WO2019187861A1 - 気体吹出しノズル及び炉、並びに加工フィルムの製造方法 - Google Patents
気体吹出しノズル及び炉、並びに加工フィルムの製造方法 Download PDFInfo
- Publication number
- WO2019187861A1 WO2019187861A1 PCT/JP2019/006877 JP2019006877W WO2019187861A1 WO 2019187861 A1 WO2019187861 A1 WO 2019187861A1 JP 2019006877 W JP2019006877 W JP 2019006877W WO 2019187861 A1 WO2019187861 A1 WO 2019187861A1
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- WIPO (PCT)
- Prior art keywords
- gas
- nozzle
- partition plate
- cylindrical body
- longitudinal direction
- Prior art date
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B12/00—Arrangements for controlling delivery; Arrangements for controlling the spray area
- B05B12/16—Arrangements for controlling delivery; Arrangements for controlling the spray area for controlling the spray area
- B05B12/18—Arrangements for controlling delivery; Arrangements for controlling the spray area for controlling the spray area using fluids, e.g. gas streams
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
- F26B21/004—Nozzle assemblies; Air knives; Air distributors; Blow boxes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B1/00—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means
- B05B1/02—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to produce a jet, spray, or other discharge of particular shape or nature, e.g. in single drops, or having an outlet of particular shape
- B05B1/04—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means designed to produce a jet, spray, or other discharge of particular shape or nature, e.g. in single drops, or having an outlet of particular shape in flat form, e.g. fan-like, sheet-like
- B05B1/044—Slits, i.e. narrow openings defined by two straight and parallel lips; Elongated outlets for producing very wide discharges, e.g. fluid curtains
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B13/00—Machines and apparatus for drying fabrics, fibres, yarns, or other materials in long lengths, with progressive movement
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B21/00—Arrangements or duct systems, e.g. in combination with pallet boxes, for supplying and controlling air or gases for drying solid materials or objects
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B1/00—Nozzles, spray heads or other outlets, with or without auxiliary devices such as valves, heating means
- B05B1/005—Nozzles or other outlets specially adapted for discharging one or more gases
Definitions
- the present invention relates to a gas blowing nozzle used for blowing gas onto the surface of a resin film, a furnace equipped with a gas blowing nozzle, and a method for producing a processed film.
- a liquid is applied to a long or web resin film raw material, and then the resin film is conveyed inside a furnace such as a drying furnace.
- a gas such as air or nitrogen may be sprayed on the surface of the resin film.
- the blowing of gas to the resin film to be transported is generally performed by a gas blowing nozzle that extends in the direction perpendicular to the resin film transport direction, that is, the width direction of the resin film, and blows the gas vertically toward the surface of the resin film. Often used.
- gas blowing nozzle extending in the film width direction, gas is supplied in the film width direction (that is, the nozzle longitudinal direction).
- Patent Document 1 discloses a wavy or zigzag pattern in which irregularities are repeated along the longitudinal direction of the gas blowing nozzle (that is, the width direction of the workpiece). What has the uneven surface cover formed in the shape is disclosed.
- the cross-sectional shape of the uneven surface cover along the longitudinal direction of the nozzle is a triangular wave.
- This gas blowing nozzle is a nozzle box having a surface facing the workpiece as a gas blowing surface, a slit-like opening provided in the nozzle box and extending in the width direction of the workpiece and allowing gas to pass toward the gas blowing surface,
- the concavo-convex surface cover is provided so as to cover the opening in the nozzle box.
- the concave / convex surface cover covers the opening, but since the cross-sectional shape is triangular, the end side of the concave / convex surface cover (the side of the cover) in the direction perpendicular to the nozzle longitudinal direction (the width direction of the gas blowing nozzle) From here, air can flow toward the opening. Furthermore, a gap is formed between the uneven surface cover and the inner wall of the nozzle box in the nozzle width direction. The gas supplied to the gas blowing nozzle flows from the gap to the side of the concave / convex surface cover, flows into the space between the concave / convex surface cover and the opening, and is further blown out from the gas blowing surface toward the work through the opening.
- Patent Document 1 discloses that the space between the opening and the gas blowing surface is a stable chamber or a pressure equalizing chamber that stabilizes the airflow.
- a gas blowing nozzle having an uneven surface cover is also disclosed in Patent Document 2.
- the gas blowing nozzle described in Patent Document 2 has a concavo-convex surface cover having a sinusoidal or trapezoidal cross-sectional shape.
- the properties of processed films produced by blowing gas in a furnace are affected by the thermal history when passing through the interior of the furnace, and in order to obtain a processed film having uniform characteristics in the width direction of the film It is required that the heat exchange between the gas blown from the gas blowing nozzle and the resin film be uniform in the width direction of the resin film. Therefore, the gas blowing nozzle needs a rectifying mechanism that makes the gas blowing speed constant along the width direction of the resin film.
- the gas blowing nozzle to which the gas for blowing is supplied from the film width direction that is, the nozzle longitudinal direction
- the gas is supplied from both sides of the nozzle longitudinal direction and the gas is supplied from only one side of the nozzle longitudinal direction.
- the gas blowing speed at the position opposite to the gas supply side with respect to the nozzle longitudinal direction is A phenomenon occurs that becomes larger than the gas blowing speed on the gas supply side.
- the gas blowing nozzles shown in Patent Documents 1 and 2 can suppress the generation of local turbulence, the gas blowing speed is sufficient in terms of uniformity along the nozzle longitudinal direction with respect to the gas blowing speed. Absent.
- An object of the present invention is to blow a gas onto a resin film, a gas blowing nozzle whose gas blowing speed is uniform along the nozzle longitudinal method, a furnace equipped with such a gas blowing nozzle, and such It is providing the manufacturing method of the processed film which uses a gas blowing nozzle.
- the gas blowing nozzle of the present invention is a gas blowing nozzle used for blowing gas onto the surface of a resin film, and is provided so that the longitudinal direction of the gas blowing nozzle extends in the width direction of the resin film,
- a housing having a gas blowing surface for blowing gas on a side surface facing the film, a gas supply port that is provided at one end of the housing and supplies gas along the nozzle longitudinal direction, and the gas supply port
- One or more pressure equalizing chambers communicating with the gas blowing surface, and at least one pressure equalizing chamber among the one or more pressure equalizing chambers is formed of a partition plate on the surface on the gas blowing surface side.
- a plurality of cylindrical bodies having openings at both ends are arranged along the nozzle longitudinal direction so that the axial direction of each cylindrical body is orthogonal to the nozzle longitudinal direction, Cylindrical body
- the angle ⁇ formed by the partition wall and the wall surface near the gas supply port among the wall surfaces rising from the partition plate is in the range of 55 ° or more and 120 ° or less as the internal angle in the cross-sectional shape of the cylindrical body,
- the surface of the cylindrical body that contacts the partition plate is provided with a gas flow hole that penetrates including the partition plate.
- the furnace of the present invention includes the gas blowing nozzle of the present invention, and performs a heating process by blowing a warming gas from the gas blowing nozzle to the resin film.
- the manufacturing method of the processed film of this invention includes the process of spraying gas with respect to the resin film with the gas blowing nozzle of this invention.
- the gas is preferably a heated gas.
- the difference between the maximum value and the minimum value of the blowing speed with respect to the average blowing speed is preferably within 11%.
- the present invention it is possible to obtain a gas blowing nozzle in which the flow velocity of the gas blown from the gas blowing surface is uniform along the nozzle longitudinal direction.
- the furnace provided with this gas blowing nozzle and performing the heating process with respect to a resin film, the processed film which has a homogeneous characteristic along the width direction of a film can be obtained.
- FIG. 1A and 1B are diagrams showing a general gas blowing nozzle, where FIG. 1A is a perspective view and FIG. 1B is a cross-sectional view.
- FIG. 2 is a cross-sectional view showing a gas blowing nozzle according to an embodiment of the present invention.
- FIG. 3 is a schematic perspective view of the gas blowing nozzle shown in FIG.
- FIG. 4 is a perspective view showing an example of the configuration and arrangement of the cylindrical body.
- FIG. 5 is a perspective view showing an example of the configuration and arrangement of the cylindrical body.
- FIG. 6 is a perspective view showing an example of the configuration and arrangement of the cylindrical body.
- FIG. 7 is a cross-sectional view showing a gas blowing nozzle according to another embodiment of the present invention.
- FIG. 8 is a schematic perspective view of the gas blowing nozzle shown in FIG. (A) to (c) of FIG. 9 are diagrams showing dimensions and angles of each part of the cylindrical body.
- a gas blowing nozzle 10 shown in FIG. 1 is used to blow a gas such as air to the surface of a resin film 50 conveyed in the furnace, for example, in a furnace such as a drying furnace or a tenter oven for stretching. It is what As shown in FIG. 1A, consider an xyz orthogonal coordinate system in which the transport direction of the resin film 50 is the z-axis direction and the width direction of the resin film 50 perpendicular to the film transport direction is the x-axis direction. The y-axis direction is the height direction of the gas blowing nozzle 10.
- the gas blowing nozzle 10 is provided so as to extend in the film width direction, that is, in the x-axis direction over the entire width of the resin film 50 while maintaining a constant interval with respect to the surface of the resin film 50. Therefore, the longitudinal direction of the nozzle is also the x-axis direction.
- the gas blowing nozzle 10 is supplied with gas from one side of the nozzle longitudinal direction (x-axis direction), and as shown as “blowing direction”, the resin film 50 A gas is blown over the entire width of the resin film 50 in a direction perpendicular to the surface of the resin film, that is, in parallel with the y-axis.
- a direction perpendicular to the nozzle longitudinal direction and parallel to the resin film 50 (that is, the z direction) is referred to as a nozzle width direction.
- FIG. 1B shows a cross-sectional configuration of the gas blowing nozzle 10 in a direction parallel to the nozzle longitudinal direction and perpendicular to the surface of the resin film 50.
- the gas blowing nozzle 10 has a housing 11 whose longitudinal direction extends in the width direction of the resin film 50, and a gas supply port 12 is provided at the left end of the housing 11 in the figure.
- An upper pressure equalizing chamber 13 is formed in the housing 11 so as to be connected to the gas supply port 12.
- the height of the upper pressure equalizing chamber 13 decreases as the distance from the gas supply port in the nozzle longitudinal direction increases. That is, it is formed in a tapered shape.
- the surface facing the surface of the resin film 50 is the gas blowing surface 14.
- Three lower pressure equalizing chambers 15 are provided between the upper pressure equalizing chamber 13 and the gas blowing surface 14.
- the gas blowing nozzle 10 provided with three lower pressure equalizing chambers 15 is shown as an example, but the number of lower pressure equalizing chambers 15 is not limited to this.
- these lower pressure equalizing chambers 15 are arranged in the height direction of the gas blowing nozzle 10, and a space between the lower pressure equalizing chambers 15 such as punching metal is provided. It is partitioned by a partition plate 17 that is permeable and breathable.
- the upper pressure equalizing chamber 13 and the lower pressure equalizing chamber 15 are also partitioned by a porous and air-permeable partition plate 16 such as punching metal.
- the partition plates 16 and 17 are both provided in parallel to the surface of the resin film 50, that is, in parallel to the x axis and the z axis.
- the entire outer walls of the upper pressure equalizing chamber 13 and the lower pressure equalizing chamber 15 constitute the casing 11 of the gas blowing nozzle 10 (that is, the nozzle casing), and the gas blowing is performed on the side surface of the casing 11 facing the resin film 50.
- the surface 14 is formed.
- the gas blowing surface 14 from the gas supply port 12 is the upper pressure equalizing chamber 13 and the lower pressure equalizing chamber. 15 to communicate with each other.
- the gas supplied to the gas supply port 12 passes through the partition plate 16 and enters the lower pressure equalization chamber 15 while flowing in the upper pressure equalization chamber 13 in the x direction in the figure, and then gradually passes through the partition plate 17.
- the direction of flow is changed to an air flow perpendicular to the surface of the resin film 50 and blown out from the gas blowing surface 14.
- FIG. 2 is a sectional view of the gas blowing nozzle 20 according to the embodiment of the present invention
- FIG. 3 is a schematic perspective view for explaining the configuration of the gas blowing nozzle 20.
- the structure of the gas blowout nozzle 20 shown in FIGS. 2 and 3 is as follows: the housing 11, the gas supply port 12, the upper pressure equalization chamber 13, the lower pressure equalization chamber 15, and the partition plate 17 are the same as the gas blowout nozzle 10 shown in FIG.
- a partition plate 21 different from that shown in FIG. 1 is used as a partition plate for partitioning the upper pressure equalization chamber 13 and the lower pressure equalization chamber 15, and the upper pressure equalization of the partition plate 21 is the same.
- 1 is different from that shown in FIG. 1 in that a plurality of cylindrical bodies 22 are arranged on the surface on the chamber 13 side.
- the partition plate 21 and the cylindrical body 22 will be described in detail.
- the partition plate 21 constitutes a gas blowing surface 14 side surface in the upper pressure equalizing chamber 13.
- the partition plate 21 is not a porous material such as punching metal but a normal plate member.
- the cylindrical body 22 is disposed in the upper pressure equalizing chamber 13 so that the axial direction of the cylinder is the nozzle width direction, that is, the z direction. If the shape when the cylindrical body 22 is cut along a plane orthogonal to the axial direction as a cylinder is the cross-sectional shape of the cylindrical body 22, the cross-sectional shape of the cylindrical body 22 is, for example, a polygonal shape such as a triangle or a quadrangle. It is.
- the cross-sectional shape of the cylindrical body 22 shown in FIG. 3 is a quadrangle.
- Both ends of the cylindrical body 22 as cylinders are openings 23.
- the length of the cylindrical body 22 (length in the nozzle width direction) is smaller than the length of the gas blowing nozzle 20 in the nozzle width direction. ) And an opening 23 of the cylindrical body 22 is formed, and the gas supplied from the gas supply port 12 may flow into the cylindrical body 22 through the opening 23 from this interval. It can be done.
- a porous and breathable member such as a punching metal or a net (mesh) may be disposed in the opening 23.
- the direction of the surface formed by the opening 23 is not particularly limited, but it is preferable that the surface be parallel to the longitudinal direction of the nozzle and be substantially perpendicular to the partition plate 21.
- FIG. 4 is a view for explaining the internal configuration of the cylindrical body 22, and shows the partition plate 21 and the cylindrical body 22.
- the arrows indicate the flow direction of the gas supplied from the gas supply port 12 to the upper pressure equalizing chamber 13.
- the cylindrical body 22 is depicted in FIG. 4 as having a height greater than that shown in FIG.
- the height of the cylindrical body 22 can be appropriately set as long as it can be accommodated in the upper pressure equalizing chamber 13, even if the cylindrical body 22 as shown in FIG. 3 is used, as shown in FIG. Even if the cylindrical body 22 having a high height is used, the effect of the present invention can be exhibited.
- both the surface in contact with the partition plate 21 of the cylindrical body 22, that is, the bottom surface of the cylindrical body 22 and the partition plate 21 are provided inside the cylindrical body 22, at a position along the longitudinal center line of the gas blowing nozzle 20, both the surface in contact with the partition plate 21 of the cylindrical body 22, that is, the bottom surface of the cylindrical body 22 and the partition plate 21 are provided.
- a gas flow hole 24 is formed so as to penetrate therethrough.
- the position of the gas flow hole 24 does not necessarily have to be along the longitudinal center line of the gas blowing nozzle 20, but is preferably disposed on the longitudinal center line.
- the gas flow hole 24 is formed in a slit shape on the bottom surface of the cylindrical body 22 over the entire length along the nozzle longitudinal direction.
- a through hole is not formed in the partition plate 21 at a position where the cylindrical body 22 is not provided.
- the gas supplied from the gas supply port 12 to the upper pressure equalizing chamber 13 flows into the cylindrical body 22 through the opening 23 of each cylindrical body 22, and the gas circulation hole 24. Then, the air flows into the lower pressure equalizing chamber 15 and blows out from the gas blowing surface 14.
- the gas flow holes 24 are provided for each cylindrical body 22, a plurality of gas flow holes 24 are arranged along the nozzle longitudinal direction as a whole of the partition plate 21. At this time, the gas flow holes 24 are preferably arranged uniformly along the longitudinal direction of the nozzle. Therefore, the cylindrical bodies 22 are arranged on the partition plate 21 while being in contact with each other or mutually in the longitudinal direction of the nozzle. It is preferable to arrange them at equal intervals.
- each cylindrical body 22 has two wall surfaces rising from the partition plate 21, and of these, the inner angle in the cross-sectional shape of the cylindrical body 22 with respect to the wall surface 25 on the gas supply port 12 side.
- the angle ⁇ formed by the wall surface 25 and the partition plate 21 is preferably about 90 °. More specifically, ⁇ is 55 ° or more and 120 ° or less, preferably 60 ° or more and 110 ° or less, and more preferably 75 ° or more and 95 ° or less. According to the study by the present inventors, as is clear from the examples described later, if the angle ⁇ formed by the wall surface 25 and the partition plate 21 is within this angle range, the gas is blown out from the gas blowing surface 14. The gas velocity distribution is uniform over the entire length in the nozzle longitudinal direction.
- the cylindrical body 22 is provided in the upper pressure equalizing chamber 13, but the pressure equalizing chamber in which the cylindrical body 22 is provided is not necessarily limited to the upper pressure equalizing chamber 13.
- the rectification effect by providing the cylindrical body 22 is most expected when the cylindrical body 22 is provided in the pressure equalizing chamber adjacent to the gas supply port 12, and therefore the upper pressure equalizing chamber 13 is cylindrical. It is preferable to arrange the body 22.
- the cylindrical body 22 is provided in the upper pressure equalizing chamber 13, it is not always necessary to provide the lower pressure equalizing chamber 15 in the gas blowing nozzle 20, and the partition plate 21 itself serves as the gas blowing surface 14 and flows out from the gas circulation hole 24. A configuration in which gas is blown directly onto the resin film 50 is also possible.
- FIG. 5 shows another example of the configuration and arrangement of the cylindrical body 22.
- cylindrical bodies 22 having a quadrangular cross-sectional shape are arranged on the partition plate 21 in the nozzle longitudinal direction so as to contact each other.
- the gas flow hole 24 is formed in a circular shape at substantially the center of the bottom surface of the cylindrical body 22, and the diameter of the gas flow hole 24 is smaller than the length along the nozzle longitudinal direction of the bottom surface of the cylindrical body 22. Yes. Also in the cylindrical body 22 shown in FIG.
- the angle ⁇ between the wall surface 25 that rises from the partition plate 21 on the gas supply port 12 side and the partition plate 21 is 55 ° or more and 120 ° or less.
- the angle is preferably from 60 ° to 110 °, more preferably from 75 ° to 95 °.
- FIG. 6 shows still another example of the configuration and arrangement of the cylindrical body 22.
- the configuration shown in FIG. 6 is obtained by changing the cross-sectional shape of the cylindrical body 22 from a square to a triangle in the configuration shown in FIG.
- the angle ⁇ between the wall surface 25 that rises from the partition plate 21 on the gas supply port 12 side and the partition plate 21 is 55 ° or more and 120 ° or less.
- the angle is preferably from 60 ° to 110 °, more preferably from 75 ° to 95 °.
- the upper pressure equalizing chamber 13 is formed in a tapered shape whose height decreases along the nozzle longitudinal direction when viewed from the gas supply port 12 side.
- the shape of the upper pressure equalizing chamber is not limited to a tapered shape.
- a gas blowing nozzle 30 according to another embodiment of the present invention shown in FIG. 7 has the same configuration as that of the gas blowing nozzle 20 shown in FIGS. 2 and 3, but has a constant height along the nozzle longitudinal direction. It differs from the gas blowing nozzle 20 shown in FIGS. 2 and 3 in that the upper pressure equalizing chamber 32 is provided. Further, similarly to those shown in FIG. 5, adjacent cylindrical bodies 22 are provided so as to contact each other.
- FIG. 8 is a schematic perspective view for explaining the configuration of the gas blowing nozzle 30 shown in FIG.
- the shape of the gas flow hole 24 is not particularly limited as long as it communicates from the upper pressure equalizing chamber 13 to the lower pressure equalizing chamber 15 or the gas blowing surface 14.
- a slit-like one extending in the longitudinal direction of the nozzle as shown in FIG. 4 or 6 is preferable.
- the opening area of the gas circulation hole 24 per cylindrical body 22 is S 1 , and the surface of the cylindrical body 22 that contacts the partition plate 21 except the surface where the wall surfaces 22 and 25 are in contact with the partition plate.
- the aperture ratio S 1 / S 2 is preferably 0.85 or less.
- the difference between the maximum value and the minimum value of the blowing speed when the distribution of the gas blowing speed along the longitudinal direction of the nozzle is determined is approximately 14 with respect to the average blowing speed. % Or less, preferably 11% or less, but depending on the type of resin film 50 to which the gas is blown, the difference between the maximum value and the minimum value of the blowing speed may be larger than this. It is not limited.
- the gas blowing speed from the gas blowing surface 14 is preferably in the range of more than 0 m / s and not more than 20 m / s, and more preferably in the range of more than 0 m / s and not more than 7 m / s. .
- the gas blowing nozzles 20 and 30 according to the present invention are provided, for example, in a drying furnace or a tenter oven, and are used to blow a gas such as air or nitrogen onto the surface of the resin film 50 when manufacturing a processed film.
- the gas blowing nozzles 20 and 30 are used when a coating solution is applied to the resin film 50 and then the coating film is dried by blowing air onto the resin film 50 in a drying furnace.
- Example 1 In the gas blowing nozzle 20 having the configuration shown in FIGS. 2 and 3, the cylindrical body 22 having a triangular cross section as shown in FIG. 6 was analyzed by simulation. In the analysis, steady calculation was performed using “STAR-CCM (ver. 11.04)” (manufactured by IDAJ), which is a commercially available general-purpose thermal fluid analysis software. The k- ⁇ turbulence model was used for the turbulent flow, and the wall law was used for the turbulent boundary layer near the wall. The above software analyzes the Navier-Stokes equations, which are fluid equations of motion, by the finite volume method.
- any thermal fluid analysis software may be used as long as the same analysis can be performed.
- An analysis space simulating the flow path inside the nozzle housing is set, the length in the nozzle longitudinal direction of the upper pressure equalizing chamber 13 is set to 1530 mm, the length in the nozzle width direction is set to 100 mm, and the height of the gas supply port 12 is set. 200 mm.
- Boundary conditions were set at the gas supply port 12 so that dry air at normal temperature (300 K) flows into the analysis space at a flow rate of 3.0 m / s.
- the gas blowing surface 14 was a pressure boundary, and atmospheric pressure (0.1 MPa) was set as the boundary condition.
- the cylindrical body 22 is continuously arranged along the nozzle longitudinal direction, and the distance L2 between the cylindrical bodies adjacent in the nozzle longitudinal direction is set to 0 mm as shown in FIG.
- the cylindrical body was arrange
- internal angles formed by two wall surfaces rising from the partition plate 21 in the cylindrical body 22 and the partition plate 21 are ⁇ and ⁇ , respectively.
- the cylindrical body 22 has two wall surfaces rising from the partition plate 21, but the angle ⁇ is an inner angle formed by the wall surface 25 on the gas supply port side and the partition plate, and the angle ⁇ is the wall surface on the side not on the gas supply port side.
- each cylindrical body 22 is an internal angle formed by the partition plate.
- the length L1 along the nozzle longitudinal direction of each cylindrical body 22 was set to 15 mm.
- the thickness of the two wall surfaces 22 and 25 was set to zero. Then, the distribution of the velocity of the gas blown out from the gas blowing surface when the angle ⁇ and the angle ⁇ were changed was determined along the nozzle longitudinal direction. And the difference R was obtained by dividing the difference between the maximum value and the minimum value of the gas velocity thus obtained by the average blowing speed. A smaller speed variation R is a better result.
- the angle ⁇ is 55 ° or more and 120 ° or less, preferably 60 ° or more and 110 ° or less, and more preferably 75 ° or more and 95 ° or less.
- Example 2 In the gas blowing nozzle 20 having the configuration shown in FIGS. 2 and 3, the cylindrical body 22 having a triangular cross section as shown in FIG. 6 was analyzed by simulation in the same manner as in Example 1. The angle ⁇ , the angle ⁇ , and the length L1 are defined in the same manner as in Example 1. And as shown in FIG.9 (b), the distance R2 between the cylindrical bodies adjacent to a nozzle longitudinal direction was changed, the dispersion
- Example 3 Analysis by the same simulation as in Example 1 was performed, and the opening ratio of the gas flow holes in the bottom surface of the cylindrical body 22 was examined.
- the speed variation R when Ws was changed was determined in the same manner as in Example 1 and determined.
- Ws / W is the area S 2 of the bottom surface of the cylindrical body 22 per one cylindrical body 22. This is the ratio (S 1 / S 2 ) of the area S 1 of the gas flow hole 24 to (the sum of the areas of the opening and the non-opening at the bottom), that is, the opening ratio.
- Table 3 The results are shown in Table 3.
- the aperture ratio is 1.0, that is, even when the entire bottom surface of the cylindrical body 22 is the gas flow hole 24, the variation R of the flow velocity is 10%, and the result is “good”. It was found that when the aperture ratio was 0.85 or less, R was 7% or less and the result was “excellent”. That is, it was found that the aperture ratio is preferably 0.85 or less.
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Abstract
Description
本発明の加工フィルムの製造方法は、本発明の気体吹出しノズルにより樹脂フィルムに対して気体を吹き付ける工程を含む。
本発明の加工フィルムの製造方法は、ノズル長手方向に沿った前記気体の吹出し速度分布において、平均吹出し速度に対する吹出し速度の最大値と最小値の差は11%以内であることが好ましい。
(1)表面粗さがフィルム幅方向において均一な加工フィルムが得られる、
(2)厚さがフィルム幅方向において均一な加工フィルムが得られる、
(3)微多孔が形成されるフィルムの場合、フィルム幅方向に均一な微多孔が形成された加工フィルムが得られる、
(4)フィルム搬送時のばたつきが低減され、フィルムの破れの発生が低減されて歩留まりが向上する、
(5)乾燥した塗膜と樹脂フィルムとの密着性がフィルム幅方向において均一な加工フィルムが得られる、
(6)外観不良がない加工フィルムが得られる、
などの利点の少なくとも1つが得られる。
[実施例1]
図2及び図3に示す構成の気体吹出しノズル20において、筒状体22として図6に示すような断面形状を三角形としたものについて、シミュレーションによる解析を行なった。解析では、市販の汎用熱流体解析ソフトウェアである「STAR-CCM(ver.11.04)」(株式会社IDAJ製)を用い、定常計算を行った。乱流の取り扱いにはk-ε乱流モデルを用い、壁近傍の乱流境界層の取り扱いには壁法則を用いた。上記のソフトウェアは、流体の運動方程式であるナヴィエ・ストークス方程式を有限体積法により解析するものである。もちろん、同様の解析ができるものであればどのような熱流体解析ソフトウェアを用いてもよい。ノズル筐体内部の流路を模擬した解析空間を設定し、上部均圧室13のノズル長手方向の長さを1530mmとし、ノズル幅方向の長さを100mmとし、気体供給口12の高さを200mmとした。気体供給口12には、解析空間内に常温(300K)の乾燥空気が3.0m/sの流速で流入するように境界条件を設定した。また、気体吹出し面14は圧力境界とし、境界条件に大気圧(0.1MPa)を設定した。
図2及び図3に示す構成の気体吹出しノズル20において、筒状体22として図6に示すような断面形状を三角形としたものについて、実施例1と同様にシミュレーションによる解析を行なった。角θ、角α及び長さL1については実施例1と同様に定義した。そして、図9(b)に示すように、ノズル長手方向に隣接する筒状体の相互間の距離L2を変化させて、実施例1と同様にばらつきRを求め、評価を行なった。結果を表2に示す。
実施例1と同様のシミュレーションによる解析を行ない、筒状体22の底面における気体流通孔の開口率について検討した。実施例1で用いた気体吹出しノズル(ただし、θ=90°、α=53.1°、L1=15mm)において、図9(c)に示すように、ノズル幅方向での筒状体22の幅Wを60mmとし、スリット状の開口として形成される気体流通孔24の幅をWsとした。Wsを変えたときの速度のばらつきRを実施例1と同様に求めて判定を行なった。気体流通孔24は、ノズル長手方向には筒状体22の底面の全長にわたって形成されているので、Ws/Wは、筒状体22一つ当たりにおける、筒状体22の底面の面積S2(底面での開口部と非開口部の面積の和)に対する気体流通孔24の面積S1の比率(S1/S2)、すなわち開口率ということになる。結果を表3に示す。
11 筐体
12 気体供給口
13、32 上部均圧室
14 気体吹出し面
15 下部均圧室
16、17、21 仕切り板
22 筒状体
23 開口
24 気体流通孔
25 壁面
Claims (11)
- 樹脂フィルムの表面に気体を吹き付けるために用いられる気体吹出しノズルであって、
前記気体吹出しノズルの長手方向が前記樹脂フィルムの幅方向に延びるように設けられ、前記樹脂フィルムに対向する側面に気体を吹き出す気体吹出し面を有する筐体と、
前記筐体の一方の端部に設けられ、ノズル長手方向に沿って気体を供給する気体供給口と、
前記気体供給口から前記気体吹出し面まで連通する1以上の均圧室と、
を有し、
前記1以上の均圧室の内の少なくとも1つの均圧室は、前記気体吹出し面の側の面が仕切り板で構成され、前記仕切り板の上には、両端に開口を有する複数の筒状体が、各筒状体の軸方向が前記ノズル長手方向に直交するように前記ノズル長手方向に沿って複数配置され、
前記筒状体は、前記仕切り板から立ち上がる壁面のうち前記気体供給口に近い側の壁面と前記仕切り板とがなす角θが、前記筒状体の断面形状における内角として55°以上120°以下の範囲にあり、
前記筒状体の前記仕切り板に接する面には、前記仕切り板を含めて貫通する気体流通孔が設けられている、気体吹出しノズル。 - 前記角θが75°以上95°以下の範囲にある、請求項1に記載の気体吹出しノズル。
- 前記筒状体が配置される均圧室は、前記気体供給口に隣接する均圧室である、請求項1または2に記載の気体吹出しノズル。
- 前記筒状体一つあたりにおける、前記気体流通孔の開口面積をS1、前記筒状体の、前記仕切り板から立ち上がる前記壁面が仕切り板に接している面を除いて、仕切り板に接する面の面積をS2としたとき、開口率S1/S2が0.85以下である、請求項1乃至3のいずれか1項に記載の気体吹出しノズル。
- 前記気体流通孔は、前記ノズル長手方向に延びるスリットである、請求項1乃至4のいずれか1項に記載の気体吹出しノズル。
- 前記筒状体の前記開口の各々が形成する面は、前記ノズル長手方向に平行、かつ、前記仕切り板に略垂直な面である、請求項1乃至5のいずれか1項に記載の気体吹出しノズル。
- 前記筒状体の前記仕切り板に接する面におけるノズル長手方向に沿う長さをL1とし、ノズル長手方向に隣接する前記筒状体の相互間の距離をL2としたとき、L2/L1が1.0以下である、請求項1乃至6のいずれか1項に記載の気体吹出しノズル。
- 前記ノズル長手方向に沿った前記気体の吹出し速度分布において、平均吹出し速度に対する吹出し速度の最大値と最小値の差は11%以内である、請求項1乃至7のいずれか1項に記載の気体吹出しノズル。
- 請求項1乃至8のいずれか1項に記載の気体吹出しノズルを備え、
前記気体吹出しノズルから樹脂フィルムに対して加温気体を吹き付けて加温処理を行なう炉。 - 請求項1乃至8のいずれか1項に記載の気体吹出しノズルにより樹脂フィルムの表面に気体を吹き付ける工程を含む、加工フィルムの製造方法。
- 前記気体が加温気体である、請求項10に記載の加工フィルムの製造方法。
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