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US1829585A - Method of preparing impregnated paper products - Google Patents

Method of preparing impregnated paper products
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Publication number
US1829585A
US1829585AUS236580AUS23658027AUS1829585AUS 1829585 AUS1829585 AUS 1829585AUS 236580 AUS236580 AUS 236580AUS 23658027 AUS23658027 AUS 23658027AUS 1829585 AUS1829585 AUS 1829585A
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United States
Prior art keywords
cellulose
paper
derivative
preparing
sheets
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Expired - Lifetime
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US236580A
Inventor
Dreyfus Camille
George W Miles
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Celanese Corp
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Celanese Corp
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Publication date
Application filed by Celanese CorpfiledCriticalCelanese Corp
Priority to US236580ApriorityCriticalpatent/US1829585A/en
Priority to GB35181/28Aprioritypatent/GB301428A/en
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Publication of US1829585ApublicationCriticalpatent/US1829585A/en
Anticipated expirationlegal-statusCritical
Expired - Lifetimelegal-statusCriticalCurrent

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Patented Oct. 27, 1931 UNITED STATES PATENT orrl ca GAMBLE DREYFUS, OF NEW YORK, N. '21, AND GEORGE W. MILES, OB BOSTON, MASSA- CHUSETTS, ASSIGNORS '10 CELANESE CORPORATION OF AMERICA, A. CORPORATION OF DELAWARE METHOD OF PREPARING" IMPREGNATED PAPER PRODUCTS No Drawing.
This invention relates to a new method of preparing paper, sheets, boards or laminated products made of fibres such as wood pulp or rag stock, asbestos, mineral wool, IL spun glass, leather fibres, etc. and having incorporated therein a derivative of cellulose. An object of our invention is to prepare a material containing the ordinary paper making fibres, or other vegetable, animal or min- 10 eral fibres, which material is strong,.water resistant-and thermoplastic.
Another object of our invention is to prepare paper, sheets, boards or comparatively thick laminated products by incorporating in a paper pulp, derivatives of cellulose in such manner that the same is thoroughly disseminated throughout the mass so that very large amountsof cellulose-derivatives may be added thereto while still obtaining a uniform product. Other objects of our invention will appear from the following detailed description.
In accordance with our invention we add a derivative of cellulose to the paper stock while it is in the beater. The paper stock may comprise wood pulp, rag fibres or any other vegetable fibres or animal fibres such as leather fibres made from leather scrap, or mineral fibres such as asbestos, mineral wool or spun glass suitable for paper making. The stock may contain one or a mixture of two or more of the above named materials. Moreover, any suitable or desired fillers, siz-. ing materials, pigments or dyes may be incorporated therein. i
In order to have the derivative of cellulose uniformly and tenaciously held in admixture with the pulp or rag fibres, we use one or preferably both of the following expedients. As one expedient we have found that if the derivative of cellulose is added in the form of fibres rather than in the form of powder, the cellulose derivative fibres intertwine with the fibres of the paper stock so that an extremely large proportion of cellulose derivative may be added to the pulp without separating out. As another expedient, we have further found that if a high boiling solvent, softener or plastic-izer is added with the cellulose derivative, a uniform product may be Application filed November 29, 1927. Serial No. 236,580.
obtained with ut the addition of large amounts of cel ulose derivative, because of the action of the high boiling point solvent, softeners or plasticizers in preparing the cellulose derivative in such physical form so that it can be thoroughly distributed throughout the aqueous mass containin the paper stock. After the admixture o the cellulose derivative in the beater with the paper stock, the same is processed in the usual manner, being eventuall passed to the Fou'rdrinier machine from w ich the paper 1s drawn to be subjected to the finishing operations.
The paper may be placed between heated rollers under 'gh pressure, whereu on the articles of cellulose derivative coa esce to orm a continuous mass embedding the wood, rag or other vegetable, animal or mineral fibres. When plasticizers or softeners are used, these aid materially in causing the cellulose derivative to coalesce. Or else, a solvent for the cellulose derivative may be applied to the paper by brushing, spraying, dipp ng or otherwise coating, and then,- with or wlthout rolling, upon evaporation of the solvent, the cellulose derivative is formed as a continuous film. When it is desired to form a laminated product, the paper, after it leaves the Fourdrinier machme, is built up in layers to the desired thickness and hotv pressed to cause the cellulose derivative to coalesce and form a solid mass. Or else, a solvent for the cellulose derivative may be applied to the paper prior to the building up of the same layers and then the mass is pressed to cause consolidation of the layers 1n one mass.
In another form ofour invention, especially for making leather boards, a pulp containing leather fibres and the cellulose derivative with or without a softener, plasticizer, or high boilin solvent, is placed in a wet machine provi ed with a revolving perforated cylinder. As the cylinder revolves in the machine, suction is applied to the interior thereof and thus a film of fibres is collected on its surface. lVhen a layer of sufficient thickness is built up on the cylinder, the cylindrical layer of fibres is slit with a knife, the sheet ished product. Thus for a writing paper, a
then removed and then dried in any suitable manner.
The amount of cellulose derivative that is.
added may be varied within wide limits dending upon the requirements of the finrelatively small amount of cellulose der vative, say from to based on the weight of the paper, is suflicient. A
The great advanta e of our invention, however, is due to the act that by our process lar e amounts as high as 100% of cellulose derlvative based on theweight of the other ingredients of the paper may be incorporated therein. With the larger percentages of cellulose derivative, hard, sti and themoplastic products ma be produced. The addition of the high boi ing point solvent, plasticizer or softener is of particular advantage when large proportions of cellulose derivatives are used, since the product thus formed is not brittle but is pliant and adaptable for many uses, and can be worked under less heat and pressure than when they are not used, and
yet the use of volatile solvents is avoided.
The cellulosederivative used in this invention 'may be cellulose nitrate or organic substitution derivatives of cellulose. Since the organic substitution derivatives of cellulose are not inflammable, they are preferred over the inflammable cellulose nitrate. The organic substitution derivatives of cellulose include cellulose esters such as cellulose formats, cellulose acetate, cellulose propionate, cellulose butyrate and cellulose ethers such as methyl cellulose, ethyl cellulose and ben zyl cellulose. However, at the present time cellulose acetate is preferred because of economy and ease of 'working. The cellulose acetate best used in this process is a hydrated cellulose acetate preferably formed by ripening the cellulose acetate after acetylatlon in the presence of 5 water and then precipitating the same with water under such conditions that the cellulose acetate assumes a fibrous form. The cellulose acetate that is added to the pulp in the beater should preferably be either freshly prepared or else kept moist so that it does not harden and become friable. The plasticizer, softener or high boiling solvent used may be of any suitable nature such as diethyl phthalate, tricresyl phosphate, triphenyl phosphate, triacetin, diacetin, etc. The volatile solvent that may be used may. be any known solvent such as acetone, alcohol, etht r, benzene, ethylene dichloride, etc.
The product formed in. accordance with our invention may be used for any of the processes for which it is adapted because of itswaterproof, electrical insulating and ther- It is to be understood that the foregoing details are given merely by way of illustration and that many variations may be made therein without departing from the spirit of our invention. 4
Having described our invention what we claim and desire to secure by Letters Patent is: l
- 1. Process of preparing an impregnated paper product comprising adding a cellulose derivative in a fibrous form to a paper stock, forming the same into sheets and fixing the said cellulose derivative therein.
2. Process of preparing an impregnated paper product comprising adding an organic substitution derivative of cellulose in a fibrous form to a paper stock, forming the same into sheets and fixing the said organic substitution derivative of cellulose therein.
3. Process of preparing an impregnated paper product comprising adding an organic ester of cellulose in a fibrous form to a paper stock, forming the same into sheets and fixing the said organic ester of cellulose therein.
4. Process of preparing an impregnated paper product comprlsing adding cellulose acetate in a fibrous form -to a paper stock, forming the same into sheets and fixing the said cellulose acetate therein.
5. Process of preparing an impregnated acetate in a fibrous form with a paper stock in a pulp beater, forming the resulting prod- .95 paper product comprising mixing cellulose cellulose acetate in a fibrous form with a paper stock in'a pulp beater forming the resulting product into sheets, removing excess moisture and then causing the cellulose acetate to coalesce.
7. Process of preparing an impregnated paper product comprising mixing hydrated cellulose acetate in a fibrous form with a paper stock in a pulp beater, forming the resulting product into sheets, removing excess moisture and then passing the sheets between heated rollers to cause the cellulose acetate to coalesce.
8. Process of preparing an impregnated paper product comprising mixing hydrated cellulose acetate in a fibrous form with a paper 'stock in a pulp beater, forming the resultingproduct into sheets, removing excess moisture, forming layers of the sheets and then causing the cellulose acetate to coalesce to form a laminated product.
9. Process of preparing an impregnated paper product comprising mixing hydrated cellulose acetate in a fibrous form with a pa- 1 per stock in a pulp beater, forming the resulting product into sheets, removing excess moisture, forming layers of the sheets and then passing the sheets between heated rollers under pressure to cause the cellulose acetate to coalesce to form a laminated product.
10. Process of preparing impregnated paper product comprising mixing a cellulose derivative in unplastified state and a plasticizer with the paper stock, forming the same. into sheets and fixing the said cellulose derivative therein.
11. Process of preparing an impregnated paper product comprising mixing an organic substitution derivative of cellulose in unplastified state and a plasticizer with the paper stock, forming the same into sheets and fixing the said organic substitution derivative of cellulose therein.
12. Process of preparing an impregnated paper product comprising mixing cellulose acetate in unplastified state and a plasticizer with the paper stock, forming the same into sheets and fixing the said cellulose acetate therein.
13. Process of preparing an impregnated paper product comprising mixing cellulose acetate in unplastified state and a plasticizer with the paper stock, forming the same into sheets and fixing the said cellulose acetate therein by passing the same between heated i-ollers to cause the cellulose acetate to coaesce.
In testimony whereof, we have hereunto subscribed our names.
CAMILLE DREYFUS. GEORGE W. MILES.
US236580A1927-11-291927-11-29Method of preparing impregnated paper productsExpired - LifetimeUS1829585A (en)

Priority Applications (2)

Application NumberPriority DateFiling DateTitle
US236580AUS1829585A (en)1927-11-291927-11-29Method of preparing impregnated paper products
GB35181/28AGB301428A (en)1927-11-291928-11-29

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US236580AUS1829585A (en)1927-11-291927-11-29Method of preparing impregnated paper products

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Cited By (45)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US2526125A (en)*1942-05-251950-10-17American Viscose CorpPaper products and methods of making the same
US2706156A (en)*1952-02-191955-04-12Hurlbut Paper CompanyMethod of making sheet material
US2787542A (en)*1951-09-171957-04-02Lof Glass Fibers CoGlass paper
US2810644A (en)*1950-02-091957-10-22American Viscose CorpPaper products and method of making the same
US2810645A (en)*1950-02-091957-10-22American Viscose CorpMethod of making textile webs
US2932601A (en)*1954-11-121960-04-12Hawley Products CoProcess of preparing felted products containing hydratable and non-hydratable fibers
US3028296A (en)*1958-10-201962-04-03American Can CoFibrous sheet material
US3039914A (en)*1959-07-071962-06-19Little Inc AProcess for forming a bonded wetformed web and resulting product
US3135590A (en)*1957-07-121964-06-02Norton CoDimensionally stabilized paper and coated abrasives made therefrom
US3157566A (en)*1962-07-171964-11-17Beloit CorpMethod of incorporating resin in molded pulp products
US4308094A (en)*1977-02-021981-12-29Sanyo Electric Co., Ltd.Diaphragm for speaker and method of producing same
WO1997020985A1 (en)*1995-12-071997-06-12Eastman Chemical CompanyHigh pressure laminates made with paper containing cellulose acetate
WO1998016688A1 (en)*1996-10-111998-04-23Eastman Chemical CompanyPlasticized sheets, laminates made from such sheets and process for preparing such laminates
WO1999011863A1 (en)*1997-09-041999-03-11Eastman Chemical CompanyMethod of making paper
US6010595A (en)*1996-10-112000-01-04Eastman Chemical CompanyMultiply paper comprising a mixture of cellulose fibers and cellulose ester fibers having imparted softening properties and a method of making the same
US11230811B2 (en)2018-08-232022-01-25Eastman Chemical CompanyRecycle bale comprising cellulose ester
US11286619B2 (en)2018-08-232022-03-29Eastman Chemical CompanyBale of virgin cellulose and cellulose ester
US11299854B2 (en)2018-08-232022-04-12Eastman Chemical CompanyPaper product articles
US11306433B2 (en)2018-08-232022-04-19Eastman Chemical CompanyComposition of matter effluent from refiner of a wet laid process
US11313081B2 (en)2018-08-232022-04-26Eastman Chemical CompanyBeverage filtration article
US11332885B2 (en)2018-08-232022-05-17Eastman Chemical CompanyWater removal between wire and wet press of a paper mill process
US11332888B2 (en)2018-08-232022-05-17Eastman Chemical CompanyPaper composition cellulose and cellulose ester for improved texturing
US11339537B2 (en)2018-08-232022-05-24Eastman Chemical CompanyPaper bag
US11390991B2 (en)2018-08-232022-07-19Eastman Chemical CompanyAddition of cellulose esters to a paper mill without substantial modifications
US11390996B2 (en)2018-08-232022-07-19Eastman Chemical CompanyElongated tubular articles from wet-laid webs
US11396726B2 (en)2018-08-232022-07-26Eastman Chemical CompanyAir filtration articles
US11401659B2 (en)2018-08-232022-08-02Eastman Chemical CompanyProcess to produce a paper article comprising cellulose fibers and a staple fiber
US11401660B2 (en)2018-08-232022-08-02Eastman Chemical CompanyBroke composition of matter
US11408128B2 (en)2018-08-232022-08-09Eastman Chemical CompanySheet with high sizing acceptance
US11414791B2 (en)2018-08-232022-08-16Eastman Chemical CompanyRecycled deinked sheet articles
US11414818B2 (en)2018-08-232022-08-16Eastman Chemical CompanyDewatering in paper making process
US11420784B2 (en)2018-08-232022-08-23Eastman Chemical CompanyFood packaging articles
US11421385B2 (en)2018-08-232022-08-23Eastman Chemical CompanySoft wipe comprising cellulose acetate
US11421387B2 (en)2018-08-232022-08-23Eastman Chemical CompanyTissue product comprising cellulose acetate
US11441267B2 (en)2018-08-232022-09-13Eastman Chemical CompanyRefining to a desirable freeness
US11466408B2 (en)2018-08-232022-10-11Eastman Chemical CompanyHighly absorbent articles
US11479919B2 (en)2018-08-232022-10-25Eastman Chemical CompanyMolded articles from a fiber slurry
US11492755B2 (en)2018-08-232022-11-08Eastman Chemical CompanyWaste recycle composition
US11492757B2 (en)2018-08-232022-11-08Eastman Chemical CompanyComposition of matter in a post-refiner blend zone
US11492756B2 (en)2018-08-232022-11-08Eastman Chemical CompanyPaper press process with high hydrolic pressure
US11512433B2 (en)2018-08-232022-11-29Eastman Chemical CompanyComposition of matter feed to a head box
US11519132B2 (en)2018-08-232022-12-06Eastman Chemical CompanyComposition of matter in stock preparation zone of wet laid process
US11525215B2 (en)2018-08-232022-12-13Eastman Chemical CompanyCellulose and cellulose ester film
US11530516B2 (en)2018-08-232022-12-20Eastman Chemical CompanyComposition of matter in a pre-refiner blend zone
US11639579B2 (en)2018-08-232023-05-02Eastman Chemical CompanyRecycle pulp comprising cellulose acetate

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
DE752791C (en)*1941-05-041953-05-11Westfaelisch Anhaltische Spren Process for the production of artificial leather-like masses
DE752630C (en)*1941-08-201953-06-15Siemens Schuckertwerke A G Process for the production of paper from esterified, in particular acetylated, fibers
DE2902957C2 (en)*1979-01-261983-11-24Deutsche Automobilgesellschaft Mbh, 3000 Hannover Process for the production of separators for galvanic cells

Cited By (49)

* Cited by examiner, † Cited by third party
Publication numberPriority datePublication dateAssigneeTitle
US2526125A (en)*1942-05-251950-10-17American Viscose CorpPaper products and methods of making the same
US2810644A (en)*1950-02-091957-10-22American Viscose CorpPaper products and method of making the same
US2810645A (en)*1950-02-091957-10-22American Viscose CorpMethod of making textile webs
DE969348C (en)*1950-02-091958-05-22American Viscose Corp Process for the production of porous fiber products such as felts, fleeces or paper from synthetic fibers
US2787542A (en)*1951-09-171957-04-02Lof Glass Fibers CoGlass paper
US2706156A (en)*1952-02-191955-04-12Hurlbut Paper CompanyMethod of making sheet material
US2932601A (en)*1954-11-121960-04-12Hawley Products CoProcess of preparing felted products containing hydratable and non-hydratable fibers
US3135590A (en)*1957-07-121964-06-02Norton CoDimensionally stabilized paper and coated abrasives made therefrom
US3028296A (en)*1958-10-201962-04-03American Can CoFibrous sheet material
US3039914A (en)*1959-07-071962-06-19Little Inc AProcess for forming a bonded wetformed web and resulting product
US3157566A (en)*1962-07-171964-11-17Beloit CorpMethod of incorporating resin in molded pulp products
US4308094A (en)*1977-02-021981-12-29Sanyo Electric Co., Ltd.Diaphragm for speaker and method of producing same
WO1997020985A1 (en)*1995-12-071997-06-12Eastman Chemical CompanyHigh pressure laminates made with paper containing cellulose acetate
US5766752A (en)*1995-12-071998-06-16Eastman Chemical CompanyHigh pressure laminates made with paper containing cellulose acetate
US5928777A (en)*1995-12-071999-07-27Eastman Chemical CompanyHigh pressure laminates made with paper containing cellulose acetate
WO1998016688A1 (en)*1996-10-111998-04-23Eastman Chemical CompanyPlasticized sheets, laminates made from such sheets and process for preparing such laminates
US5922451A (en)*1996-10-111999-07-13Eastman Chemical CompanyPlasticized sheets, laminates made from such sheets, and process for preparing such laminates
US6010595A (en)*1996-10-112000-01-04Eastman Chemical CompanyMultiply paper comprising a mixture of cellulose fibers and cellulose ester fibers having imparted softening properties and a method of making the same
WO1999011863A1 (en)*1997-09-041999-03-11Eastman Chemical CompanyMethod of making paper
US11332885B2 (en)2018-08-232022-05-17Eastman Chemical CompanyWater removal between wire and wet press of a paper mill process
US11414818B2 (en)2018-08-232022-08-16Eastman Chemical CompanyDewatering in paper making process
US11299854B2 (en)2018-08-232022-04-12Eastman Chemical CompanyPaper product articles
US11306433B2 (en)2018-08-232022-04-19Eastman Chemical CompanyComposition of matter effluent from refiner of a wet laid process
US11313081B2 (en)2018-08-232022-04-26Eastman Chemical CompanyBeverage filtration article
US11230811B2 (en)2018-08-232022-01-25Eastman Chemical CompanyRecycle bale comprising cellulose ester
US11332888B2 (en)2018-08-232022-05-17Eastman Chemical CompanyPaper composition cellulose and cellulose ester for improved texturing
US11339537B2 (en)2018-08-232022-05-24Eastman Chemical CompanyPaper bag
US11390991B2 (en)2018-08-232022-07-19Eastman Chemical CompanyAddition of cellulose esters to a paper mill without substantial modifications
US11390996B2 (en)2018-08-232022-07-19Eastman Chemical CompanyElongated tubular articles from wet-laid webs
US11396726B2 (en)2018-08-232022-07-26Eastman Chemical CompanyAir filtration articles
US11401659B2 (en)2018-08-232022-08-02Eastman Chemical CompanyProcess to produce a paper article comprising cellulose fibers and a staple fiber
US11401660B2 (en)2018-08-232022-08-02Eastman Chemical CompanyBroke composition of matter
US11408128B2 (en)2018-08-232022-08-09Eastman Chemical CompanySheet with high sizing acceptance
US11414791B2 (en)2018-08-232022-08-16Eastman Chemical CompanyRecycled deinked sheet articles
US11286619B2 (en)2018-08-232022-03-29Eastman Chemical CompanyBale of virgin cellulose and cellulose ester
US11420784B2 (en)2018-08-232022-08-23Eastman Chemical CompanyFood packaging articles
US11421385B2 (en)2018-08-232022-08-23Eastman Chemical CompanySoft wipe comprising cellulose acetate
US11421387B2 (en)2018-08-232022-08-23Eastman Chemical CompanyTissue product comprising cellulose acetate
US11441267B2 (en)2018-08-232022-09-13Eastman Chemical CompanyRefining to a desirable freeness
US11466408B2 (en)2018-08-232022-10-11Eastman Chemical CompanyHighly absorbent articles
US11479919B2 (en)2018-08-232022-10-25Eastman Chemical CompanyMolded articles from a fiber slurry
US11492755B2 (en)2018-08-232022-11-08Eastman Chemical CompanyWaste recycle composition
US11492757B2 (en)2018-08-232022-11-08Eastman Chemical CompanyComposition of matter in a post-refiner blend zone
US11492756B2 (en)2018-08-232022-11-08Eastman Chemical CompanyPaper press process with high hydrolic pressure
US11512433B2 (en)2018-08-232022-11-29Eastman Chemical CompanyComposition of matter feed to a head box
US11519132B2 (en)2018-08-232022-12-06Eastman Chemical CompanyComposition of matter in stock preparation zone of wet laid process
US11525215B2 (en)2018-08-232022-12-13Eastman Chemical CompanyCellulose and cellulose ester film
US11530516B2 (en)2018-08-232022-12-20Eastman Chemical CompanyComposition of matter in a pre-refiner blend zone
US11639579B2 (en)2018-08-232023-05-02Eastman Chemical CompanyRecycle pulp comprising cellulose acetate

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