WO2006095669A1 - 塗布装置、塗布方法および塗膜を有するウェブの製造方法 - Google Patents
塗布装置、塗布方法および塗膜を有するウェブの製造方法 Download PDFInfo
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- WO2006095669A1 WO2006095669A1 PCT/JP2006/304237 JP2006304237W WO2006095669A1 WO 2006095669 A1 WO2006095669 A1 WO 2006095669A1 JP 2006304237 W JP2006304237 W JP 2006304237W WO 2006095669 A1 WO2006095669 A1 WO 2006095669A1
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- Prior art keywords
- coating
- coating liquid
- web
- liquid
- bar
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05C—APPARATUS FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05C1/00—Apparatus in which liquid or other fluent material is applied to the surface of the work by contact with a member carrying the liquid or other fluent material, e.g. a porous member loaded with a liquid to be applied as a coating
- B05C1/04—Apparatus in which liquid or other fluent material is applied to the surface of the work by contact with a member carrying the liquid or other fluent material, e.g. a porous member loaded with a liquid to be applied as a coating for applying liquid or other fluent material to work of indefinite length
- B05C1/08—Apparatus in which liquid or other fluent material is applied to the surface of the work by contact with a member carrying the liquid or other fluent material, e.g. a porous member loaded with a liquid to be applied as a coating for applying liquid or other fluent material to work of indefinite length using a roller or other rotating member which contacts the work along a generating line
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05C—APPARATUS FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05C11/00—Component parts, details or accessories not specifically provided for in groups B05C1/00 - B05C9/00
- B05C11/02—Apparatus for spreading or distributing liquids or other fluent materials already applied to a surface ; Controlling means therefor; Control of the thickness of a coating by spreading or distributing liquids or other fluent materials already applied to the coated surface
- B05C11/023—Apparatus for spreading or distributing liquids or other fluent materials already applied to a surface
- B05C11/025—Apparatus for spreading or distributing liquids or other fluent materials already applied to a surface with an essentially cylindrical body, e.g. roll or rod
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05C—APPARATUS FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05C11/00—Component parts, details or accessories not specifically provided for in groups B05C1/00 - B05C9/00
- B05C11/02—Apparatus for spreading or distributing liquids or other fluent materials already applied to a surface ; Controlling means therefor; Control of the thickness of a coating by spreading or distributing liquids or other fluent materials already applied to the coated surface
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05C—APPARATUS FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05C5/00—Apparatus in which liquid or other fluent material is projected, poured or allowed to flow on to the surface of the work
- B05C5/02—Apparatus in which liquid or other fluent material is projected, poured or allowed to flow on to the surface of the work the liquid or other fluent material being discharged through an outlet orifice by pressure, e.g. from an outlet device in contact or almost in contact, with the work
- B05C5/0254—Coating heads with slot-shaped outlet
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D1/00—Processes for applying liquids or other fluent materials
- B05D1/28—Processes for applying liquids or other fluent materials performed by transfer from the surfaces of elements carrying the liquid or other fluent material, e.g. brushes, pads, rollers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D7/00—Processes, other than flocking, specially adapted for applying liquids or other fluent materials to particular surfaces or for applying particular liquids or other fluent materials
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05B—SPRAYING APPARATUS; ATOMISING APPARATUS; NOZZLES
- B05B15/00—Details of spraying plant or spraying apparatus not otherwise provided for; Accessories
- B05B15/50—Arrangements for cleaning; Arrangements for preventing deposits, drying-out or blockage; Arrangements for detecting improper discharge caused by the presence of foreign matter
- B05B15/55—Arrangements for cleaning; Arrangements for preventing deposits, drying-out or blockage; Arrangements for detecting improper discharge caused by the presence of foreign matter using cleaning fluids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D1/00—Processes for applying liquids or other fluent materials
- B05D1/40—Distributing applied liquids or other fluent materials by members moving relatively to surface
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B05—SPRAYING OR ATOMISING IN GENERAL; APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D—PROCESSES FOR APPLYING FLUENT MATERIALS TO SURFACES, IN GENERAL
- B05D2252/00—Sheets
- B05D2252/02—Sheets of indefinite length
Definitions
- Coating apparatus Coating apparatus, coating method, and method for producing web having coating film
- the present invention relates to a coating apparatus and a coating method for coating a coating liquid on a top surface of a running web such as a film with a coating bar.
- the present invention also relates to a method for producing a web having a coating film using the coating apparatus or the coating method.
- the present invention provides a coating defect on the web surface, such as a supply line or bubble streak appearing on the web surface on which the coating liquid is applied, and a coating liquid thickness that reduces coating thickness unevenness.
- An apparatus and a coating method are provided.
- the coating liquid 103 is supplied from the die 102 as the coating liquid supply means to the upper surface of the running web 101, and four rollers are provided on the downstream side of the die 102.
- 104 Measuring and smoothing the coating thickness of the coating liquid supplied to the upper surface of the web 101 with a metalling bar 105 as a coating bar supported in a freely rotating manner (one pair at each end in the width direction).
- the power of the coating device is known.
- a coating liquid supply line 106 and a bubble line 107 resulting from an aerodynamic force S mixed from the outside may be generated as shown in FIG.
- These supply stripe 106 and bubble stripe 107 are regarded as application defects.
- the coating defect is caused by the air at the position indicated by the arrow A between the supplied coating liquid 103 and the web 101. It is thought that this occurs because it enters the web 101 and is not properly excluded at the part 105 of the cutting bar.
- Patent Document 1 discloses a coating liquid coating method on the premise that a coating liquid having a relatively low viscosity is used.
- the coating liquid is supplied onto a coating bar installed in the vicinity of the coating bar to form a puddle at the contact portion between the coating bar and the web, and the coating liquid is applied to the surface of the web. Made up of.
- the present inventors have received a request for development of a technique for applying a high-viscosity coating liquid having a viscosity of 0.1 lPa's (lOOcp) or more to the surface of a web.
- Use coating method Tried to do is not eliminate the phenomenon that supply streaks occur in the coating film applied to the web surface.
- Patent Document 1 Japanese Patent No. 2805177
- Non-Patent Document 1 Yoshinobu Katagiri, Theory of Die Coater's Commentary, Past of Coating Hardware Technology ⁇ Learn the Future from Present—Japan, Processing Technology Research Group, March 25, 2002, p 399
- An object of the present invention is to solve the above-described problems, to prevent the occurrence of supply streaks that are likely to occur during the supply of coating liquid, and the generation of bubble streaks due to air stagnation. It is an object of the present invention to provide a coating apparatus and a coating method that can reduce coating thickness unevenness caused by the above.
- a coating apparatus of the present invention for achieving the above object is as follows.
- a coating apparatus that applies a coating liquid to an upper surface of a running web using a coating bar, A coating apparatus having a coating liquid supply means for directly supplying a coating liquid to a liquid pool formation site in the vicinity of the upstream side of the contact portion between the coating bar and the web.
- this coating apparatus is referred to as a first coating apparatus.
- the “liquid pool” is a coating liquid that is formed around a region sandwiched between the web and the coating bar on the upstream side of the coating EVA from the contact portion between the coating bar and the web during coating. This is a pool. Needless to say, the coating liquid remaining thinly on the surface of the coating bar or on the surface of the web during continuous application is not a liquid pool here. This is because these thin coating solutions move following the movement of the coating bar and web surface as they are, and are not accumulated coating solutions.
- a puddle formation site The vicinity of the upstream side of the coating bar where the puddle is to be formed.
- directly supplying a coating liquid to a puddle formation site means supplying a coating liquid discharged from a coating liquid supply unit, for example, a nozzle or a die, to the puddle formation site. This means that the supplied coating liquid is brought into direct contact with the liquid pool before the coating liquid contacts the web and the coating bar.
- coating bar refers to the application of a conventionally applied coating liquid such as a rod, a wire bar in which a wire is wound around a rod, and a bar with a groove in which a rod is cut. This is the bar used in The coating bar is usually allowed to rotate in the same direction as the web travel direction, but it can also be rotated in the opposite direction of the web travel direction.
- a coating apparatus of the present invention for achieving the above object is as follows.
- a coating apparatus that applies a coating liquid to an upper surface of a running web by a coating bar, and supplies the coating liquid to the upper surface of the web at a position upstream from the position of the coating bar.
- a coating apparatus having a coating liquid supply means for performing the coating liquid supply, and the coating liquid supply means has a smooth portion where the coating liquid flows down in a state where the upper part is opened.
- this coating apparatus is referred to as a second coating apparatus.
- the “open state” means a state in which the coating liquid flows down on the object, and a state in which a substance other than gas is in contact with the vertical upper surface of the coating liquid.
- the “smooth part” defines the lower surface of the flow path through which the coating liquid flows when the coating liquid is supplied with the coating liquid supply means open. On the surface Therefore, the surface roughness (maximum height Ry) of the portion where the coating liquid flows is 100 or less and the flatness is 0.
- the surface roughness is measured using an ultra-deep surface shape measuring microscope (VK8500, manufactured by Keyence Corporation) from the direction of arrow X with the angle ⁇ shown in Fig. 11 being 90 degrees, that is, in a smooth region.
- VK8500 ultra-deep surface shape measuring microscope
- the flatness is measured with a high-precision three-dimensional shape measurement system (XYZAXGC60 manufactured by Tokyo Seimitsu Co., Ltd.)
- an inclination angle of the smooth portion with respect to a horizontal direction is 10 to 60 degrees, and a distance through which the coating liquid flows in a state where an upper portion is opened is 10 to 200 mm. It is preferable.
- inclination angle with respect to the horizontal direction refers to an angle formed by a horizontal line and a surface of a smooth portion, and is indicated by an inclination angle ⁇ in FIG. If the inclination angle ⁇ is less than 10 degrees, both ends of the smooth part may leak when the coating liquid flows down, dripping on the web, and this may cause supply streaks. In addition, when the inclination angle ⁇ exceeds 60 degrees, the effect of the coating liquid becoming flat on a smooth part may be insufficient.
- the coating liquid supply means is positioned so as to directly supply the coating liquid to a puddle formation site in the vicinity of the upstream side of the contact portion between the coating bar and the web. Is preferred.
- the tip force on the coating bar side of the smooth portion has a concave shape in which both ends extend downward from the center in the width direction of the web. It is preferable to have it.
- FIGS. 12A and 12B show an embodiment of the coating apparatus of the present invention.
- a die 110 as a coating liquid supply means has a smooth portion 111 at the tip. A part of the front end portion of the smooth portion 111 is located in contact with the liquid pool 108.
- the coating liquid is supplied to the liquid pool 108, and the coating liquid is weighed or smoothed by, for example, the metalling bar 105 provided on the downstream side, which is supported by two rollers 104 on the left and right sides.
- a coating liquid having a desired thickness is applied to the upper surface of the web 101 running in the direction indicated by the arrow 12X.
- the shape of the outer surface of the liquid pool 108 often bulges outward at the center in the width direction of the web 101, and then bulges toward both ends from there.
- the tip of the smooth part 111 is brought into contact with the liquid pool 108 and the coating liquid is supplied, both ends of the part of the smooth part 111 in contact with the liquid pool 108 as shown in FIG. 12B.
- a streak 109 may occur at a position corresponding to. In this case, the product width that can be collected as a coated web product is narrowed.
- FIGS. 13A and 13B This problem can be solved by setting the coating apparatus 11 to the embodiment shown in FIGS. 13A and 13B. That is, in FIGS. 13A and 13B, the shape of the tip 1 l ie of the smooth portion 11 la is substantially aligned with the outer shape of the liquid pool 108a, and particularly at both ends, the shape is matched to the outer shape of the liquid pool 108a. As shown to 13B, it also becomes the force which makes most of the full width of the front-end
- the downward concave shape refers to a shape in which the shape of the tip of a smooth portion extends downward from the center in the width direction of the web.
- the shape thereof preferably corresponds to the shape of the outer surface of the liquid pool 108a, but may not be an arc, and may be formed by a series of at least two straight lines.
- the coating liquid supply means has a means power for continuously supplying the coating liquid. That is, it is preferable that the coating liquid supplied from the coating liquid supply means is supplied in a continuously connected state without interruption. This is because, as will be described later, when the coating liquid is intermittently supplied onto the liquid pool, supply stripes are likely to occur.
- the coating liquid supply means has a distance of 80 mm or less until the coating liquid supplied from the coating liquid supply means falls into the liquid pool. It is preferable to have a means for putting in. If the coating liquid leaves the end of the coating liquid supply means, falls into the puddle and reaches the puddle, and the distance to reach the puddle is too large, the liquid puddle becomes unstable due to the pressure fluctuation of the coating liquid that occurs at the time of dropping. Because there are cases. If the puddle becomes unstable, application defects are likely to occur.
- the “distance until the coating liquid falls into the liquid pool” means that the coating liquid away from the coating liquid supply means comes into contact with the liquid pool while dropping in the gas. This is the vertical distance of movement.
- FIG. 1 shows a schematic side view of the first coating apparatus
- FIG. 11 shows a schematic side view of the second coating apparatus.
- the coating liquid 4 discharged from the die 3 as a coating liquid supply means is directly supplied to the pool 6 and is applied by the coating bar 1. It is applied to the upper surface of the web 2.
- the coating liquid supply means comprises a die 3a and a smooth portion 20 coupled to the tip thereof, and is discharged from the die 3a and flows down the upper surface of the smooth portion 20.
- the liquid 4a is directly supplied to the liquid pool 6a, and is applied to the upper surface of the running web 2a by the liquid application force la of the liquid pool 6a.
- the “distance until the coating liquid falls into the liquid pool” refers to the vertical distance H from the lower tip of the die 3 to the upper tip of the liquid pool 6, and in FIG.
- the lower tip force of the smooth part 20 is also the vertical distance Ha to the upper tip of the liquid pool 6a.
- FIG. 17 shows a schematic side view of another aspect of the second coating apparatus.
- the coating liquid supply means is composed of a die 110b and a smooth part 11 lc coupled to the tip thereof, and the coating liquid 4b discharged from the die 110b and flowing down the upper surface of the smooth part 11 lc is The liquid is applied directly onto the upper surface of the running web 101b by a coating bar (metal ring bar) 105b that is directly supplied to the liquid pool 108b and is rotatably supported by the coating force roller 104b of the liquid pool 108b.
- the tip of the smooth portion 111c of the coating liquid supply means is inserted into the liquid pool 108b.
- the tip of the coating liquid supply means is inserted into the liquid pool! In this mode, the “distance until the coating liquid falls into the liquid pool” is 0 (zero ).
- the coating liquid supply means includes It is preferable that a moving means that can move independently of the coating bar is provided. By enabling the coating liquid supply means to move independently with respect to the coating bar, for example, when the coating liquid being supplied is shaken by static electricity of the web, the coating liquid is controlled so as to suppress the shaking of the coating liquid. It is possible to appropriately adjust the relative position of the coating liquid supply means with respect to the bar. In addition, when the application is completed, the coating liquid supply means can be quickly retracted to an appropriate position.
- the coating liquid supply means be movable with respect to the coating bar within a range of 0.1 to 500 mm during coating of the coating liquid.
- the “distance” of the coating liquid supply means to the coating bar means the shortest distance from the surface of the coating bar to the coating liquid supply means. This distance is indicated by distance L in FIG. 1 and distance La in FIG.
- the “distance” means the smooth part at each position in the web width direction. The shortest distance to the surface of the coating bar.
- the coating liquid supply means By making the coating liquid supply means movable in such a range, the relative position of the coating liquid supply means with respect to the coating bar described above can be adjusted, and the coating liquid supply means can be retracted at the end of coating. Can be done easily.
- the first coating device or the second coating device has a liquid receiver capable of receiving a coating liquid from the coating liquid supply means.
- a liquid receiver capable of receiving a coating liquid from the coating liquid supply means.
- the coating method of the present invention for achieving the above object is as follows.
- a coating method in which a coating liquid having a viscosity of 0.1 to 3. OPa's (100 to 30 OOcp) is applied to the upper surface of a running web by a coating bar, the coating bar and the A coating method in which the coating liquid is directly supplied by a coating liquid supply means to a liquid pool formed on the upstream side of the web contact portion.
- This coating method is characterized in that the coating liquid supplied from the coating liquid supply means first comes into contact with the liquid pool and then contacts the coating bar or web through the liquid pool. This feature point is indicated by the expression that the coating liquid is directly supplied to the liquid pool.
- this coating method is referred to as a first coating method.
- the viscosity is measured using a rheometer (RC20 manufactured by Rheotech Co., Ltd.). SZ8803 standard [Do this!
- “directly supplying the coating liquid to the liquid pool” means that the coating liquid discharged from a coating liquid supply means, for example, a nozzle or a die, is applied to the web and the coating bar. Direct contact with the puddle before contact.
- a coating liquid supply means for example, a nozzle or a die
- the coating method of the present invention for achieving the above object is as follows.
- this coating method is referred to as a second coating method.
- an inclination angle of the smooth portion with respect to the horizontal direction is 10 to 60 degrees, and a distance in which the coating liquid flows in an open state is 10 to 200 mm. I prefer to be! /
- the coating liquid is directly supplied to the liquid pool formed at the contact portion between the coating bar and the web by the coating liquid supply means.
- the end of the smooth portion has a shape in which both ends extend downward from the center in the width direction of the web corresponding to the outline of the liquid pool. Is preferred.
- the coating liquid supply means continuously supply the coating liquid without interruption.
- the distance from which the coating liquid supplied from the coating liquid supply unit falls into a liquid pool is 80 mm or less.
- the web on which the coating liquid is applied and the coating film is formed on the surface is stretched and dried. These stretching and drying are performed by stretching after stretching, stretching after drying, or simultaneously stretching and drying.
- the web production method of the present invention for achieving the above object is as follows. [0054] The polymer is extruded by an extruder, and the polymer is formed into a sheet shape to form a web. The first application method is! / Is the second application method, and the coating liquid is applied to the web. A method for producing a web having a coating film on a surface formed by coating on top and forming a coating film.
- the above-described coating defects due to the conventional coating liquid supply do not occur. Moreover, coating thickness unevenness can be reduced.
- the coating liquid supply means can be adjusted independently with respect to the coating bar, the coating liquid can be accurately applied to the target position with respect to the liquid pool regardless of the electrostatic charge state of the web. Liquid can be supplied. In addition, even if the size of the liquid puddle changes, it is possible to respond to various varieties and coating widths. Furthermore, when the application is finished, it can be finished quickly. For example, by separating the coating liquid supply means from the web force and then separating the coating bar, even if the coating liquid drops from the coating liquid supply means, it is smoothed by the coating bar. It prevents contamination of the device due to insufficient drying of the membrane.
- FIG. 1 is a schematic side view of an example of a coating apparatus of the present invention.
- FIG. 2 is an enlarged side view of the vicinity of a liquid pool in the apparatus shown in FIG.
- FIG. 3 is an explanatory view showing a state where a coating liquid is dropped in the state shown in FIG. 2.
- FIG. 4 is an explanatory diagram for explaining the effectiveness of position adjustment of the coating liquid supply means.
- FIG. 4A on the left side of FIG. 4 is a schematic side view showing a state in which the coating liquid supply means is in the initial position;
- FIG. 4B on the right side of FIG. 4 is a schematic side view showing a state where the coating liquid supply means has moved from the state of FIG.
- FIG. 5 is a schematic side view for explaining a defect occurrence state when the die and the coating bar do not move independently.
- FIG. 6 is a schematic side view for explaining a state in which a failure is prevented when the die and the coating bar can move independently.
- FIG. 7 is a schematic side view of a conventional general metering bar type coating apparatus.
- FIG. 8 is a schematic plan view showing a state of occurrence of coating defects in the apparatus of FIG. [9]
- FIG. 9 is a schematic side view for explaining the state of air stagnation in the conventional apparatus.
- ⁇ 10 A schematic side view for explaining the state of air stagnation in another conventional apparatus.
- ⁇ 11 A schematic side view of another example of the coating apparatus of the present invention.
- FIG. 12A is a schematic plan view of an example of a coating liquid supply unit in the coating apparatus shown in FIG.
- FIG. 12B is a schematic plan view for explaining the relationship between the coating liquid supply means and the liquid pool shown in FIG. 12A.
- FIG. 13A is a schematic plan view of another example of the coating liquid supply means in the coating apparatus shown in FIG.
- FIG. 13B is a schematic plan view for explaining the relationship between the coating liquid supply means and the liquid pool shown in FIG. 13A.
- FIG. 14 is a schematic front view of the coating apparatus of the present invention shown in FIG. 1 as viewed from the direction of arrow Y shown in FIG.
- FIG. 16 is an enlarged schematic front view illustrating another example of the relationship between the coating bar, the coating liquid, and the web.
- FIG. 17 is a schematic side view illustrating a state where the tip of the smooth portion of the coating liquid supply means is inserted into the liquid pool in the coating apparatus of the present invention shown in FIG. [18]
- FIG. 18 is a process schematic diagram illustrating one embodiment of a web manufacturing process.
- FIG. 19 is a process schematic diagram for explaining an embodiment of a web manufacturing process in which a coating liquid coating process is provided in the web manufacturing process shown in FIG. 18.
- FIG. 20 is a schematic plan view for explaining a coating state of the coating liquid in the width direction of the web when a coated web is manufactured using the coating apparatus of the present invention shown in FIG.
- a coating apparatus 10 includes a coating bar 1, a web conveying device (not shown) for running the web 2 below the coating bar 1, and an upstream side of the coating bar 1.
- the liquid is provided with a liquid supply means (die) 3 provided so that the liquid is directly supplied to the liquid pool 6 formed in contact with the traveling web 2 and the coating bar 1.
- the coating liquid 4 is directly supplied to the liquid pool 6 from the die 3 as a coating liquid supply means.
- the die 3 can be moved between a coating liquid supply position indicated by a solid line and a retracted position indicated by a broken line by a moving mechanism 5. At the position directly above the contact area between coating bar 1 and web 2, there is a force that forms liquid puddle 6. Before contact with coating bar 1 and web 2, coating liquid 4 discharged from die 3 Directly supplied to puddle 6.
- the coating solution 4 is supplied into the die 3 through a pump 7 and a filter 8 from a suitable coating solution tank (not shown).
- a liquid receiver 9 is provided below the retreat position of the die 3. The liquid receiver 9 receives the coating liquid dripping from the die 3.
- FIG. 14 is a schematic front view of the coating apparatus 10 of the present invention shown in FIG. 1 when viewed in the direction of arrow Y shown in FIG. 15 and 16 are enlarged front views of a portion C surrounded by a dotted line in FIG.
- the coating bar include a rod, a wire bar obtained by winding a wire around the rod, and a bar with a groove obtained by cutting a groove in the rod. Paint EVA shown in Figure 14 One is in the form of a wire bar.
- the coating bar 1 has a groove formed on the surface thereof by a wire wound around the surface of the rod.
- the coating bar 1 is brought into contact with the web 2 to apply the coating liquid onto the upper surface of the web 2.
- the contact between coating bar 1 and web 2 contains coating liquid, and the gap (coating between coating bar 1 and web 2) An amount of coating liquid according to the size of the groove on the bar surface and the gap between the coating bar and the web) is applied to the web 2.
- FIG. 2 shows a side view of an example in which the coating bar 1 is rotated forward in the running direction of the web 2, but the coating liquid 4 discharged from the die 3 as described above is a liquid. Supply streaks are less likely to occur due to direct supply on the pool 6. In addition, since the liquid is directly supplied onto the liquid pool 6, there is no room for air to be trapped in this portion, and the possibility of bubble streaks due to air trapping is eliminated.
- the coating liquid supply means used in the present invention is preferably a die, nozzle, spray, or the like that can discharge the coating liquid without interruption.
- the coating liquid can be supplied directly to the liquid pool 6 by the method of supplying it directly to the surface of the liquid pool, or the nozzle or die outlet can be inserted into the liquid pool and supplied directly to the inside.
- the pump has a discharge fluctuation, the size of the liquid pool fluctuates, which causes the coating width to fluctuate. Therefore, as the pump 7, it is preferable to use a metering pump such as a gear pump, a mono pump, or a diaphragm pump. To stabilize the puddle, it is recommended to use a pump with a pulsation rate of 3.5% to + 3.5%.
- the pulsation rate is based on the following definition.
- Pulsation rate [(Instantaneous maximum discharge amount-Instantaneous minimum discharge amount) Z Average discharge amount] x (100/2)
- the pulsation rate is measured using a mass flow meter (for example, model 63FS08-NE W00A30B1A manufactured by Endless Hauser) ) At a measurement cycle of 0.15 s.
- the coating apparatus 10 when the coating liquid 4 is interrupted and supplied to the liquid pool 6 in the form of droplets, for example, as shown in FIG. Fluid pressure fluctuations occur in 6 and there is a risk of coating defects due to it. Therefore, it is preferable that the coating liquid is continuously supplied to the liquid pool 6 without interruption.
- the coating liquid 4 discharged from the die 3 may be pulled by static electricity and come into contact with the web 2 before being supplied to the liquid pool 6. In the presence of such static effects, it is preferable to adjust the position of die 3 to achieve direct supply of liquid to puddle 6.
- This position adjustment is achieved by the moving mechanism 5 in the coating apparatus 10 shown in FIG.
- the moving mechanism 5 in the coating apparatus 10 shown in FIG. By appropriately adjusting the relative position of die 3 with respect to coating Ever 1 and web 2, especially the position of die 3 with respect to liquid pool 6, the effect of static electricity can be reduced as shown in the right figure (B) of FIG. Even in some cases, the coating liquid 4 can be directly supplied to the liquid pool 6.
- the die 3 as the coating liquid supply means and the coating bar 1 can be moved independently. If die 3 and coating bar 1 cannot move independently, for example, as shown in Fig. 5, at the end of coating, die 3 and coating bar 1 are integrated together, as indicated by arrow 5a.
- the dripping liquid 5b from the die 3 causes a thick coating portion of the coating liquid on the web 2.
- the thick coating portion of the coating liquid there is a risk of contamination of the apparatus after the drying process due to insufficient drying of the coating film in the subsequent drying process. Therefore, when the application is to be finished, it is necessary to wait so that the die 3 and the coating bar 1 do not move until the coating liquid drips.
- the die 3 and the coating bar 1 are moved and retracted as shown by an arrow 6a.
- the liquid receiver 9 receives the coating liquid dripping from the die 3, prevents the coating liquid from dripping onto the web 2, and then retracts the coating bar 1 as shown by the arrow 6b. The inconveniences that occur at the end of application can be prevented, and application can be completed promptly.
- the coating apparatus and the coating method of the present invention can be used in-line in the web manufacturing process, and the process of separating the web from the web manufacturing process, that is, the offline process. Can be used in
- FIG. 18 shows an example of a web manufacturing process
- FIG. 19 shows an example of a process when coating is performed inline during the web manufacturing process of FIG.
- the web manufacturing process includes an extruder 200, a base 201, and casting. It comprises a drum 202, a longitudinal stretching machine 203, a lateral stretching machine 204, and a weeding roll 205.
- a polymer is extruded by an extruder 200, and the polymer is formed into a web shape (sheet shape) through a die 201 and a casting drum 202.
- the formed web is stretched longitudinally and laterally by a longitudinal stretching machine 203 and a lateral stretching machine 204, and the stretched web is continuously wound by a take-up roll 205.
- a coating device 206 was installed between the longitudinal stretching machine 203 and the lateral stretching machine 204, and the longitudinal stretching was performed. Apply to later web.
- a sequential biaxial stretching method in which transverse stretching is performed after longitudinal stretching has been shown, but the present coating apparatus may be installed before the simultaneous biaxial stretching method.
- FIG. 11 shows a coating apparatus 11 as another example of the coating apparatus of the present invention.
- a coating apparatus 11 is such that a die 3a as a coating liquid supply means has a smooth portion 20, and the other configuration is the same as that of the coating apparatus 10 shown in FIG.
- a coating apparatus using a smooth portion has a configuration similar to the slide coater of Non-Patent Document 1.
- the coating liquid is supplied to the puddle, the coating liquid supplied to the puddle stays there as a liquid puddle, and then, a constant amount is applied by the coating bar. Used for forming a coating on a web. Therefore, the thickness of the coating film formed on the web does not depend on the supply amount of the coating liquid.
- the supplied coating liquid is applied to the web as it is, so the thickness of the coating film formed on the web depends on the supply amount of the coating liquid. At least in this respect, the coating mechanisms of the two are completely different.
- the smooth portion in the coating apparatus of the present invention is for flattening the flow of the coating liquid, the purpose, action, and effect are different from those of the slide coater intended for multilayer lamination.
- the supply of the coating liquid is performed by applying the coating liquid from the coating liquid supply means (die 3 and smooth portion 20) in the same manner as in the coating apparatus shown in FIG. Bar 1 and web 2 It is better to supply directly to the puddle 6 continuously and without interruption before it touches.
- the liquid may be supplied to the surface of the liquid pool, or the tip of a smooth portion may be inserted into the liquid pool and supplied directly to the inside.
- the insertion length of the smooth part is preferably within 2 mm from the surface of the puddle.
- the coating width of the coating liquid applied on the web As a method of adjusting the coating width of the coating liquid applied on the web, the position of the coating edge immediately after coating is monitored with a camera or the like, and the result is fed back so that the coating width is not excessively widened. It is preferable to do.
- the coating width can be adjusted by any one of the following: pumping amount of coating liquid, web conveyance speed, web tension, coating liquid viscosity, coating bar rotation speed, and coating bar pressing amount .
- a PET resin sheet extruded on the casting drum was also stretched three times in the longitudinal direction to form a uniaxially stretched film, and this film was subsequently conveyed at a speed of 25 mZ, The coating solution was coated using the coating apparatus 10 of the present invention shown in FIG.
- Coating bar Wire bar (diameter 19mm, length 300mm, wire diameter 0.356mm)
- Coating width W is a plan view of the coating apparatus 10 shown in FIG. Is the coating width W.
- the coating liquid was directly supplied in the form of a thin sheet for coating.
- no supply streaks or bubble streaks were found on the coating surface after drying.
- slight thickness unevenness in the width direction of the film was observed.
- coating was performed in exactly the same manner as in Example 1, except that the coating liquid supply position was set above the wire bar.
- the coating liquid supply position was set above the wire bar.
- supply streaks and slight thickness unevenness were observed on the coating surface after drying.
- 4 to 8 foam streaks were constantly generated over the entire width of the coating surface, and the traces of the foam streaks were visually observed even after drying. For this reason, the sheet on which this coating film was formed did not satisfy the quality as a product and became a defective product.
- coating was carried out in exactly the same manner as in Example 1, except that the coating liquid supply position was above the film surface upstream of the coating bar force.
- the coating liquid supply position was above the film surface upstream of the coating bar force.
- supply streaks and thickness unevenness were observed on the coating surface after drying.
- 2 to 5 bubble streaks always occurred over the entire width of the coating surface, and the traces of the bubble streaks were visually observed even after drying. Therefore, the sheet on which this coating film was formed did not satisfy the quality as a product, and became a defective product.
- Coating was performed in exactly the same manner as in Example 1, except that the distance from the coating liquid starting to fall from the coating liquid supply means and reaching the liquid pool was 90 mm. As a result of visual observation, it was observed that there were slight supply streaks and uneven thickness on the coated film surface after drying, which seemed to have occurred when the coating liquid was supplied. These slight supply streaks and thickness irregularities make the distance 80mm By making it within the range, it can be solved.
- coating was performed in exactly the same manner as in Example 1, except that the supply of the coating liquid from the die was forced into a discontinuous dropping state. As a result of visual observation, it was observed that supply streaks were generated at a location corresponding to the dripping position on the coating surface after drying. Moreover, although it was slight, the thickness nonuniformity was also observed.
- a smooth portion 111 having a flat tip as shown in FIGS. 12A and 12B is used as a smooth portion, and the tip of the smooth portion 111 is liquid-filled.
- Coating was carried out in exactly the same way as in Example 4 except that it was inserted in a lump.
- streaks 109 were visually observed at a central force in the width direction of the coated film surface after drying at a position of 80 mm left and right.
- the width of the obtained product was 160 mm.
- This product width of 160 mm is smaller than the product width of 210 mm in Example 4. This means that the shape of the tip of the smooth part is an arc shape corresponding to the shape of the liquid puddle. It is preferable for me to show.
- the smooth part 11 la shown in FIGS. 13A and 13B having an arcuate shape 11 la tilt angle ⁇ is 70 degrees, and the coating liquid is opened at the top.
- the coating was performed in exactly the same manner as in Example 2 except that the flow distance was 5 mm.
- supply lines and foam lines were not observed on the coating film surface after drying.
- a slight thickness unevenness was observed on the coating surface. This slight thickness unevenness can be eliminated by adjusting the inclination angle ⁇ of the smooth part and the distance that the coating liquid flows with the upper part opened.
- the coating liquid is supplied to the upper surface of the web by flowing down on a smooth portion where the upper part is open to the outside. It is characterized by supplying the liquid directly to the liquid pool of the coating liquid.
- This feature makes it possible to manufacture a product having a coating film with a good surface without the presence of foam streaks due to air mixing on the coating film surface of the product.
- the shape of the tip of the smooth part it is possible to increase the gap in the width direction of the streaks appearing along the longitudinal direction of the web at both ends of the coating surface as much as possible. It is possible to manufacture a product having Furthermore, the coating liquid can be applied in-line to the web using a high-viscosity coating liquid in the web (sheet or film) manufacturing process.
Landscapes
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Wood Science & Technology (AREA)
- Coating Apparatus (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
Abstract
Description
Claims
Priority Applications (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2006800079182A CN101137447B (zh) | 2005-03-11 | 2006-03-06 | 涂布装置、涂布方法以及具有涂膜的带状物的制造方法 |
| EP06728656A EP1857189B1 (en) | 2005-03-11 | 2006-03-06 | Application apparatus, application method and method for manufacturing web having coating film |
| US11/908,198 US8733275B2 (en) | 2005-03-11 | 2006-03-06 | Application apparatus, application method and method for manufacturing web having coating film |
| DE602006016745T DE602006016745D1 (de) | 2005-03-11 | 2006-03-06 | Auftragsvorrichtung, auftragsverfahren und verfahren zur herstellung einer bahn mit einem überzugsfilm |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2005068947 | 2005-03-11 | ||
| JP2005-068947 | 2005-03-11 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2006095669A1 true WO2006095669A1 (ja) | 2006-09-14 |
Family
ID=36953264
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP2006/304237 Ceased WO2006095669A1 (ja) | 2005-03-11 | 2006-03-06 | 塗布装置、塗布方法および塗膜を有するウェブの製造方法 |
Country Status (7)
| Country | Link |
|---|---|
| US (1) | US8733275B2 (ja) |
| EP (1) | EP1857189B1 (ja) |
| KR (1) | KR101267858B1 (ja) |
| CN (1) | CN101137447B (ja) |
| DE (1) | DE602006016745D1 (ja) |
| TW (1) | TWI361726B (ja) |
| WO (1) | WO2006095669A1 (ja) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100117255A1 (en) * | 2006-09-08 | 2010-05-13 | Hiroyuki Inoue | Coating method and coating apparatus |
| US20210387222A1 (en) * | 2020-03-09 | 2021-12-16 | Kabushiki Kaisha Toshiba | Coating head, coating apparatus, and coating method |
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| PL2151282T3 (pl) | 2007-05-18 | 2021-08-02 | Musashi Engineering, Inc. | Sposób i aparat do wyrzucania ciekłego materiału |
| JP5062002B2 (ja) * | 2008-03-31 | 2012-10-31 | 住友化学株式会社 | 塗工方法および塗工装置 |
| JP5563752B2 (ja) * | 2008-06-26 | 2014-07-30 | 東京応化工業株式会社 | 塗布装置及び塗布方法 |
| TW201016331A (en) * | 2008-10-28 | 2010-05-01 | Chulan Ind Co Ltd | Method for coating surface of formwork plate and product thereof |
| WO2010134122A1 (ja) * | 2009-05-18 | 2010-11-25 | フォイト パテント ゲゼルシャフト ミット ベシュレンクテル ハフツング | 脱泡機 |
| TWI453071B (zh) * | 2011-08-03 | 2014-09-21 | Nat Univ Chung Cheng | Coating thickness adjustment device |
| JP5619057B2 (ja) * | 2012-03-15 | 2014-11-05 | パナソニック株式会社 | 塗布装置 |
| CA2886571C (en) * | 2012-09-28 | 2016-06-07 | Nissan Motor Co., Ltd. | Coating apparatus |
| CN102909158A (zh) * | 2012-10-10 | 2013-02-06 | 江苏安捷蓝环境科技有限公司 | 一种金属载体波纹板涂膏机 |
| JP5899424B2 (ja) * | 2013-01-28 | 2016-04-06 | パナソニックIpマネジメント株式会社 | 塗布装置および塗布方法 |
| EP2772584A1 (en) * | 2013-02-27 | 2014-09-03 | Valmet Technologies, Inc. | Method and arrangement for a fiber web production line |
| EA036072B1 (ru) * | 2014-04-25 | 2020-09-23 | Сонвон Индастриал Ко., Лтд. | Способ и устройство получения поверхностно сшитых водоабсорбирующих полимерных частиц с использованием полимеризационной ленты определенной формы |
| WO2016170581A1 (ja) * | 2015-04-20 | 2016-10-27 | 富士機械製造株式会社 | グリス塗布具 |
| WO2022102179A1 (ja) * | 2020-11-11 | 2022-05-19 | パナソニックIpマネジメント株式会社 | 電極合剤スラリーの塗工装置 |
| IT202100013085A1 (it) * | 2021-05-20 | 2022-11-20 | Cefla Soc Cooperativa | Apparato e metodo per la verniciatura a rullo di pannelli, preferibilmente pannelli fotovoltaici |
| CN113522675B (zh) * | 2021-09-14 | 2021-12-07 | 常州铭赛机器人科技股份有限公司 | 气泡检测装置及检测方法 |
| CN117249743B (zh) * | 2023-11-17 | 2024-02-13 | 中铁城建集团第一工程有限公司 | 一种预制板平整度检测装置及其检测方法 |
| CZ2023515A3 (cs) * | 2023-12-24 | 2025-07-02 | Leancat Electrolyzers S.R.O. | Způsob přesného nanášení katalytických inkoustů a zařízení k jeho provedení |
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- 2006-03-06 KR KR1020077020022A patent/KR101267858B1/ko not_active Expired - Fee Related
- 2006-03-06 CN CN2006800079182A patent/CN101137447B/zh not_active Expired - Fee Related
- 2006-03-06 EP EP06728656A patent/EP1857189B1/en not_active Expired - Lifetime
- 2006-03-06 DE DE602006016745T patent/DE602006016745D1/de not_active Expired - Lifetime
- 2006-03-06 WO PCT/JP2006/304237 patent/WO2006095669A1/ja not_active Ceased
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20100117255A1 (en) * | 2006-09-08 | 2010-05-13 | Hiroyuki Inoue | Coating method and coating apparatus |
| US8535763B2 (en) * | 2006-09-08 | 2013-09-17 | Toray Industries, Inc. | Coating method and coating apparatus |
| US20210387222A1 (en) * | 2020-03-09 | 2021-12-16 | Kabushiki Kaisha Toshiba | Coating head, coating apparatus, and coating method |
| US11707759B2 (en) * | 2020-03-09 | 2023-07-25 | Kabushiki Kaisha Toshiba | Coating head, coating apparatus, and coating method |
Also Published As
| Publication number | Publication date |
|---|---|
| US8733275B2 (en) | 2014-05-27 |
| US20090079105A1 (en) | 2009-03-26 |
| EP1857189B1 (en) | 2010-09-08 |
| CN101137447B (zh) | 2011-02-02 |
| DE602006016745D1 (de) | 2010-10-21 |
| CN101137447A (zh) | 2008-03-05 |
| KR20070110316A (ko) | 2007-11-16 |
| TWI361726B (en) | 2012-04-11 |
| TW200637660A (en) | 2006-11-01 |
| KR101267858B1 (ko) | 2013-05-27 |
| EP1857189A4 (en) | 2009-11-18 |
| EP1857189A1 (en) | 2007-11-21 |
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