JP5932356B2 - How to use the drying oven - Google Patents

Description

  The present invention relates to a drying furnace.

  Conventionally, a drying furnace for drying a sheet coated with a slurry is known. For example, Patent Document 1 discloses a drying furnace in which four drying zones each having a carry-in port and a carry-out port are connected in a predetermined direction. The top plate of each drying zone is provided with an air supply port and an exhaust port. An air supply means for forcibly supplying air is attached to each air supply opening, and an exhaust means for forcibly discharging air is attached to each exhaust opening. In this drying furnace, the air flow in each drying zone is made to be the same and parallel to the sheet conveying direction. This air flow may be opposite to the sheet conveyance direction, but in order to efficiently remove the evaporated organic solvent, the air flow should be the same and parallel to the sheet conveyance direction. Preferred is described.

JP 2008-302297 A

  By the way, Patent Document 1 neither describes nor suggests how to connect adjacent drying zones. According to general technical common sense, it is considered that a sealing material such as packing is sandwiched between adjacent drying zones and the outlet of one drying zone and the inlet of the other drying zone are connected in an airtight manner. It is done.

  However, when connected in this way, since there is no heat source at the connection location, the temperature of the sheet having the coated surface decreases when passing through the connection location, which may reduce the drying efficiency. In addition, since the carry-out port of one drying zone and the carry-in port of the other drying zone communicate with each other, there is a problem that air cannot be prevented from flowing from one drying zone to the other drying zone. there were.

  The main object of the present invention is to prevent a decrease in the temperature of a sheet to be dried and prevent air from flowing from one drying furnace unit to the other drying furnace unit at a connecting portion between adjacent drying furnace units. Objective.

The drying furnace of the present invention is
A drying furnace in which a plurality of drying furnace units that dry a sheet coated with slurry on at least one side are connected so that each conveyance path of the drying furnace unit is continuous along a predetermined direction,
A connecting portion between adjacent drying furnace units is provided with a pair of gas injectors that inject gas from both the upper and lower sides toward the sheet,
The gas injected by the gas injector is temperature-adjusted so that the temperature of at least one atmosphere gas of the adjacent drying furnace unit is maintained at the connecting portion.

  In this drying furnace, a pair of gas injectors for injecting gas from both the upper and lower sides toward the sheet are provided at a connecting portion between adjacent drying furnace units. The temperature of the gas injected by the gas injector is adjusted so that the temperature of the atmosphere gas of at least one of the adjacent drying furnace units is maintained at the connecting portion. Therefore, according to this drying furnace, since the temperature of the slurry application surface of the sheet hardly changes at the connecting portion of the drying furnace unit, the slurry application surface can be efficiently dried. Moreover, since gas is injected from both the upper and lower sides toward the sheet at the connecting portion, it is possible to prevent the atmospheric gas from flowing from one of the adjacent drying furnace units to the other.

  In addition, it is preferable that the gas which a gas injector injects is temperature-controlled so that the temperature of the atmospheric gas of both adjacent drying furnace units may be maintained in a connection part. The atmosphere gas is not particularly limited, and examples thereof include air and an inert gas (such as nitrogen). Furthermore, it is preferable to use the same type of gas as the atmosphere gas as the gas injected by the gas injector.

  In the drying furnace of the present invention, the pair of gas injectors may support the sheet in a floating state. This eliminates the need to support the sheet with a support roller or the like.

  In the drying furnace of the present invention, the sheet has a slurry applied on both sides, and the adjacent drying furnace unit dries each slurry application surface by circulating hot air along each slurry application surface. It may be a thing. In this way, the sheet coated with the slurry on both sides can be dried at the same time, so the time is shortened compared to the case of drying one by one. As a result, production efficiency increases. Also, when drying one side at a time, either side will pass through the drying oven twice, so there may be a difference in performance on both sides, but since both sides are dried simultaneously, there is a difference in performance on both sides. It does not occur.

  In the drying furnace of the present invention, the pair of gas injectors can approach and separate from the sheet, and the adjacent drying furnace units circulate hot air in the same direction along the slurry application surface of the sheet. It is good also as switchable whether it makes it distribute | circulate or distribute | circulate a hot air to the opposite direction. In the adjacent drying furnace unit, for example, when hot air is circulated in the opposite directions along the slurry application surface of the sheet, the hot air circulated through one drying furnace unit and the other by bringing a pair of gas injectors closer to each other It is possible to prevent the hot air flowing through the drying furnace unit from affecting each other. On the other hand, when circulating hot air in the same direction along the slurry application surface of the sheet, by separating the pair of gas injectors, one drying furnace unit and the other drying furnace unit are the same. The hot air in the direction can be easily passed.

  In the drying furnace of the present invention, the drying furnace unit circulates hot air along the application surface of the sheet, and infrared rays are applied to the application surface of the sheet by an infrared heater installed to face the application surface of the sheet. It is good also as what irradiates. If it carries out like this, a slurry application surface can be dried in a short time by using hot air and an infrared heater together. As such an infrared heater, for example, filaments are concentrically covered by a plurality of tubes functioning as a filter that absorbs infrared rays having a wavelength exceeding 3.5 μm, and the surface temperature of the infrared heater is increased between the plurality of tubes. It is also possible to use a cooling fluid passage (see Japanese Patent No. 4790092) that suppresses the above. In such a drying furnace, a transparent flat plate having a size covering the infrared heater may be provided between the slurry application surface and the infrared heater. If it carries out like this, it can prevent that the scattered material from a slurry application surface adheres to an infrared heater by a transparent flat plate. Since the cleaning work for removing the deposits on the transparent flat plate is simpler than the cleaning work for removing the deposits on the infrared heater, the work efficiency during cleaning is improved. In particular, when the infrared heater is disposed in the arch-shaped depression of the reflecting plate, the cleaning work becomes more complicated, so that the merit of installing the transparent flat plate is great. In addition, if it is a drying furnace unit (or drying furnace) which dries the sheet | seat in which the slurry application surface was formed in at least one side with the infrared heater installed in the position facing this slurry application surface, the significance of installing such a transparent flat plate There is. Further, when performing double-sided drying, an infrared heater is installed at a position facing both surfaces of the slurry application surface, but it is useful to install a transparent flat plate on the lower surface side. In this way, not only dripping of the slurry and adhesion of solvent volatile components, but also direct contact when the slurry coating sheet is damaged during transportation and dropped can be prevented. In such a transparent flat plate, the filament is concentrically covered by a plurality of tubes functioning as a filter that absorbs infrared light having a wavelength exceeding 3.5 μm as an infrared heater, and the surface temperature of the infrared heater is between these tubes. In the case of using a cooling fluid flow path that suppresses the rise, a flat plate that transmits a wavelength of 3.5 μm or less is used.

  In the drying furnace of the present invention, the drying furnace unit is provided so as to penetrate the furnace body and the furnace body in a predetermined direction, and a conveyance passage through which a sheet coated with slurry on at least one surface is conveyed in the predetermined direction. And first and second vent holes provided at both ends of the transport passage so that air flows along the slurry application surface of the sheet, and connected to the first and second vent holes, respectively. The air supply means and the air from the air supply means flow from the first air vent to the second air vent along the coating surface of the sheet, or the sheet from the second air vent to the first air vent. Air direction switching means for switching whether to send the air from the air supply means along the coating surface. If it carries out like this, the flow of the air in each drying furnace unit can be changed freely by switching a wind direction switching means.

3 is a longitudinal sectional view of a drying furnace 70. FIG. 3 is a longitudinal sectional view of an infrared heater 36. FIG. It is AA sectional drawing of FIG. FIG. 3 is a perspective view of a pair of gas injectors 60 installed at a connecting portion 16. It is explanatory drawing when the direction of the hot air of the adjacent drying furnace unit 10 is opposite. It is explanatory drawing in case the direction of the hot air of the adjacent drying furnace unit 10 is the same. It is explanatory drawing at the time of providing the transparent flat plate 37 in the drying furnace unit 10. FIG. It is explanatory drawing in case the direction of the hot air of the adjacent drying furnace unit 10 is the same.

  Next, a preferred embodiment of the present invention will be described with reference to the drawings. 1 is a longitudinal sectional view of a drying furnace 70, FIG. 2 is a longitudinal sectional view of an infrared heater 36, FIG. 3 is a sectional view taken along line AA of FIG. 2, and FIG. 4 is a perspective view of a pair of gas injectors 60.

  As shown in FIG. 1, the drying furnace 70 is formed by connecting a plurality of drying furnace units 10 so that the respective transport passages 14 are connected in a predetermined direction, and a pair of upper and lower gas injectors is connected to the connecting portion. 60 is provided. In each conveyance path 14, a long sheet 54 is conveyed from left to right in FIG. This sheet 54 has a slurry coated on both sides. The surface on which the slurry is applied is referred to as a slurry application surface 56.

  The drying furnace unit 10 includes a furnace body 12, a transfer passage 14, a pipe structure 20 having first and second vent holes 21a and 22a, a hot air generator 26, an exhaust blower 28, and a wind direction switching valve 30. And an infrared heater 36. Among these, the pipe structure 20, the hot air generator 26, the exhaust blower 28, the air direction switching valve 30, and the infrared heater 36 are provided corresponding to each slurry application surface 56.

  The furnace body 12 is a heat insulating structure formed in a substantially rectangular parallelepiped shape, and has openings 14a and 14b on the front end face 12a and the rear end face 12b, respectively. The furnace body 12 has a length of 2 to 6 m from the front end surface 12a to the rear end surface 12b.

  The conveyance passage 14 is a passage from the opening 14a to the opening 14b, and penetrates the furnace body 12 in the horizontal direction. The sheet 54 coated with the slurry on both sides passes through the conveyance path 14. Specifically, the sheet 54 is carried in from the opening 14a, proceeds in the horizontal direction in the furnace body 12, and is carried out from the opening 14b.

  Of the two pipe structures 20, one is installed corresponding to the slurry application surface 56 formed on the upper surface of the sheet 54, and the other corresponds to the slurry application surface 56 formed on the lower surface of the sheet 54. Installed. Each pipe structure 20 is provided with a hot air generator 26, an exhaust blower 28, and a wind direction switching valve 30. Since the two pipe structures 20 have the same configuration, the pipe structure 20 installed corresponding to the slurry application surface 56 formed on the upper surface of the sheet 54 will be described below.

  The pipe structure 20 penetrates in the vertical direction at a location near the rear end surface 12b in the ceiling of the furnace body 12 and the first pipe portion 21 that penetrates in the vertical direction at a location near the front end surface 12a in the ceiling of the furnace body 12. The second pipe part 22 to be connected, the third pipe part 23 connecting the upper end of the first pipe part 21 and the upper end of the second pipe part 22, the intermediate position of the first pipe part 21 and the intermediate position of the second pipe part 22 And a fourth pipe portion 24 that connects the two. That is, the third pipe portion 23 and the fourth pipe portion 24 are passages that connect the first pipe portion 21 and the second pipe portion 22 in parallel. The first pipe portion 21 is bent so as to be bent in the furnace body 12 so that the vicinity of the lower end faces the horizontal direction. For this reason, the 1st vent 21a which is the lower end opening of the 1st pipe part 21 is the state opened toward the rear-end surface 12b. The second pipe portion 22 is processed so that the vicinity of the lower end bent inside the furnace body faces the horizontal direction. For this reason, the 2nd vent 22a which is the lower end opening of the 2nd pipe part 22 is the state opened toward the front end surface 12a. The first vent 21a and the second vent 22a are provided so as to face each other and have the same height. For this reason, the air flowing out from one of the first and second vent holes 21a, 22a flows into the other, and the flow of the air at that time is in a direction along the slurry application surface 56 of the sheet 54. In addition, the height of the 1st ventilation hole 21a and the height of the 2nd ventilation hole 22a do not necessarily need to be the same.

  The hot air generator 26 is attached to the fourth pipe portion 24 and supplies hot air to the inside of the fourth pipe portion 24. The hot air generator 26 can adjust the air volume.

  The exhaust blower 28 is attached to the third pipe portion 23 and has a function of discharging the gas inside the third pipe portion 23 to the outside. This exhaust blower 28 can also adjust the air volume.

  The air direction switching valve 30 is provided at the joint between the first valve 31 provided at the joint between the first pipe part 21 and the fourth pipe part 24 and the second pipe part 22 and the fourth pipe part 24. And a second valve 32. The first valve 31 communicates the first pipe portion 21 and the fourth pipe portion 24 and at the same time blocks the communication between the first pipe portion 21 and the third pipe portion 23 (see the solid line in FIG. 1, the air supply position). Any of the positions where the communication between the first pipe portion 21 and the fourth pipe portion 24 is blocked and the first pipe portion 21 and the third pipe portion 23 are communicated (see the dotted line in FIG. 1, exhaust position). Can be switched. The second valve 32 shuts off the communication between the second pipe part 22 and the fourth pipe part 24 and also communicates the second pipe part 22 and the third pipe part 23 (refer to the solid line in FIG. 1, referred to as the exhaust position). ) And the second pipe portion 22 and the fourth pipe portion 24 and the position where the communication between the second pipe portion 22 and the third pipe portion 23 is blocked (refer to the dotted line in FIG. 1, referred to as the air supply position). It can be switched to either. The valves 31 and 32 may be switched manually, or may be switched electrically using an electromagnetic solenoid or the like.

  A plurality of infrared heaters 36 are attached near the ceiling of the furnace body 12. The longitudinal direction of each infrared heater 36 is attached so as to be orthogonal to the transport direction. As shown in FIGS. 2 and 3, the infrared heater 36 includes a heater body 42 formed so that the inner tube 40 surrounds the filament 38, an outer tube 44 formed so as to surround the heater body 42, and an outer tube 44. A bottomed cylindrical cap 46 that is airtightly fitted to both ends of the pipe 44 and a flow path 48 that is formed between the heater body 42 and the outer pipe 44 and through which cooling fluid can flow. The filament 38 is energized and heated to 700 to 1200 ° C., and emits infrared light having a peak at a wavelength near 3 μm. The electrical wiring 38 a connected to the filament 38 is led out to the outside airtightly through a wiring lead-out portion 46 a provided in the cap 46. The inner tube 40 is made of quartz glass, borosilicate crown glass, or the like, and functions as a filter that passes infrared rays having a wavelength of 3.5 μm or less and absorbs infrared rays having a wavelength exceeding 3.5 μm. The heater body 42 is supported by holders 50 arranged at both ends inside the cap 46. As with the inner tube 40, the outer tube 44 is made of quartz glass, borosilicate crown glass, or the like, and passes through infrared rays having a wavelength of 3.5 μm or less and absorbs infrared rays having a wavelength exceeding 3.5 μm. Function. Each cap 46 has a fluid inlet / outlet 46b. The flow path 48 is configured such that the cooling fluid flows from one fluid inlet / outlet 46b to the other fluid inlet / outlet 46b. The cooling fluid flowing through the flow channel 48 is, for example, air or an inert gas, and cools each of the tubes 40 and 44 by contacting the inner tube 40 and the outer tube 44 to remove heat. In the infrared heater 36, when infrared light having a peak near 3 μm is emitted from the filament 38, infrared light having a wavelength of 3.5 μm or less passes through the inner tube 40 and the outer tube 44 and passes through the conveyance path 14. The slurry application surface 56 of the sheet 54 is irradiated. Infrared light having this wavelength is said to be excellent in the ability to break hydrogen bonds of the organic solvent contained in the slurry application surface 56 of the sheet 54, and can efficiently evaporate the organic solvent. On the other hand, the inner tube 40 and the outer tube 44 absorb infrared rays having a wavelength exceeding 3.5 μm, but are cooled by the cooling fluid flowing through the flow path 48, and thus are less than the ignition point of the organic solvent evaporating from the slurry application surface 56. It is possible to maintain the temperature.

  Such an infrared heater 36 is arranged in an internal space of an arch-shaped recess 52 provided on a reflector near the ceiling of the furnace body 12. Similarly to the infrared heater 36, the arch-shaped recess 52 is formed so as to extend in a direction orthogonal to the conveyance direction, and has a cross-sectional shape that is a curved shape such as a parabola, an elliptical arc, or an arc, and has a focal point or a center position. Infrared heater 36 is arranged. As a result, the infrared light having a wavelength of 3.5 μm or less emitted from the infrared heater 36 is reflected by the arch-shaped depression 52 and efficiently irradiated onto the slurry application surface 56.

  The pair of upper and lower gas injectors 60 is provided in the connecting portion 16 of the adjacent drying furnace unit 10. In the connecting portion 16, the rear end surface 12 b of one drying furnace unit 10 and the front end surface 12 a of the other drying furnace unit 10 are connected via a packing 18 by a bolt (not shown). For this reason, the opening 14b of the rear end surface 12b of one drying furnace unit 10 and the opening 14a of the front end surface 12a of the other drying furnace unit 10 are kept airtight. The material of the packing 18 may be any material that can withstand an organic solvent, and examples thereof include polytetrafluoroethylene. If the sealing property of the packing 18 is good, the bolt connection may be omitted. The pair of upper and lower gas injectors 60 are disposed across the opening 14 b of one drying furnace unit 10 and the opening 14 a of the other drying furnace unit 10. As shown in FIG. 4, each gas injector 60 is provided with a pipe 64 for sending hot air into an injector main body 62 formed of a rectangular parallelepiped inside, and a surface facing the slurry application surface 56 is A porous nozzle 66 is formed. A dryer (not shown) is connected to the pipe 64. When heated gas (heated air here) is supplied from the dryer, the gas injector 60 injects heated gas from the porous nozzle 66 toward the slurry application surface 56. The dryer has a function of adjusting the temperature of the heated gas. In addition, the pair of upper and lower gas injectors 60 are provided with an air cylinder (not shown) so as to approach and separate from each other by adjusting the air pressure to the air cylinder. Specifically, it can move between a proximity position indicated by a solid line in FIG. 1 and a separation position indicated by a one-dot chain line. Note that the pair of upper and lower gas injectors 60 may be moved closer to and away from each other without using an air cylinder, and the height may be adjusted manually, for example.

  Next, the air direction switching of the drying furnace 70 will be described. 5 and 6 are explanatory views of the air direction switching of the drying furnace 70. FIG. The white arrow indicates the direction of hot air.

  When flowing hot air from the first vent 21a to the second vent 22a, the first valve 31 is set to the supply position and the second valve 32 is set to the exhaust position as in the drying furnace unit 10 shown on the left side of FIG. . Specifically, the first valve 31 is set at a position where the first pipe portion 21 and the fourth pipe portion 24 communicate with each other and the communication between the first pipe portion 21 and the third pipe portion 23 is blocked. Further, the second valve 32 is set at a position where the communication between the second pipe portion 22 and the fourth pipe portion 24 is blocked and the second pipe portion 22 and the third pipe portion 23 are communicated. Then, the hot air supplied from the hot air generator 26 to the fourth pipe part 24 is blown out from the first vent 21 a through the first pipe part 21. On the other hand, the exhaust blower 28 exhausts gas from the third pipe portion 23 via the second vent 22 a and the second pipe portion 22. As a result, hot air flows into the furnace body 12 from the first vent 21a to the second vent 22a, that is, in the same direction as the conveying direction of the sheet 54.

  When hot air flows from the second vent 22a to the first vent 21a, the second valve 32 is set to the supply position and the first valve 31 is set to the exhaust position as in the drying furnace unit 10 shown on the right side of FIG. . Specifically, the second valve 32 is set at a position where the second pipe portion 22 and the fourth pipe portion 24 communicate with each other and the communication between the second pipe portion 22 and the third pipe portion 23 is blocked. Further, the first valve 31 is set at a position where the communication between the first pipe part 21 and the fourth pipe part 24 is blocked and the first pipe part 21 and the third pipe part 23 are communicated. Then, the hot air supplied from the hot air generator 26 to the fourth pipe portion 24 is blown out from the second vent 22 a through the second pipe portion 22. On the other hand, the exhaust blower 28 exhausts gas from the third pipe part 23 via the first vent 21 a and the first pipe part 21. As a result, hot air flows into the furnace body 12 from the second vent 22a to the first vent 21a, that is, in the direction opposite to the conveying direction of the sheet 54.

  In FIG. 5, the air direction switching valve 30 of each drying furnace unit 10 is set so that the direction of hot air of the adjacent drying furnace units 10 is opposite. In FIG. 6, the air direction switching valves 30 (first and second valves 31 and 32) of each drying furnace unit 10 are set so that the directions of hot air of adjacent drying furnace units 10 are the same. 5 and 6, the pair of upper and lower gas injectors 60 are set at close positions. The interval between the two gas injectors 60 set at the close positions is such that the sheet 54 can be lifted and supported (air nip) when heated gas is injected from above and below at a low speed (for example, a wind speed of 1 m / sec). It has become narrower. At this time, since the heated gas injected from the pair of upper and lower gas injectors 60 serves as a curtain, the hot air flowing through one drying furnace unit 10 and the hot air flowing through the other drying furnace unit 10 affect each other. Independent. The temperature of the heated gas injected from both gas injectors 60 is set to be the same as the temperature of the hot air supplied from the hot air generator 26. For this reason, the temperature of the sheet | seat 54 which passes the connection part 16 does not fall. Further, the space S on the back side of the first and second pipe portions 21 and 22 is a place where air easily stagnates. However, the heated gas injected from the pair of upper and lower gas injectors 60 contains the organic solvent in the space S. Since the entry of the vapor is blocked, the vapor of the organic solvent is not easily accumulated in the space S.

  As the case where the direction of the hot air is opposite, in addition to the case where the hot airs collide with each other as shown in FIG. 5, the case where the hot airs are separated from each other (in the left drying oven unit 10 in FIG. 5, the second vent 22 a From the first vent hole 21a to the second vent hole 22a in the right drying oven unit 10), but in this case, the pair of upper and lower gas injectors 60 are set at close positions. The Moreover, as a case where the directions of the hot air are the same, in addition to the case where both the drying oven units 10 flow from the first ventilation port 21a to the second ventilation port 22a as shown in FIG. There is a case where the gas flows from the opening 22a to the first ventilation hole 21a. In this case as well, the pair of upper and lower gas injectors 60 are set at close positions.

  Next, the case where the sheet 54 whose both surfaces are the slurry application surfaces 56 is dried in the drying furnace 70 will be described. The sheet 54 is unwound from a roll (not shown) disposed on the left side of the drying furnace 70 in a state where the slurry is not applied on both sides, and immediately before being loaded into the drying furnace 70, the slurry is applied to the upper and lower surfaces by a coater (not shown). Applied. And it passes along the conveyance path 14 of each drying furnace unit 10 which comprises the drying furnace 70. As shown in FIG. At that time, the organic solvent evaporates from the upper and lower slurry application surfaces 56, and the evaporated organic solvent is discharged to the outside by each exhaust blower 28 and finally carried out from the drying furnace 70. Then, it is wound up on a roll (not shown) installed on the right side of the drying furnace 70. The organic solvent evaporates from the slurry application surface 56 due to the action of infrared rays irradiated from the infrared heater 36 and hot air supplied from the hot air generator 26.

  The sheet 54 is not particularly limited. For example, a sheet coated with an electrode for a lithium ion secondary battery may be used. Examples of such a sheet include a sheet obtained by applying an electrode material slurry obtained by kneading a positive electrode active material (or a negative electrode active material) together with a binder, a conductive material, and an organic solvent onto a metal sheet such as aluminum or copper. Or you may use the sheet | seat made from the baking ceramic which apply | coated the unfired ceramic molded object. Examples of such sheets include those obtained by applying a slurry obtained by kneading ceramic particles in a binder and water (or an organic solvent) onto a sheet made of fired ceramics.

  According to the drying furnace 70 of the present embodiment described above, the slurry application surface 56 is efficiently formed in order to prevent the temperature of the slurry application surface 56 of the sheet 54 from changing at the connecting portion 16 of the adjacent drying furnace unit 10. Can be dried.

  In addition, the pair of upper and lower gas injectors 60 disposed in the close positions inject the heated gas toward the sheet 54 at the connecting portion 16, thereby preventing air from flowing from one of the adjacent drying furnace units 10 to the other. can do. In addition, since the sheet 54 is supported in a floating state, it is not necessary to support the sheet 54 with a support roller or the like.

  Furthermore, since the drying furnace unit 10 can dry both the slurry application surfaces 56 of the sheet 54 at the same time, the time is shortened as compared with the case of drying one by one. As a result, production efficiency increases. Also, when drying one side at a time, either side will pass through the drying oven twice, so there may be a difference in performance on both sides, but since both sides are dried simultaneously, there is a difference in performance on both sides. It does not occur.

  Furthermore, since the infrared heater 36 is provided, when it is difficult to dry the slurry application surface 56 only with hot air, the slurry application surface 56 can be dried in a short time by using the infrared heater 36 together. it can. In particular, since the infrared heater 36 irradiates infrared rays having a wavelength of 3.5 μm or less and keeps the heater surface temperature below the ignition point of the organic solvent, the organic solvent can be efficiently evaporated, and the organic solvent ignites. There is no risk of doing so.

  Moreover, since the hot air generator 26 and the exhaust blower 28 can adjust the air volume, not only the direction of the hot air but also the air volume can be freely changed.

  Further, since the drying furnace 70 is formed by connecting a plurality of drying furnace units 10 such that each conveyance passage 14 is continuous along the conveyance direction of the sheet 54, the air direction switching valve 30 of each drying furnace unit 10. By switching, the flow of air can be freely changed for each drying furnace unit 10.

  It should be noted that the present invention is not limited to the above-described embodiment, and it goes without saying that the present invention can be implemented in various modes as long as it belongs to the technical scope of the present invention.

  For example, in the above-described embodiment, the drying furnace 70 that dries the sheet 54 coated with the slurry on both sides is illustrated, but a drying furnace that dries the sheet coated with the slurry only on the upper surface may be used. In this case, since the lower surface of the sheet is not the slurry application surface, the pipe structure 20 (including the air direction switching valve 30, the hot air generator 26, and the exhaust blower 28) or infrared rays provided opposite to the lower surface of the sheet in FIG. The heater 36 and the like may be omitted.

  In the above-described embodiment, as illustrated in FIG. 7, a transparent flat plate 37 having a size that covers the infrared heater 36 may be provided between the slurry application surface 56 of the sheet 54 and the infrared heater 36. By doing so, the transparent flat plate 37 can prevent the scattered matter from the slurry application surface 56 from adhering to the infrared heater 36 and the arch-shaped depression 52. Since the cleaning work for removing the deposits on the transparent flat plate 37 is simpler than the cleaning work for removing the deposits on the infrared heater 36 and the arch-shaped recess 52, the work efficiency during cleaning is improved. In the embodiment described above, since the infrared heater 36 is of a type that transmits a wavelength of 3.5 μm or less, the transparent flat plate 37 is also a flat plate that transmits a wavelength of 3.5 μm or less.

  In the above-described embodiment, when the directions of hot air of the adjacent drying furnace units 10 are the same, the pair of upper and lower gas injectors 60 are set at close positions. In this case, as shown in FIG. The injector 60 may be set at a separated position. The distance between the gas injectors 60 set at the separated positions is wide enough to prevent the air nip described above. As a result, the hot air flowing through one drying furnace unit 10 can enter the other drying furnace unit 10 as it is without being affected by the heated gas injected from both gas injectors 60. As a result, since the hot air flows from one drying furnace unit 10 to the other drying furnace unit 10, a large flow can be created. The point that the temperature of the sheet 54 and the slurry application surface 56 that passes through the connecting portion 16 does not decrease, and the point that the vapor of the organic solvent does not easily accumulate in the space S is when the pair of upper and lower gas injectors 60 are set at close positions. It is the same. 8 illustrates the case where hot air flows from the first vent 21a to the second vent 22a in both the drying furnace units 10, but hot air may flow from the second vent 22a to the first vent 21a. The pair of upper and lower gas injectors 60 may be set at a separated position.

  In the embodiment described above, the infrared heater 36 is provided in the furnace body 12. However, if the thickness of the slurry application surface 56 of the sheet 54 is thin and sufficient drying is possible only with hot air, the infrared heater 36 may be omitted. Good.

  In the above-described embodiment, the outer periphery of the filament 38 is concentrically covered by the plurality of tubes 40 and 44 that function as a filter that absorbs infrared rays having a wavelength exceeding 3.5 μm as the infrared heater 36. , 44 in which a cooling fluid flow path 48 that suppresses the rise in the surface temperature of the infrared heater 36 is formed, but other infrared heaters may be used.

  In the embodiment described above, air is used as the atmosphere gas of each drying furnace unit 10, but an inert gas such as nitrogen may be used instead of air. Moreover, it is preferable to use the same kind of heating gas injected from the gas injector 60 as the atmosphere gas of the drying furnace unit 10.

  In the above-described embodiment, the temperature of the atmospheric gas in each drying furnace unit 10 is set to the same temperature, and the heating gas is set to the same temperature. However, when the temperature of the atmospheric gas in each drying furnace unit 10 is different, The temperature of the heating gas may be the same as the temperature of any one of the atmospheric gases.

  In the above-described embodiment, the gas injected from the gas injector 60 is the heating gas. However, when the temperature of the atmospheric gas in each drying furnace unit 10 is low (for example, normal temperature or 40 to 50 ° C.), the gas is injected. The gas to be used may be a low temperature gas to suppress the temperature rise at the connecting portion.

  INDUSTRIAL APPLICABILITY The present invention relates to an industry in which a sheet coated with a slurry needs to be dried, for example, a battery industry for producing an electrode coating film of a lithium ion secondary battery, or a ceramic for producing a ceramic laminate comprising two layers of ceramic sintered bodies It can be used in industry, film industry for manufacturing optical film products, and the like.

DESCRIPTION OF SYMBOLS 10 Drying furnace unit, 12 Furnace body, 12a Front end surface, 12b Rear end surface, 14 Conveyance path, 14a Opening, 14b Opening, 16 Connection part, 18 Packing, 20 Pipe structure, 21 1st pipe part, 21a 1st vent , 22 Second pipe part, 22a Second vent, 23 Third pipe part, 24 Fourth pipe part, 26 Hot air generator, 28 Exhaust blower, 30 Air direction switching valve, 31 First valve, 32 Second valve, 36 Infrared heater, 37 transparent flat plate, 38 filament, 38a electrical wiring, 40 inner tube, 42 heater body, 44 outer tube, 46 cap, 46a wiring outlet, 46b fluid inlet / outlet, 48 channel, 50 holder, 52 arched recess , 54 sheets, 56 slurry application surface, 60 gas injector, 62 injector body, 64 pipe, 66 Porous nozzle, 70 a drying oven, S Space

Claims (6)

A method of using a drying furnace in which a plurality of drying furnace units for drying a slurry application surface of a sheet coated with slurry on at least one side thereof are connected so that each conveyance path of the drying furnace unit is connected along a predetermined direction. ,
A pair of gas injectors for injecting gas from both the upper and lower sides toward the sheet are provided at the connecting portion of the adjacent drying furnace units so as to face each other .
Gas pair of the gas injector for injecting, with the temperature of at least one of the atmospheric gas in the drying oven units wherein adjacent thermostated so as to maintain in said connecting portion, said pair of gas injectors injects Gas to act as a curtain so that one and the other of the adjacent drying oven units are independent of each other;
How to use the drying oven. The gas is ejected from the pair of gas injectors, and the sheet is supported in a floating state.
A method for using the drying furnace according to claim 1. The sheet is a slurry coated on both sides,
The adjacent drying furnace unit is for drying each slurry application surface by circulating hot air along each slurry application surface,
The use method of the drying furnace of Claim 1 or 2. The pair of gas injectors can approach and separate from the sheet;
The adjacent drying furnace unit can switch between circulating hot air in the same direction or circulating hot air in the opposite direction along the slurry application surface of the sheet.
The usage method of the drying furnace of any one of Claims 1-3. The drying furnace unit, together with circulating hot air along the slurry coated surface of the sheet, which irradiates an infrared ray to the slurry coated surface of the sheet by the installed infrared heaters so as to face the slurry-coated surface of the sheet Is,
The usage method of the drying furnace of any one of Claims 1-4. The drying furnace unit includes a transparent flat plate having a size covering the infrared heater between the slurry application surface of the sheet and the infrared heater.
A method for using the drying furnace according to claim 5.

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