US3720573A - Resin bonded dry creped tissue laminate having the crepe removed therefrom and method of making same - Google Patents
Resin bonded dry creped tissue laminate having the crepe removed therefrom and method of making same Download PDFInfo
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- US3720573A US3720573A US3720573DA US3720573A US 3720573 A US3720573 A US 3720573A US 3720573D A US3720573D A US 3720573DA US 3720573 A US3720573 A US 3720573A
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- crepe
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- creped tissue
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- 229920005989 resin Polymers 0.000 title abstract description 54
- 239000011347 resin Substances 0.000 title abstract description 54
- 238000004519 manufacturing process Methods 0.000 title description 4
- 238000005470 impregnation Methods 0.000 claims abstract description 12
- 239000004745 nonwoven fabric Substances 0.000 claims abstract description 11
- 239000000835 fiber Substances 0.000 claims description 13
- 239000002952 polymeric resin Substances 0.000 claims description 10
- 229920003002 synthetic resin Polymers 0.000 claims description 10
- 239000000839 emulsion Substances 0.000 abstract description 23
- 229920000642 polymer Polymers 0.000 abstract description 16
- 239000002759 woven fabric Substances 0.000 abstract description 9
- 239000007900 aqueous suspension Substances 0.000 abstract description 7
- 229920001577 copolymer Polymers 0.000 abstract description 7
- 239000004744 fabric Substances 0.000 abstract description 3
- 239000000123 paper Substances 0.000 description 47
- 239000000725 suspension Substances 0.000 description 13
- 238000000034 method Methods 0.000 description 8
- 239000000463 material Substances 0.000 description 7
- 229920006395 saturated elastomer Polymers 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 6
- 239000011101 paper laminate Substances 0.000 description 5
- 239000007787 solid Substances 0.000 description 4
- -1 ethyl hexyl acrylates Chemical class 0.000 description 3
- 235000011187 glycerol Nutrition 0.000 description 3
- 229920001223 polyethylene glycol Polymers 0.000 description 3
- 239000004925 Acrylic resin Substances 0.000 description 2
- 229920000178 Acrylic resin Polymers 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000007858 starting material Substances 0.000 description 2
- 101100264195 Caenorhabditis elegans app-1 gene Proteins 0.000 description 1
- JIGUQPWFLRLWPJ-UHFFFAOYSA-N Ethyl acrylate Chemical class CCOC(=O)C=C JIGUQPWFLRLWPJ-UHFFFAOYSA-N 0.000 description 1
- 229920000877 Melamine resin Polymers 0.000 description 1
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical class COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- 229920001131 Pulp (paper) Polymers 0.000 description 1
- 239000002174 Styrene-butadiene Substances 0.000 description 1
- 229920001807 Urea-formaldehyde Polymers 0.000 description 1
- 238000005299 abrasion Methods 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- MTAZNLWOLGHBHU-UHFFFAOYSA-N butadiene-styrene rubber Chemical compound C=CC=C.C=CC1=CC=CC=C1 MTAZNLWOLGHBHU-UHFFFAOYSA-N 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000003475 lamination Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229920005594 polymer fiber Polymers 0.000 description 1
- ODGAOXROABLFNM-UHFFFAOYSA-N polynoxylin Chemical compound O=C.NC(N)=O ODGAOXROABLFNM-UHFFFAOYSA-N 0.000 description 1
- 229920002689 polyvinyl acetate Polymers 0.000 description 1
- 239000011118 polyvinyl acetate Substances 0.000 description 1
- 239000013055 pulp slurry Substances 0.000 description 1
- 238000009738 saturating Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000011115 styrene butadiene Substances 0.000 description 1
- 229920003048 styrene butadiene rubber Polymers 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000037303 wrinkles Effects 0.000 description 1
Images
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B29/00—Layered products comprising a layer of paper or cardboard
- B32B29/002—Layered products comprising a layer of paper or cardboard as the main or only constituent of a layer, which is next to another layer of the same or of a different material
- B32B29/005—Layered products comprising a layer of paper or cardboard as the main or only constituent of a layer, which is next to another layer of the same or of a different material next to another layer of paper or cardboard layer
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B29/00—Layered products comprising a layer of paper or cardboard
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B38/00—Ancillary operations in connection with laminating processes
- B32B38/08—Impregnating
-
- 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
- D21H25/00—After-treatment of paper not provided for in groups D21H17/00 - D21H23/00
- D21H25/04—Physical treatment, e.g. heating, irradiating
- D21H25/06—Physical treatment, e.g. heating, irradiating of impregnated or coated paper
-
- 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
- D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
- D21H27/30—Multi-ply
-
- 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
- D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
- D21H27/30—Multi-ply
- D21H27/40—Multi-ply at least one of the sheets being non-planar, e.g. crêped
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2250/00—Layers arrangement
- B32B2250/26—All layers being made of paper or paperboard
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2260/00—Layered product comprising an impregnated, embedded, or bonded layer wherein the layer comprises an impregnation, embedding, or binder material
- B32B2260/02—Composition of the impregnated, bonded or embedded layer
- B32B2260/028—Paper layer
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2260/00—Layered product comprising an impregnated, embedded, or bonded layer wherein the layer comprises an impregnation, embedding, or binder material
- B32B2260/04—Impregnation, embedding, or binder material
- B32B2260/046—Synthetic resin
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2432/00—Cleaning articles, e.g. mops or wipes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2437/00—Clothing
- B32B2437/04—Caps, helmets
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B32—LAYERED PRODUCTS
- B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
- B32B2601/00—Upholstery
-
- 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
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/03—Non-macromolecular organic compounds
- D21H17/05—Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
- D21H17/06—Alcohols; Phenols; Ethers; Aldehydes; Ketones; Acetals; Ketals
-
- 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
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/14—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties characterised by function or properties in or on the paper
- D21H21/18—Reinforcing agents
-
- 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
- D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
- D21H23/02—Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
- D21H23/22—Addition to the formed paper
- D21H23/32—Addition to the formed paper by contacting paper with an excess of material, e.g. from a reservoir or in a manner necessitating removal of applied excess material from the paper
- D21H23/42—Paper being at least partly surrounded by the material on both sides
-
- 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
- D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
- D21H23/02—Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
- D21H23/22—Addition to the formed paper
- D21H23/52—Addition to the formed paper by contacting paper with a device carrying the material
- D21H23/56—Rolls
-
- 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
- Y10T156/00—Adhesive bonding and miscellaneous chemical manufacture
- Y10T156/17—Surface bonding means and/or assemblymeans with work feeding or handling means
- Y10T156/1702—For plural parts or plural areas of single part
- Y10T156/1712—Indefinite or running length work
-
- 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
- Y10T428/31906—Ester, halide or nitrile of addition polymer
-
- 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
- Y10T428/31909—Next to second addition polymer from unsaturated monomers
Definitions
- ABSTRACT An impregnated paper product having strength, toughness, tear resistance, softness, hand and breathability sufficient to permit such papers to be used as substitutes for woven or non-woven fabrics in making disposable fabric products.
- This invention relates to paper, and more particularly, is directed to improved paper products useful as a substitute for woven and non-woven fabrics.
- paper and paper-like products for woven and non-woven fabrics would be ideal for the making of disposable products, but paper, in general, has had several serious drawbacks from the standpoint of physical characteristics. While paper can be made from very inexpensive wood pulp fibers at a very high rate of speed, such papers that might be suitable as a substitute for fabrics such as creped or uncreped tissues or waddings suffer from an inherent lack of strength and toughness, particularly in the cross direction.
- tear resistance and tensile strength can be imparted to papers by the addition of other materials such as styrene-butadiene polymers, methyl-methacrylates, urea formaldehyde and melamine resins, etc.
- other materials such as styrene-butadiene polymers, methyl-methacrylates, urea formaldehyde and melamine resins, etc.
- the strength and tear resistance may be increased to acceptable levels, but the papers do not have the desirable characteristics of hand, drape, softness and breathability inherent in woven fabrics.
- Some degree of softness can be imparted to resin impregnated papers by the addition of glycerin or polyethylene glycol softeners to the paper. But, even in such instances, the hand, drape and breathability have been so inferior as to prevent the use of resin or polymer strengthened papers as a substitute for woven or non-woven fabrics.
- FIG. 1 is a schematic flow diagram showing one method of making the paper products of the present invention.
- FIG. 2 is a schematic flow diagram showing another method of making the paper products of the present invention.
- the first mentioned tubbing" or impregnation method is required since at least two preformed dry creped tissue sheets must be first superimposed before being subjected to treatment with the resin emulsion. After the preformed sheets have been superimposed they are then passed through the emulsion of the particular strength imparting resin employed.
- the resin concentration of the emulsion and the speed with which the paper is passed through the emulsion is controlled within limits to give the desired tensile strength and tear resistance characteristics as set forth more fully hereafter.
- the unique paper products of the present invention are shown being made by first superimposing two webs, 10 and 12, of dry creped tissue or wadding being delivered from supply rolls l4 and 16, respectively.
- the superimposed webs 10 and 12 then pass over a driven vacuum roll 18 which is provided in the usual manner to control tension in the web.
- An idler roll 19 is provided to change direction of the web prior to its passing over a spreader roll 20.
- the spreader roll 20 is a conventional Mount Hope" type and is used to maintain the combined web 10 and 12 at its maximum width and wrinkle free.
- the combined web 10 and 12 is passed into a nip 22 existent between a pair of superimposed, rotating squeeze rolls 24 and 26, the latter of which is positioned with a portion of its lower half in vat 28 containing an aqueous emulsion or suspension 30 of the resins or polymeric substances to be impregnated into the web.
- squeeze roll 26 picks up on its surface the resin or polymer suspension 30 and carries it into the nip 22 where the webs l0 and 12 become saturated with the suspension by impregnation.
- Rolls 24 and 26 are normally biased together to exert a squeezing pressure on the webs l0 and 12 at the nip 22 to squeeze out and remove any excess of the resin or polymer suspension from the web.
- the webs l0 and 12 are a dry creped tissue or wadding (i.e., the crepe has been imparted thereto while the paper is in a dry state whereby the fiber to fiber bonds have been formed therein while in the uncreped wet state prior to creping), passing through the aqueous suspension 30 readily causes the crepe to be removed therefrom, thus forming an uncreped, overall resin bonded laminate.
- vacuum roll 18 mentioned earlier is driven at an angular velocity slightly under the angular velocity of the squeeze rolls 24 and 26 thereby imparting sufficient tension in the webs l0 and 12 to add a mechanical force for the removal of the crepe.
- the resin emulsion or suspension is impregnated into the superimposed dry creped webs by passing them directly into the vat containing the aqueous suspension or emulsion.
- the webs 50 and 52 of dry creped tissue or wadding are delivered separately from supply rolls 54 and 56 respectively into superimposed relationship over and under respectively a pair of idler rolls 58 and 59.
- the superimposed webs 50 and 52 are then passed under the lower roll 66 of a pair of superimposed squeeze rolls 64 and 66, which lower roll 66 is positioned in a vat 68 with a portion of its lower half immersed in the aqueous resin or polymeric suspension or emulsion 70 contained therein.
- the combined webs 50 and 52 then follow around the lower roll 66 passing through the nip 60 defined between rolls 64 and 66 where the excess emulsion or suspension picked up by the web is squeezed out.
- the impregnated and saturated web passes through the conventional hot-air tunnel 32 and the series of heated can driers 34 to remove excess water and to cure the resin or polymeric materials in precisely the same manner as shown and described with respect to the method depicted in FIG. 1.
- the resin bonded, uncreped laminate 36 is also then rewound into rolls 38 ready for use in fabric-like products.
- the crepe present in the dry creped webs 50 and 52 is readily removed when the combined webs pass into the aqueous emulsion or suspension 70 in the vat 68, thus assuring overall resin bonding between the webs in the uncreped laminate ultimately produced.
- the papers used as the starting materials for making the products of the present invention are of the class known as dry creped wadding or tissues which are of a porous character having a thickness ranging from about 2 mils to about 20 mils.
- Their basis weight can be from about 5 pounds up to about 30 pounds which means the weight in pounds of a standard ream (3,000 square feet) of paper. Most preferred is a basis weight of about 10 pounds.
- the wadding used can have a crepe based stretch level in the machine direction ranging from about 5 to about 50 percent and most preferred is a stretch level of about 15 percent, and an inter-fiber stretch level in the cross direction ranging from about 2.3 percent to about 6 percent and most preferred is a stretch level of about 4.5 percent.
- the combined web will have a total basis weight ranging from about 10 pounds to about 60 pounds and most preferably about 30 pounds. Its machine direction stretch level due to creping will remain substantially unchanged from the individual plies as will the cross-direction stretch level due to inter-fiber bonding.
- the saturation bath in general will be made up of an aqueous suspension or emulsion containing from about 5 to about 50 percent resin or polymer solids and preferably about percent solids.
- the particular resins or polymers used or mixtures thereof can be any and all of those well known in the paper making art as strength imparting additives;
- the superimposed dry creped webs are delivered together to the aqueous emulsion or suspension of resins or polymeric materials at a controlled rate of speed to provide a dwell time in the suspension sufficient to obtain a wet pick-up of the suspension or emulsion ranging from about 75 percent to about 250 percent based upon the weight of the combined superimposed webs. Most preferred is a wet pick-up of about 150 percent of the suspension or emulsion.
- the wet pick-up is further controlled by adjusting the biasing force between the squeeze rolls where any excess pickup of the emulsion or suspension is pressed out of the webs.
- the saturated webs are dried at 240F 350F for about 2 minutes to remove the water from the webs and to cure the resins or polymers in their water insoluble state.
- Such treatment results in a lightweight, resin bonded, uncreped paper laminate containing from about 10 percent to about 30 percent resin and most preferred, about percent of resin or polymer solids based upon the weight of the dry resin bonded laminate.
- the resin. bonded uncreped paper laminate thus formed exhibits substantially equal stretch levels in both the machine and cross directions, and since the crepe has been removed, the stretch exhibited by the laminate is due solely to the internal resinfiber bonding relationship.
- the resin bonded, uncreped laminate produced exhibits an internal resin or polymer-fiber stretch level in both the machine and cross directions ranging from about 8 to about 20 percent and most preferred is a stretch level of about 13 percent.
- the paper product of the present invention even though containing hardening water-insoluble resins, has excellent softness, hand, drape and breathability.
- Softeners such as glycerin or polyethylene glycols are not required when practicing the present invention to produce a suitable paper substitute for woven and nonwoven fabrics, but they may be included where it is desired to produce a paper product having a very high degree of softness.
- softeners When such conventional softeners are used, they are added to the saturation emulsion or sus ension alon with the resin or 0] mer solids. If use Medicare at all, the b ath will contain no r nor e than 25 percent of the glycerin or polyethylene glycols. But it is emphasized, softeners are not required in most instances to make the unique resin bonded, uncreped paper laminate of the present invention.
- An uncreped laminated paper product suitable as a substitute for woven and dry-laid non-woven fabrics comprising at least two plies of lightweight, dry creped tissue, said laminate having impregnated therein a uniformly distributed strength imparting polymeric resin by which said dry creped tissue plies are overall bonded together with the crepe being removed to the extent that said uncreped laminate has a stretch level due solely to the internal resin-fiber bonding relationship, said stretch level in both the machine and cross direction ranging from about 8 to about 20 percent.
- each of said plies of dry creped tissue has a basic weight ranging from about 5 pounds up to about 30 pounds, a crepe-based stretch level in the machine direction ranging from about 5 percent to about 50 percent and an inter-fiber stretch level in the cross directions ranging from about 2.3 percent to about 6 percent prior to impregnation with said polymeric resin.
- each of said plies of dry creped tissue has a basis weight of about 10 pounds, a crepe based stretch level in the machine direction of about 15 percent and an inter-fiber stretch level in the cross direction of about 4.5 percent prior to impregnation with said polymeric resin and the removal of the crepe therefrom and said laminate has a resin-fiber based stretch level in both the machine and cross directions of about 13 percent.
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- Laminated Bodies (AREA)
- Paper (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
An impregnated paper product having strength, toughness, tear resistance, softness, hand and breathability sufficient to permit such papers to be used as substitutes for woven or non-woven fabrics in making disposable fabric products. By applying conventionally known strength imparting resins, polymers, and copolymers to multi-ply, dry creped tissue papers of low basis weight, which multi-ply laminate has the crepe removed therefrom as a result of passing through an aqueous suspension or emulsion of such resins, polymers or copolymers, the stiffness, noisiness and loss of breathability that result from such impregnation of single ply creped or uncreped papers does not occur.
Description
nited States Patent 1 Mayer 3,720,573 1March 13, 1973 [75] Inventor:
[73] Assignee: Johnson & Johnson [22] Filed: March 26, 1970 Warren C. Mayer, Somerville, NJ.
- 21} App1.N0.: 22,942
Related 1.1.8. Application Data [63] Continuation-impart of Ser. No. 671,963, Oct. 2,
1967, abandoned.
I 156/229 [51] Int. Cl ..B32b 7/04, B32b 29/00 [58] Field of Search ..161/129, 128, 148, 146, 147, 161/127,130,156,l49;156/l63,164,183, 229; 117/155J [56] References Cited UNITED STATES PATENTS 2,043,351 6/1936 Fourness et al ..l6l/l29 X 2,143,911 H1939 Fourness ..I61/l29X 3,017,291 l/l962 McLaughlin et a1. ..1 17/] 19.6
3,020,178 2/1962 Sweeny et a] ..1 17/155 3,047,445 7/1962 Gresham ..l6l/129 X 3,377,224 4/1968 Gresham et a1. ..156/209 FOREIGN PATENTS OR APPLICATIONS 1,016,486 l/l966 Great Britain ..161/128 484,526 7/1952 Canada ..161/129 Primary ExaminerWilliam J. Van Balen Attorney-W. Frederick Mayer, Jr. and Robert L. Minier [57] ABSTRACT An impregnated paper product having strength, toughness, tear resistance, softness, hand and breathability sufficient to permit such papers to be used as substitutes for woven or non-woven fabrics in making disposable fabric products. By applying conventionally known strength imparting resins, polymers, and copolymers to multi-ply, dry creped tissue papers of low basis weight, which multi-ply laminate has the crepe removed therefrom as a result of passing through an aqueous suspension or emulsion of such resins, polymers or copolymers, the stiffness, noisiness and loss of breathability that result from such impregnation of single ply creped or uncreped papers does not occur.
5 Claims, 2 Drawing Figures I PATENTEDHAR 1 3l875 RESIN BONDED DRY CREPED TISSUE LAMINATE HAVING TIIE CREPE REMOVED THEREFROM AND METHOD OF MAKING SAME RELATED APPLICATIONS FOR PATENT This application is a continuation-in-part of application Ser. No. 671,963 filed Oct. 2, 1967 and now abandoned.
BACKGROUND OF THE INVENTION This invention relates to paper, and more particularly, is directed to improved paper products useful as a substitute for woven and non-woven fabrics.
caps, masks, gowns, bedding, and the like have' acquired wide acceptance. Similarly, disposable aprons, towels, frocks, etc. are in ever increasing demand by food processing and handling establishments. Even the clothing industry today is looking to inexpensive disposable dresses as a fashionable and practical item.
To satisfy the need for disposable products, it is readily apparent that they must be made of inexpensive materials to warrant but a single use. The first approach to making disposable fibrous products was to substitute dry-laid non-woven fabrics for the woven fabrics from which reusable products had been made in the past. However, while this was a step in the right direction, such non-woven fabrics are still relatively expensive and in many instances have not reached full acceptance for disposable products because of the expense involved.
Substituting paper and paper-like products for woven and non-woven fabrics would be ideal for the making of disposable products, but paper, in general, has had several serious drawbacks from the standpoint of physical characteristics. While paper can be made from very inexpensive wood pulp fibers at a very high rate of speed, such papers that might be suitable as a substitute for fabrics such as creped or uncreped tissues or waddings suffer from an inherent lack of strength and toughness, particularly in the cross direction.
Tear resistance and tensile strength of papers have been increased considerably by saturating or impregnating them with polymeric resins. Particularly suitable have been self-crosslinking acrylic resins such as ethyl acrylates, ethyl hexyl acrylates, ethyl acrylatemethylmethacrylate copolymers, ethyl hexyl acrylatemethyl methacrylate copolymers, ethyl acrylate-polyvinyl acetate copolymers, and ethyl hexyl acrylatepolyvinyl acetate copolymers.
It is also well known that tear resistance and tensile strength can be imparted to papers by the addition of other materials such as styrene-butadiene polymers, methyl-methacrylates, urea formaldehyde and melamine resins, etc. However, when papers are impregnated or saturated with acrylic resins and such other polymeric materials, the strength and tear resistance may be increased to acceptable levels, but the papers do not have the desirable characteristics of hand, drape, softness and breathability inherent in woven fabrics. Some degree of softness can be imparted to resin impregnated papers by the addition of glycerin or polyethylene glycol softeners to the paper. But, even in such instances, the hand, drape and breathability have been so inferior as to prevent the use of resin or polymer strengthened papers as a substitute for woven or non-woven fabrics.
SUMMARY OF THE INVENTION l have found, quite unexpectedly, and for some unknown reason, that if two or more plies of light weight, dry creped tissue or wadding are superimposed and are then saturated or impregnated with an emulsion of well-known strength imparting resins of the types set forth above, the resin bonded laminated, uncreped paper produced does not loose to any appreciable degree its preimpregnated characteristics of hand, drape, softness, and most importantly, breathability. Further, by starting with dry creped tissues having a relatively high level of stretch in the machine direction due to the crepe, and then removing the crepe from the superimposed plies by passing them through the aqueous suspension or emulsion of resins, an overall resin bonded, uncreped laminate results in which the stretch level due to internal fiber-polymer association in both the machine and cross directions are increased and substantially equalized. By contrast, if a single ply of light weight, dry creped tissue wadding of the same basis weight as the combined basis weight of the two or more plies of dry creped tissue wadding are saturated with the same amount of the same strength imparting resins, the tensile strength and tear resistance of the paper is about the same, but it is hard, noisy and of greatly reduced breathability.
Thus it is seen, that by using at least two superimposed sheets of dry creped tissue prior to impregnation or saturation with the strength imparting resin additives, not only is an uncreped paper product produced that has increased wet strength and tear resistance as would be expected, but also a paper product is produced having excellent hand, drape, softness and breathability making it eminently suitable as a substitute for woven or non-woven fabrics in the making of disposable products of the type mentioned above.
DESCRIPTION OF DRAWING The present invention will be even more readily understood by reference to the following detailed description when read in conjunction with the attached drawings wherein:
FIG. 1 is a schematic flow diagram showing one method of making the paper products of the present invention; and
FIG. 2 is a schematic flow diagram showing another method of making the paper products of the present invention.
DETAILED DESCRIPTION OF THE INVENTION Treatment of papers with strength imparting resins is conventionally accomplished by two well-known methods. These are known as the tubbing" or impregnation" method and the internal addition method. In the former, an aqueous solution of pulp from which the paper is to be made is processed as a slurry and is placed upon a screen where the actual formation of the paper sheet takes place. Once the paper sheet is formed it is dried to extract the water. The preformed paper sheet is then impregnated with an emulsion of the particular resin desired. In the latter method, the emulsion of the resin is added to the pulp slurry prior to the paper sheet being formed on the screen. In both methods the paper sheet, subsequent to being treated with the emulsion of the resin, is heated to remove any water which may remain and to cure the resin in its water insoluble state.
In practicing the present invention, the first mentioned tubbing" or impregnation method is required since at least two preformed dry creped tissue sheets must be first superimposed before being subjected to treatment with the resin emulsion. After the preformed sheets have been superimposed they are then passed through the emulsion of the particular strength imparting resin employed. The resin concentration of the emulsion and the speed with which the paper is passed through the emulsion is controlled within limits to give the desired tensile strength and tear resistance characteristics as set forth more fully hereafter.
Referring now particularly to FIG. 1, the unique paper products of the present invention are shown being made by first superimposing two webs, 10 and 12, of dry creped tissue or wadding being delivered from supply rolls l4 and 16, respectively. The superimposed webs 10 and 12 then pass over a driven vacuum roll 18 which is provided in the usual manner to control tension in the web. An idler roll 19 is provided to change direction of the web prior to its passing over a spreader roll 20. The spreader roll 20 is a conventional Mount Hope" type and is used to maintain the combined web 10 and 12 at its maximum width and wrinkle free.
From the spreader roll 20, the combined web 10 and 12 is passed into a nip 22 existent between a pair of superimposed, rotating squeeze rolls 24 and 26, the latter of which is positioned with a portion of its lower half in vat 28 containing an aqueous emulsion or suspension 30 of the resins or polymeric substances to be impregnated into the web. During its rotation, squeeze roll 26 picks up on its surface the resin or polymer suspension 30 and carries it into the nip 22 where the webs l0 and 12 become saturated with the suspension by impregnation. Rolls 24 and 26 are normally biased together to exert a squeezing pressure on the webs l0 and 12 at the nip 22 to squeeze out and remove any excess of the resin or polymer suspension from the web.
Because the webs l0 and 12 are a dry creped tissue or wadding (i.e., the crepe has been imparted thereto while the paper is in a dry state whereby the fiber to fiber bonds have been formed therein while in the uncreped wet state prior to creping), passing through the aqueous suspension 30 readily causes the crepe to be removed therefrom, thus forming an uncreped, overall resin bonded laminate. To further aid in removal of the crepe, however, vacuum roll 18 mentioned earlier, is driven at an angular velocity slightly under the angular velocity of the squeeze rolls 24 and 26 thereby imparting sufficient tension in the webs l0 and 12 to add a mechanical force for the removal of the crepe.
From the squeeze rolls 24 and 26 the combined, saturated webs l0 and 12 pass through a conventional hot-air heating tunnel 32 to drive off excess water and to start curing of the resin or polymeric materials impregnated therein. Curing of the resin or polymeric materials is completed in a series of conventional heated can driers 34 following which the resin bonded, uncreped laminate 36 is rewound into rolls 38 ready to be made into disposable products having true woven and non-woven fabric-like properties. i
In FIG. 2 of the drawings, the resin emulsion or suspension is impregnated into the superimposed dry creped webs by passing them directly into the vat containing the aqueous suspension or emulsion. As shown, the webs 50 and 52 of dry creped tissue or wadding are delivered separately from supply rolls 54 and 56 respectively into superimposed relationship over and under respectively a pair of idler rolls 58 and 59. The superimposed webs 50 and 52 are then passed under the lower roll 66 of a pair of superimposed squeeze rolls 64 and 66, which lower roll 66 is positioned in a vat 68 with a portion of its lower half immersed in the aqueous resin or polymeric suspension or emulsion 70 contained therein. The combined webs 50 and 52 then follow around the lower roll 66 passing through the nip 60 defined between rolls 64 and 66 where the excess emulsion or suspension picked up by the web is squeezed out. From following over the upper roll 64, the impregnated and saturated web passes through the conventional hot-air tunnel 32 and the series of heated can driers 34 to remove excess water and to cure the resin or polymeric materials in precisely the same manner as shown and described with respect to the method depicted in FIG. 1. The resin bonded, uncreped laminate 36 is also then rewound into rolls 38 ready for use in fabric-like products.
As with the method of FIG. I, the crepe present in the dry creped webs 50 and 52 is readily removed when the combined webs pass into the aqueous emulsion or suspension 70 in the vat 68, thus assuring overall resin bonding between the webs in the uncreped laminate ultimately produced.
The papers used as the starting materials for making the products of the present invention are of the class known as dry creped wadding or tissues which are of a porous character having a thickness ranging from about 2 mils to about 20 mils. Their basis weight (each single ply) can be from about 5 pounds up to about 30 pounds which means the weight in pounds of a standard ream (3,000 square feet) of paper. Most preferred is a basis weight of about 10 pounds. As a dry creped paper, the wadding used can have a crepe based stretch level in the machine direction ranging from about 5 to about 50 percent and most preferred is a stretch level of about 15 percent, and an inter-fiber stretch level in the cross direction ranging from about 2.3 percent to about 6 percent and most preferred is a stretch level of about 4.5 percent.
When two or more continuous webs of dry creped tissue or wadding having the above characteristics, are superimposed prior to removal of the crepe and impregnation with aqueous suspension of the particular resins or polymers, the combined web will have a total basis weight ranging from about 10 pounds to about 60 pounds and most preferably about 30 pounds. Its machine direction stretch level due to creping will remain substantially unchanged from the individual plies as will the cross-direction stretch level due to inter-fiber bonding.
The saturation bath in general will be made up of an aqueous suspension or emulsion containing from about 5 to about 50 percent resin or polymer solids and preferably about percent solids. As mentioned earlier, the particular resins or polymers used or mixtures thereof, can be any and all of those well known in the paper making art as strength imparting additives;
whether they are added to impart increased dry strength or wet strength or to increase abrasion or tear resistance or any combination of such properties to papers of all types. It is only essential in making the uncreped, resin bonded paper laminate of the present invention that a lightweight dry creped tissue or wadding be used as a starting material and that at least two plies of such tissue or wadding be superimposed prior to saturation or impregnation of the superimposed webs with the strength imparting resins or polymers.
The superimposed dry creped webs are delivered together to the aqueous emulsion or suspension of resins or polymeric materials at a controlled rate of speed to provide a dwell time in the suspension sufficient to obtain a wet pick-up of the suspension or emulsion ranging from about 75 percent to about 250 percent based upon the weight of the combined superimposed webs. Most preferred is a wet pick-up of about 150 percent of the suspension or emulsion. The wet pick-up is further controlled by adjusting the biasing force between the squeeze rolls where any excess pickup of the emulsion or suspension is pressed out of the webs.
Following 1 such saturation, the saturated webs are dried at 240F 350F for about 2 minutes to remove the water from the webs and to cure the resins or polymers in their water insoluble state. Such treatment results in a lightweight, resin bonded, uncreped paper laminate containing from about 10 percent to about 30 percent resin and most preferred, about percent of resin or polymer solids based upon the weight of the dry resin bonded laminate.
The resin. bonded uncreped paper laminate thus formed exhibits substantially equal stretch levels in both the machine and cross directions, and since the crepe has been removed, the stretch exhibited by the laminate is due solely to the internal resinfiber bonding relationship. The resin bonded, uncreped laminate produced exhibits an internal resin or polymer-fiber stretch level in both the machine and cross directions ranging from about 8 to about 20 percent and most preferred is a stretch level of about 13 percent.
It is also found that removal of the crepe in the aqueous saturation of the dry creped webs assures overall lamination of the webs and reduces the bulk of the resulting resin bonded laminate, thus also assuring low flexural resistance which, among other factors, contributes to the paper laminate s fabric-like quality.
The paper product of the present invention, even though containing hardening water-insoluble resins, has excellent softness, hand, drape and breathability.
Softeners such as glycerin or polyethylene glycols are not required when practicing the present invention to produce a suitable paper substitute for woven and nonwoven fabrics, but they may be included where it is desired to produce a paper product having a very high degree of softness. When such conventional softeners are used, they are added to the saturation emulsion or sus ension alon with the resin or 0] mer solids. If use?! at all, the b ath will contain no r nor e than 25 percent of the glycerin or polyethylene glycols. But it is emphasized, softeners are not required in most instances to make the unique resin bonded, uncreped paper laminate of the present invention.
While I have described my invention with some degree of particularly in the resins or polymers employed, it is to be understood that such resins and many other equivalents are well known in the paper making art, and that many substitutions can be made while still remaining within the spirit and scope of the invention as defined in the appended claims.
I claim:
1. An uncreped laminated paper product suitable as a substitute for woven and dry-laid non-woven fabrics comprising at least two plies of lightweight, dry creped tissue, said laminate having impregnated therein a uniformly distributed strength imparting polymeric resin by which said dry creped tissue plies are overall bonded together with the crepe being removed to the extent that said uncreped laminate has a stretch level due solely to the internal resin-fiber bonding relationship, said stretch level in both the machine and cross direction ranging from about 8 to about 20 percent.
2. A laminated paper product according to claim 1 wherein each of said plies of dry creped tissue has a basic weight ranging from about 5 pounds up to about 30 pounds, a crepe-based stretch level in the machine direction ranging from about 5 percent to about 50 percent and an inter-fiber stretch level in the cross directions ranging from about 2.3 percent to about 6 percent prior to impregnation with said polymeric resin.
3. A laminated paper product according to claim 1 wherein said polymeric resin is present in an amount ranging from about 10 percent to about 30 percent based upon the dry weight of said laminate.
4. A laminated paper product according to claim 2 wherein each of said plies of dry creped tissue has a basis weight of about 10 pounds, a crepe based stretch level in the machine direction of about 15 percent and an inter-fiber stretch level in the cross direction of about 4.5 percent prior to impregnation with said polymeric resin and the removal of the crepe therefrom and said laminate has a resin-fiber based stretch level in both the machine and cross directions of about 13 percent.
5. A laminated paper product according to claim 3 wherein said polymeric resin is present in an amount of about 20 percent based upon the dry weight of said laminate.
c a: a w a l
Claims (4)
1. An uncreped laminated paper product suitable as a substitute for woven and dry-laid non-woven fabrics comprising at least two plies of lightweight, dry creped tissue, said laminate having impregnated therein a uniformly distributed strength imparting polymeric resin by which said dry creped tissue plies are overall bonded together with the crepe being removed to the extent that said uncreped laminate has a stretch level due solely to the internal resin-fiber bonding relationship, said stretch level in both the machine and cross direction ranging from about 8 to about 20 percent.
2. A laminated paper product according to claim 1 wherein each of said plies of dry creped tissue has a basic weight ranging from about 5 pounds up to about 30 pounds, a crepe-based stretch level in the machine direction ranging from about 5 percent to about 50 percent and an inter-fiber stretch level in the cross directions ranging from about 2.3 percent to about 6 percent prior to impregnation with said polymeric resin.
3. A laminated paper product according to claim 1 wherein said polymeric resin is present in an amount ranging from about 10 percent to about 30 percent based upon the dry weight of said laminate.
4. A laminated paper product according to claim 2 wherein each of said plies of dry creped tissue has a basis weight of about 10 pounds, a crepe based stretch level in the machine direction of about 15 percent and an inter-fiber stretch level in the cross direction of about 4.5 percent prior to impregnation with said polymeric resin and the removal of the crepe therefrom and said laminate has a resin-fiber based stretch level in both the machine and cross directions of about 13 percent.
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU55644/69A AU5564469A (en) | 1969-05-27 | 1969-05-27 | Dry creped tissue laminate |
GB2694369 | 1969-05-28 | ||
AT512469A AT298227B (en) | 1969-05-27 | 1969-05-29 | Process for the manufacture of a paper product suitable as a substitute for woven and non-woven textiles |
US2294270A | 1970-03-26 | 1970-03-26 | |
US23541372A | 1972-03-16 | 1972-03-16 |
Publications (1)
Publication Number | Publication Date |
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US3720573A true US3720573A (en) | 1973-03-13 |
Family
ID=27506438
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US3720573D Expired - Lifetime US3720573A (en) | 1969-05-27 | 1970-03-26 | Resin bonded dry creped tissue laminate having the crepe removed therefrom and method of making same |
US3772124D Expired - Lifetime US3772124A (en) | 1969-05-27 | 1972-03-16 | Method of forming tissue laminate |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US3772124D Expired - Lifetime US3772124A (en) | 1969-05-27 | 1972-03-16 | Method of forming tissue laminate |
Country Status (8)
Country | Link |
---|---|
US (2) | US3720573A (en) |
AT (1) | AT298227B (en) |
AU (1) | AU5564469A (en) |
BE (1) | BE734951A (en) |
CA (1) | CA951629A (en) |
GB (2) | GB1257953A (en) |
NO (1) | NO132698C (en) |
SE (1) | SE372785B (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3935336A (en) * | 1972-03-09 | 1976-01-27 | Th. Goldschmidt Ag | Process for making carrier sheets impregnated with aminoplast condensation resins |
CN109972458A (en) * | 2019-05-17 | 2019-07-05 | 杭州添丽装饰纸有限公司 | The preparation method and preparation facilities of wear-resistant decorative paper |
Families Citing this family (4)
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US4292360A (en) * | 1980-03-05 | 1981-09-29 | Minnesota Mining And Manufacturing Company | Pressure sensitive adhesive tape |
US7294230B2 (en) * | 2004-12-20 | 2007-11-13 | Kimberly-Clark Worldwide, Inc. | Flexible multi-ply tissue products |
ES2264372B1 (en) * | 2005-03-10 | 2007-12-01 | Fabrica Nacional De Moneda Y Timbre - Real Casa De La Moneda | SAFETY STRIP, SECURITY PAPER THAT INCLUDES SUCH STRIP AND SECURITY DOCUMENT AND TICKET THAT INCORPORATE SUCH PAPER. |
CN105887557A (en) * | 2014-12-24 | 2016-08-24 | 天津元鸿科技有限公司 | Novel environmental protection impregnated paper |
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US2043351A (en) * | 1935-06-01 | 1936-06-09 | Int Cellucotton Products | Method of making a tissue paper product |
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GB1016486A (en) * | 1963-06-28 | 1966-01-12 | Crown Zellerbach Corp | Process for making an extensible dry-creped sheet material |
US3377224A (en) * | 1966-03-11 | 1968-04-09 | Kimberly Clark Co | Method of embossing differentially creped tissue paper |
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US3300368A (en) * | 1964-12-11 | 1967-01-24 | Crown Zellerbach Corp | Creped sheet materials and the process of producing the same |
US3684643A (en) * | 1969-11-17 | 1972-08-15 | Akwell Ind Inc | Paper layers laminated by polyethylene layer |
-
1969
- 1969-05-27 AU AU55644/69A patent/AU5564469A/en not_active Expired
- 1969-05-28 GB GB1257953D patent/GB1257953A/en not_active Expired
- 1969-05-29 AT AT512469A patent/AT298227B/en not_active IP Right Cessation
- 1969-06-20 BE BE734951A patent/BE734951A/xx unknown
-
1970
- 1970-03-26 US US3720573D patent/US3720573A/en not_active Expired - Lifetime
-
1971
- 1971-03-16 NO NO99771A patent/NO132698C/no unknown
- 1971-03-25 CA CA108,758,A patent/CA951629A/en not_active Expired
- 1971-03-25 SE SE388971A patent/SE372785B/xx unknown
- 1971-04-19 GB GB2540271A patent/GB1341637A/en not_active Expired
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1972
- 1972-03-16 US US3772124D patent/US3772124A/en not_active Expired - Lifetime
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CA484526A (en) * | 1952-07-01 | B. Catlin John | Filter materials and process for making such materials | |
US2043351A (en) * | 1935-06-01 | 1936-06-09 | Int Cellucotton Products | Method of making a tissue paper product |
US2143911A (en) * | 1935-10-17 | 1939-01-17 | Paper Patents Co | Method of making a cellulosic product |
US3020178A (en) * | 1957-09-06 | 1962-02-06 | Rohm & Haas | Paper impregnating compositions, impregnated papers and the process of impregnating paper |
US3047445A (en) * | 1958-06-02 | 1962-07-31 | Kimberly Clark Co | Cellulosic wiping material |
US3017291A (en) * | 1959-01-06 | 1962-01-16 | Rohm & Haas | Wet-strength paper and method of producing same |
GB1016486A (en) * | 1963-06-28 | 1966-01-12 | Crown Zellerbach Corp | Process for making an extensible dry-creped sheet material |
US3377224A (en) * | 1966-03-11 | 1968-04-09 | Kimberly Clark Co | Method of embossing differentially creped tissue paper |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
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US3935336A (en) * | 1972-03-09 | 1976-01-27 | Th. Goldschmidt Ag | Process for making carrier sheets impregnated with aminoplast condensation resins |
CN109972458A (en) * | 2019-05-17 | 2019-07-05 | 杭州添丽装饰纸有限公司 | The preparation method and preparation facilities of wear-resistant decorative paper |
Also Published As
Publication number | Publication date |
---|---|
US3772124A (en) | 1973-11-13 |
SE372785B (en) | 1975-01-13 |
BE734951A (en) | 1969-12-22 |
GB1257953A (en) | 1971-12-22 |
AT298227B (en) | 1972-04-25 |
GB1341637A (en) | 1973-12-25 |
AU5564469A (en) | 1970-12-03 |
NO132698C (en) | 1975-12-17 |
NO132698B (en) | 1975-09-08 |
CA951629A (en) | 1974-07-23 |
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