US2887429A - Method of preparing webs from cellulose esters - Google Patents

Method of preparing webs from cellulose esters Download PDF

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Publication number
US2887429A
US2887429A US661623A US66162357A US2887429A US 2887429 A US2887429 A US 2887429A US 661623 A US661623 A US 661623A US 66162357 A US66162357 A US 66162357A US 2887429 A US2887429 A US 2887429A
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cellulose
water
sheet
cellulose ester
suspension
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US661623A
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William H Griggs
Ralph D Zaffrann
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Eastman Kodak Co
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Eastman Kodak Co
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    • DTEXTILES; PAPER
    • D21PAPER-MAKING; PRODUCTION OF CELLULOSE
    • D21HPULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
    • D21H13/00Pulp or paper, comprising synthetic cellulose or non-cellulose fibres or web-forming material
    • D21H13/02Synthetic cellulose fibres
    • D21H13/06Cellulose esters

Definitions

  • the Snead and Peters application describes a method for making webs and sheets from cellulose esters in which a fibrous flocculated precipitate of the cellulose ester is suspended in water and the resulting suspension is laid down on a foraminous surface such as the wire of a paper machine to form a sheet thereof.
  • the sheets thus formed are useful for the preparation of cellulose ester sheeting of good properties.
  • a cellulose ester in the form of a fibrous flocculated precipitate is dispersed in water and the dispersion so formed is laid down on the wire of the paper machine.
  • the cellulose acetate staple fiber employed is desirably material of the conventional type, unplasticized and having a fiber length of A to 1 inch.
  • Cellulose acetate staple fiber is a well-known material and is described in texts such as The New Fibers, by Sherman and Sher- 2,887,429 Patented May 19, 1959 "ice man (1946), Van Nostrand, pp. 235-245, and Rayon and Staple Fiber Handbook, by Mauersberger and Schwarz, 3d edition, page 42, Rayon Handbook Co.
  • the cellulose acetate staple fiber can be varied from 5l0% of the total fiber furnish, approximately 8% being preferred.
  • Also added is an emulsion of a liquid plasticizer in aqueous dispersion.
  • any of the liquid plasticizers compatible with the cellulose ester may be added to the mass in this manner.
  • cellulose acetate plasticizers such as diethyl phthalate or dimethyl phthalate has been found to be eminently suitable while for other fatty acid esters of cellulose such as cellulose acetate butyrate, plasticizers such as dibutyl sebacate, dibutyl phthalate or dioctyl phthalate are useful.
  • Plasticizers of the glycol type such as triethylene glycol dicaprylate are useful for the propionic acid esters of cellulose.
  • a slurry or suspension of cellulose ester fiber and staple is prepared in any suitable apparatus such as a hollander, hydrapulper, turbomixer or the like wherein the slurry is formed without breaking up or otherwise altering the physical properties of the fibers.
  • the aqueous suspension of fibrous cellulose ester, staple fiber and plasticizer emulsion is diluted to a low consistency such as on the order of 0.51% (if not already dilute) and is applied to the wire of the paper machine.
  • the web after formation may be pressed to impart increased strength and compactness and may be dried at a moderately elevated temperature such as in an oven or a drying drum.
  • the product may be marketed either in that form or after subjecting to a partial or complete fusion by the use of heat and pressure. The product is useful for forming into sheet material or shaped products by the use of elevated temperatures and pressures as desired.
  • Example 1 A slurry of pounds of precipitated fibrous cellulose acetate in 1250 pounds of water was added to a conventional paper machine mixing chest having 1250 pounds of water therein. After this addition, 800 pounds more water were added.
  • Example 2 A procedure as described in the preceding example was carried out but a shower of steam of sufiicient width to cover the span of the web was applied to the Web surface at a point from two to six inches ahead of the nip of the pressure couch employed in the web making operation.
  • the steam had a softening effect on the plasticized cellulose acetate web which was sufiicient to permit the pressure from the couch rolls to partially fuse the acetate fibers of the web.
  • the sheet thus obtained exhibited extraordinary high wet strength and could be readily handled.
  • the plasticizers used in cellulose dispersions in carrying out our invention are first emulsified to form an aqueous emulsion thereof by means of a surface active agent which will retain the plasticizer in the water in dispersed form.
  • the surface active agent used may be any compound which is commonly known as suitable for use in preparing oil-in-water emulsions. It may be of the non-ionic type, for instance, an alkyl aryl polyether alcohol, such as is marketed as Triton N-IOO, or it may be of the cationic type, for instance stearyl dimethyl benzyl ammonium chloride, such as is marketed as Triton X-400.
  • a method of making sheets adapted to be formed into products which comprises forming a dilute suspension in water of a fibrous fiocculated precipitate of a lower fatty acid ester of cellulose and 510% of cellulose ester staple fiber, laying down the suspension onto a foraminous surface to form a sheet therefrom and drying the so formed sheet.
  • a method of forming sheets adapted to be formed into desired products which comprises forming a dilute suspension in water of a fibrous fiocculated precipitate of a lower fatty acid ester of cellulose and 510% of cellulose ester staple fiber, adding thereto an aqueous emulsion of a plasticizer for the cellulose esters, laying down the suspension onto a foraminous surface to form a sheet therefrom and drying the so formed sheet.
  • a method of making colloidized cellulose ester sheeting which comprises forming a suspension in water of a fibrous fiocculated precipitate of a lower fatty acid ester of cellulose and 5-10% of cellulose ester staple fiber, adding thereto an aqueous emulsion of a cellulose assmes 4 ester plasticizer, laying down the suspension onto a. foraminous sheet and subjecting to sufficient heat and pressure to at least partially fuse the material.
  • a method of making sheets adapted to be formed into desired products which comprises forming a dilute suspension in water of a fibrous fiocculated precipitate of a lower fatty acid ester of cellulose and 540% of cellulose ester staple fiber, adding thereto an aqueous emulsion of a plasticizer, laying down the suspension onto a foraminous surface to form a sheet therefrom, subjecting the sheet thus formed to a jet of steam followed by subjecting the sheet to pressure suflicient to at least partially fuse the fibers thereof.
  • a method of making sheets adapted to be formed into desired products which comprises forming a dilute suspension in water of a fibrous fiocculated precipitate of a lower fatty acid ester of cellulose and 5-10% of cellulose ester staple fiber, laying down the suspension thus formed onto the wire of a paper machine and drying the thus formed product.
  • a method of making sheets adapted to be formed into desired products which comprises forming a dilute suspension in water of a fibrous fiocculated precipitate of a lower fatty acid ester of cellulose and 5-10% of cellulose acetate staple fiber, laying down the suspension onto a foraminous surface to form a sheet therefrom and drying the thus formed sheet.
  • a method of making sheets adapted to be formed into desired products which comprises forming a dilute suspension in water of a fibrous fiocculated precipitate of cellulose acetate and 5-10% of cellulose acetate staple fiber, adding thereto an aqeous emulsion of a cellulose acetate plasticizer, laying down the suspension onto a foraminous surface to form a sheet therefrom and drying the thus formed sheet.

Description

METHOD OF PREPARING WEBS FROM CELLULOSE ESTERS William H. Griggs and Ralph D. Zafirann, Rochester,
N.Y., assignors to Eastman Kodak Company, Rochester, N.Y., a corporation of New Jersey No Drawing. Application May 27, 1957 Serial No. 661,623
7 Claims. (Cl. 162-146) This application relates to an improved method of preparing cellulose ester webs which includes the incorporation of staple fibers and plasticizer in the slurry of fibrous cellulose ester from which the web is formed. This invention is an improvement of the invention described in U.S. application Serial No. 533,526, of Charles D. Snead and Ralph W. Peters, filed September 9, 1955.
The Snead and Peters application describes a method for making webs and sheets from cellulose esters in which a fibrous flocculated precipitate of the cellulose ester is suspended in water and the resulting suspension is laid down on a foraminous surface such as the wire of a paper machine to form a sheet thereof. The sheets thus formed are useful for the preparation of cellulose ester sheeting of good properties.
One object of our invention is to provide a method of preparing sheets or webs of cellulose ester material. Another object of our invention is to provide a method of preparing cellulose ester sheeting in which the use of solvent is eliminated. A further object of our invention is to provide a method of making cellulose ester web in which the stock on the paper machine wire is freer and has better drainage than the web which has been formed heretofore from cellulose ester fibers. A still further object of our invention is to provide a method of preparing cellulose ester webs which possess considerably more internal strength than that of the webs which have been prepared heretofore by similar procedures. Other objects of our invention appear herein.
In the Snead and Peters method of preparing cellulose ester webs a cellulose ester in the form of a fibrous flocculated precipitate is dispersed in water and the dispersion so formed is laid down on the wire of the paper machine.
We have found that by incorporating, in the cellulose ester material, to 10% of cellulose acetate staple fiber, based on the total weight of the fiber furnish prior to depositing it on the wire of the paper machine, additional advantages are obtained over those obtained when merely precipitated cellulose ester is employed for this purpose. By incorporating the cellulose acetate staple in the mass there is obtained a furnish which gives a much freer stock on the paper machine wire with much faster drainage and as a result the machine speed may be increased several fold. The staple fiber also acts as a bonding agent which gives the sheet good internal strength so that it may be stripped from the wire and moved to the press rolls without the necessity for a carrying felt. In addition, an emulsion of a liquid plasticizer is incorporated in the dispersion from which the paper is made. The plasticizer becomes intimately associated with the cellulose ester mass and thereby facilitates the conversion of the web into sheeting in subsequent operations.
The cellulose acetate staple fiber employed is desirably material of the conventional type, unplasticized and having a fiber length of A to 1 inch. Cellulose acetate staple fiber is a well-known material and is described in texts such as The New Fibers, by Sherman and Sher- 2,887,429 Patented May 19, 1959 "ice man (1946), Van Nostrand, pp. 235-245, and Rayon and Staple Fiber Handbook, by Mauersberger and Schwarz, 3d edition, page 42, Rayon Handbook Co. The cellulose acetate staple fiber can be varied from 5l0% of the total fiber furnish, approximately 8% being preferred. Also added is an emulsion of a liquid plasticizer in aqueous dispersion. Any of the liquid plasticizers compatible with the cellulose ester (particularly those of the ester type) may be added to the mass in this manner. For cellulose acetate plasticizers such as diethyl phthalate or dimethyl phthalate has been found to be eminently suitable while for other fatty acid esters of cellulose such as cellulose acetate butyrate, plasticizers such as dibutyl sebacate, dibutyl phthalate or dioctyl phthalate are useful. Plasticizers of the glycol type such as triethylene glycol dicaprylate are useful for the propionic acid esters of cellulose.
A slurry or suspension of cellulose ester fiber and staple is prepared in any suitable apparatus such as a hollander, hydrapulper, turbomixer or the like wherein the slurry is formed without breaking up or otherwise altering the physical properties of the fibers.
In making the web, the aqueous suspension of fibrous cellulose ester, staple fiber and plasticizer emulsion is diluted to a low consistency such as on the order of 0.51% (if not already dilute) and is applied to the wire of the paper machine. The web after formation may be pressed to impart increased strength and compactness and may be dried at a moderately elevated temperature such as in an oven or a drying drum. The product may be marketed either in that form or after subjecting to a partial or complete fusion by the use of heat and pressure. The product is useful for forming into sheet material or shaped products by the use of elevated temperatures and pressures as desired.
We have found that in our operations it is often desirable to use a steam jet on the surface of the web which is formed on the wire of the paper machine shortly prior to the time the web is subjected to treatment in a pressure couch roll operation which acts to compact the sheet, makes it very much stronger and contributes to softening of the product prior to the pressing operation. Thereby the operating conditions in the pressing and drying ends of the machine are greatly facilitated. The following examples are illustrative of the invention:
Example 1 A slurry of pounds of precipitated fibrous cellulose acetate in 1250 pounds of water was added to a conventional paper machine mixing chest having 1250 pounds of water therein. After this addition, 800 pounds more water were added.
10 pounds of inch cellulose acetate staple fiber of the conventional type was dispersed in 450 pounds of water in a 35 pound Valley beater for 10 minutes at minimum roll pressure. The staple fiber dispersion thus formed was added to the machine mixing chest together with 200 pounds of water.
pounds of an emulsion of dimethyl phthalate in equal parts of water prepared by using Triton N-lOO (or any oil-in-water emulsifying agent) was prepared and was added to the mass in the mixing chest. The stock slurry was allowed to stand for 45 minutes. The slurry was then formed into a web on the wire of a conven tional Fourdrinier paper machine and was dried in the normal manner employed in making paper. The addition of the cellulose acetate staple permitted much faster drainage on the wire of the paper machine and the web obtained could be handled without the necessity of using felt.
Example 2 A procedure as described in the preceding example was carried out but a shower of steam of sufiicient width to cover the span of the web was applied to the Web surface at a point from two to six inches ahead of the nip of the pressure couch employed in the web making operation. The steam had a softening effect on the plasticized cellulose acetate web which was sufiicient to permit the pressure from the couch rolls to partially fuse the acetate fibers of the web. The sheet thus obtained exhibited extraordinary high wet strength and could be readily handled.
The plasticizers used in cellulose dispersions in carrying out our invention are first emulsified to form an aqueous emulsion thereof by means of a surface active agent which will retain the plasticizer in the water in dispersed form. The surface active agent used may be any compound which is commonly known as suitable for use in preparing oil-in-water emulsions. It may be of the non-ionic type, for instance, an alkyl aryl polyether alcohol, such as is marketed as Triton N-IOO, or it may be of the cationic type, for instance stearyl dimethyl benzyl ammonium chloride, such as is marketed as Triton X-400.
We claim:
1. A method of making sheets adapted to be formed into products which comprises forming a dilute suspension in water of a fibrous fiocculated precipitate of a lower fatty acid ester of cellulose and 510% of cellulose ester staple fiber, laying down the suspension onto a foraminous surface to form a sheet therefrom and drying the so formed sheet.
2. A method of forming sheets adapted to be formed into desired products which comprises forming a dilute suspension in water of a fibrous fiocculated precipitate of a lower fatty acid ester of cellulose and 510% of cellulose ester staple fiber, adding thereto an aqueous emulsion of a plasticizer for the cellulose esters, laying down the suspension onto a foraminous surface to form a sheet therefrom and drying the so formed sheet.
3. A method of making colloidized cellulose ester sheeting which comprises forming a suspension in water of a fibrous fiocculated precipitate of a lower fatty acid ester of cellulose and 5-10% of cellulose ester staple fiber, adding thereto an aqueous emulsion of a cellulose assmes 4 ester plasticizer, laying down the suspension onto a. foraminous sheet and subjecting to sufficient heat and pressure to at least partially fuse the material.
4. A method of making sheets adapted to be formed into desired products which comprises forming a dilute suspension in water of a fibrous fiocculated precipitate of a lower fatty acid ester of cellulose and 540% of cellulose ester staple fiber, adding thereto an aqueous emulsion of a plasticizer, laying down the suspension onto a foraminous surface to form a sheet therefrom, subjecting the sheet thus formed to a jet of steam followed by subjecting the sheet to pressure suflicient to at least partially fuse the fibers thereof.
5. A method of making sheets adapted to be formed into desired products which comprises forming a dilute suspension in water of a fibrous fiocculated precipitate of a lower fatty acid ester of cellulose and 5-10% of cellulose ester staple fiber, laying down the suspension thus formed onto the wire of a paper machine and drying the thus formed product.
6. A method of making sheets adapted to be formed into desired products which comprises forming a dilute suspension in water of a fibrous fiocculated precipitate of a lower fatty acid ester of cellulose and 5-10% of cellulose acetate staple fiber, laying down the suspension onto a foraminous surface to form a sheet therefrom and drying the thus formed sheet.
7. A method of making sheets adapted to be formed into desired products which comprises forming a dilute suspension in water of a fibrous fiocculated precipitate of cellulose acetate and 5-10% of cellulose acetate staple fiber, adding thereto an aqeous emulsion of a cellulose acetate plasticizer, laying down the suspension onto a foraminous surface to form a sheet therefrom and drying the thus formed sheet.
References Cited in the file of this patent UNITED STATES PATENTS 2,208,652 Whitehead July 23, 1940 2,260,343 Seiberlich Oct. 28, 1941 2,357,392 Francis Sept. 5, 1944 2,357,962 Leemann et al Sept. 12, 1944 2,414,833 Osborne Jan. 28, 1947 2,430,868 Francis Nov. 18, 1947 2,626,214 Osborne Jan. 20, 1953

Claims (1)

1. A METHOD OF MAKING SHEETS ADAPTED TO BE FORMED INTO PRODUCTS WHICH COMPRISES FORMING A DILUTE SUSPENSION IN WATER OF A FIBROUS FLOCCULATED PRECIPITATE OF A LOWER FATTY ACID ESTER OF CELLULOSE AND 5-10% OF CELLULOSE ESTER STAPLE FIBER, LAYING DOWN THE SUSPENSION ONTO A FORAMINOUS SURFCE TO FORM A SHEET THEREFROM AND DRYING THE SO FORMED SHEET.
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Cited By (45)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3033209A (en) * 1959-08-28 1962-05-08 Eastman Kodak Co Tobacco smoke filter
US3062679A (en) * 1961-02-06 1962-11-06 Eastman Kodak Co Sized partially esterified paper and its method of preparation
US3103462A (en) * 1960-04-18 1963-09-10 Eastman Kodak Co Method of improving the strength characteristics of paper prepared from partially acylated cellulose fibers
US4283186A (en) * 1976-10-06 1981-08-11 Celanese Corporation Method of forming cigarette filter material
US5022964A (en) * 1989-06-06 1991-06-11 The Dexter Corporation Nonwoven fibrous web for tobacco filter
US5114537A (en) * 1990-10-23 1992-05-19 Bio Associates, A California Partnership Dry sheet-like filtering material for liquid depth filtration
US5573640A (en) * 1995-07-28 1996-11-12 Eastman Chemical Company Paper made with cellulose fibers having an inner core of cellulose acetate
WO1997020985A1 (en) * 1995-12-07 1997-06-12 Eastman Chemical Company High pressure laminates made with paper containing cellulose acetate
US5662773A (en) * 1995-01-19 1997-09-02 Eastman Chemical Company Process for preparation of cellulose acetate filters for use in paper making
US5726664A (en) * 1994-05-23 1998-03-10 Hughes Electronics End launched microstrip or stripline to waveguide transition with cavity backed slot fed by T-shaped microstrip line or stripline usable in a missile
WO1998016687A1 (en) * 1996-10-11 1998-04-23 Eastman Chemical Company Composition and paper comprising cellulose ester and alkylpolyglycosides
WO1998016688A1 (en) * 1996-10-11 1998-04-23 Eastman Chemical Company Plasticized sheets, laminates made from such sheets and process for preparing such laminates
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
US6193841B1 (en) 1998-11-30 2001-02-27 Eastman Chemical Company Shaped, plastic articles comprising a cellulose fiber, a cellulose ester, and a non-ionic surfactant
US20040214702A1 (en) * 2003-04-25 2004-10-28 Stroud Herbert D. Process for the conversion of cellulose acetate waste fibers into a suitable form for paper production and the resultant paper products
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
US11390991B2 (en) 2018-08-23 2022-07-19 Eastman Chemical Company Addition of cellulose esters to a paper mill without substantial modifications
US11390996B2 (en) 2018-08-23 2022-07-19 Eastman Chemical Company Elongated tubular articles from wet-laid webs
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
US11421387B2 (en) 2018-08-23 2022-08-23 Eastman Chemical Company Tissue product comprising cellulose acetate
US11421385B2 (en) 2018-08-23 2022-08-23 Eastman Chemical Company Soft wipe comprising cellulose acetate
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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
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US11639579B2 (en) 2018-08-23 2023-05-02 Eastman Chemical Company Recycle pulp comprising cellulose acetate

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Cited By (51)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3033209A (en) * 1959-08-28 1962-05-08 Eastman Kodak Co Tobacco smoke filter
US3103462A (en) * 1960-04-18 1963-09-10 Eastman Kodak Co Method of improving the strength characteristics of paper prepared from partially acylated cellulose fibers
US3062679A (en) * 1961-02-06 1962-11-06 Eastman Kodak Co Sized partially esterified paper and its method of preparation
US4283186A (en) * 1976-10-06 1981-08-11 Celanese Corporation Method of forming cigarette filter material
US5022964A (en) * 1989-06-06 1991-06-11 The Dexter Corporation Nonwoven fibrous web for tobacco filter
US5114537A (en) * 1990-10-23 1992-05-19 Bio Associates, A California Partnership Dry sheet-like filtering material for liquid depth filtration
US5726664A (en) * 1994-05-23 1998-03-10 Hughes Electronics End launched microstrip or stripline to waveguide transition with cavity backed slot fed by T-shaped microstrip line or stripline usable in a missile
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
US5766752A (en) * 1995-12-07 1998-06-16 Eastman Chemical Company High pressure laminates made with paper containing cellulose acetate
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US5928777A (en) * 1995-12-07 1999-07-27 Eastman Chemical Company High pressure laminates made with paper containing cellulose acetate
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US5922451A (en) * 1996-10-11 1999-07-13 Eastman Chemical Company Plasticized sheets, laminates made from such sheets, and process for preparing such laminates
WO1998016688A1 (en) * 1996-10-11 1998-04-23 Eastman Chemical Company Plasticized sheets, laminates made from such sheets and process for preparing such laminates
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
US6228895B1 (en) 1996-10-11 2001-05-08 Eastman Chemical Company Method for plasticizing a composition comprised of cellulose fiber and a cellulose ester
US6268028B1 (en) 1996-10-11 2001-07-31 Eastman Chemical Company Composition and paper comprising cellulose ester, alkylpolyglycosides, and cellulose
US6309509B1 (en) 1996-10-11 2001-10-30 Eastman Chemical Company Composition and paper comprising cellulose ester, alkylpolyglycosides, and cellulose
US6193841B1 (en) 1998-11-30 2001-02-27 Eastman Chemical Company Shaped, plastic articles comprising a cellulose fiber, a cellulose ester, and a non-ionic surfactant
US20040214702A1 (en) * 2003-04-25 2004-10-28 Stroud Herbert D. Process for the conversion of cellulose acetate waste fibers into a suitable form for paper production and the resultant paper products
US11306433B2 (en) 2018-08-23 2022-04-19 Eastman Chemical Company Composition of matter effluent from refiner of a wet laid process
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
US11230811B2 (en) 2018-08-23 2022-01-25 Eastman Chemical Company Recycle bale comprising cellulose ester
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