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US1631750A - Paper product and method of making same - Google Patents

Paper product and method of making same Download PDF

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Publication number
US1631750A
US1631750A US91815A US9181526A US1631750A US 1631750 A US1631750 A US 1631750A US 91815 A US91815 A US 91815A US 9181526 A US9181526 A US 9181526A US 1631750 A US1631750 A US 1631750A
Authority
US
United States
Prior art keywords
paper
product
cellulose
paper product
cellulose acetate
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US91815A
Inventor
Mcintosh James
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
DIAMOND STATE FIBRE Co
Original Assignee
DIAMOND STATE FIBRE Co
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by DIAMOND STATE FIBRE Co filed Critical DIAMOND STATE FIBRE Co
Priority to US91815A priority Critical patent/US1631750A/en
Application granted granted Critical
Publication of US1631750A publication Critical patent/US1631750A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Classifications

    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • 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
    • D21H17/25Cellulose
    • D21H17/27Esters thereof

Definitions

  • Impregnated and laminated materials have been made by passing the manufactured paper through a bath of synthetic resin solutions and the like, and thereafter heating the sheets under pressure to giveuniform and highly polished surfaces.
  • cellulose ester embraces tha class of compounds which are formed by the action of acids on cellulose, and includes the cellulose acetates and cellulose nitrates but due to the non-infla1nmable nature of the former, I prefer to use that compound.
  • I add the solid ester to the pulp and rag fibres in the beater together with the filling, sizing and dyeing compounds.
  • the action of the beater commlnutes the cellulose ester and uniform ly disperses it throughout the mass.
  • the percentage of the cellulose compound added de ends upon the'properties desired in the finished product.
  • a relatively low ercentage, that is from to (base on the finished product), will give a paper product after treatment, as hereinafter described which will be somewhat "flexible, while a productcontaining about 50% of the cellu- PAPER PRODUCT AND METHOD OF MAKING SAME.
  • lose ester will resemble vulcanized fibre and will be hard, compact and mechanically strong.
  • the paper is processed in the usual manner, since the-presence of the ester has no effect on the materials entering into the paper nor on the mechanical operations. After the paper has left the Fourdrinier machine, it is ready to be vulcanized, that is to be sub- .jected to heat and pressure.
  • the single sheets if they are of the desired thickness, are vulcanized er se, ora laminated product is built up y su erimposing one sheet upon another until tie requisite thickness is obtained. In either case, the heat and pressure step is accomplished in the same manner.
  • the sheets are placed between the heated platens of a suitable press whereby they are subjected to pressure such as one thousand 75 pounds per square inch at a temperature of one hundred and twenty-five pounds of steam. This heat and pressure are maintained for a time sufiicient to cause the cellulose ester to fuse throu hout the fibrous mass and to flow complete y over the surface,
  • the paper sheetscontaining the cellulose acetate after they leave the Fourdrinier machine may be parchmentized in the. usual manner, in which case, for example, the sheets may be passed through a bath of 70-72 Baum zinc chloride at a temperature of 100 to 125 F. whereupon the paper .sheets will be changed to a vegetable parch- I ment membrane and may be, if desired, superimposed to obtain the required thickness.
  • the archmentizing agent is freed from the membrane by leaching in a succession of water baths, called puring baths.
  • parchment membrane containing the cellulose acetate is dried then subjected to the heat 'and pressure treatment hereinbefore described, whereupon thecellulose acetate will fuse throughout the product .and render it morewater-resistant and more durable.
  • a parchmentized paper product comprising a cellulose ester intimately dispersed throughout the paper and rag fibres.
  • a parchmentized paper product comprising cellulose acetate intimately dispersed throughout the paper and rag fibres.

Landscapes

  • Paper (AREA)

Description

Patented June 7, 1927.
UNITED STATES.
VKPATENTA OFFICE.
JAMES MOINTOSH, OF NORRISTOWN, PENNSYLVANIA, ASSIGNOR TO DIAMOND STATE FIBRE COMPANY, OF BBIDGEPORT, PENNSYLVANIA, A CORPORATION 01' DELA- I WARE.
No Drawing.
Impregnated and laminated materialshave been made by passing the manufactured paper through a bath of synthetic resin solutions and the like, and thereafter heating the sheets under pressure to giveuniform and highly polished surfaces.
I have found that if a cellulose ester is added to the pulp or rag fibres during proc-' essing, that treatment under heat and pressure subsequent to the completion of the paper will give a product resembling that 25 made by impregnation. My process ives a product in which the cellulose ester is intimately and uniformly dispersed throughout the fibres as well'as upon the surface, resulting in a more water-proof and more durable product than has previously been possible by impregnation. A further advantage of my process resides in the elimination of one step in the .process, to wit, that of impregnation. r
The term cellulose ester embraces tha class of compounds which are formed by the action of acids on cellulose, and includes the cellulose acetates and cellulose nitrates but due to the non-infla1nmable nature of the former, I prefer to use that compound. In carrying out my process, I add the solid ester to the pulp and rag fibres in the beater together with the filling, sizing and dyeing compounds. The action of the beater commlnutes the cellulose ester and uniform ly disperses it throughout the mass. The percentage of the cellulose compound added de ends upon the'properties desired in the finished product. A relatively low ercentage, that is from to (base on the finished product), will give a paper product after treatment, as hereinafter described which will be somewhat "flexible, while a productcontaining about 50% of the cellu- PAPER PRODUCT AND METHOD OF MAKING SAME.
Application filed March 2, 1826. Serial llo. 91,815.
lose ester will resemble vulcanized fibre and will be hard, compact and mechanically strong.
' The paper is processed in the usual manner, since the-presence of the ester has no effect on the materials entering into the paper nor on the mechanical operations. After the paper has left the Fourdrinier machine, it is ready to be vulcanized, that is to be sub- .jected to heat and pressure. The single sheets, if they are of the desired thickness, are vulcanized er se, ora laminated product is built up y su erimposing one sheet upon another until tie requisite thickness is obtained. In either case, the heat and pressure step is accomplished in the same manner.
The sheets are placed between the heated platens of a suitable press whereby they are subjected to pressure such as one thousand 75 pounds per square inch at a temperature of one hundred and twenty-five pounds of steam. This heat and pressure are maintained for a time sufiicient to cause the cellulose ester to fuse throu hout the fibrous mass and to flow complete y over the surface,
forming a continuous coating. If the platens are highly polished, there will result a .smooth, uniform and highly polished coating of the ester on the surface of the fibrous material. The cellulose ester binds the sheets into a compact inseparable body.
The paper sheetscontaining the cellulose acetate after they leave the Fourdrinier machine may be parchmentized in the. usual manner, in which case, for example, the sheets may be passed through a bath of 70-72 Baum zinc chloride at a temperature of 100 to 125 F. whereupon the paper .sheets will be changed to a vegetable parch- I ment membrane and may be, if desired, superimposed to obtain the required thickness. The archmentizing agent is freed from the membrane by leaching in a succession of water baths, called puring baths. parchment membrane containing the cellulose acetate is dried then subjected to the heat 'and pressure treatment hereinbefore described, whereupon thecellulose acetate will fuse throughout the product .and render it morewater-resistant and more durable.
Instead of treating the parchment membraneafte'r puring by heat and. 'ressure, I
The
have found that satisfactory re ts are obtained if the membrane taken from the puring bath is immersed in a solvent for the cellulose acetate, such as acetone, the solvent will enter the pores displacing the water and causing a film of the acetate to form throughout the product. Upon evaporation of the solvent, a water-resistant fibrous sheet homogeneously impregnated with cellulose acetate will result.
The above described materials are available for a wide variety of uses, such as a raw material from which machine elements such as gears, pulleys, or the like may be formed or machined, and also as an electrical insulator, especially in the construction of switchboards for radio apparatus, a material for making containers, or other structures which it is desirable shall be unafiected by moisture, oil or other liquids. It is also applicable for the surfaceveneering of Wood or cardboard.
Considerable modification is possible in the processing of the paper and in the percentages of cellulose acetate used with no departure from the essential features of the invention.
I claim:
1. The process of making a paper product which comprises adding a cellulose ester to the paper and rag fibres prior to the Fourdrinier machine, processing the paper in the usual manner, parchmentizing the paper,
and thereafter subjecting the sheet to heat and pressurev to cause the cellulose ester to flow throughout the mass.
2. The process of making a paper product which comprises adding cellulose acetate to the paper and rag fibres prior to the Fourdrinier machine, processing the paper in the usual manner, parchmentizing the paper, and thereafter subjecting the sheet to heat and pressure to cause the'cellulose acetate to flowthroughout the mass.
3. The process of making a paper product which comprises adding a cellulose ester to the paper and rag fibres in the beater,
processing the paper in. the usual manner,
parchment-izing the paper, superimposing the sheets to obtain the thickness desired, and thereafter heating the same under pressure to cause the cellulose ester rto flow? throughout the mass. I
4;. The process of making a paper product which comprises adding cellulose acetate to the paper and rag fibres prior to the Fourdrinier' machine, processing the paper in the usual manner, parchmentizing' the paper,
superimposing the sheets to obtain the thickness desired, and thereafter heating the same under pressure to cause the cellulose acetate to flow throughout the mass.
' 5; The process of making a paper product Which comprises adding a cellulose ester to the paper and rag fibres prior to the Fourdrinier machine, processing the paper 'in the usual manner, parchmentizing the paper,
leaching out the parchmentizing agent with water, and thereafter subjecting the parchmentized sheet to the action of a solvent for the cellulose ester whereupon the solvent displaces the water in the pores and causes a film of cellulose ester to form in the parchment membrane.-
6. The process of making a paper product which comprises adding cellulose acetate to the paper and rag fibres prior to the Fourdrinier machine, processing the paper in the usual manner, parchmentizing the paper, leaching out the parchmentizing agent with Water, and thereafter subjecting the parchmentized sheet to the action of a solvent for the cellulose acetate whereupon the solvent displaces the water in the pores and causes a film of the cellulose acetate to form in the parchment membrane.
7. The process of making a paper product which comprises adding'a cellulose ester to the paper and rag fibres prior to the Fourclrinier machine, processing the paperin the .usual manner, parchmentizing the paper,
superimposing the sheets to obtain the thickness desired, and thereafter subjecting the parchmentized sheets to the action-of a solvent for the cellulose ester whereupon the solvent displaces the water in the pores and causes a film of the'cellulose ester to form in the parchment membrane.
8. The process of making a paper product which comprises adding cellulose acetate to the paper and rag fibres prior to the Fourdrinier machine, processing the paper in the usual manner, parchmentizing the paper, superimposing the sheets to obtain the thickness desired, and thereafter subjecting the parchmentized sheets to the action of a solvent for the cellulose acetate whereupon the solvent displaces the water in the pores and causes a film of the cellulose acetate to form in the parchment membrane.
9. A parchmentized paper product comprising a cellulose ester intimately dispersed throughout the paper and rag fibres.
10. A parchmentized paper product comprising cellulose acetate intimately dispersed throughout the paper and rag fibres.
JAMES MoINTOSH.
US91815A 1926-03-02 1926-03-02 Paper product and method of making same Expired - Lifetime US1631750A (en)

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Cited By (40)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2495043A (en) * 1943-10-08 1950-01-17 United States Gypsum Co Laminated product and process of making same
US2806190A (en) * 1952-11-06 1957-09-10 Sprague Electric Co Low power factor capacitor
US3288630A (en) * 1962-08-30 1966-11-29 Hercules Inc Process for coating cellulosic substrates
US5573640A (en) * 1995-07-28 1996-11-12 Eastman Chemical Company Paper made with cellulose fibers having an inner core of cellulose acetate
US5631078A (en) * 1995-10-30 1997-05-20 Eastman Chemical Company Films made from paper containing cellulose ester fiber
US5662773A (en) * 1995-01-19 1997-09-02 Eastman Chemical Company Process for preparation of cellulose acetate filters for use in paper making
WO1997034044A1 (en) * 1996-03-15 1997-09-18 Eastman Chemical Company A method for incorporating cellulose esters into cellulose by immersing cellulose in an acid-dope solution
US5766752A (en) * 1995-12-07 1998-06-16 Eastman Chemical Company High pressure laminates made with paper containing cellulose acetate
US6010595A (en) * 1996-10-11 2000-01-04 Eastman Chemical Company Multiply paper comprising a mixture of cellulose fibers and cellulose ester fibers having imparted softening properties and a method of making the same
US20050042470A1 (en) * 2003-08-22 2005-02-24 Vogler John William Cellulose ester based products and methods for making them
US11230811B2 (en) 2018-08-23 2022-01-25 Eastman Chemical Company Recycle bale comprising cellulose ester
US11286619B2 (en) 2018-08-23 2022-03-29 Eastman Chemical Company Bale of virgin cellulose and cellulose ester
US11299854B2 (en) 2018-08-23 2022-04-12 Eastman Chemical Company Paper product articles
US11306433B2 (en) 2018-08-23 2022-04-19 Eastman Chemical Company Composition of matter effluent from refiner of a wet laid process
US11313081B2 (en) 2018-08-23 2022-04-26 Eastman Chemical Company Beverage filtration article
US11332885B2 (en) 2018-08-23 2022-05-17 Eastman Chemical Company Water removal between wire and wet press of a paper mill process
US11332888B2 (en) 2018-08-23 2022-05-17 Eastman Chemical Company Paper composition cellulose and cellulose ester for improved texturing
US11339537B2 (en) 2018-08-23 2022-05-24 Eastman Chemical Company Paper bag
US11390996B2 (en) 2018-08-23 2022-07-19 Eastman Chemical Company Elongated tubular articles from wet-laid webs
US11390991B2 (en) 2018-08-23 2022-07-19 Eastman Chemical Company Addition of cellulose esters to a paper mill without substantial modifications
US11396726B2 (en) 2018-08-23 2022-07-26 Eastman Chemical Company Air filtration articles
US11401660B2 (en) 2018-08-23 2022-08-02 Eastman Chemical Company Broke composition of matter
US11401659B2 (en) 2018-08-23 2022-08-02 Eastman Chemical Company Process to produce a paper article comprising cellulose fibers and a staple fiber
US11408128B2 (en) 2018-08-23 2022-08-09 Eastman Chemical Company Sheet with high sizing acceptance
US11414791B2 (en) 2018-08-23 2022-08-16 Eastman Chemical Company Recycled deinked sheet articles
US11414818B2 (en) 2018-08-23 2022-08-16 Eastman Chemical Company Dewatering in paper making process
US11421385B2 (en) 2018-08-23 2022-08-23 Eastman Chemical Company Soft wipe comprising cellulose acetate
US11420784B2 (en) 2018-08-23 2022-08-23 Eastman Chemical Company Food packaging articles
US11421387B2 (en) 2018-08-23 2022-08-23 Eastman Chemical Company Tissue product comprising cellulose acetate
US11441267B2 (en) 2018-08-23 2022-09-13 Eastman Chemical Company Refining to a desirable freeness
US11466408B2 (en) 2018-08-23 2022-10-11 Eastman Chemical Company Highly absorbent articles
US11479919B2 (en) 2018-08-23 2022-10-25 Eastman Chemical Company Molded articles from a fiber slurry
US11492757B2 (en) 2018-08-23 2022-11-08 Eastman Chemical Company Composition of matter in a post-refiner blend zone
US11492755B2 (en) 2018-08-23 2022-11-08 Eastman Chemical Company Waste recycle composition
US11492756B2 (en) 2018-08-23 2022-11-08 Eastman Chemical Company Paper press process with high hydrolic pressure
US11512433B2 (en) 2018-08-23 2022-11-29 Eastman Chemical Company Composition of matter feed to a head box
US11519132B2 (en) 2018-08-23 2022-12-06 Eastman Chemical Company Composition of matter in stock preparation zone of wet laid process
US11525215B2 (en) 2018-08-23 2022-12-13 Eastman Chemical Company Cellulose and cellulose ester film
US11530516B2 (en) 2018-08-23 2022-12-20 Eastman Chemical Company Composition of matter in a pre-refiner blend zone
US11639579B2 (en) 2018-08-23 2023-05-02 Eastman Chemical Company Recycle pulp comprising cellulose acetate

Cited By (41)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2495043A (en) * 1943-10-08 1950-01-17 United States Gypsum Co Laminated product and process of making same
US2806190A (en) * 1952-11-06 1957-09-10 Sprague Electric Co Low power factor capacitor
US3288630A (en) * 1962-08-30 1966-11-29 Hercules Inc Process for coating cellulosic substrates
US5662773A (en) * 1995-01-19 1997-09-02 Eastman Chemical Company Process for preparation of cellulose acetate filters for use in paper making
US5573640A (en) * 1995-07-28 1996-11-12 Eastman Chemical Company Paper made with cellulose fibers having an inner core of cellulose acetate
US5631078A (en) * 1995-10-30 1997-05-20 Eastman Chemical Company Films made from paper containing cellulose ester fiber
US5766752A (en) * 1995-12-07 1998-06-16 Eastman Chemical Company High pressure laminates made with paper containing cellulose acetate
US5928777A (en) * 1995-12-07 1999-07-27 Eastman Chemical Company High pressure laminates made with paper containing cellulose acetate
WO1997034044A1 (en) * 1996-03-15 1997-09-18 Eastman Chemical Company A method for incorporating cellulose esters into cellulose by immersing cellulose in an acid-dope solution
US6010595A (en) * 1996-10-11 2000-01-04 Eastman Chemical Company Multiply paper comprising a mixture of cellulose fibers and cellulose ester fibers having imparted softening properties and a method of making the same
US20050042470A1 (en) * 2003-08-22 2005-02-24 Vogler John William Cellulose ester based products and methods for making them
US11390991B2 (en) 2018-08-23 2022-07-19 Eastman Chemical Company Addition of cellulose esters to a paper mill without substantial modifications
US11414818B2 (en) 2018-08-23 2022-08-16 Eastman Chemical Company Dewatering in paper making process
US11299854B2 (en) 2018-08-23 2022-04-12 Eastman Chemical Company Paper product articles
US11306433B2 (en) 2018-08-23 2022-04-19 Eastman Chemical Company Composition of matter effluent from refiner of a wet laid process
US11313081B2 (en) 2018-08-23 2022-04-26 Eastman Chemical Company Beverage filtration article
US11332885B2 (en) 2018-08-23 2022-05-17 Eastman Chemical Company Water removal between wire and wet press of a paper mill process
US11332888B2 (en) 2018-08-23 2022-05-17 Eastman Chemical Company Paper composition cellulose and cellulose ester for improved texturing
US11339537B2 (en) 2018-08-23 2022-05-24 Eastman Chemical Company Paper bag
US11390996B2 (en) 2018-08-23 2022-07-19 Eastman Chemical Company Elongated tubular articles from wet-laid webs
US11230811B2 (en) 2018-08-23 2022-01-25 Eastman Chemical Company Recycle bale comprising cellulose ester
US11396726B2 (en) 2018-08-23 2022-07-26 Eastman Chemical Company Air filtration articles
US11401660B2 (en) 2018-08-23 2022-08-02 Eastman Chemical Company Broke composition of matter
US11401659B2 (en) 2018-08-23 2022-08-02 Eastman Chemical Company Process to produce a paper article comprising cellulose fibers and a staple fiber
US11408128B2 (en) 2018-08-23 2022-08-09 Eastman Chemical Company Sheet with high sizing acceptance
US11414791B2 (en) 2018-08-23 2022-08-16 Eastman Chemical Company Recycled deinked sheet articles
US11286619B2 (en) 2018-08-23 2022-03-29 Eastman Chemical Company Bale of virgin cellulose and cellulose ester
US11421385B2 (en) 2018-08-23 2022-08-23 Eastman Chemical Company Soft wipe comprising cellulose acetate
US11420784B2 (en) 2018-08-23 2022-08-23 Eastman Chemical Company Food packaging articles
US11421387B2 (en) 2018-08-23 2022-08-23 Eastman Chemical Company Tissue product comprising cellulose acetate
US11441267B2 (en) 2018-08-23 2022-09-13 Eastman Chemical Company Refining to a desirable freeness
US11466408B2 (en) 2018-08-23 2022-10-11 Eastman Chemical Company Highly absorbent articles
US11479919B2 (en) 2018-08-23 2022-10-25 Eastman Chemical Company Molded articles from a fiber slurry
US11492757B2 (en) 2018-08-23 2022-11-08 Eastman Chemical Company Composition of matter in a post-refiner blend zone
US11492755B2 (en) 2018-08-23 2022-11-08 Eastman Chemical Company Waste recycle composition
US11492756B2 (en) 2018-08-23 2022-11-08 Eastman Chemical Company Paper press process with high hydrolic pressure
US11512433B2 (en) 2018-08-23 2022-11-29 Eastman Chemical Company Composition of matter feed to a head box
US11519132B2 (en) 2018-08-23 2022-12-06 Eastman Chemical Company Composition of matter in stock preparation zone of wet laid process
US11525215B2 (en) 2018-08-23 2022-12-13 Eastman Chemical Company Cellulose and cellulose ester film
US11530516B2 (en) 2018-08-23 2022-12-20 Eastman Chemical Company Composition of matter in a pre-refiner blend zone
US11639579B2 (en) 2018-08-23 2023-05-02 Eastman Chemical Company Recycle pulp comprising cellulose acetate

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