EP0567071A1

EP0567071A1 - Curtain coating method

Info

Publication number: EP0567071A1
Application number: EP93106385A
Authority: EP
Inventors: Yasushi Suga; Tetsuo Kajiwara; Kiyoshi Kobayashi
Original assignee: Fuji Photo Film Co Ltd
Current assignee: Fujifilm Holdings Corp
Priority date: 1992-04-21
Filing date: 1993-04-20
Publication date: 1993-10-27
Anticipated expiration: 2013-04-20
Also published as: JP3552113B2; JPH05293429A; EP0567071B1; DE69319371T2; DE69319371D1

Abstract

A coating method in which an auxiliary liquid, flowing onto upper surfaces of guide plates and having higher surface tension and lower viscosity than a coating film, is joined with both edges of a coating film which flows on a slide surface of a die to be supported by the guide plates. The coating film free falling from the slide surface along edge guides collides with a running web so as to coat the web with the coating film, wherein the auxiliary liquid is poured from a position on a distance of not more than 10 mm from a boundary line between the guide plates and the edge guides in a side of the guide plates.

Description

BACKGROUND OF THE INVENTION

The present invention relates to a curtain coating method by a slide hopper, and particularly to a coating method which eliminates unevenness of coating thickness produced in both edge portions of a coating film which is formed by causing a free falling coating film to collide with a web running continuously.
As conventional coating methods for eliminating unevenness of coating thickness produced in both edge portions of a coating film which is formed by causing a free falling coating film to collide with a web running continuously, it is provided that a method for eliminating the unevenness by means of supplying an auxiliary liquid between a coating film and guide plates for making even both edges of the coating film on a slide surface or between a coating film and edge guides for supporting both edge portions of a free falling coating film. For example, there are (1) a multiple layers coating method by free falling films, in which a film width of at least one layer is wider than the other layers (Japanese Patent Examined Publication No. Sho-62-47075); (2) a coating method pouring an auxiliary liquid having a lower surface tension than a coating film at both edge portions of a slide surface (Japanese Patent Unexamined Publication No. Sho-64-144378); and etc.
However, in a case where the free falling liquid film is formed by a slide hopper in the method (1), it is difficult to form an even film because of the surface tension difference between front and reverse sides of a free falling coating film contacting with the guide edge.
The reason is that the surface tension σ₂ of the reverse side is dynamic surface tension with high and the surface tension σ₁ of the front side is substantially static surface tension because of a time lapse difference of the surface under effect of a surface active agent in the coating liquid, instead it seems that an unbalance is occurred due to the surface tension difference between the front and reverse sides.
In a case where the free falling liquid film is formed in the method (2), because an auxiliary liquid being lower in surface tension than a coating liquid is poured, the liquid at the both edge portions near the edge guides is attracted to the center of a coating film because of the surface tension difference between the coating liquid and the auxiliary liquid, so that it is not able to form an even film. The above problems and such have been produced.

SUMMARY OF THE INVENTION

It is therefore an object of the present invention to solve the foregoing problems and provide a coating method by which a stable film forming is performed and the both edge portions of the coating film is formed relatively uniformly and stably.
The foregoing object of the present invention is attained by a coating method in which coating liquids ejected from a die are coated onto a running web as a coating film, said coating method comprising the steps of; pouring at least one layer of said coating liquid as the coating film on a slide surface of said die along guide plates for supporting both edge portions of said coating film; pouring an auxiliary liquid being higher in surface tension and lower in viscosity than said coating liquid, onto upper surfaces of said guide plates; joining said auxiliary liquid to said both edges of said coating film flowing on said slide surface; free dropping said coating film joined together with said auxiliary liquid along edge guides which succeed said guide plates and support the both edges of said free dropping coating film joined with said auxiliary liquid; and colliding said free dropping coating film with said running web so as to coat said web with said coating film; wherein said auxiliary liquid in said pouring step is poured from a position on a distance of not more than 10 mm from a boundary line between said guide plates and edge guides in a direction of said guide plates.
Further preferably, in the above coating method, a quantity of flow of said auxiliary liquid to be poured onto each of said guide plates is not more than 10 cc/min.
As a guide plate used in the present invention, in order to pour an auxiliary liquid 2 to the side of the coating film 1 on a slide surface, preferably an upper surface 4 of the guide plate 3 has an inclination of an angle ϑ=10° to 80° with respect to a slide plane 5 as shown in Fig. 2(B). In addition, an edge portion of the guide plate 3 on the slide surface side is provided with a wall of height h 0.5 to 5 mm perpendicular to the slide surface. The height h and inclination angle 0 may be set free within thus ranges.
Further, preferably portions where the guide plate 3 and an edge guide 6 are in contact with the coating film have a same shape each other in order to prevent a disturbance from being produced in the flow of the coating film in the boundary portion thereof.
Examples of material for the guide plate and the edge guide used in the present invention include stainless steel, vinyl chloride, acrylic resin, Teflon, or the like.
According to the present invention, the surface tension of the auxiliary liquid is higher than that of the coating film, so that there is no case where the auxiliary liquid is attracted to the center of a coating film to thereby make film coating unstable. Furthermore, a relation among the surface tension σ₃ of the auxiliary liquid, the static surface tension σ₁ of the coating film and the dynamic surface tension σ₂ of the coating film is expressed by σ₃>σ₂,σ₁, so that a stable film can be formed. Moreover, in the present invention, the auxiliary liquid is poured to the upper surface of a guide plate 3 with separation of a distance of not more than 10 mm in the direction of the guide plate from a boundary line 7 between the guide plate 3 and an edge guide 6 as shown in Fig. 2(A), so as to prevent that the uneven portions of the film broaden.
Furthermore, the present invention preferably sets the supplied quantity of the auxiliary liquid to be not more than 10 cc/min, so as to prevent that the uneven coating portion broadens and to perform an uniform coating.
The auxiliary liquid is continuously supplied from a pump to the upper surface of a guide plate 3 by means of a small tube, which end being in contact with the surface of the guide plate 3.

BRIEF DESCRIPTION OF THE DRAWINGS

Fig. 1 is a side view of a slide hopper type curtain coating apparatus of an embodiment for realizing the present invention.
Fig. 2(A) and Fig. 2(B) are plan and sectional views, respectively, of the periphery portion of a boundary between a guide plate and an edge guide of the embodiment for realizing the present invention.
Fig. 3 is a front sectional view for explaining a method for calculating the width wi of an uneven portion at an edge portion of a coating composition film relating to the present invention.

DESCRIPTION OF THE PREFERRED EMBODIMENT

The present invention will be described in accordance with the following examples.

(Example 1)

An alkali-treated gelatin solution (10 % by weight) containing sodium dodecylbenzene-sulfonate (0.15 % by weight) was thickened with sodium polystyrene-sulfonate so as to provide a viscosity of 55 cp and a surface tension of 32 dyne/cm. The solution thus prepared was used as a coating liquid.
As a coating method as shown in Fig. 1, a method of ejecting the coating liquid at the rate of 0.6 cc/cm·s from each of slits 9a, 9b and 9c of a slide hopper 8 for applying three layers simultaneously was used.
As an auxiliary liquid 2, a liquid having 2 cp viscosity, 37 dyne/cm surface tension and 4 cc/min supplied quantity was used. As a guide plate and an edge guide, a plate having an edge portion height h of 0.5 mm on a side of a slide surface and a guide having the angle ϑ of 45° between the upper surface of the guide plate and the slide surface were used respectively.
The position of a comparative example from which the auxiliary liquid was to be poured to the upper surface of the guide plate was set to the position B of Fig. 1 which was upper than the slot for the uppermost layer of the three layers to be coated simultaneously. The position, as an auxiliary liquid injection point in the present invention, from which the auxiliary liquid was to be poured to the upper surface of the guide plate was set to the position A which was at a distance of not more than 10 mm in the direction of the guide plate from a boundary line 7 between the guide plate and the edge guide. The regions of uneven coating in the above two cases of the comparative embodiment and the present invention were compared each other by each of the three layers. Results were shown in Fig. 3 and Table 1. Width wi of an uneven portion represents the width from a coating edge portion to a position corresponding to the thickness difference |Δdi|>0.03di (i=1,2,3,···) of a measured layer. Here di represents film thickness at the even portion of the measured layer. Table 1

auxiliary liquid injection point width of an uneven portion

lowermost layer intermediate layer uppermost layer

A

5 7 10

B 5 19 27
As shown in Fig. 3 and Table 1, in the case where the auxiliary liquid is poured at the position A according to the present invention, the uneven coating portion in the three layers could be limited to a range of not more than 10 mm from the coating edge portion. However, in the case where the auxiliary liquid was poured at the position B, the uneven coating portion in the three layers was broadened to a range of 27 mm from the coating edge portion.

(Example 2)

An alkali-treated gelatin solution (10 % by weight) containing sodium dodecylbenzene-sulfonate (0.15 % by weight) was thickened with sodium polystyrene-sulfonate so as to provide a liquid having viscosity of 60 cp and surface tension of 32 dyne/cm. The liquid thus thickened was used as a coating liquid.
As a coating method, a method of ejecting the coating liquid from each of three slits at the rate of 1.3 cc/cm·s by using a slide hopper for applying three layers simultaneously was used.
As an auxiliary liquid, a liquid having viscosity of 1 to 2 cp was used and injected from the above-mentioned position A while changing its surface tension into three cases.
In the case where the surface tension of the auxiliary liquid was 30 dyne/cm which was lower than the surface tension of the coating film of 32 dyne/cm, a free falling coating film was instable. However, in the cases where the surface tension of the auxiliary liquid was changed to 37 and 70 dyne/cm, a free falling coating film could be applied stably. Consequently, a stable free falling film could be formed by setting the surface tension of the auxiliary liquid to be higher than the surface tension of the coating film.

(Example 3)

The same conditions for the coating liquid and the coating method as in Example 2 were used. As an auxiliary liquid, a liquid having viscosity of 2 cp and surface tension of 37 dyne/cm higher than the surface tension of the coating liquid was poured from the above-mentioned position A as an auxiliary liquid injection point while the quantity of flow of the auxiliary liquid was changed successively to 5 cc/min and 20 cc/min. In the case of 5 cc/min, the width w₃ of the uneven portion was 5 mm, but in the case of 20 cc/min, the width w₃ was broadened to be 10 mm. It is to be understood from the above results that preferably the quantity of flow of the auxiliary liquid is set to be lower than 10 cc/min.
As is apparent from the above examples, the uneven coating portion at the edge portion of the coating film can be reduced due to the auxiliary liquid injection point, surface tension and pouring amount of the auxiliary liquid according to the present invention. It is possible to construct and coat a stable free falling film.

Claims

A coating method in which coating liquids ejected from a die are coated onto a running web as a coating film, said coating method comprising the steps of:
pouring at least one layer of said coating liquid as the coating film on a slide surface of said die along guide plates for supporting both edge portions of said coating film;
pouring an auxiliary liquid being higher in surface tension and lower in viscosity than said coating liquid, onto upper surfaces of said guide plates;
joining said auxiliary liquid to said both edges of said coating film flowing on said slide surface;
free dropping said coating film joined together with said auxiliary liquid along edge guides which succeed said guide plates and support the both edges of said free dropping coating film joined with said auxiliary liquid; and
colliding said free dropping coating film with said running web so as to coat said web with said coating film;
wherein said auxiliary liquid in said pouring step is poured from a position on a distance of not more than 10 mm from a boundary line between said guide plates and edge guides in a direction of said guide plates.
A coating method according to claim 1, wherein a quantity of flow of said auxiliary liquid to be poured onto each of said guide plates is not more than 10 cc/min.