Patent Application
20140272160
1. Field of the Invention
The present invention relates to a slot curtain coating apparatus and a slot curtain coating method, in both of which a coating liquid ejected from a slit is applied on a continuously running web, while so guiding the coating liquid in the form of a curtain with curtain edge guides.
2. Description of the Related Art
As a coating film is formed in the slot curtain coating method, a portion where a flow of a coating liquid is slow, which is called a boundary layer, is created adjacent to both edge guides of a curtain film, when the coating liquid free falls. Due to this difference in the flow rate, a difference in surface tension is generated. A phenomenon that parts of the coating liquid adjacent to the both edges of the curtain film move towards the center is caused by Marangoni flow that is generated due to the surface tension difference. As a coating film is formed with hitting the coating liquid onto a continuously running web in the aforementioned state, there is a problem that thin film parts 20a are formed at edges of the coating film 20 with respect to the width direction thereof, as illustrated in
For example, disclosed is a method for preventing a formation of a boundary layer in a curtain film (Japanese Patent Application Laid-Open (JP-A) No. 2008-520753). This method involves providing a porous material to a surface of an edge guide at which a curtain film is flown down, and ejecting auxiliary water from the porous material to cover the porous material with the auxiliary water, to reduce friction resistance of the curtain film with the surface of the edge guide at which the curtain film flows down. to prevent reduction in a flow-down speed of the coating liquid adjacent to the edge guides, to thereby prevent a formation of a boundary layer.
This method has an effect when a viscosity of the coating liquid is relatively low, such as a several tens cp. As a coating liquid having a high viscosity is used, however, a thickness of the film becomes uneven due. to an influence of a boundary layer. Moreover, clogging of the porous material is caused with the coating liquid, and ejection of the edge guide auxiliary water becomes uneven, causing coating defects, such as uneven film thickness.
A method for solving the aforementioned clogging is disclosed in U.S. Pat. No. 7,081,163. Disclosed is a technique where a metal surface is provided as an auxiliary ater flow-down surface of the edge guide, and auxiliary water is ejected from an outlet provided in the metal surface.
The aforementioned technique however has a problem that it is hard to uniformly eject the edge guide auxiliary water, as it employs a structure where the edge guide auxiliary water is directly flown from the outlet, a problem that a curtain film is not stabilized, as the auxiliary water does not linearly fall and the auxiliary water flow-down surface is a flat surface, and a problem that a curtain film is swung by a disturbance of wind.
Moreover, disclosed in JP-A No. 2001-46939 in order to solve the problem that it is difficult to uniformly eject the edge guide auxiliary water is a method containing providing a slit portion and a manifold portion that is a liquid retention section, through which the edge guide auxiliary water pass until being ejected from the outlet. In this method, however, the ejection direction of the edge guide auxiliary water is different from the flow down direction of the coating liquid, and therefore the coating liquid cannot be sufficiently accelerated.
As for another method, disclosed is a method, in which a S formation of a boundary layer is prevented adjacent to both edges of the curtain film by ejecting the edge guide auxiliary water to the edge guide in the flow-down direction of the coating liquid (JP-A No. 01-199668). In this method, however, acceleration of the curtain film with the edge guide auxiliary water is not sufficient, and therefore a boundary layer cannot be completely eliminated.
Moreover, it is also disclosed in JP-A No. 06-218314 that the edge guide auxiliary water is ejected to the edge guide in the flow-down direction of the coating liquid. This further discloses a size of a flow channel of the auxiliary water inside the edge guide. However, this disclosure does not include a speed of the edge guide auxiliary water. With regard to the size of the flow channel, the flow channel length and the radius R of the curved portion of the flow channel just before the outlet are disclosed. With such sizes, there is a significant difference to an obtainable effect of the present invention.
Furthermore, as a coating liquid having a relatively high viscosity and having a strong shear viscosity reducing effect, such as an adhesive, is used, a thickening effect of the slot curtain film due to an influence of a boundary layer increases.
Similarly to JP-A No. 06-218314, the edge guide auxiliary water is ejected in the curtain flow down direction in JP-A No. 2004-105960. However, there is no description about a radius R of the curved portion of the flow channel just before the outlet therein. Based upon the sizes of the flow channel of the auxiliary water and the outlet, or the size of the flow-down surface of the auxiliary water, an effect of reducing a boundary layer is not large with a coating liquid having a relatively high viscosity, and a strong shear viscosity educing effect, such as an adhesive.
Moreover, disclosed is an ejection speed of an edge guide auxiliary water at which an effect of accelerating a coating liquid is exhibited, a boundary layer is prevented so that an uneven thickness of a curtain film can be prevented with a coating liquid having a relatively high viscosity and a strong shear viscosity reducing effect, such as an adhesive (JP-A No. 2011-78966). In this disclosure, also disclosed are edge guides having resistance to disturbances, such as wind, i.e., a strong aligning effect, as a coating liquid having a relatively high surface tension (35 mN/m or greater) is used.
In the case where a coating liquid having a low surface tension (less than 35 mN/m) is used, disclosed are edge guide having resistance to disturbances, such as wind (JP-A No. 2012-35210).
An influence of a boundary layer is inhibited by flowing an auxiliary water along a surface of an edge guide at which a curtain film falls down, but there is no auxiliary water from the upper plane of the edge guide to the auxiliary water outlet. In the case where a coating liquid having a relatively high viscosity and strong shear viscosity reducing effect is applied, therefore, a boundary layer is easily generated between the aforementioned areas, and an influence of the boundary layer is caused, which have been found from the studies conducted by the present inventors.
The present inventors have come to an insight that an influence of a boundary layer adjacent to edge guides can be inhibited by reducing a distance between the top plane of the edge guide and the auxiliary water outlet. To reduce the distance between the top plane of the edge guide and the auxiliary water outlet, however, is not simple, as it is closely related to a flow channel for introducing auxiliary water.
In fact, a distance h from the top plane of the edge guide to the auxiliary water outlet is determined with h=T+R+S, which is a sum of a thickness T of the thinnest part of the upper part of the curved portion, a curvature radius R of the lower part of the curved portion from the straight-line portion to the auxiliary water outlet, and a thickness S of the slit portion, as illustrated in
There is a problem of rigidity in order to reduce T, which is a thickness from the top plane of the edge guide to the slit portion. As a downside caused by reducing the curvature radius R of the lower part of the curved portion from the slit portion to the auxiliary water outlet, there is a problem that a flow in a flow channel in the curved portion becomes fast due to a centrifugal force, to thereby generate a disturbance in the flow. As a downside caused by reducing the thickness S of the slit portion, there is a problem that Reynolds number becomes large and a turbulent flow is caused.
The present invention aims to provide a slot curtain coating apparatus, which can make a thickness of a curtain film along a width direction uniform with preventing the curtain film from thickening or thinning adjacent to edge guide due to an influence of a boundary layer, to thereby improve a yield.
As for the means for solving the aforementioned problems, he slot curtain coating apparatus of the present invention contains:
an ejecting unit containing a coating liquid outlet configured to eject a coating liquid;
a pair of guiding units, each containing an auxiliary water outlet configured to eject auxiliary water, where the guiding units are configured to support both edges of a curtain film, which is formed of the coating liquid ejected from the coating liquid outlet, along a width direction that is substantially vertical to a flow-down direction of the curtain film, and to guide the curtain film onto a support to be transported; and
a transporting unit configured to transport he support,
wherein the guiding unit has a manifold portion configured to retain the auxiliary water, and a slit portion connecting between the manifold portion and the auxiliary water outlet,
wherein the slit portion is composed of a straight-line portion, and a curved portion configured to eject the auxiliary water substantially vertically downwards, and
wherein the curved portion is provided to a position at which h=T+R+S is 1.5 mm to 5 mm, where T is a thickness of the thinnest part of a top part of the curved portion, R is a curvature radius of a bottom part of the curved portion and is 0.5 mm to 3 mm, S is a gap of the slit portion, and h is a height of the auxiliary water outlet from a top plane of the guiding unit.
The present invention can solve the aforementioned various problems in the art, achieve the aforementioned object, and can provide a slot curtain coating apparatus, which can make a thickness of a curtain film along a width direction uniform with preventing the curtain film from thickening or thinning adjacent to edge guide due to an influence of a boundary layer, to thereby improve a yield.
One example of embodiments of the slot curtain coating apparatus and slot curtain coating method is explained hereinafter.
The slot curtain coating apparatus of the present invention contains an ejecting unit containing a coating liquid outlet configured to eject a coating liquid; a pair of guiding units, each containing an auxiliary water outlet configured to eject auxiliary water, where the guiding units are configured to support both edges of a curtain film, which is formed of the coating liquid ejected from the coating liquid outlet, along a width direction that is substantially vertical to a flow-down direction of the curtain film, and to guide the curtain film onto a support to be transported; and a transporting unit configured to transport the support, wherein the guiding unit has a manifold portion configured to retain the auxiliary water, and a slit portion connecting between the manifold portion and the auxiliary water outlet, wherein the slit portion is composed of a straight-line portion, and a curved portion configured to eject the auxiliary water substantially vertically downwards, and wherein the curved portion is provided to a position at which h=T+R+S is 1.5 mm to 5 mm, where T is a thickness of the thinnest part of a top part of the curved portion, R is a curvature radius of a bottom part of the curved portion and is 0.5 mm to 3 mm, S is a gap of the slit portion, and h is a height of the auxiliary water outlet from a top plane of the guiding unit.
The thinnest part of the top part of the curved portion means a portion where a distance between a top plane of the guiding unit and the curved portion is the shortest.
The slot curtain coating apparatus of the present invention may further contain other units that are appropriately selected according to the necessity.
The slot curtain coating method of the present invention contains: ejecting a coating liquid from a coating liquid outlet (ejection step); supporting both edges of a curtain film, which is formed of the coating liquid ejected from a coating liquid outlet, by a pair of guiding units each containing auxiliary water outlet configured to eject the auxiliary water, along a width direction that is substantially vertical to a flow-down direction of the curtain film, and guiding the curtain film onto a support to be transported (guiding step); and transporting the support (transportating step), wherein the guiding unit has a manifold portion configured to retain the auxiliary water, and a slit portion connecting between the manifold portion and the auxiliary water outlet, wherein the slit portion is composed of a straight-line portion, and a curved portion configured to eject the auxiliary water substantially vertically downwards, and wherein the curved portion provided to a position at which h=T+R+S is 1.5 mm to 5 mm, where T is a thickness of the thinnest part of a top part of the curved portion, R is a curvature radius of a bottom part of the curved portion and is 0.5 mm to 3 mm, S is a gap of the slit portion, and h is a height of the auxiliary water outlet from a top plane of the guiding unit.
The slot curtain coating method of the present invention may further contain other steps that are appropriately selected according to the necessity.
Structural elements of the slot curtain coating apparatus and slot curtain coating method of the present invention are explained hereinafter. The present invention is targeted for web coating.
The ejecting unit contains a manifold configured to retain a coating liquid, and a coating liquid outlet (slit) configured to eject he coating liquid.
The ejection step is ejecting the coating liquid from the coating liquid outlet to make a curtain film, which is formed of the coating liquid, fall.
The coating liquid is appropriately selected depending on the intended purpose without any limitation, but a fluid that reduces apparent viscosity as a shear rate increases, such as an acryl emulsion-based adhesive, exhibits a significant effect in the present invention.
A viscosity of the coating liquid is appropriately selected depending on the intended purpose. In order to sufficiently exhibits an effect of the present invention, however, the coating liquid is preferably a fluid that reduces apparent viscosity as a shear rate increases, and viscosity properties thereof are preferably in the ranges of 300≦η1≦3,000 (mPa·sec), and 10≦η2≦300 (mPa·sec). where η1 is a viscosity of the coating liquid at a shear rate of 1 sec−1, and η2 is a viscosity thereof at a shear rate of 1,000 sec−1.
When a viscosity of a coating liquid is low at low shear in slot curtain, the liquid may be dripped from the slit from a die as coating is temporary stopped during the operation due to adjustments or the like. When the viscosity is greater than 3,000 mPa·sec at low shear (shear rate of 1 sec−1), (1) it is difficult to release air bubbles in the liquid to thereby cause bubble defects due to air bubbles in the liquid, (2) load to a feeding pump increases, as the pressure for ejecting the coating liquid increases, and therefore it is necessary to give pressure resistance to a feeding system.
In the present invention, the viscosity of the coating liquid is relatively low, in the case where the viscosity η1 at low shear (shear rate of 1 sec−1) is less than 300 mPa·sec, and therefore a proportion of a thinning of the curtain film caused by an influence of a boundary layer is small. There is no problem on practice, even when the edge guides of the curtain coating apparatus of the present invention are not used.
The viscosity can be measured, for example, by means of a B-type viscometer (product name: Vismetron VS-A1, manufactured by SHIBAURA SEMTEK CO., LTD.), or a pressure control rheometer VAR-100 (manufactured by Reologica Instruments AB).
A surface tension of the coating liquid is appropriately selected depending on the intended purpose without any limitation, but the surface tension thereof is preferably 20 mN/m to 40 mN/m.
When the surface tension is less than 20 mN/m, the tension of the film is weak as the surface tension of the film itself is weak, and therefore the film is easily deformed and waved by a disturbance by wind. When the surface tension is greater than 40 mN/m, moreover, the curtain film is cut upwards.
The surface tension can be measured, for example, by measuring static surface tension in accordance with a platinum plate method by means of a FACE automatic surface tensiometer (manufactured by Kyowa Interface Science Co., Ltd.). As described in the literature of Brown, A study of the behavior of a thin sheet of moving liquid J. Fluid Mechanics, 10:297-305, a dynamic surface tension of the curtain film can be measured by measuring a split angle of the curtain film, which is formed by inserting a needle-like object into the curtain film.
A mechanism of the cutting upwards of the curtain film is caused by a balance between a dynamic surface tension of the curtain film and dynamic pressure, and therefore it is important to measure and evaluate the dynamic surface tension of the film
A cross-sectional shape of the coating liquid outlet is a rectangular cross section.
A size of the coating liquid outlet is appropriately selected depending on the intended purpose without any limitation, but a gap of the slit is preferably about 0.2 mm to about 0.5 mm.
The gap of the slit has a function for making the coating liquid uniform along a width direction, and a size of the gap varies depending on a size and shape of a die manifold, a distance from the manifold to a slit outlet, a presence and position of a second manifold, and a flow rate or viscosity of the coating liquid, as described in “Slot Coating: Fluid mechanics and die design, Sartor, Luigi, Ph.D. University of Minnesota, 1990.”
A material of the coating liquid outlet is appropriately selected depending on the intended purpose without any limitation, but the coating liquid outlet is preferably a metal plane, such as SUS, aluminum, and plating (e.g., hard chrome plating).
As for the material thereof, metal is preferable, as clogging is prevented even when a resin is contained in the coating liquid.
A slot die curtain used as an ejection system is used when one or two layers of a coating liquid are applied. As the slit faces downwards, in the case where the viscosity of the coating liquid is low, dripping of the liquid may be caused, or air bubbles in the liquid may be held in the manifold of the die head. However, as the ejection speed of the coating liquid is fast compared to slide die curtain, the slot die curtain is hardly cut upwards, considering a mechanism of cutting up of the curtain film. In the mechanism thereof, when the dynamic surface tension is large, the curtain film is cut upwards due to a balance between the dynamic surface tension of the coating liquid and dynamic pressure (inertial force) as the coating liquid falls. Moreover, it is easy to wash, and an amount of a washing liquid, such as water, used for washing is small, as there is less open space, such as a slide flow down surface. In the case where the viscosity of the coating liquid is high, moreover, it is also easy to temporally stop the operation.
A flow rate o ejecting the coating quid is appropriately selected depending on the intended purpose without any limitation, provided that the curtain film can be formed. There is no problem as long as the coating liquid is ejected at the intended flow rate, and shapes of the slit and manifold are the shapes with which a curtain film can be formed.
The support is appropriately selected depending on the intended purpose without any limitation, provided that the coating liquid can be supported thereon.
A shape, structure, and size of the support are appropriately selected depending on the intended purpose without any limitation.
Examples of the support include release paper, base paper, synthetic paper, and a polyethylene terephthalate (PET) film.
The transporting unit is a unit configured to transport the support, and the transportating step is a step containing transporting the support. The transporting unit is appropriately selected depending on the intended purpose without any limitation, and examples thereof include a transporting roller, and a transporting roller, and a transporting belt.
The guiding unit is also called an edge guide, and contains a manifold portion configured to retain auxiliary water, and a slit portion connecting between the manifold portion and the auxiliary water outlet. The auxiliary water passes through the manifold, the straight-line portion of the slit portion, and then the curved portion of the slit portion, and is ejected substantially vertically downwards from the outlet, to thereby be introduced to a curtain film.
The guiding step is supporting both edges of a curtain film, which is formed of the coating liquid ejected from a coating liquid outlet, by a pair of guiding units each containing auxiliary water outlet configured to eject the auxiliary water, along a width direction that is substantially vertical to a flow-down direction of the curtain film, and guiding the curtain film onto a support to be transported.
The auxiliary water is appropriately selected depending on the coating liquid for use. An effect of retaining a curtain film with the edge guides, i.e., an aligning effect, is exhibited by pulling the coating liquid with the auxiliary water. Therefore the surface tension of the auxiliary water needs to be set always higher than the surface tension of the coating liquid. Examples of the auxiliary water include water in the case where the coating liquid is a water-based liquid, the same solvent to the one used in the coating liquid in the case where the coating liquid is a solvent-based liquid, and a blended liquid formed by blending a resin, a surfactant, etc. with water or a solvent.
The manifold portion may be a two stage manifold or a one stage manifold. As described in Slot Coating: Fluid mechanics and die design, Sartor, Luigi, Ph.D. University of Minnesota, 1990, a size of the manifold portion varies depending on a distance between the manifold portion and the slit outlet (auxiliary water outlet), and a flow rate or viscosity of the auxiliary water.
The curved portion is explained with reference to
Determining the thickness of the thinnest part of the upper part of the curved portion 32 as T, the curvature radius of the lower part of the curved portion 32 as R, and the gap of the slit portion as S as illustrated in
Accordingly, the curved portion 32 has the curvature radius R of 0.5 mm to 3 mm, and is provided at a position at which the height of the auxiliary water outlet from the top plane of the guiding unit, i.e., h=T+R+S is 1.5 mm to 5 mm.
Note that, a flow in a flow channel inside the guiding unit cannot be confirmed visually, and therefore the flow is evaluated through numerical analysis (Fluent).
In order to shorten the distance h from the top plane of the guiding unit to the auxiliary water outlet, as illustrated in
Meanwhile, the edge guide having a structure containing the manifold and the slit portion, as in the present invention, is composed of three plates (see
However, the rigidity of the part of the guide unit at the upper side of the manifold portion and the slit portion is reduced by thinning the thickness T of the thinnest part of the upper part of the curved portion. Moreover, the plates cannot be held with bolts at the area adjacent to the slit portion, and therefore leakage may be caused from the mating surfaces of the plates.
In the present invention, a thickness T can be reduced with maintaining the rigidity of the part of the guide unit at the upper side of the manifold portion and slit portion, and therefore a cross-section area of the circular part 40 of
Specifically, as illustrated in
In order to realize the thickness T of the thinnest part required for attaining the desirable rigidity, the angle θ is preferably 30° to 60°. When the angle is smaller than 30°, the thickness T of the thinnest part cannot be made thin. When the angle thereof is greater than 60°, the length of the curved portion of the slit portion becomes large, and therefore a problem may be caused in handling, such as cleaning.
As illustrated in
As illustrated an
When the maximum gap G is smaller than 0.2 mm, it is not easy to clean the inside of the outlet. When the maximum gap G is larger than 0.5 mm, the ejection uniformity of the auxiliary water may be impaired.
As illustrated in
When the maximum width w is smaller than 1.5 mm, a problem may be caused in accuracy upon processing. When the maximum width w is greater than 4 mm, the auxiliary water may not flow uniformly in the entire width.
The speed for introducing the auxiliary water is appropriately selected depending on the intended purpose without any limitation, provided that it is in the range at which the auxiliary water flows on a flow down surface. The speed thereof is preferably 0.4 m/sec to 2.1 m/sec, inure preferably 0.8 m/sec to 1.6 m/sec.
When the speed for introducing the auxiliary water is less than 0.4 m/sec, a boundary layer may be generated. When the speed thereof is greater than 2.1 m/sec, the auxiliary water may be introduced diagonally downwards.
A shape of the auxiliary water outlet 9 is a slit shape having a rectangular cross section. Originally, the flow channel of the auxiliary water inside the edge guide is preferably in the form of a long slit. However, if the slit is long, in the case where clogging is caused, it is difficult to clean, and practically, it is structurally difficult to provide a long slit inside.
The auxiliary water flow-down groove (concave portion) is explained with reference to
As illustrated in
The concave portion side surface and an exposed surface, which is formed to continue to the concave portion side surface, and to face the concave portion side surface, form an acute angle (α in
When the acute angle is smaller than 30°, accuracy in processing may be adversely affected. When the acute angle is greater than 80°, an effect obtained by providing the acute angle may be impaired. When the acute angle is in the aforementioned preferable range, on the other hand, it is advantageous for retaining the edge guide auxiliary water.
The maximum depth (x in
When the maximum depth x is smaller than 0.2 mm, the auxiliary water may be overflown from the auxiliary water flow-down groove (concave portion). When the maximum depth x is greater than 0.5 mm, a turbulent flow may be generated.
The maximum gap between the side surfaces of the auxiliary water flow-down groove (concave portion side surfaces) is appropriately selected depending on the intended purpose without any limitation, but it is preferably 1.5 mm to 4.0 mm, more preferably 2 mm to 3 mm.
When the maximum gap is smaller than 1.5 mm, it may be difficult for the auxiliary water to flow through the auxiliary water flow-down groove, and the auxiliary water may be overflown from the concave portion. When the maximum gap is greater than 4.0 mm, the curtain film may become unstable, and a turbulent flow may be generated at the bottom.
Note that, in the case where the auxiliary water outlet is provided from one side surface to the other side surface, the maximum gap of the concave portion is identical to the maximum width w of the auxiliary water outlet.
Examples of a structure of the guiding unit include a structure where 3 plates (11, 12, 12′) are combined, as illustrated in
Examples of a processing method for forming the manifold portion 30, and the straight-line portion 31 and curved portion 32 of the slit portion in the central plate 11 include wire cutting, and laser processing.
A material of the guiding unit is appropriately selected for use, but metal is preferable as clogging of the coating liquid can be prevented. Moreover, as for the central plate among the three plates, stainless steel is preferably used in view of processing accuracy, because processing accuracy is required as the gap S of the slit is narrow.
One example of the embodiment of the curtain coating apparatus and curtain coating method of the present invention is specifically explained with reference to drawings.
Note that, technically preferable various restrictions are mentioned, as he embodiment described below is the preferable embodiment of the present invention. However, the scope of the present invention is not limited to the embodiment described below, unless otherwise stated in the description below.
As illustrated in
As illustrated in
As illustrated in
As illustrated in
The straight-line portion 31 of the slit portion forms an angle (θ in
As illustrated in
Meanwhile, the edge guide 2 has, at an upper part thereof, an auxiliary water outlet 9, which is configured to substantially uniformly eject the auxiliary water 10 downwards along the width direction of the auxiliary water flow-down groove (concave portion) 13 of the central plate 11, as illustrated in
The curtain film 6 flows down in the direction depicted with an arrow, and both edges thereof are supported with the auxiliary water 10 flown down in the auxiliary water flow-down grooves (concave portions) 13 of the edge guides 2.
The speed for introducing the auxiliary water 10 is set by varying the opening of the flow rate control valve (not illustrated), or an ejection amount of the pump.
At the bottom of the edge guide 2, an outlet (not illustrated) configured to discharge a mixed liquid of the auxiliary water 10 and the coating liquid, and a vacuum system (not illustrated) configured to enable the mixed liquid to discharge easily are provided. In order to prevent solidification of the coating liquid, the auxiliary water may be passed through the bottom of the edge guide 2.
As illustrated in
An aligning effect is exhibited owing to the surface tension of the auxiliary water by providing the auxiliary water flow-down groove (concave portion) 13, and therefore a curtain film, which is stable to disturbance, such as by wind, can be formed. Moreover, a formation of a boundary layer in the curtain film can be prevented further by introducing the auxiliary water in the flow-down direction along the edge curtain film 6, and introducing the auxiliary water at the introduction initial speed of 0.4 m/sec to 1.6 m/sec.
Note that, a distance between a pair of the edge guides provided the both side of the curtain film 6 with respect to the width direction thereof may be identical to a width of the coating liquid outlet (slot) of the slot curtain coating head 1, or may be narrower than the coating liquid outlet.
The slot curtain coating apparatus and slot curtain coating method of the present invention can inhibit an influence of a boundary layer, and can form a curtain film having a uniform film thickness.
The present invention is more specifically explained through Examples hereinafter, but Examples shall not be construed as to limit the scope of the present invention. Any modification appropriately applied to Examples is also included within the scope of the present invention, as long as it is in the spirit of the present invention.
In order to confirm an effect of the present invention, a slot curtain coating apparatus illustrated in
Specific details of sizes of the curved portions of the edge guides of Examples 1 to 6 and Comparative Examples 1 to 4 are depicted in Table 3.
The slot gap of the slot curtain coating head 1 was set to 0.4 mm, and the falling width of the curtain was set to 250 mm. The width of the coating liquid outlet (slot) of the slot curtain coating head 1 was 250 mm.
As for a coating liquid, an acryl emulsion-based adhesive (product name: X-407-102E-10, manufactured by SAIDEN CHEMICAL INDUSTRY CO., LTD.) was used.
The viscosity of the coating liquid was 750 mPa·sec (as measured by a B-type viscometer, product name: Vismetron VS-A1, manufactured by SHIBAURA SEMTEK CO., LTD.), the viscosity thereof at the shear rate of 1 sec−1 was 2,000 mPa·sec, and the viscosity thereof at the shear rate of 1,000 sec−1 was 250 mPa·sec.
The static surface tension of the coating liquid was measured through a platinum plate method, by means of a FACE automatic surface tensiometer CBVP-A3 (manufactured by Kyowa Interface Science Co., Ltd.). As a result, the static surface tension was 33 mN/m.
A flow rate of the coating liquid was set to 1.25 cc/cm·sec (as measured by a flow meter for a coating liquid (product name: CN015C-SS-440K, manufactured by OVAL Corporation)).
As for the edge guide 2, an edge guide composed of 3 plates, as illustrated in
As for he size of the edge guide 2, the length of flow down was 140 mm, the maximum width (w) of the introduction opening of the auxiliary water was 3 mm, the maximum depth (x) of the auxiliary ater flow-down groove (concave portion) was 0.25 mm, the maximum width of the auxiliary rater flow-down groove (concave portion) was 3 mm, and the acute angle (α) was 60°.
A distance between the pair of the edge guides (an edge formed at an acute angle of the concave portion of one edge guide to an edge formed at an acute angle of the other edge guide) was 250 mm.
A feeding rate of the edge guide auxiliary water was set to 50 mL/min.
The edge guide auxiliary water was supplied from the pressure tank compressed at 0.2 MPa to the edge guide 2 by means of a micro motion flow meter (manufactured by OVAL Corporation) (flow meter main body: E010S-SS-311, transmitter: RFT9739-3MD11, integrating meter: EL0122-132011) and a float-type flow meter (P100L-4, manufactured by TOKYO SEISO CO., LTD.). The opening of the throttle valve of the float-type flow meter was adjusted to give the auxiliary water flow down speed of about 1.1 m/s, which was determined by converting from the flow rate.
A: the auxiliary water was ejected almost uniformly
B: there was a slight disturbance in ejection of the auxiliary water
C: the auxiliary water a not ejected uniformly
A curtain film was formed, and the light and shade of the film was visually observed with applying light from the opposite side of the curtain film, to thereby confirm the presence of a thin film part.
A: the curtain film was almost uniform along the width direction thereof
B: there was a slightly thick film part in the width direction of the curtain film
C: there was a thick film part in the width direction of the curtain film
A plate of SUS304 having a thickness of 0.1 mm was folded to form a flume having a width of 8 mm, and a depth of 8 mm. The curtain film was blocked with the flume to measure an amount of the flume flow down liquid in a gravimetric method to thereby determine a fall down flow rate. The measured value was converted into a flow rate distribution by regulation, in which the flow rate obtained by converting the value of the flow meter with the flume width of 8 mm was determined as 100%.
A: the thickness of the thick film part was less than 105% relative to the average value
B: the thickness of the thick film part was 105% or greater but less than 110% relative to the average value
C: the thickness of the hick film part was 110% or greater relative to the average value
In order to make clear an effect of the curvature radius R at the bottom part of the curved portion of the slit portion, in Experiment 1, the edge guide auxiliary water was ejected from an edge guide whose R was varied to thereby confirm an ejection state. Moreover, a curtain film was formed under the experiment basic conditions, to thereby observe a film thickness of the curtain film.
In Example 1, the curvature radius Rat the bottom part of the curved portion was set to 1 mm, the gap S of the slit was set to 0.25 mm, and the thickness T of the thinnest part of the trapezoidal portion was set to 1.25 mm. As a result, the height h (=T+R+S) of the auxiliary water outlet from the top plane of the edge guide was 2.5 mm.
Example 2 was carried out in the same manner as in Example 1, provided that the bottom part of the curvature radius R of he curved portion was changed to 2 mm.
Example 3 was carried out in the same manner as in Example 1, provided that the bottom part of the curvature radius R of the curved portion was changed to 0.5 mm.
Example 4 was carried out in the same manner as in Example 1, provided that the bottom part of the curvature radius R of the curved portion was changed to 3 mm.
Comparative Example 1 was carried out in the same manner as in so Example 1, provided that the bottom part of the curvature radius R of the curved portion was changed to 4 mm.
Comparative Example 2 was carried out in the same manner as in Example 1, provided that the bottom part of the curvature radius R of the curved portion was changed to 0.4 mm.
Comparative Example 3 was carried out in the same manner as in Example 1, provided that the bottom part of the curvature radius R of the curved portion was changed to 0.3 mm.
The evaluation results of Examples 1 to 4 and Comparative Examples 1 to 3 are presented in Table 1. Moreover, the flow rate distributions of the width direction of the curtain films are depicted in
In Examples 1 to 4, the auxiliary water was ejected desirably, and the curtain film was also formed almost uniformly.
In Comparative Example 1, the auxiliary water was ejected desirably, but the curtain film was thinned in the area adjacent to the edge guide. This was caused probably because the height h of the auxiliary water outlet from the top plane of the edge guide was 5.5 mm in Comparative Example 1, and the curtain film received the influence of the boundary layer in the area between the auxiliary water outlet and the top plane of the edge guide.
In Comparative Example 2, the ejection of the auxiliary water was slightly disturbed, and the curtain film was thinned in the area adjacent to the edge guide.
In Comparative Example 3, the auxiliary water was not ejected uniformly in the width direction. This was caused probably because a centrifugal force affected the flow of the auxiliary water, as the curvature radius at the bottom part of the curved portion of the slit was small.
Moreover, a flow rate distribution in the width direction was measured. As a result, the result was matched to the result of the visual observation, as depicted in
It was found from the results above, the curvature radius R at he bottom part of the curved portion of the slit was 0.5 mm to 3 mm, preferably 2 mm or smaller.
In order to make clear a relation ship between the height h of the auxiliary water outlet from the top plane of the edge guide and uniformity of the curtain film, in Experiment 2, the edge guide auxiliary water was ejected using the edge guide whose h was varied, and the ejection state was confirmed. Moreover, a curtain film was formed under the experiment basic conditions, and a flow rate distribution of the curtain film in the width direction was measured.
In Example 5, the curvature radius Rat the bottom part of the curved portion was set to 0.5 mm, the gap S of the slit was set to 0.2 mm, and the thickness T of the thinnest part of the trapezoidal portion was set to 0.8 mm. As a result, the height h (=T+R+S) of the auxiliary water outlet from the top plane of the edge guide was 1.5 mm.
Example 6 was carried out in the same manner as in Example 5, provided that T was changed to 4.3 mm (h=5 mm).
Comparative Example 4 was carried out in the same manner as in Example 5, provided that T was changed to 5.3 mm (h=6 mm).
Note that, in the case where the thickness T is 0.8 mm or less, there is problem in processing. Therefore, such example was not carried out. When the thickness T of the thinnest part is 0.8 mm, the conditions thereof are identical to those of Example 5.
The evaluation results of Examples 5 and 6, and Comparative Example 4 are depicted in Table 2. Moreover, the flow rate distribution of the curtain film in the width direction is depicted in
In Example 5, the auxiliary water was ejected desirably, and the flow rate distribution of the curtain film in the width direction was less than 105% in the entire width, which was no problem.
In Example 6, the auxiliary water was ejected desirably, the flow rate distribution of the curtain film in the width direction was 105% or greater but less than 110% in the entire width, and a slightly thick film part was present. However, this degree of the thickness was not a problem on practical use after subjecting to a treatment, such as blowing off the edges of the coating film.
In Comparative Example 4, the flow rate distribution of the curtain film in the width direction was 110% or greater in the entire width, and the curtain film was thickened in the areas adjacent to the edge guides. This was caused probably because the curtain film received the influence of the boundary layer in the aforementioned areas, as the height h of the auxiliary water outlet from the top plane of the edge guide was 6 mm in Comparative Example 4.
It was found from the results above that the height h of the auxiliary water outlet from the top plane of the edge guide was 1.5 mm to 5 mm.
Table 3 is presented below.
The present invention exhibits an effect when a liquid having relatively high viscosity, such as an adhesive, is used. In order to make clear an effect of the present invention with a difference in viscosity characteristics of the coating liquid, therefore, a curtain film was formed with varying the viscosity of the coating liquid under the experiment basic conditions, and a film thickness of the curtain film was observed.
As for a shape of the edge guide, the edge guide identical to the one in Example 1 was used.
In Test Example 1, the viscosity η1 at the shear rate of 1 sec−1 was set to 3,000 (mPa·sec), and the viscosity η2 at the shear rate of 1,000 sec−1 was set to 300 (mPa·sec).
In Test Example 2, the viscosity rp at the shear rate of 1 sec−1 was set to 300 (mPa·sec), and the viscosity η2 at the shear rate of 1,000 sec−1 was set to 10 (mPa·sec).
In Test Example 3, the viscosity rp at the shear rate of 1 sec−1 was set to 3,200 (mPa·sec), and the viscosity η2 at the shear rate of 1,000 sec−1 was set to 300 (mPa·sec).
In Test Example 4, the viscosity η1 at the shear rate of 1 sec−1 was set to 250 (mP·sec), and the viscosity η2 at the shear rate of 1,000 sec−1 was set to 10 (mPa·sec).
The evaluation results of Test Examples 1 to 4 are depicted in Table 4.
In Test Examples 1 and 2, a curtain film was formed almost uniformly.
In Test Example 3, it was difficult to eject the liquid, as the viscosity thereof was high, and therefore a curtain film could not be formed.
In Test Example 4, a curtain film was formed almost uniformly, but this was because an influence of a boundary layer became small when the viscosity was low, and a ratio of thinning the curtain film was small. In the case where the viscosity is low, therefore, an effect of the present invention is small. As the dripping of the liquid was caused at the time when the operation was terminated, it was considered that there was a problem for use on the operation.
It was found from the results above that, as for the viscosity characteristics of the coating liquid, which exhibited the effect of the present invention, the viscosity η1 at the shear rate of 1 sec−1, and the viscosity η2 at the shear rate of 1,000 sec−1 were respectively 300≦η1≦3,000 (mPa·sec), and 10≦η2≦300 (mPa·sec). Specifically, even in the case where a coating liquid having a strong shear viscosity reducing effect is used, a curtain film having a uniform film thickness can be attained without being influenced by a boundary layer, by using the slot curtain coating apparatus and slot curtain coating method of the present invention.
The slot curtain coating apparatus and slot curtain coating method of the present invention can be suitable used, for example, for productions of an adhesive label to which an adhesive has been applied, a silver halide photographic photosensitive material, a magnetic recording material, pressure sensitive or heat sensitive recording paper, art paper, coated paper, and an inkjet recording sheet.
The embodiments of the present invention are, for example, as follows:
<1> A slot curtain coating apparatus, including:
an ejecting unit containing a coating liquid outlet configured to eject a coating liquid;
a pair of guiding units, each containing an auxiliary water outlet configured to eject auxiliary water, where the guiding units are configured to support both edges of a curtain film, which is formed of the coating liquid ejected from the coating liquid outlet, along a width direction that is substantially vertical to a flow-down direction of the curtain film, and to guide the curtain film onto a support to be transported; and
a transporting unit configured to transport the support,
wherein the guiding unit has a manifold portion configured to retain the auxiliary water, and a slit portion connecting between the manifold portion and the auxiliary water outlet,
wherein the slit portion is composed of a straight-line portion, and a curved portion configured to eject the auxiliary water substantially vertically downwards, and
wherein the curved portion is provided to a position at which h=T+R+S is 1.5 mm to 5 mm, where T is a thickness of the thinnest part of a top part of the curved portion, R is a curvature radius of a bottom part of the curved portion and is 0.5 mm to 3 mm, S is a gap of the slit portion, and his a height of the auxiliary a outlet from a top plane of the guiding unit.
<2> The slot curtain coating apparatus according to <1>, wherein the straight-line portion forms an angle of 30° to 60° with the top plane of the guiding unit.
<3> A slot curtain coating method, containing;
ejecting a coating liquid from a coating liquid outlet;
supporting both edges of a curtain film, which is formed of the coating liquid ejected from a coating liquid outlet, by a pair of guiding units each containing an auxiliary water outlet configured to eject the auxiliary water, along a width direction that is substantially vertical to a flow-down direction of the curtain film, and guiding the curtain film onto a support to be transported, and
transporting the support,
wherein the guiding unit has a manifold portion configured to retain the auxiliary water, and a slit portion connecting between the manifold portion and the auxiliary water outlet,
wherein the slit portion is composed of a straight-line portion, and a curved portion configured to eject the auxiliary water substantially vertically downwards, and
wherein the curved portion is provided to a position at which h=T+R+S is 1.5 mm to 5 mm, where T is a thickness of the thinnest part of a top part of the curved portion, R is a curvature radius of a bottom part of the curved portion and is 0.5 mm to 3 mm, S is a gap of the slit portion, and his a height of the auxiliary water outlet from a top plane of the guiding unit.
<4> The slot curtain coating method according to <3>, wherein the straight-line portion forms an angle of 30° to 60° with the top plane of the guiding unit.
<5> The slot curtain coating method according to any of <3> or <4>, wherein the coating liquid is a fluid that reduces apparent viscosity thereof as a shear rate increases, and satisfies:
300≦η1≦3,000 (mPa·sec), and
10≦η2≦300 (mPa·sec)
where η1 is a viscosity of the coating liquid at a shear rate of 1 sec−1, and η2 is a viscosity of the coating liquid at a shear rate of 1,000 sec−1.
<6> The slot curtain coating method according to any one of <3> to <5>, wherein the coating liquid is an acryl emulsion-based adhesive.
This application claims priority to Japanese application No. 2013-053145, filed on Mar. 15, 2013 and incorporated herein by reference.
| Number | Date | Country | Kind |
|---|---|---|---|
| 2013-053145 | Mar 2013 | JP | national |
