US3210240A - Sizing paper with a foamed starch - Google Patents

Sizing paper with a foamed starch Download PDF

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Publication number
US3210240A
US3210240A US295386A US29538663A US3210240A US 3210240 A US3210240 A US 3210240A US 295386 A US295386 A US 295386A US 29538663 A US29538663 A US 29538663A US 3210240 A US3210240 A US 3210240A
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United States
Prior art keywords
paper
starch
foam
newsprint
sheet
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Expired - Lifetime
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US295386A
Inventor
Douglas E Read
William B Cranford
Anthony J Petricola
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Cip Inc
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International Paper Canada Inc
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Priority to US295386A priority Critical patent/US3210240A/en
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Publication of US3210240A publication Critical patent/US3210240A/en
Assigned to CIP INC. reassignment CIP INC. MERGER (SEE DOCUMENT FOR DETAILS). , EFFECTIVE 10-8-81 Assignors: CANADIAN INTERNATIONAL PAPER COMPANY, CIP PAPER PRODUCTS LIMITED, INTERNATIONAL PAPER SALES COMPANY INC., PORTEMIAC PAPER CORPORATION
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Expired - Lifetime legal-status Critical Current

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    • 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
    • D21H21/00Non-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
    • D21H21/50Non-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 form
    • D21H21/56Foam
    • 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
    • D21H17/00Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
    • D21H17/20Macromolecular organic compounds
    • D21H17/21Macromolecular organic compounds of natural origin; Derivatives thereof
    • D21H17/24Polysaccharides
    • D21H17/28Starch

Definitions

  • This invention relates to the manufacture of paper having improved surface qualities. More particularly, it relates to a process for improving newsprint, newsroto, novel news, directory, catalog and similar papers.
  • uncooked starch particles tend to remain near the top surface of the sheet where they are needed, when, upon entering the dryer section of the machine, the combination of heat and moisture causes the particles to swell, become sticky, and to form fiberstarch-fiber linkages which bond the loose surface fibers to the main body of the sheet.
  • starcheswhether raw, cooked, modified, or any mixture thereof-- are foamed by means of compressed air and with the aid of wetting agents or surfactants; the starch foam is dried by draining and the dried starch foam is applied to the paper sheet (without any submersion or immersion thereof in the foam) by conventional means such as applicator I (1) gm./l. dispersion of an uncooked modified (hydroxyethylated) starch commercially available as SLS 240 (2.) 9 gm./l. sodium lauryl sulfate (an anionic'wetting agent) These were metered to the bottom of a column 2 inches in diameter by 3 feet high.
  • Compressed air was also admitted to the bottom of the column and the resulting foam was led from the top of the column to asmall size press having a nip formed by an upper steel roll and a lower rubber roll.
  • a 15" wide web of newsprint paper was pulled into, through, and out of the size press nip at about 100 fL/min. and, at the same time, the foam was applied to the top roll so as to form a head of foam in the nip between the steel roll and the newsprint.
  • the pumping rates of the two solutions entering the column were regulated so as to coat the web on its felt side with about 15 to 20 lbs. of the starch and about 1.8 lbs. of wetting agent per ton of newsprint. About 15 to 20% moisture was added to the newsprint in the process.
  • the specific volume of the foam was about 20 times that of the liquid giving rise to the foam.

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  • Paper (AREA)

Description

0ct.5, 1965 D. s. READ ETAL SIZING'PAPER WITH A FOAMED ST-ARCH Filed July is, 1965 DRY FOAM SiZE y g TRAP PRESS FOAM LlQUID PINCH FG E c0ce \-FOAM GENERATOR STARCH AND WETTING w y 'j/FOAM 'RECYCLED LIQUID g- LIQUID Q compasssau AIR ' DRY FOAM TRAP F PRESS WE? FOAM FQAM- LlQUlD comsmm mom Fig 2 VALVE --FOAM RECYCLEQ FRESH GENERATOR BY STARCH WETTING smwrrv SOLUTION AGENT A /F0AM uqum Mmmcs I m ZONE INVENTORS:
WAIQPRESSED ooueuxs E. READ WILLIAM B.CRANFORD ANTHONY J. PETRICOLA ATTORNEY list This invention relates to the manufacture of paper having improved surface qualities. More particularly, it relates to a process for improving newsprint, newsroto, novel news, directory, catalog and similar papers.
Many press rooms using newsprint or the like are con- .verting to offset presses. In such presses, the ink, which is considerably more viscous and adhesive than the ink generally used in letterpress printing, is transferred to the paper from a rubber blanket.- An appreciable force is required to remove the printed paper from the rubber blanket, because of the nature of the ink, and such force and the ink cooperate to pick up on the blanket any relatively loose fibers occurring on the surface of the paper and to accumulate such pick-up or lint on the blanket and the printing plate. This ultimately causes a deterioration of the printing quality and eventually forces a shutdown of the press for clean-up. This problem is usually satisfactorily mitigated when the paper is newsprint by doing the offset printing on the wire side of the sheet from which loose fibers are relatively absent, but it is not always possible or convenient to print the wire side of the sheet only and the problem is a significant one with respect to the top-side or felt-side of the sheet.
Accordingly, there is a need to develop means capable of bonding top surface fibers relatively firmly to the main body of a sheet of paper useful in offset printing. These means must be cheap or the economic advantage of using a paper such as newsprint will be lost. In addition, certain deleterious side effects must be avoided. Thus, for instance, since many newsprint offset inks dry mainly by absorption, the porosity of the sheet must be reasonably maintained. Again, since Customs regulations restrict the water penetration resistance of papers which they permit to be imported into the US. duty-free, they practically eliminate the use of rosin size or water resistant film coatings on such papers.
It is, therefore, an object of the present invention to enable the manufacture of the newsprint and other comparable paper stocks having an improved bonding between the top surface fibers and the bodies of such papers simply and inexpensively and with substantially no change in their characteristics of porosity and water penetration resistance. 7
It has heretofore been proposed to apply an uncooked starch to the top suface of a travelling paper web before it is heat dried. See co-pending U.S. Serial No. 178,874, filed March 12, 1962, and now abandoned in favor of continuation-in-part application Serial No. 331,643, filed December 11, 1963. The starch, in the form of an aqueous slurry with or without an admixture of papermakers alum, is not highly viscous and, therefore, does not interfere appreciably with the removal of water from the sheet on, for instance, the wire of a Fourdrinier paper machine. Furthermore, the uncooked starch particles tend to remain near the top surface of the sheet where they are needed, when, upon entering the dryer section of the machine, the combination of heat and moisture causes the particles to swell, become sticky, and to form fiberstarch-fiber linkages which bond the loose surface fibers to the main body of the sheet.
A further refinement is now proposed, one which greatly minimizes the rather large addition of water to the paper sheet which is inherent in the use of a starch slurry the vehicle of which is water and one which, thereby, affords not only greater economy in paper production, but also provides for a more even and better surface sizing of the paper as established by iodine developing. Moreover, such refinement permits the use of minimal quantities of cooked or uncooked starches or mixtures thereof per ton of paper, i.e., about 10 to 20 lbs. of starch per air dried ton of a paper such as newsprint.
In accordance with the present invention, starcheswhether raw, cooked, modified, or any mixture thereof-- are foamed by means of compressed air and with the aid of wetting agents or surfactants; the starch foam is dried by draining and the dried starch foam is applied to the paper sheet (without any submersion or immersion thereof in the foam) by conventional means such as applicator I (1) gm./l. dispersion of an uncooked modified (hydroxyethylated) starch commercially available as SLS 240 (2.) 9 gm./l. sodium lauryl sulfate (an anionic'wetting agent) These were metered to the bottom of a column 2 inches in diameter by 3 feet high. Compressed air was also admitted to the bottom of the column and the resulting foam was led from the top of the column to asmall size press having a nip formed by an upper steel roll and a lower rubber roll. A 15" wide web of newsprint paper was pulled into, through, and out of the size press nip at about 100 fL/min. and, at the same time, the foam was applied to the top roll so as to form a head of foam in the nip between the steel roll and the newsprint. The pumping rates of the two solutions entering the column were regulated so as to coat the web on its felt side with about 15 to 20 lbs. of the starch and about 1.8 lbs. of wetting agent per ton of newsprint. About 15 to 20% moisture was added to the newsprint in the process. The specific volume of the foam was about 20 times that of the liquid giving rise to the foam.
Again, in another example, two aqueous solutions were made up as follows:
(2) 9 gm./l. sodium lauryl sulfate These solutions were employed as were those in the first example. In this case, the rate of application of the starch was about cc./min. and that of the wetting agent was about 60 cc./rnin. Subsequent testing showed the addition to the felt side of the web of about 21 lbs. of starch and the addition of about 24.4% more moisture to the web.
Further work has shown that, in some cases, it is preferable to add some carboxymethylcellulose to the starch to heighten viscosity slightly and to provide a trap in the line from the foaming column to the size press for assistance in drying the foam by draining excess liquid therefrom (the resulting foam is quite stable and is capable of standing in the open atmosphere for several hours with very little liquid drainage). In addition, it has shown that raw starch solutions of 10% or higher concentration can easily be foamed to volume/weight ratios of as high as 50/1 and that cooked starches of up to about 3.3% concentration can be foamed to volume/ weight ratios of about 20/1, a reduction in concentration leading to an increase in ratio. Similarly, mixtures of up to about 3% cooked and about 7% raw starches

Claims (1)

1. IN THE MANUFACTURE OF A PAPER SELECTED FROM THE GROUP CONSISTING OF NEWSPRINT, NEWSROTO, NOVEL NEWS, DIRECTORY AND CATALOG PAPERS, A PROCESS OF BONDING TWO SURFACE FIBERS OF THE PAPER TO THE BODY THEREOF COMPRISING FOAMING STARCH DISPERSED IN WATER BY MEANS OF COMPRESSED AIR AND WITH THE AID OF A WETTING AGENT, DRAINING THE STARCH FOAM TO THE PAPER, AT A RATE EQUIVALENT TO ABOUT 10 TO 20 LBS. PER TON OF AIR DRIED PAPER.
US295386A 1963-07-16 1963-07-16 Sizing paper with a foamed starch Expired - Lifetime US3210240A (en)

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Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3395201A (en) * 1964-07-14 1968-07-30 Johnson & Johnson Method and apparatus for producing an absorbent product
US3461032A (en) * 1967-07-19 1969-08-12 Cons Paper Bahamas Ltd Apparatus for applying dry powdered additives to paper on the forming wire using electrostatic attraction
US3919042A (en) * 1967-01-05 1975-11-11 Ransburg Electro Coating Corp Method and apparatus for applying dry starch particles to water wet cellulosic webs using electrostatic attraction
US4353993A (en) * 1981-05-12 1982-10-12 Hercules Incorporated Foam compositions for surface application to fibrous substrates
US4548649A (en) * 1983-11-23 1985-10-22 Westvaco Corporation Foaming agent
US5411637A (en) * 1992-05-22 1995-05-02 Westvaco Corporation Method for producing high pressure laminates
US5433826A (en) * 1992-05-22 1995-07-18 Westvaco Corporation Method for reducing fuzz in the production of saturating kraft paper
US20060121278A1 (en) * 2004-12-02 2006-06-08 Vinson Kenneth D Fibrous structures comprising a nanoparticle additive
US20060121207A1 (en) * 2004-12-02 2006-06-08 Prodoehl Michael S Process for making a fibrous structure comprising an additive
US20060121814A1 (en) * 2004-12-02 2006-06-08 The Procter & Gamble Company Fibrous structures comprising a low surface energy additive
WO2018011667A1 (en) * 2016-07-11 2018-01-18 Stora Enso Oyj Process for creating a foam utilizing an antimicrobial starch within a process for manufacturing a paper or board product
US11130257B2 (en) 2016-07-11 2021-09-28 Stora Enso Oyj Lignin-based phenolic resin
US11365515B2 (en) 2018-04-04 2022-06-21 Solenis Technologies, L.P. Foam assisted application of strength additives to paper products
US20220243401A1 (en) * 2019-05-14 2022-08-04 Stora Enso Oyj Method for applying starch to a paper or paperboard web
WO2023137301A1 (en) * 2022-01-11 2023-07-20 Solenis Technologies Cayman, L.P. Foam-assisted application of sizing agents to paper products

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2214641A (en) * 1937-07-17 1940-09-10 Combined Locks Paper Company Process of producing rotogravure paper and the like
US2337915A (en) * 1940-04-30 1943-12-28 Menger Adolf Shaped body and process of preparing the same
US2442928A (en) * 1945-03-23 1948-06-08 Us Agriculture Food products and method of making them
US2666718A (en) * 1950-05-25 1954-01-19 Nashua Corp Preparation of sheet material with remoistenable gum coating
US2947647A (en) * 1958-09-24 1960-08-02 Minnesota & Ontario Paper Co Fissured coated fiberboard and method of manufacture

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2214641A (en) * 1937-07-17 1940-09-10 Combined Locks Paper Company Process of producing rotogravure paper and the like
US2337915A (en) * 1940-04-30 1943-12-28 Menger Adolf Shaped body and process of preparing the same
US2442928A (en) * 1945-03-23 1948-06-08 Us Agriculture Food products and method of making them
US2666718A (en) * 1950-05-25 1954-01-19 Nashua Corp Preparation of sheet material with remoistenable gum coating
US2947647A (en) * 1958-09-24 1960-08-02 Minnesota & Ontario Paper Co Fissured coated fiberboard and method of manufacture

Cited By (21)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3395201A (en) * 1964-07-14 1968-07-30 Johnson & Johnson Method and apparatus for producing an absorbent product
US3919042A (en) * 1967-01-05 1975-11-11 Ransburg Electro Coating Corp Method and apparatus for applying dry starch particles to water wet cellulosic webs using electrostatic attraction
US3461032A (en) * 1967-07-19 1969-08-12 Cons Paper Bahamas Ltd Apparatus for applying dry powdered additives to paper on the forming wire using electrostatic attraction
US4353993A (en) * 1981-05-12 1982-10-12 Hercules Incorporated Foam compositions for surface application to fibrous substrates
US4548649A (en) * 1983-11-23 1985-10-22 Westvaco Corporation Foaming agent
US5411637A (en) * 1992-05-22 1995-05-02 Westvaco Corporation Method for producing high pressure laminates
US5433826A (en) * 1992-05-22 1995-07-18 Westvaco Corporation Method for reducing fuzz in the production of saturating kraft paper
US7208429B2 (en) 2004-12-02 2007-04-24 The Procter + Gamble Company Fibrous structures comprising a nonoparticle additive
US20060121207A1 (en) * 2004-12-02 2006-06-08 Prodoehl Michael S Process for making a fibrous structure comprising an additive
US20060121814A1 (en) * 2004-12-02 2006-06-08 The Procter & Gamble Company Fibrous structures comprising a low surface energy additive
US20060121278A1 (en) * 2004-12-02 2006-06-08 Vinson Kenneth D Fibrous structures comprising a nanoparticle additive
US7459179B2 (en) 2004-12-02 2008-12-02 The Procter & Gamble Company Process for making a fibrous structure comprising an additive
US7976679B2 (en) 2004-12-02 2011-07-12 The Procter & Gamble Company Fibrous structures comprising a low surface energy additive
US8398821B2 (en) 2004-12-02 2013-03-19 The Procter & Gamble Company Fibrous structures comprising a low surface energy additive
WO2018011667A1 (en) * 2016-07-11 2018-01-18 Stora Enso Oyj Process for creating a foam utilizing an antimicrobial starch within a process for manufacturing a paper or board product
US11001969B2 (en) 2016-07-11 2021-05-11 Stora Enso Oyj Process for creating a foam utilizing an antimicrobial starch within a process for manufacturing a paper or board product
US11130257B2 (en) 2016-07-11 2021-09-28 Stora Enso Oyj Lignin-based phenolic resin
US11365515B2 (en) 2018-04-04 2022-06-21 Solenis Technologies, L.P. Foam assisted application of strength additives to paper products
US20220243401A1 (en) * 2019-05-14 2022-08-04 Stora Enso Oyj Method for applying starch to a paper or paperboard web
EP3969660A4 (en) * 2019-05-14 2023-06-14 Stora Enso Oyj Method for applying starch to a paper or paperboard web
WO2023137301A1 (en) * 2022-01-11 2023-07-20 Solenis Technologies Cayman, L.P. Foam-assisted application of sizing agents to paper products

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Date Code Title Description
AS Assignment

Owner name: CIP INC.

Free format text: MERGER;ASSIGNORS:CANADIAN INTERNATIONAL PAPER COMPANY;PORTEMIAC PAPER CORPORATION;INTERNATIONAL PAPER SALES COMPANY INC.;AND OTHERS;REEL/FRAME:003933/0966

Effective date: 19811001