US1631750A - Paper product and method of making same - Google Patents
Paper product and method of making same Download PDFInfo
- 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
Links
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/20—Macromolecular organic compounds
- D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
- D21H17/24—Polysaccharides
- D21H17/25—Cellulose
- D21H17/27—Esters 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.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US91815A US1631750A (en) | 1926-03-02 | 1926-03-02 | Paper product and method of making same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US91815A US1631750A (en) | 1926-03-02 | 1926-03-02 | Paper product and method of making same |
Publications (1)
Publication Number | Publication Date |
---|---|
US1631750A true US1631750A (en) | 1927-06-07 |
Family
ID=22229780
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US91815A Expired - Lifetime US1631750A (en) | 1926-03-02 | 1926-03-02 | Paper product and method of making same |
Country Status (1)
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US (1) | US1631750A (en) |
Cited By (40)
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 |
-
1926
- 1926-03-02 US US91815A patent/US1631750A/en not_active Expired - Lifetime
Cited By (41)
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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