US1829585A - Method of preparing impregnated paper products - Google Patents
Method of preparing impregnated paper products Download PDFInfo
- Publication number
- US1829585A US1829585A US236580A US23658027A US1829585A US 1829585 A US1829585 A US 1829585A US 236580 A US236580 A US 236580A US 23658027 A US23658027 A US 23658027A US 1829585 A US1829585 A US 1829585A
- Authority
- US
- United States
- Prior art keywords
- cellulose
- paper
- derivative
- preparing
- sheets
- 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
- D21H13/00—Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
- D21H13/02—Synthetic cellulose fibres
-
- 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
- D21H11/00—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only
- D21H11/16—Pulp or paper, comprising cellulose or lignocellulose fibres of natural origin only modified by a particular after-treatment
- D21H11/20—Chemically or biochemically modified fibres
-
- 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
- D21H13/00—Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
- D21H13/02—Synthetic cellulose fibres
- D21H13/06—Cellulose esters
-
- 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
- D21H13/00—Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
- D21H13/10—Organic non-cellulose fibres
- D21H13/28—Organic non-cellulose fibres from natural polymers
- D21H13/34—Protein fibres
-
- 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
- D21H13/00—Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
- D21H13/36—Inorganic fibres or flakes
- D21H13/38—Inorganic fibres or flakes siliceous
- D21H13/40—Inorganic fibres or flakes siliceous vitreous, e.g. mineral wool, glass fibres
-
- 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
- D21H13/00—Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
- D21H13/36—Inorganic fibres or flakes
- D21H13/38—Inorganic fibres or flakes siliceous
- D21H13/42—Asbestos
-
- 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
Definitions
- 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.
- 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.
- any suitable or desired fillers, siz-. ing materials, pigments or dyes may be incorporated therein.
- 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.
- plasticizers or softeners these aid materially in causing the cellulose derivative to coalesce.
- 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.
- the paper 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.
- 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.
- 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.
- the great advanta e of our invention 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
- 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.
- 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.
- 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.
- 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.
- 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.
- 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.
- 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.
- 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.
- 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.
- 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.
- 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.
Landscapes
- Paper (AREA)
- Laminated Bodies (AREA)
- Synthetic Leather, Interior Materials Or Flexible Sheet Materials (AREA)
Description
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.
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US236580A US1829585A (en) | 1927-11-29 | 1927-11-29 | Method of preparing impregnated paper products |
GB35181/28A GB301428A (en) | 1927-11-29 | 1928-11-29 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US236580A US1829585A (en) | 1927-11-29 | 1927-11-29 | Method of preparing impregnated paper products |
Publications (1)
Publication Number | Publication Date |
---|---|
US1829585A true US1829585A (en) | 1931-10-27 |
Family
ID=22890088
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US236580A Expired - Lifetime US1829585A (en) | 1927-11-29 | 1927-11-29 | Method of preparing impregnated paper products |
Country Status (2)
Country | Link |
---|---|
US (1) | US1829585A (en) |
GB (1) | GB301428A (en) |
Cited By (45)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2526125A (en) * | 1942-05-25 | 1950-10-17 | American Viscose Corp | Paper products and methods of making the same |
US2706156A (en) * | 1952-02-19 | 1955-04-12 | Hurlbut Paper Company | Method of making sheet material |
US2787542A (en) * | 1951-09-17 | 1957-04-02 | Lof Glass Fibers Co | Glass paper |
US2810645A (en) * | 1950-02-09 | 1957-10-22 | American Viscose Corp | Method of making textile webs |
US2810644A (en) * | 1950-02-09 | 1957-10-22 | American Viscose Corp | Paper products and method of making the same |
US2932601A (en) * | 1954-11-12 | 1960-04-12 | Hawley Products Co | Process of preparing felted products containing hydratable and non-hydratable fibers |
US3028296A (en) * | 1958-10-20 | 1962-04-03 | American Can Co | Fibrous sheet material |
US3039914A (en) * | 1959-07-07 | 1962-06-19 | Little Inc A | Process for forming a bonded wetformed web and resulting product |
US3135590A (en) * | 1957-07-12 | 1964-06-02 | Norton Co | Dimensionally stabilized paper and coated abrasives made therefrom |
US3157566A (en) * | 1962-07-17 | 1964-11-17 | Beloit Corp | Method of incorporating resin in molded pulp products |
US4308094A (en) * | 1977-02-02 | 1981-12-29 | Sanyo Electric Co., Ltd. | Diaphragm for speaker and method of producing same |
WO1997020985A1 (en) * | 1995-12-07 | 1997-06-12 | Eastman Chemical Company | High pressure laminates made with paper containing cellulose acetate |
WO1998016688A1 (en) * | 1996-10-11 | 1998-04-23 | Eastman Chemical Company | Plasticized sheets, laminates made from such sheets and process for preparing such laminates |
WO1999011863A1 (en) * | 1997-09-04 | 1999-03-11 | Eastman Chemical Company | Method of making paper |
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 |
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 |
US11332888B2 (en) | 2018-08-23 | 2022-05-17 | Eastman Chemical Company | Paper composition cellulose and cellulose ester for improved texturing |
US11332885B2 (en) | 2018-08-23 | 2022-05-17 | Eastman Chemical Company | Water removal between wire and wet press of a paper mill process |
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 |
US11401659B2 (en) | 2018-08-23 | 2022-08-02 | Eastman Chemical Company | Process to produce a paper article comprising cellulose fibers and a staple fiber |
US11401660B2 (en) | 2018-08-23 | 2022-08-02 | Eastman Chemical Company | Broke composition of matter |
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 |
US11420784B2 (en) | 2018-08-23 | 2022-08-23 | Eastman Chemical Company | Food packaging articles |
US11421385B2 (en) | 2018-08-23 | 2022-08-23 | Eastman Chemical Company | Soft wipe comprising cellulose acetate |
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 |
US11492756B2 (en) | 2018-08-23 | 2022-11-08 | Eastman Chemical Company | Paper press process with high hydrolic pressure |
US11492755B2 (en) | 2018-08-23 | 2022-11-08 | Eastman Chemical Company | Waste recycle composition |
US11492757B2 (en) | 2018-08-23 | 2022-11-08 | Eastman Chemical Company | Composition of matter in a post-refiner blend zone |
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 |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE752791C (en) * | 1941-05-04 | 1953-05-11 | Westfaelisch Anhaltische Spren | Process for the production of artificial leather-like masses |
DE752630C (en) * | 1941-08-20 | 1953-06-15 | Siemens Schuckertwerke A G | Process for the production of paper from esterified, in particular acetylated, fibers |
DE2902957C2 (en) * | 1979-01-26 | 1983-11-24 | Deutsche Automobilgesellschaft Mbh, 3000 Hannover | Process for the production of separators for galvanic cells |
-
1927
- 1927-11-29 US US236580A patent/US1829585A/en not_active Expired - Lifetime
-
1928
- 1928-11-29 GB GB35181/28A patent/GB301428A/en not_active Expired
Cited By (49)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2526125A (en) * | 1942-05-25 | 1950-10-17 | American Viscose Corp | Paper products and methods of making the same |
US2810645A (en) * | 1950-02-09 | 1957-10-22 | American Viscose Corp | Method of making textile webs |
US2810644A (en) * | 1950-02-09 | 1957-10-22 | American Viscose Corp | Paper products and method of making the same |
DE969348C (en) * | 1950-02-09 | 1958-05-22 | American Viscose Corp | Process for the production of porous fiber products such as felts, fleeces or paper from synthetic fibers |
US2787542A (en) * | 1951-09-17 | 1957-04-02 | Lof Glass Fibers Co | Glass paper |
US2706156A (en) * | 1952-02-19 | 1955-04-12 | Hurlbut Paper Company | Method of making sheet material |
US2932601A (en) * | 1954-11-12 | 1960-04-12 | Hawley Products Co | Process of preparing felted products containing hydratable and non-hydratable fibers |
US3135590A (en) * | 1957-07-12 | 1964-06-02 | Norton Co | Dimensionally stabilized paper and coated abrasives made therefrom |
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