Search Images Maps Play YouTube News Gmail Drive More »
Sign in
Screen reader users: click this link for accessible mode. Accessible mode has the same essential features but works better with your reader.

Patents

  1. Advanced Patent Search
Publication numberUS3690910 A
Publication typeGrant
Publication dateSep 12, 1972
Filing dateJan 19, 1971
Priority dateMay 4, 1965
Also published asDE1629324A1
Publication numberUS 3690910 A, US 3690910A, US-A-3690910, US3690910 A, US3690910A
InventorsDevillas Jean-Luc, Letourneur Gilbert, Mahe Yves
Original AssigneeCellophane Sa
Export CitationBiBTeX, EndNote, RefMan
External Links: USPTO, USPTO Assignment, Espacenet
Coating process for regenerated cellulose film
US 3690910 A
Images(2)
Previous page
Next page
Description  (OCR text may contain errors)

Sept. l2, 1972 v MAHE l-rrAL 3,690,910

COATING PROCESS FOR REGENERATED CELLULOSE FILM Filed Jan. 19, 1971 2 Sheets-Sheet 1 GILBERT LETOURNEUR JEAN-LUC DEVILLAS Y. MAHE ET AL Sept. l2, 1972 COATING PROCESS FOR REGENERATED CELLULOSE FILM Filed Jan. 19, 1971 2 Sheets-Sheet 2 W m f www@ OHM/MMU B Wmmm YGIU :United States Patent O Inf. ci. ima 1/16 U.S. Cl. 117-7 6 Claims ABSTRACT oF THE DISCLOSURE A process yfor coating a Water-absorbent support, e.g., regenerated cellulose films, with an aqueous solution or dispersion whereby the support poses little or no tendency to roll up upon itself, which comprises coating the support with such aqueous solution or dispersion along its entire width on both faces successively and without intermediate drying, the support, after being coated on one face traveling over a supported path which is of suficient length to permit the deposited coating to reach a degree of coalescence so that the coating will not be altered by passage of a detour roll; coating the second face while allowing coalescence thereof in substantially the same manner, and drying the coated support.

This application is a continuation-in-part of application Ser. No. 544,219 filed Apr. 21, 1966, now abandoned.

The present invention is directed to a process for coating of water-absorbent supports and more particularly to a process for coating such supports, eg., regenerated cellulose films, from an aqueous solution or dispersion.

In general, it is known to coat water-absorbent supports such as regenerated cellulose films, with suitable products in aqueous solutions or dispersions. Such a process ordiwith a rigorously constant thickness and as slight as de-V sired.

Such a procedure, however, suffers from various serious drawbacks. With the individual coating of the faces of the support material with intermediate drying, there is a great tendency for the support to roll up upon itself lengthwise immediately yafter each coating operation and inside the driers.

In order to employ this process on a commercial scale, therefore, it has been necessary to leave an uncoated zone of about 25 mm. in width on each edge of both faces of the support material. In this way, the support keeps a suiiicient degree of atness to be treated, but after it has been dried twice, the uncoated edges become fragile and brittle. This frequently results in the starting of tears lwhich hinder winding and make it necessary to take precautions which limit the feed rate. In any event, losses from cutting the uncoated edges are considerable and costly. For these reasons it has long been the desire of the coating industry lto provide a process forthe coating of t ICC such water-absorbent supports by a process which will substantially eliminate this costly loss of materials and accompanying reduction in quality of the product which is prepared.

It has now been found that it is possible to eliminate the various drawbacks of such previously employed processes by employment of the process of the present invention wherein a water-absorbent support is coated all along its width with an aqueous composition on its two faces successively and without intermediate drying.

Additionally, it has not been possible until this development of the present invention, for the reasons indicated above, to proceed from spinning to coating of regenerated cellulose films, i.e., coating directly on freshly made film coming from the dryer. The present invention makes it possible to apply such a process thereby bringing about considerable saving.

It is therefore a principal object of the present invention to provide a process for coating water-absorbent supports which are free from the drawbacks and deliciencies present in previously employed processes.

It is a further object of the present invention to provide a process for coating a water-absorbent support, such as a regenerated cellulose film, in which there is no tendency for loss of materials or for the rolling up of the lm length upon itself.

It is yet a further object of the present invention to provide a process for the coating of water-absorbent supports in which the support is coated all along its width on its two faces successively and without intermediate drying.

Still further objects and advantages will become more apparent from the following more detailed description of the present invention and accompanying drawings.

By the proecss of the present invention, a suitable waterabsorbent film, eg., a regenerated cellulose `film, is coated all along its width with a suitable aqueous solution or dispersion on its two faces successively and without intermediate drying. The support after being coated on one of its faces, travels between the lirst and second coating stand, or station along a rather long supported path to permit the deposited varnish to reach a suflicient degree of coalescence so that it will not be altered by passage on a detour roll.

Under the effect of the lirst coating, the water-absorbent support reacts by presenting a tendency to roll up on itself lengthwise. It is essential to oppose this tendency for the entire period of time that is necessary for the water contained in the coating composition to penetrate the interior of the water-absorbent support. The tensions balance each other during this time, and the tendency of the support to roll up on itself decreases considerably. At the same time as the penetration of the water into the support, the particles in dispersion accumulate on the surface of the support and dry. A time comes when the coated surface presents a sufficient coalescence so that it can come into contact with the detour roll without being altered. It is then possible to proceed to the coating of the reverse side without prior drying. This coating causes a tendency of the support to roll up on itself lengthwise in the opposite direction, a tendency opposed in part by the wetting caused by the first coating, but which also has to be opposed by supporting the other face during the time necessary for the tensions to balance each other. The coating support can then go into a drier without diiculty where a drying is carried out, preferably balanced on both faces. The support may then be removed.

This process, therefore, consists in replacing the first drying by a coalescence operation carried out on a supported path and in also employing a second traveling on a supported path after the second coating. By the process of this invention, it is possible to attain a sufficient degree of fiatness during the operation without loss of edges which are also coated, and to obtain thereby a better output. Another advantage of the process lies in the simplification and savings involved in the elimination of the first drying. Finally, it makes it possible, due to the fact that there is only one drying, to obtain a better balanced film.

The depositing of the coating in accordance with the present invention can be carried out according to conventional coating processes and the amount of coating deposited can be regulated by known means in the art, for example, by an air jet doctor, etc.

The tendency to roll which is possessed by regenerated cellulose films results from the unsymmetrical taking up of Water undergone by the absorbing material when only one of its faces is wetted, the other remaining dry. The rolling occurs in such a way that the wet face envelops the dry face.

The tendency to roll is accentuated by the fact that the regenerated cellulose film is a molecularly oriented material. Its crosswise expansion capacity when it is wetted with water reaches 10% between the edges, while, the crosswise expansion capacity of ordinary paper is only 1% under the same conditions.

The purpose of the intermediate rollers according to the present invention is therefore to support the freshly coated film and to prevent it from rolling up on itself.

Since the film totally lacks rigidity by itself to a greater extent than paper, for example, the support rollers also have to produce an uncreasing effect. For this reason, spreading rollers, preferably, positively driven, are utilized in accordance with the present invention to produce a spreading effect.

The gap between the spreading rollers used in the present invention should be smaller for slower machines than for fast machines. These rollers should be closer together when the film has just been wetted, i.e. immediately after the coating station rather than farther from it, because the tendency of the film to roll up on itself decreases as it absorbs water, Finally, the gap between these rollers can be greater when the -back of the film has already been coated, i.e., after the second coating station.

It is noted that the coat cellulose films with aqueous compositions, with a vinylidene chloride base, for example, the minimal time to obtain coalescence of the coating is 3 to 4 seconds. Accordingly the time for passage of the coated film over the suggested path is at least 3 seconds, there being no disadvantage to continuing passage after coalescence of the coating.

Coating of cellulose films is performed at speeds which can be between 30 meters and 300 meters per minute (.5 to 5 meters per second). The minimal distance that the cellulose film has to travel to reach its coalescene is therefore 2 m. for the slowest machines and can reach 20 m. for the fastest machines.

This travel should be supported, according to the present invention, by a number of rollers arranged closer together as the speed is slower, i.e., the distance between rollers being proportional to the speed of advancement of the film, these rollers being, as indicated above, closer together near the coating station.

The number of necessary spreading rollers between the first coating station and the second is between rollers, spaced an average of 25 to 30 centimeters apart for coalescence travel of 2 to 3 m. which corresponds to slow speeds, and 30 rollers, spaced an average of 50 to 70 centimeters apart for a travel f 30 meters corresponding to the fast speeds.

After coating of the back side, the coalescence of the coating deposited on the second face should beobtained before the film goes into the vertical dryer. As in the case of coating the front side and in the same way, the travel should be supported by spreading rollers overau equivalent length, the spacing of the rollersbeing slightly less if desired, the number of rollers being reduced about 10% for the same length.

Referring now to the accompanying drawing:

FIG. 1 schematically illustrates a coating device embodying the present invention.

FIG. 2 schematically illustrates spreading or enlarging rollers useful in accordance with the present invention.

A water-absorbent film 2 is unwound from a reel 4 and after passing aroundl'a plurality of guide rolls 6, is coated at the time ofV its passage in coating stand 8 with an aqueous dispersion the thickness of which is regulated by a pneumatic doctor 10. The film then passes overa number of guide rolls 12 over a sufficiently long path to permit the water contained in the coating composition to penetrate inside the film while `the surface coat reaches the desired degree of coalescence.

The reverse side of the film is then coated, on a coating stand 14 with an identical or somewhat different composition, the thickness of which is regulated by pneumatic doctor 16, while the face ofthe film which underwent the first coating passes over detour roll 18. The film then passes over a number of guide rolls 20 which make it follow a sufiiciently long path to permit the water of the second emulsion to penetrate the inside of the support. The coated film then goes into the drier 22 Where it follows a vertical upward path. Then, after passing around guide drum 24 the film follows a downward path. During these travels, hot air, shown by arrows 26, is blown on each of its faces.

Following its course through the drier, the coated film passes over cold rolls 28 before being wound around reel 30 for ultimate storage or use. Although the film can be dried in any suitable drier, it is preferable to employ a pulsed air drier, the draft of which acts symmetrically on both faces of the film.=A balanced drying and an excellent degree of fiatness are thereby obtained.

FIG. 2 schematically illustrates the type of spreading rollers preferably utilized in accordance with the present invention. In FIG. 2, spreading or enlarging rollers 41 are positively driven in the directions indicated by suitable driving means (not shown). The regenerated cellulose film 2 passes over the spreading or enlarging rollers 41 with the width of the film to be increased upon passage of the film over the spreading or enlarging rollers 41. The width B designates the width of the film 2 before passing over spreading or enlarging rollers 41 while width A designates the Width thereafter. By utilizing such spreading or enlarging rollers 41 as. support or guide rollers 12 and 20, the rigidity of the film is maintained and an uncreasing effect is achieved through passage of the film over the support rollers.

While the process of the present invention has been described particularly with respect to the regenerated cellulose film, it is to be understood that the invention is not limited thereto butin actuality any water-absorbent support capable of absorbing water sufficiently rapidly, can be advantageously employed. Thus, for example, suitable supports can include hydroxyethyl cellulose films, films of carboxymethyl cellulose, cellulose ether films, paper of various varieties and many other various materials, it again only being necessary that such material have a fairly substantial degree of water-absorbency.

Similarly, it is possible to deposit on such water-absorbent supports all products that can be dispersed or dissolved in water. Especially suitable are film-forming resins and particularly, waterproofing resin with a copolymer base having a large proportion of vinylidene chloride to which may be added other monomers, for example, lower alkyl acrylates, lower alkyl methacrylates, unsaturated acids, vinyl esters e.g., vinylchloride, vinyl acetate or acrylonitrile, etc.

The process of the present invention is particularly suitable for the waterproofing of water-absorbent films,

eg., regenerated cellulose films, and for making them thermosealable. In particular, in the preferred embodiment of the present invention, such a support is coated with an aqueous solution or dispersion of polyvinylidene chloride or a copolymer of vinylidene chloride and one of the various other monomers set forth above.

- The following examples illustrate the'process of theY present invention. It is to be understood that the examples are for purposes of illustration only, and the invention is in no way deemed to be limited thereto.

EXAMPLE I A regenerated cellulose film 1/2 meter in width is coated at a first coating stand with an aqueous dispersion of polyvinylidene chloride, the coating material comprising about 30% solids. Using such a dispersion, it is possible to deposit without any diiiiculty, from 20-25 gr. of the coating composition per square meter, corresponding to approximately 7-8 gr. of the solid material per square meter per face of support. With subsequent experimentation, it is found that although these amounts could possibly be reduced to about 4.55 gr. of composition per square meter, i.e., about 1.5 gr. of solid material per square meter per face, it is not advantageous to reduce these amounts too much because it becomes necessary to bring the coating roll extremely close to the doctor and to increase greatly the air pressure of the latter.

Similarly it is found that it is advisable not to reduce too much, i.e., below about -20%, the proportion of the solid materials in the coating composition. When too great a proportion of water is employed, there is a possibility of slight shrinkage of the support in the drier and an accompanying increase of the weight per square meter for the same amount of coating.

After the excess coating from the first stand is removed by the doctor, the coated film is passed over a number of guide rolls, the passage being sufficient to allow penetration into the film and coalescence of the coating material. At a rate of approximately 40 meters per minute, some 10 guide rolls, spaced approximately 0.30 meter apart, are utilized in such operation.

The cellulose film support is then coated on the reverse face with a composition and amount that is the same as employed in the first coating operation. Here again, excess is removed by a doctor and the film is passed over guide rolls of a similar arrangement as used previously. The coated film is then passed into a pulsed air drier Where it moved first upwardly and then downwardly, pulsed air being symmetrically applied to both faces of the support. The dried film is then wound upon a reel for storage or further use.

This procedure is accompanied by no noticeable loss of materials since coating is performed along the entire width of the support, and no rolling up of the support lengthwise or cracking or tearing of the support along the edges, is observed. The material, also, is found to possess excellent waterproof properties and possesses an excellent degree of lasting flatness.

EXAMPLE II The procedure of Example I is repeated except that the coating composition consists of an aqueous dlspersion of a copolymer of 92% vinylidene chloride and 8% methyl methacrylate and the coating is applied at a rate of approximately 90 meters per minute, with 15 rollers spaced a distance of 0.40 m. apart being utilized. Here agam there is no tendency for the film to roll up upon itself lengthwise, nor is any cracking or tearing of the support observed.

What is claimed is:

1.A process for coating a regenerated cellulose film with an aqueous composition which consists essentially of:

(l) coating said regenerated cellulose film across the entire width of a first face with a first film-forming aqueous composition;

(2) passing said regenerated cellulose film coated in step (l) over a supported path at a speed of from about-30 to 300 meters per minute for a period of at least three seconds, whereby the coating on said first face reaches a degree of coalescence, without drying, so that said coating will not he altered by passage of a detour roll, said supported path comprising a plurality of rollers which stretch said regenerated cellulose film in the width direction, said rollers being spaced from each other by a distance of from 30 to 70 centimeters;

(3) passing said film from step (2) over a detour roll and thereafter coating said regenerated cellulose film across the entire width of the second face with a second film-forming aqueous composition;

(4) passing said film lfrom step (3) over a supported path at a speed of from about 30 to 300 meters per minute for a period of at least three seconds, whereby the coating on said second face coalesces, said supported path comprising a plurality of rollers which stretch said regenerated cellulose film in the Width direction, said rollers being spaced from each other by a distance of from 30 to 70 centimeters; and

(5) thereafter drying said regenerated cellulose film.

2. The process of claim 1 wherein said first and second film-forming aqueous compositions are the same.

3. The process of claim 2 wherein said first and second film-forming aqueous compositions comprise an aqueous solution or dispersion of a homopolymer or coplymer of vinylidene chloride.

4. The process of claim 1 wherein said first and second film-forming aqueous compositions are different.

5. The process of claim 4 wherein one of said first and second film-forming aqueous compositions comprises au aqueous solution or dispersion of a homopolymer or copolymer of vinylidene chloride.

6. The process of claim 1 wherein the distance between said rollers in steps (2) and (4) is directed proportionally to the speed of passage of said film over said supported path.

References Cited UNITED STATES PATENTS 2,325,798 8/1943 Porter 117--68 2,406,057 8/ 1946 Barrett et al. 118--224 X 2,402,860 6/ 1946 Wilckens 117-68 3,404,660 10/ 1968 Sievers 11S-34 3,320,086 5/1967 Rose et al 117-68 WILLIAM D. MARTIN, Primary Examiner T. G. DAVIS, Assistant Examiner

Referenced by
Citing PatentFiling datePublication dateApplicantTitle
US3983201 *Jun 9, 1972Sep 28, 1976Fmc CorporationMethod of preparing a lacquer coated regenerated cellulose film with an intermediate layer of hydroxyalkyl cellulose
US4287217 *Aug 4, 1978Sep 1, 1981Hoechst AktiengesellschaftMultiple-layer tubing
US6168661Oct 23, 1998Jan 2, 2001Johnson Controls Technology CompanyBattery cell coating apparatus and method
US6680084Jun 12, 2000Jan 20, 2004Simex Technologies Inc.Formation of oriented multilayer polymeric films
US7799170Mar 9, 2005Sep 21, 2010Metso Paper, Inc.Method and device in a paper or board machine line for straining paper
WO2000025375A1 *Nov 4, 1998May 4, 2000Johnson Controls Tech CoBattery cell coating apparatus and method
WO2001096661A1 *Jun 1, 2001Dec 20, 2001Simex Technologies IncFormation of oriented multilayer polymeric films
WO2005088008A1 *Mar 9, 2005Sep 22, 2005Kari HolopainenMethod and device in a paper or board machine line
Classifications
U.S. Classification427/173, 427/412.2, 427/389.9
International ClassificationB05D3/04, B05D7/04, D06B15/09, D06B15/00, B05C9/08
Cooperative ClassificationB05D7/04, D21H23/72, D21H5/0052, B05D3/0413, D06B15/09, B05D2252/10
European ClassificationD21H23/72, D21H5/00C16B, B05D3/04C3, D06B15/09, B05D7/04