing unit that obtains a primary processed product by heat-treating the solar cell panel in a non-oxidizing atmosphere while conveying it on the endless belt, and a secondary processing unit that obtains a heat-treated product by heat-treating the primary processed product in an oxidizing atmosphere while conveying it on the endless belt. A flexible sealing curtain that crosses the transport direction of the solar cell panel and is in contact with the endless belt is suspended in the heating furnace between the primary processing unit and the secondary processing unit. At least one of the primary processing unit and the secondary processing unit utilizes the thermal energy generated by the combustion of pyrolysis gas produced when the sealing material of the solar cell panel is heat-treated and decomposed in the primary processing unit, A continuous heating device in which the amount of soot adhering to the heat-treated material is 100 ppm or less.

2. The system includes a heating furnace that obtains a heat-treated product by heat-treating solar cell panels while they are being transported by an endless belt. The heating furnace comprises a primary processing unit that obtains a primary processed product by heat-treating the solar cell panel in a non-oxidizing atmosphere while conveying it on the endless belt, and a secondary processing unit that obtains a heat-treated product by heat-treating the primary processed product in an oxidizing atmosphere while conveying it on the endless belt. At least one of the primary processing unit and the secondary processing unit utilizes the thermal energy generated by the combustion of pyrolysis gas produced when the sealing material of the solar cell panel is heat-treated and decomposed in the primary processing unit, A continuous heating device in which a heat exchanger that utilizes the thermal energy generated by the combustion of the pyrolysis gas is located in at least one of the primary processing unit and the secondary processing unit.

3. The continuous heating apparatus according to claim 2, wherein a flexible seal curtain that crosses the transport direction of the solar cell panels and is in contact with the endless belt is suspended in at least one place within the heating furnace.

4. The continuous heating apparatus according to claim 3, wherein the seal curtain is suspended in the heating furnace between the primary processing unit and the secondary processing unit.

5. The continuous heating apparatus according to claim 1 or 3, wherein the seal curtain is suspended in the heating furnace upstream of the primary processing unit.

6. The continuous heating apparatus according to claim 1 or 3, wherein the seal curtain is suspended in the heating furnace downstream of the secondary processing unit.

7. The continuous heating apparatus according to claim 1 or 2, wherein at least one of the primary processing unit and the secondary processing unit utilizes the thermal energy of the exhaust gas generated after the combustion of the pyrolysis gas.

8. The continuous heating device according to claim 1 or 2, further comprising a combustion chamber for burning the pyrolysis gas generated when the sealing material of the solar cell panel is heat-treated and decomposed in the primary processing unit.

9. The continuous heating device according to claim 8, wherein at least one of the primary processing unit and the secondary processing unit utilizes the thermal energy of exhaust gas discharged from the combustion chamber.

10. The continuous heating apparatus according to claim 1, wherein a heat exchanger that utilizes the thermal energy generated by the combustion of the pyrolysis gas is arranged in at least one of the primary processing unit and the secondary processing unit.

11. The continuous heating device according to claim 2 or 10, wherein the heat exchanger utilizes the thermal energy of the exhaust gas generated after the combustion of the pyrolysis gas.

12. The heating furnace has a muffle that surrounds the endless belt and an outer wall that surrounds the muffle, The continuous heating apparatus according to claim 2 or 10, wherein the heat exchanger is arranged in the space between the muffle and the outer wall.

13. The continuous heating apparatus according to claim 2 or 10, wherein the heat exchanger is an indirect heat exchanger.

14. The continuous heating device according to claim 12, wherein an electric heater is arranged in the space between the muffle and the outer wall.

15. The continuous heating apparatus according to claim 2, wherein the amount of soot adhering to the heat-treated material is 100 ppm or less.

16. A continuous heating device according to claim 1 or 2, A sorting device for separating glass material and valuable metal-containing materials from the heat-treated material, A system for recovering components of solar cell panels, equipped with the following features.

17. The solar cell panel component recovery system according to claim 16, wherein the sorting device has a sieving section that sieves the heat-treated material into a first valuable metal-containing material including cells and copper wires and a first glass material.

18. The solar cell panel component recovery system according to claim 17, wherein the sorting device further comprises an air separation unit that separates the first glass material sieved in the sieving unit into a second valuable metal-containing material including cells and the second glass material by air separation.

19. The solar cell panel component recovery system according to claim 18, further comprising an air table sorting unit for sorting a third glass material from the second glass material using an air table.

20. A solar cell panel component recovery system according to claim 19, wherein the glass purity of the third glass material after sorting is 99.99% or higher.

21. The solar cell panel component recovery system according to claim 16, wherein the recycling rate of the glass material contained in the heat-treated product is 85% or more.

22. A solar cell panel component recovery system according to claim 16, wherein the recycling rate of cells contained in the heat-treated material is 90% or more.

23. The solar cell panel component recovery system according to claim 16, wherein the recycling rate of copper wire contained in the heat-treated material is 90% or more.

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