US2186957A - Coating method - Google Patents

Coating method Download PDF

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Publication number
US2186957A
US2186957A US201753A US20175338A US2186957A US 2186957 A US2186957 A US 2186957A US 201753 A US201753 A US 201753A US 20175338 A US20175338 A US 20175338A US 2186957 A US2186957 A US 2186957A
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United States
Prior art keywords
coating
viscosity
sheet
solution
per cent
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US201753A
Inventor
William R Collings
John J Hoeltzel
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Dow Chemical Co
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Dow Chemical Co
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Priority to US201753A priority Critical patent/US2186957A/en
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Publication of US2186957A publication Critical patent/US2186957A/en
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Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H25/00After-treatment of paper not provided for in groups D21H17/00 - D21H23/00
    • D21H25/08Rearranging applied substances, e.g. metering, smoothing; Removing excess material
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H19/00Coated paper; Coating material
    • D21H19/10Coatings without pigments
    • D21H19/14Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12
    • D21H19/34Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12 comprising cellulose or derivatives thereof
    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H5/00Special paper or cardboard not otherwise provided for
    • D21H5/0005Processes or apparatus specially adapted for applying liquids or other fluent materials to finished paper or board, e.g. impregnating, coating
    • D21H5/006Controlling or regulating
    • D21H5/0062Regulating the amount or the distribution, e.g. smoothing, of essentially fluent material already applied to the paper; Recirculating excess coating material applied to paper

Landscapes

  • Paper (AREA)
  • Application Of Or Painting With Fluid Materials (AREA)

Description

Patented Jan. 16, 1940 UNITED STATES PATENT OFFICE 2,186,957 I COATING METHOD William RQCollings and John J. Hoeltzel, Midland, Mich., assignors to The Dow Chemical Company, Midland, Mich., a corporation of Michigan No Drawing. Application April 13, 1938,
Serial No. 201,753 1 1 Claim.
This invention relates to a method for uniformly coating paper and other fibrous materials, particularly embossed paper and the like.
In coating embossed paper and the llke'with 5 solutions of film-forming materials for the purpose of protecting the paper and for decorative eifect, it has been found desirable to employ the film-formingsolution in a comparatively narrow range of viscosity, as is pointed out in our concurrently filed co-pending application-Serial No.
201,742. When the film-forming solution is too fiuid,,it is found to be readily absorbed by the paper and does not deposit a glossyfilm. If, on the other hand, the coating solution is too viscous, its 1; application to an uneven surface, such as that of embossed paper, results in entrapping air bubbles in the depressions of the surface to be coated. The high viscosity of the so-deposited film prevents the air bubbles from rising to the surface prior to hardening of the film on the material.
When embossed paper, textiles, and similar materials, the surface of which is rough and uneven are to be coated, it is desirable to provide the entire surface with a uniform thin film of the protecting material. In order that the film be not discontinuous, the aforesaid desired results are] most economically obtained by extruding or castingv a thin web of the protecting material in the form of a solution having a high solids content,
and hence a high viscosity, on to the fibrous sheet.
It is accordingly an object of the present invention to provide a method'whereby a. uniform continuous protective coating may be applied to a fibrous material, such as embossed paper or textiles, from a high viscosity solution of ,such coating material.
We have found that the foregoing and other objects may be accomplished and that entrap- 40 ment of air bubbles beneath the coating film may be avoided, while at the same time providinga means whereby the composition is caused to penetrate the porous surface sufficiently to provide good adhesion between the material and the protective film, by spreading a layer of a viscous solution of the coating composition on a porous fibrous sheet, while subjecting the sheet to reduced pressure or vacuum. Such reduced pressure may be applied simultaneously with, or imgo mediately after, the application of the coating film to the sheet. Such procedure results in removing air bubbles from between the newly deposited film and the fibrous sheet, and draws a certain amount of the coating solution to a sufficient depth into the pores of the fibrous material to insure good penetration and adhesion of the coating composition to the treated surface. The method may be made continuous by drawing the sheet of fibrous material past the points at whcih the solution and the suction are applied.
Our method is particularly advantageous when employed in coating heavy paper stocks, such .as are used for the covers of catalogues, magazines,
. books, etc., since it provides a means of uniformly coating the paper while holding the same flat during the coating process. The deposition of a uniform coating obviates the heretofore existing difficulty of Warping inherent in old coating methods which deposited films of uneven thickness. I 15 Since the coating deposited by the method of r the. present invention is uniform, it emphasizes the decorative appearance of rough-textured or embossed papers by providing such surfaces with a uniform gloss which follows the contours of the 20 paper. Thus the normal shadow lines in an embossed paper stand out more clearly after application of a coating by means of the present method than before treatment. Modes of application not involving the herein-described vacuum 25 I method have almost invariably resulted in filling the depressions of embossed paper and the like with a thick deposit of the coating composition, while at the same time leaving the high spots of the paper surface only very thinly covered. 30 Such prior methods have had the effect of impairing rather' than enhancing the decorative effect of an embossed paper.
The herein-described method may be satisfac torily employed with coating compositions of 35 relatively high viscosity'as compared with those which are described in our aforesaid co-pending application. In fact, it is possible to produce a continuous and uniform coating according to the present method by employing a solution, the viscosity of which may vary from 50 to as high as 1000 seconds or more when tested by the fallingball method at 25" Q. (AJS, T. M. D301-33).
, In carrying out the method of the invention the coating composition in the form of a solution .of high solids content is preferably applied to a running sheet or web of fibrous material, which is supported horizontally. The application of such solution may be done in various ways For example, the web of fibrous material may be passed between rollers, at least one of which dips in a bath of the solution in the known manner. Another way is 'to extrude a film of the viscous solution upon the moving sheet from a hopper providedwith a transverse slot, the length of 56 Y which is the same as the width of the sheet to be coated. In a further modification the coating composition may be poured or dropped on or otherwise applied to the stock and evenly distributed by means of a doctor blade. The coating composition is ordinarily applied to the upper surface of the sheet just prior to applying the suction to the under surface of the sheet. This may be done by passing the sheet horizontally over a perforated plate or table which is connected to a vacuum pump, the degree of suction being adjusted to the material being coated and v the rate of travel of the sheet over the vacuum element. The moving sheet is then passed through a drier to remove the remaining solvent from the coating composition deposited thereon.
If desired, the coating composition and suction may be applied to the same surface of the sheet. thus making possible the use of a vacuum coating process for successively covering both surfaces of a fibrous material. We have'observed that when paper is drawn past a vacuum slot, the effective suction extends at least 0.25 inch beyond the slot. -Hence, if suction is applied by means of a perforated or slitted orifice at a point about 0.25 inch or less from the point at which the coating composition is being deposited on a fibrous material, and if the fibrous material is conveyed away from the point at which suction is applied past that at which the coating composiion is deposited, the same results are obtained as though the suction had been applied beneath the fibrous sheet while depositing the coating composition from above.
Suitable coating compositions, which we have employed and found satisfactory, are solutions of the cellulose derivatives, including both esters and ethcrs thereof. Examples of such materials are cellulose nitrate, cellulose acetate, cellulose aceto-butyrate, ethyl cellulose, ethyl-propyl cellulose, benzyl cellulose, benzyl-ethyl cellulose, and the like. Such compositions are applied in the form of a substantially clear solution having a viscosity in the range from about to about 1000 seconds, or higher, and preferably from about 350 to about 400 seconds, as determined at 25 C. by the falling-ball method. In the case of the water-insoluble cellulose ethers in the usual solvents for these materials, this viscosity range represents concentrations varying from about 10 to about per cent. By using a cellulose derivative which has a low intrinsic viscosity, it is possible to produce a low viscosity solution having a high solids content. Conversely, where the cellulose derivative has a high intrinsic viscosity, high viscosity solutions may have a low solids content.
The following examples define compositions which we have employed satisfactorily according to the herein-described method:
Example 1 4'7 grams of a cellulose acetate containing 40 per cent acetyl'groups is mixed with 20.1 grams of triphenyl'phosphate as a plasticizer and dissolved in 142 grams of a solvent consisting of 50 per cent acetone and 50 per cent dioxane, by
volume. The viscosity of the resulting solution is 370 seconds.
Example 2 45 grams of nitrocellulose (6 second R. S.) and 19.3 grams of dibutyl phthalate are dissolved in 135 grams of a solvent mixture consisting of 20 per cent butyl acetate, 10 per cent butyl alcohol. 10 per cent ethyl acetate, 10 per cent ethyl alcohol, 25 per cent toluene, and 25 per cent "troluoil, by volume. (Troluoil is a petroleum hydrocarbon distillate having an evaporation rate equivalent to that of toluene.) The viscosity of the resulting solution is about 350 seconds.
Example 3 grams of a medium viscosity benzyl cellulose and 23 grams of triphenyl phosphate is dissolved in 120 grams of a solvent consisting of 50 per cent toluene, 20 per'cent ethanol, and 30 per cent butyl acetate, by volume. This composition has a viscosity of 445 seconds.
Example 4 A white pigmented ethyl cellulose composition having a viscosity of about 250 to 300 seconds'was prepared as follows: Equal parts of ethyl cellulose and titanium oxide chips were mixed and dissolved to form a 30 per cent solution in a mixture of parts of toluene and 20 parts of per cent ethanol, by volume. A plasticizer, monophenyl-di-orthoxenyl phosphate, and a small amount of stearic acid were added and the resulting composition adjusted to the desired viscosity by the addition of a suitable amount of 30 per cent solution of a "70 centipoise" ethyl cellulose in an 80:20 toluenezethanol mixture. The solids in the final composition had the following approximate analysis:
Per cent Titanium oxide 8.8 Plasticizer 24.5 Ethyl cellulose 64.7 Stearic acid 2.0
tour of the surface variations of the paper, which consists in spreading a layer of a cellulose derivative solution, having a falling ball viscosity at 25 C. of between 350 and 400 seconds, upon a horizontally moving fiat sheet of embossed coverstock,
and immediately subjecting the embossed sheet to suction applied to the undersurface thereof,
whereby there is produced a uniformly coated,
non-warping paper having a uniform high gloss.
WILLIAM R.COLLINGS. JOHN J. HOELTZEL..
US201753A 1938-04-13 1938-04-13 Coating method Expired - Lifetime US2186957A (en)

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Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3047391A (en) * 1959-01-12 1962-07-31 Eastman Kodak Co Method of coating partially acetylated paper with plasticized cellulose ester and resulting paper coated with a photographic emulsion
US3057755A (en) * 1959-01-12 1962-10-09 Eastman Kodak Co Treatment of paper composed of partially acylated cellulose fibers
US3068116A (en) * 1959-01-12 1962-12-11 Eastman Kodak Co Manufacture of partially acetylated paper
US3133855A (en) * 1961-07-24 1964-05-19 Kimberly Clark Co Minimizing scratches in a blade coated paper web by roughening the smooth side of the web prior to the blade coating operation
US4045598A (en) * 1976-05-06 1977-08-30 Milliken Research Corporation Coating method and apparatus
EP0117054A1 (en) * 1983-01-17 1984-08-29 Unilever Plc Method and apparatus for coating paper and the like
WO1988004959A1 (en) * 1987-01-05 1988-07-14 Beloit Corporation Coating apparatus and method
US5447753A (en) * 1991-06-07 1995-09-05 Nippon Paper Industries Co., Ltd. Method of manufacturing coated paper for printing
US5660882A (en) * 1994-09-23 1997-08-26 Tredegar Industries, Inc. Vacuum assisted application of thin coatings on apertured substrates and articles produced therefrom
US6352744B1 (en) 2000-05-31 2002-03-05 Owens Corning Fiberglas Technology, Inc. Vacuum treatment of asphalt coating
US20030015209A1 (en) * 2001-07-06 2003-01-23 Gingras Brian James Method for wetting and winding a substrate
US20030113458A1 (en) * 2001-12-18 2003-06-19 Kimberly Clark Worldwide, Inc. Method for increasing absorption rate of aqueous solution into a basesheet
US6649262B2 (en) 2001-07-06 2003-11-18 Kimberly-Clark Worldwide, Inc. Wet roll having uniform composition distribution
US6866220B2 (en) 2001-12-21 2005-03-15 Kimberly-Clark Worldwide, Inc. Continuous motion coreless roll winder
US20100062186A1 (en) * 2008-09-10 2010-03-11 Peiffer Dennis G Ultra-thin polymeric membrane

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3047391A (en) * 1959-01-12 1962-07-31 Eastman Kodak Co Method of coating partially acetylated paper with plasticized cellulose ester and resulting paper coated with a photographic emulsion
US3057755A (en) * 1959-01-12 1962-10-09 Eastman Kodak Co Treatment of paper composed of partially acylated cellulose fibers
US3068116A (en) * 1959-01-12 1962-12-11 Eastman Kodak Co Manufacture of partially acetylated paper
US3133855A (en) * 1961-07-24 1964-05-19 Kimberly Clark Co Minimizing scratches in a blade coated paper web by roughening the smooth side of the web prior to the blade coating operation
US4045598A (en) * 1976-05-06 1977-08-30 Milliken Research Corporation Coating method and apparatus
EP0117054A1 (en) * 1983-01-17 1984-08-29 Unilever Plc Method and apparatus for coating paper and the like
WO1988004959A1 (en) * 1987-01-05 1988-07-14 Beloit Corporation Coating apparatus and method
US5447753A (en) * 1991-06-07 1995-09-05 Nippon Paper Industries Co., Ltd. Method of manufacturing coated paper for printing
US5660882A (en) * 1994-09-23 1997-08-26 Tredegar Industries, Inc. Vacuum assisted application of thin coatings on apertured substrates and articles produced therefrom
US5753342A (en) * 1994-09-23 1998-05-19 Tredegar Industries, Inc. Vacuum assisted application of thin coatings on apertured substrates and articles produced therefrom
US6352744B1 (en) 2000-05-31 2002-03-05 Owens Corning Fiberglas Technology, Inc. Vacuum treatment of asphalt coating
US20030015209A1 (en) * 2001-07-06 2003-01-23 Gingras Brian James Method for wetting and winding a substrate
US6649262B2 (en) 2001-07-06 2003-11-18 Kimberly-Clark Worldwide, Inc. Wet roll having uniform composition distribution
US6651924B2 (en) 2001-07-06 2003-11-25 Kimberly-Clark Worldwide, Inc. Method and apparatus for making a rolled wet product
US20050031779A1 (en) * 2001-07-06 2005-02-10 Kimberly Clark Worldwide, Inc. Wet roll having uniform composition distribution
US7101587B2 (en) 2001-07-06 2006-09-05 Kimberly-Clark Worldwide, Inc. Method for wetting and winding a substrate
US7179502B2 (en) 2001-07-06 2007-02-20 Kimberly-Clark Worldwide, Inc. Wet roll having uniform composition distribution
US20030113458A1 (en) * 2001-12-18 2003-06-19 Kimberly Clark Worldwide, Inc. Method for increasing absorption rate of aqueous solution into a basesheet
US6866220B2 (en) 2001-12-21 2005-03-15 Kimberly-Clark Worldwide, Inc. Continuous motion coreless roll winder
US20100062186A1 (en) * 2008-09-10 2010-03-11 Peiffer Dennis G Ultra-thin polymeric membrane

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