US2656286A - Process of coating paper webs and product thereof - Google Patents

Process of coating paper webs and product thereof Download PDF

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Publication number
US2656286A
US2656286A US613436A US61343645A US2656286A US 2656286 A US2656286 A US 2656286A US 613436 A US613436 A US 613436A US 61343645 A US61343645 A US 61343645A US 2656286 A US2656286 A US 2656286A
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Prior art keywords
starch
coating
water
paperboard
gloss
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US613436A
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Harry C Fisher
Brainard E Sooy
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Consolidated Water Power and Paper Co
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Consolidated Water Power and Paper Co
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Classifications

    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP 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
    • D21H19/00—Coated paper; Coating material
    • D21H19/80—Paper comprising more than one coating
    • D21H19/82—Paper comprising more than one coating superposed
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP 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
    • D21H19/00—Coated paper; Coating material
    • D21H19/10—Coatings without pigments
    • D21H19/12—Coatings without pigments applied as a solution using water as the only solvent, e.g. in the presence of acid or alkaline compounds
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP 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
    • D21H19/00—Coated paper; Coating material
    • D21H19/10—Coatings without pigments
    • D21H19/14—Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12
    • D21H19/34—Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12 comprising cellulose or derivatives thereof
    • D—TEXTILES; PAPER
    • D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21H—PULP 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
    • D21H19/00—Coated paper; Coating material
    • D21H19/36—Coatings with pigments
    • D21H19/44—Coatings with pigments characterised by the other ingredients, e.g. the binder or dispersing agent
    • D21H19/54—Starch
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/31504—Composite [nonstructural laminate]
    • Y10T428/31855—Of addition polymer from unsaturated monomers
    • Y10T428/3188—Next to cellulosic
    • Y10T428/31895—Paper or wood
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/31504—Composite [nonstructural laminate]
    • Y10T428/31971—Of carbohydrate
    • Y10T428/31975—Of cellulosic next to another carbohydrate
    • Y10T428/31978—Cellulosic next to another cellulosic
    • Y10T428/31982—Wood or paper

Definitions

  • the present specification relates to an additional development based on subsequent treating of the coated web in order to bring about a very glossy effect upon printing of the coated web with oil or varnish base inks.
  • a breaker stack of calender rolls which is the first stack of calenders used in general practice to smooth out a web of paper or paperboard as it comes from a paper or board machine, prior to sheeting or reeling the web.
  • a coating imprinting roll on which is spread a thin coating of mineral matter and starch in an aqueous base, the binder element of the mineral coating mixture perhaps including other adhesive and carrier agents, but in which starch is the principal one.
  • a drier including heated rolls over which the web passes after it has picked up its coating from the imprinting roll.
  • the web may be passed through one or more stacks of finishing calenders depending upon the surface finish desired.
  • the binder of the mineral coat is mainly starch
  • an aqueous solution to the web while it passes through the breaker stack of calender rolls which contains, for example, urea formaldehyde resin in its syrupy stage of incomplete polymerization.
  • melamine resin or other resin substances having the quality of insolubilizing starch in the presence of a catalyst.
  • the imprinting roll is supplied, as set forth in the said specification, with a mineral matter coating mixture in an aqueous base, the binder consisting mainly of starch.
  • a coating of adhesive and mineral pigment containing 54% solids and 46% water was used, and spread onto the imprinting roll which was in turn coated by means of a gate roll, taking the mixture from a supply, and by spreading rolls in a series from the gate roll to the imprinting roll, operating similarly to the mode of supplying ink to the inking roll of a rotary printing press.
  • the film on the imprinting roll was, and indeed must be, quite thin or else the operation will not be a success due to treeing, patterning, etc.
  • a coating picked up by the web while still moist from its treatment in the calender stack of a film of around .001" thick, more or less, of the wet coating mixture.
  • the web After the web has passed the imprinting roll it moves to the heated driers where the reaction which insolubilizes the starch is completed.
  • the whole process can be timed to take the product from a board machine or paper machine using standard drier rolls so as to be fully continuous.
  • the coated board itself when finished and-before printing, does not differ markedly in outer appearance over board which does not have the final treatment which we will discuss in more detail, and the difference appears only in the result of the oil or varnish base: ink printing.
  • ink printing For convenience we will refer to the substance applied over the coated surface as a sealer. It dries out on the coated surface of'board.
  • Each of these substances as applied to the coated surface of the web is a minute film or filling in andon the waterproof coated surface to seal and reduce or eliminatethe comparatively porous or absorbent surface of the coating thus to prevent the absorption ofvehicleand/or ink from the printing ink down into the coated surface.
  • those substances be film-formers in the strictest sense of the word providing that they do fill in the coated surface to reduce its absorptivity to the subsequently applied ink. While it is unlikely that any substance used, as described, will be soluble in the base or vehicle of the ink, we note that such solubility must be absent or at least be negligible '4 in effect if the printing ink is to remain substantially unabsorbed into the coated surface.
  • sealer used is quite small with reference to the area coveredsince it is not desired to create a complete-visible film of material on the coated surface, but merely to employ a material dispersible in water which will durin the finishing calendering stage be deposited on or into the-surface pores of the existing mineral coating and fill them.
  • the amount of dry material imposed on the coating ofthe-web in the-final-calendering nat-' tration in water the number of water'boxes used to applyit to the coated surface,.the absorptivity of thecoated surface,,etc.
  • the amount needed to give desirable gloss of printedink on the coated surface similarly will vary depending, as it does, on the quality of printing ink. However, all-these variations are relatively unimportant in view of the low quantity of sealer required, which is of the order of a few ounces dry sealer per one thousand square feet of coated surface.
  • a process of producing a non-glosspaperboard suitable for gloss ink printing which comprises applying to the surface of finished'paperboard a coating ofplasticizing agent in an aqueous vehicle and plasticizingthe saidsurface by passing the paperboard through. rolls, thereafter applying to the plasticized surface a coating of mineral matter and starch in an aqueous vehicle by imprinting, one of said coatings containing a resin capable of reacting with starch to insolubilize it and the other of said coatings containing a catalyst for said insolubilizing reaction, heating the treated board so as to produce said reaction and insolubilize the starch thereon, and afterward passing said treated board through a calender stack and applying to the coated surface thereof in said calender stack a water solution of a sealing substance resistant to the vehicles of gloss printing inks in quantity sufficient to seal the pores of said starch-mineral matter coating without affecting the non-gloss characteristics thereof, the said sealing substance being a water soluble substance chosen from a class consisting of starch, methyl
  • polyvinyl alcohol polyvinyl alcohol, vegetable protein, sodium sill cate and aliginate compounds.
  • a non-gloss mineral coated paperboard suitable for gloss ink printing produced by the process of claim 1.
  • a non-gloss mineral coated paperboard suitable for gloss ink printing produced by the process of claim 2.

Description

Patented Oct. 20, i953 PROCESS OF COATING PAPER WEBS AND PRODUCT THEREOF Harry 0. Fisher, Cincinnati, and Brainard E. Sooy, Middletown, Ohio, assignors, by mesne assignments, to Consolidated Water Power & Paper Company, Wisconsin Rapids, Wis., a corporation of Wisconsin No Drawing. Application August 29, 1945, Serial No. 613,436
4 Claims.
In our application for patent, Serial Number ing a coated web by continuous process, which has a water-resistant surface. Alternatively, we may treat the web surface with activating substance and introduce the insolubilizing agent into the coating mixture, and otherwise, the principal feature being that the complete reactive or reacted mixture is not applied with the mineral matter.
The present specification relates to an additional development based on subsequent treating of the coated web in order to bring about a very glossy effect upon printing of the coated web with oil or varnish base inks.
To review briefly the practice set forth in our earlier application, we indicate the use of a breaker stack of calender rolls which is the first stack of calenders used in general practice to smooth out a web of paper or paperboard as it comes from a paper or board machine, prior to sheeting or reeling the web. Immediately after this breaker stack of calender rolls, we provide a coating imprinting roll on which is spread a thin coating of mineral matter and starch in an aqueous base, the binder element of the mineral coating mixture perhaps including other adhesive and carrier agents, but in which starch is the principal one. Then follows a drier including heated rolls over which the web passes after it has picked up its coating from the imprinting roll. Finally the web may be passed through one or more stacks of finishing calenders depending upon the surface finish desired.
As set forth in said application we apply, where the binder of the mineral coat is mainly starch, an aqueous solution to the web while it passes through the breaker stack of calender rolls which contains, for example, urea formaldehyde resin in its syrupy stage of incomplete polymerization. We can use, alternatively, melamine resin or other resin substances having the quality of insolubilizing starch in the presence of a catalyst.
The imprinting roll is supplied, as set forth in the said specification, with a mineral matter coating mixture in an aqueous base, the binder consisting mainly of starch. We note in our application an example wherein a coating of adhesive and mineral pigment containing 54% solids and 46% water was used, and spread onto the imprinting roll which was in turn coated by means of a gate roll, taking the mixture from a supply, and by spreading rolls in a series from the gate roll to the imprinting roll, operating similarly to the mode of supplying ink to the inking roll of a rotary printing press. The film on the imprinting roll was, and indeed must be, quite thin or else the operation will not be a success due to treeing, patterning, etc. Thus in our said specification we mention as an example a coating picked up by the web while still moist from its treatment in the calender stack, of a film of around .001" thick, more or less, of the wet coating mixture.
In this coating mixture we introduce the catalyst for the resin reaction when the resin has been introduced on the breaker stack. Thus in one example we employ 15 parts of ammonium chloride to parts of the wet coating mixture above noted.
In another practice in our application we supply both the incompletely polymerized resin and its catalyst on the breaker stack of calender rolls. We also note that the resin can be supplied with the coating and the catalyst supplied on the breaker stack. Also it is noted that we can apply a thickened starch or starch and polyvinyl alcohol material to the web in the breaker stack along with one or the other of the two resin reactants, giving the web a plastic working in the presence of this material before it reaches the imprinting roll.
- After the web has passed the imprinting roll it moves to the heated driers where the reaction which insolubilizes the starch is completed. The whole process can be timed to take the product from a board machine or paper machine using standard drier rolls so as to be fully continuous. As noted in the said specification we may also calender the web after the coating is dry and cured, in calenders, in the presence of water, impossible when the starch is not insolublilized.
The above is intended as a statement of our development exclusive of the added step to be described below.
Our investigations have gone further in connection with the final calendering treatment, in an eifort to develop an insolubilized coating which takes an extremely glossy ink impression. We have found that following the process of our application above referred to, we may calender the dried, insolubilized starch and mineral coated web with a variety of substances which act to seal or close the tiny pores of the coating to a considerable degree, whereby the after-applied oil or varnish base inks will drop out to a very glossy appearance because the coated surface no longer is so absorbent to the inks vehicles. The coated board itself, when finished and-before printing, does not differ markedly in outer appearance over board which does not have the final treatment which we will discuss in more detail, and the difference appears only in the result of the oil or varnish base: ink printing. For convenience we will refer to the substance applied over the coated surface as a sealer. It dries out on the coated surface of'board.
Our present improvement over our practice as above described has been to add by means of the water boxes of the calender stack different agents L which will have film-forming or surface-filling or sealing power when applied in Water solution or dispersion to-the insolubilized coated surface. Where the paper or board machine is equipped with more than one stack of calenders to finish the web as a final treatment, we may employ water boxes on more than one stack or run certain stacks dry.
Thus We have used on a finishing calender stack a strong solution of modified or converted starch in water, for example, a gelled solution of 8% by weight of a chlorinated corn starch in water. In this solution we included a small amount of wax size which acts as a lubricant to overcomeany stickiness of starch solution. We have also applied a 3% by weight solution in water of carboxymethyl cellulose. We have used a 3% solution by weight in water of the alginate compound known as Kelgin. Another substance we have used is sodium silicate or water glass of 42 B. gravity (factor 3.25 SiOzzlNazO) in the ratio of one volume silicate to 3 volumes of water. Another type of starch used 4% in water was Flexgum, as it is known in the trade, being a modified corn starch which gels rapidly in cool water. Among other substances usable in water are methyl cellulose, carboxyethyl cellulose, polyvinyl alcohol and vegetable protein as from soya beans. The list can be extended to include a wide variety of substances which are water-borne to be handled in an inexpensivepractical manner in the Water boxes of a stack of calenders, as described. For purposes of economy, to obtain special effects, etc., blends of certain of these substances can be used. Such a blend might comprise polyvinyl alcohol and modified starch, in water, in almost any desired proportion and to which a small amount of plasticizer such as a polyhydric alcohol can be added. There are many possible blends and variations thereof;
Each of these substances as applied to the coated surface of the web is a minute film or filling in andon the waterproof coated surface to seal and reduce or eliminatethe comparatively porous or absorbent surface of the coating thus to prevent the absorption ofvehicleand/or ink from the printing ink down into the coated surface. We do not require that those substances be film-formers in the strictest sense of the word providing that they do fill in the coated surface to reduce its absorptivity to the subsequently applied ink. While it is unlikely that any substance used, as described, will be soluble in the base or vehicle of the ink, we note that such solubility must be absent or at least be negligible '4 in effect if the printing ink is to remain substantially unabsorbed into the coated surface.
The amount of sealer used is quite small with reference to the area coveredsince it is not desired to create a complete-visible film of material on the coated surface, but merely to employ a material dispersible in water which will durin the finishing calendering stage be deposited on or into the-surface pores of the existing mineral coating and fill them.
Were the coating not made water resistant by our insolubilizing process, it would be impossible to use aqueous dispersions of sealers on the finishingcalenders. The result would simply be to remove the coating which the web had received which removal would be accompanied by a pluggingof the rolls of the calender stack due to the reformation of a sticky mixture of mineral coatingv and adhesive in water. Also, so far as we are advised, an attempt to use such sealers as on a webwith a relatively thick mineralcoating, such as is ordinarily applied in anaqueousstarchvehicle-foll'oWed-bypolishing with brushes or reversely-turning rolls, would not be successful. It is because we have the thin printed-on coating which has been insolubilized that we are able not only to give the coated surface afinish-calendering with water but to add to that water an inkresistantsubstance which is ironed into the pores of and onto the coated surface.
The amount of dry material imposed on the coating ofthe-web in the-final-calendering nat-' tration in water,the number of water'boxes used to applyit to the coated surface,.the absorptivity of thecoated surface,,etc. The amount needed to give desirable gloss of printedink on the coated surface similarly will vary depending, as it does, on the quality of printing ink. However, all-these variations are relatively unimportant in view of the low quantity of sealer required, which is of the order of a few ounces dry sealer per one thousand square feet of coated surface.
Since the nip pressure of astack of calender rollsis extremely high and the concentration of sealer substance-in the water solution used on the calender stack is low, a natural safeguard exists against use of too much-sealer substance.
The sealer should have the following characteristics:
It should be- 1. Soluble or dispersible in water.
2. Effective in smallamount Inert toward mineral coating andprinting in Non-sticky in water when applied to web by calender nip.
5. Substantially colorless on the coated surface.
6. Odorless, tasteless,.non-toxic, etc.
7. Capable of forming a solution or dispersion of low viscosity.
8. Without adverse effect on foldability of the coated board.
9. Permanent in effect, as regards life of the coated board.
Havin thus described our invention, what we claim as new and desire to secure by Letters Patent is:
l. A process of producing a non-glosspaperboard suitable for gloss ink printing which comprises applying to the surface of finished'paperboard a coating ofplasticizing agent in an aqueous vehicle and plasticizingthe saidsurface by passing the paperboard through. rolls, thereafter applying to the plasticized surface a coating of mineral matter and starch in an aqueous vehicle by imprinting, one of said coatings containing a resin capable of reacting with starch to insolubilize it and the other of said coatings containing a catalyst for said insolubilizing reaction, heating the treated board so as to produce said reaction and insolubilize the starch thereon, and afterward passing said treated board through a calender stack and applying to the coated surface thereof in said calender stack a water solution of a sealing substance resistant to the vehicles of gloss printing inks in quantity sufficient to seal the pores of said starch-mineral matter coating without affecting the non-gloss characteristics thereof, the said sealing substance being a water soluble substance chosen from a class consisting of starch, methyl cellulose, carboxymethyl cellulose, carboxyethyl cellulose, polyvinyl alcohol, vegetable protein, sodium silicate and alginate compounds.
2. A process of treating non-gloss mineral coated paperboard which is resistant to wet rubbing, to render the mineral coating thereof nonabsorptive to gloss printing inks, whereby said inks will print with a glossy finish while at the same time the non-gloss characteristics of the coated board are retained, which process involves calendaring the coated paperboard while applying thereto a water solution of a sealing substance resistant to the vehicles of gloss printing inks in quantity sufiicient to seal the pores of said mineral coating but insufficient to destroy the non-gloss characteristics thereof, the said sealing substance being a water soluble substance chosen from a class consisting of starch, methyl cellulose, carboxymethyl cellulose, carboxyethyl cellulose,
polyvinyl alcohol, vegetable protein, sodium sill cate and aliginate compounds.
3. A non-gloss mineral coated paperboard suitable for gloss ink printing produced by the process of claim 1.
4. A non-gloss mineral coated paperboard suitable for gloss ink printing produced by the process of claim 2.
HARRY C. FISHER. BRAINARD E. SOOY.
References Cited in the file of this patent UNITED STATES PATENTS Number Name Date 1,913,329 Bradner June 6, 1933 1,940,363 McLaurin Dec. 19, 1933 1,982,018 Owen Nov. 27, 1934 2,083,441 Frost June 8, 1937 2,121,205 Lippert et a1 June 21, 1933 2,185,746 Goencz et a1. Jan. 2, 1940 2,212,314 Bauer Aug. 20, 1940 2,256,853 Schwartz Sept. 23, 1941 2,293,278 Oates Aug. 18, 1942 2,301,509 Boch Nov. 10, 1942 2,304,818 Grupe Dec. 15, 1942 2,317,696 Rich Apr. 27, 1943 2,322,887 Schwartz June 29, 1943 2,331,922 Montgomery Oct. 19, 1943 2,333,023 Manor Oct. 26, 1943 2,342,785 Boch Feb. 29, 1944 2,356,879 Pense et a1 Aug. 29, 1944 2,359,858 Iler Oct. 10, 1944 2,369,427 Bennett Feb. 13, 1945 2,414,313 Leek Jan. 14, 1947 2,419,207 Fischer Apr. 22, 1947 2,424,284 Olpin et a1 July 22, 1947 2,460,998 Nelson Feb. 8, 1949

Claims (1)

1. A PROCESS OF PRODUCING A NON-GLOSS PAPERBOARD SUITABLE FOR GLASS INK PRINTING WHICH COMPRISES APPLYING TO THE SURFACE OF FINISHED PAPERBOARD A COATING OF PLASTICIZING AGENT INAN AQUEOUS VEHICLE AND PLASTICIZING THE SAID SURFACE BY PASSING THE PAPERBOARD THROUGH ROLLS, THEREAFTER APPLYING TO THE PLASTICIZED SURFACE A COATING OF MINERAL MATTER AND STARCH IN AN AQUEOUS VEHICLE BY IMPRINTING, ONE OF SAID COATINGS CONTAINING A RESIN CAPABLE OF REACTING WITH STARCH TO INSOLUBILIZE IT AND THE OTHER OF SAID COATINGS CONTAINING A CATALYST FOR SAID INSOLUBILIZING REACTION, HEATING THE TREATED BOARD SO AS TO PRODUCE SAID REACTION AND INSOLUBLIZE THE STARCH THEREON, AND AFTERWARD PASSING SAID TREATED BOARD THROUGH A CALENDER STACK AND APPLYING TO THE COATED SURFACE THEREOF IN SAID CALENDER STACK A WATER SOLUTION OF A SEALING SUBSTANCE RESISTANT TO THE VEHICLE OF GLOSS PRINTING INKS IN QUANTITY SUFFICIENT TO SEAL THE PORES OF SAID STARCH-MINERAL MATTER COATING WITHOUT AFFECTING THE NON-GLASS CHARACTERISTICS THEREOF, THE SAID SEALING SUBSTANCE BEING A WATER SOLUBLE SUBSTANCE CHOSEN FROM A CLASS CONSISTING OF STARCH, METHYL CELLULOSE, CARBOXYMETHYL CELLULOSE, CARBOXYETHYL CELLULOSE, POLYVINYL ALCOHOL, VEGETABLE PROTEIN, SODIUM SILICATE AND ALIGNATE COMPOUNDS.
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US2772184A (en) * 1953-09-21 1956-11-27 Kimberly Clark Co Paper coating
US2790730A (en) * 1954-07-12 1957-04-30 Gardner Board & Carton Co Process of making and finishing coated paperboard and the like
US2818169A (en) * 1954-08-17 1957-12-31 Permacel Le Page S Inc Adhesive sheet
US2818349A (en) * 1954-08-17 1957-12-31 Permacel Le Page S Inc Adhesive sheet product and method of making
US2819184A (en) * 1953-10-22 1958-01-07 Warren S D Co Production of cast surfaced coated paper
US2869722A (en) * 1957-10-14 1959-01-20 Fibreboard Paper Products Corp Paper products having a release coating and method of preparation thereof
US2927865A (en) * 1956-02-24 1960-03-08 Crown Zellerbach Corp Coated heat-sealable wrapper and process of making same
US2999787A (en) * 1957-10-04 1961-09-12 Thilmany Pulp & Paper Company Machine glazed paper
US3047427A (en) * 1958-11-17 1962-07-31 Kimberly Clark Co Paper substrate having a coating of mineral pigment, natural adhesive binder, and homopolymer of butadiene
US3086884A (en) * 1959-10-14 1963-04-23 Betschmann Otto Method for the production of a coated paper product
US3413139A (en) * 1964-12-30 1968-11-26 Cons Papers Inc Method of making coated paper of low gloss and improved ink holdout

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US1940363A (en) * 1928-12-19 1933-12-19 Company Old Colony Trust Gummed paper
US1982018A (en) * 1931-11-14 1934-11-27 Naugatuck Chem Co Coated paper
US1913329A (en) * 1932-05-14 1933-06-06 Champion Coated Paper Company Filled surface paper and process of making same
US2083441A (en) * 1936-02-06 1937-06-08 Warren S D Co Lacquer coated sheet material and method of making the same
US2185746A (en) * 1936-07-23 1940-01-02 Arnold Print Works Method of producing permanent glaze chintz
US2121205A (en) * 1936-11-07 1938-06-21 Bancroft & Sons Co J Blueprint, photo-vellum, and similar sensitized cloths
US2293278A (en) * 1937-06-25 1942-08-18 Warren S D Co Process for finishing paper and product
US2212314A (en) * 1937-08-18 1940-08-20 Stein Hall Mfg Co Water resistant amylaceous compositions
US2256853A (en) * 1938-06-01 1941-09-23 Du Pont Paper product
US2342785A (en) * 1939-04-11 1944-02-29 Rohm & Haas Improving the wash-fastness of sizes with urea derivatives
US2301509A (en) * 1939-10-21 1942-11-10 Rohm & Haas Fixation of sizes
US2356879A (en) * 1939-12-12 1944-08-29 Pense Walter Process of preparing lustrous coatings
US2304818A (en) * 1940-05-01 1942-12-15 John R Ditmars Art of coating paper
US2333023A (en) * 1940-05-23 1943-10-26 Cons Paper Company Container wall
US2331922A (en) * 1940-08-03 1943-10-19 Champion Paper & Fibre Co Process of coating paper
US2322887A (en) * 1940-10-15 1943-06-29 Du Pont Chemical treatment of paper
US2369427A (en) * 1940-10-23 1945-02-13 Champlon Paper And Fibre Compa Paper coating composition and method of making
US2317696A (en) * 1942-05-13 1943-04-27 Edward D Rich Process for imparting greaseproof characteristics to paper
US2359858A (en) * 1942-11-26 1944-10-10 Du Pont Water-resistant starch and paper containing it
US2424284A (en) * 1943-02-22 1947-07-22 British Celanese Fixation of finely divided substances
US2419207A (en) * 1943-09-04 1947-04-22 Cons Water Power & Paper Co Method of production of coated board and paper
US2460998A (en) * 1944-03-20 1949-02-08 Stein Hall & Co Inc Method of coating paper
US2414313A (en) * 1944-08-24 1947-01-14 Edgar Brothers Company Process of coating web surfaces

Cited By (13)

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US2733997A (en) * 1956-02-07 Asnes
US2772184A (en) * 1953-09-21 1956-11-27 Kimberly Clark Co Paper coating
US2760883A (en) * 1953-10-12 1956-08-28 Roy L Pickett Photographic ferrotyping process
US2819184A (en) * 1953-10-22 1958-01-07 Warren S D Co Production of cast surfaced coated paper
US2790730A (en) * 1954-07-12 1957-04-30 Gardner Board & Carton Co Process of making and finishing coated paperboard and the like
US2818349A (en) * 1954-08-17 1957-12-31 Permacel Le Page S Inc Adhesive sheet product and method of making
US2818169A (en) * 1954-08-17 1957-12-31 Permacel Le Page S Inc Adhesive sheet
US2927865A (en) * 1956-02-24 1960-03-08 Crown Zellerbach Corp Coated heat-sealable wrapper and process of making same
US2999787A (en) * 1957-10-04 1961-09-12 Thilmany Pulp & Paper Company Machine glazed paper
US2869722A (en) * 1957-10-14 1959-01-20 Fibreboard Paper Products Corp Paper products having a release coating and method of preparation thereof
US3047427A (en) * 1958-11-17 1962-07-31 Kimberly Clark Co Paper substrate having a coating of mineral pigment, natural adhesive binder, and homopolymer of butadiene
US3086884A (en) * 1959-10-14 1963-04-23 Betschmann Otto Method for the production of a coated paper product
US3413139A (en) * 1964-12-30 1968-11-26 Cons Papers Inc Method of making coated paper of low gloss and improved ink holdout

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