US3173830A - Paper comprising collapsed regenerated cellulose fibers - Google Patents
Paper comprising collapsed regenerated cellulose fibers Download PDFInfo
- Publication number
- US3173830A US3173830A US820602A US82060259A US3173830A US 3173830 A US3173830 A US 3173830A US 820602 A US820602 A US 820602A US 82060259 A US82060259 A US 82060259A US 3173830 A US3173830 A US 3173830A
- Authority
- US
- United States
- Prior art keywords
- paper
- fibers
- regenerated cellulose
- weight
- fiber
- 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
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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
- D21H13/08—Synthetic cellulose fibres from regenerated cellulose
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
- Y10T428/2913—Rod, strand, filament or fiber
- Y10T428/2973—Particular cross section
Definitions
- regenerated cellulose fibers have sufiicient natural cohesion to form a strong bond without the addition of any external adhesive.
- Such fibers are characterized by a crosssection (taken in a direction substantially perpendicular to their axes) in which one dimension is from about five to about fifteen times the other. Preferably, they contain between about 1.5 and about 4.0% by weight of a finely divided inert particulate material.
- Such fibers can be used by themselves in conventional paper-making processes, without added adhesive, to give a smooth, strong sheet.
- the invention therefore, comprises a paper containing between about 10% and 100% by weight of regenerated cellulose fiber, each of said fibers having a crosssection in a plane perpendicular to its axis such that one dimension is from 5 to 15 times the other.
- the invention further comprises in a method for making paper wherein a slurry of fibers is deposited on a surface and liquid is moved therefrom .to form a paper sheet, the improvement which comprises forming said slurry at least in part from generated cellulose fibers having a crosssection in a plane perpendicular to its axis such that one dimension is between about 5 and about 15 times the other.
- the drawing is a cross sectional view, greatly enlarged, of a regenerated cellulose fiber as used in the present invention, taken in a plane perpendicular to its axis.
- the fibers which are used in the present invention are preferably collapsed hollow fibers made by extruding a viscose containing a suitable gas-forming agent and preferably also containing an inert particulate material, into a ice conventional spinning bath. As they are removed from the spinning bath the fibers are of tubular shape, but upon subsequent washing and drying, they collapse to give fiat filaments.
- filaments having the dimensions required for the present invention may be made by extruding a conventional viscose containing 1040% on the weight of the cellulose, of an alkali or alkaline earth metal carbonate or bicarbonate into an acid spin bath.
- suitable fibers can be made by extruding a viscose containing 610% by Weight cellulose, 57% NaOI-i, 1-4% sodium carbonate, having a total sulfur content of say 1.5 to 3 and a salt number of 5.0 to 7.0 into a spinning containing 11.5-12.5% by weight H 0.5 to 2% ZnSO and 18-25% Na SO
- the viscose will also contain from about 0.15% to about 0.40% of an inert particulate material.
- the fibers After emerging from the spinning bath, the fibers may be cut up to form a blanket of staple fibers and then subjected in the form of a blanket to the various washing treatments customarily given regenerated cellulose fibers, such as a regenerating treatment with dilute acid, a desulfurizing treatment with Na 'S and a sou-ring treatment, again with dilute acid.
- the blanket may be dried and stored; or it may be sent directly to a papermaking plant, where it can be opened by jets of water to form a suitably slurry.
- the fibers may be treatedin the form of a tow with the various washes'outlined above; and cut up into staple at some later time.
- the fiber on coming from the spinning bath may be laid down as a tow in a plaited pattern on a moving belt, and subjected to the various washes in that form.
- the tow After treatment the tow may be dried and stored. It may be furnished to the paper-making plant as tow; or it may be cut up into staple fiber beforehand.
- the fiber as used preferably has a denier of about 1.5 to about 8 and is from say A3" to 1 /2", preferably from A" to ,42 long.
- the inert particulate material used in the present invention may be virtually any solid material which is inert with respect to the viscose and the spinning bath. Titanium dioxide is preferred, but alumina, silica, carbon black, and various pigments may also be used.
- the role of the inert material is twofold. In the first place it aids in forming fibers which are evenly inflated or tubular along their length by providing nuclei for the formation of gas bubbles. Thisfunction of the solid particles has been used hitherto in making inflated fibers. However, were the solid used only as an aid in gas formation, a much smaller amount, say 0.1% on the weight of cellulose, would be sulficient.
- the second function of the solid material is to raise fiber to fiber friction.
- the means by which this is accomplished is not known, but at least 1% on the weight of cellulose appears to be necessary for an appreciable effect to be obtained. There is no great advantage in using more than about 4%.
- the average particle size of the material should be not greater than about 1 micron and, preferably, particles above 5 microns in size should be absent.
- Paper according to the present invention may consist wholly of regenerated cellulose fibers or it may consist partly of regenerated cellulose fibers and partly of conventional natural cellulose fibers, e.g. paper pulp.
- the invention includes blends of the special regenerated cellulose fibers with nylons, acrylic fibers, polyester fibers; cellulose acetate and other cellulose organic ester fibers.
- Such blends may or may not include conventional cellulose paper-making fibers. Normally at least regenerated cellulose fibers arerequired toappreciably affect the characteristics of the final product.
- the regenerated cellulose staple fiber need not be subjected to the prolonged beating that is required forconventional, natural paper-making fibers, since the cohesion of the novel paper does not depend on fibrillation, which is one of the more important effects of beating conventional fibers. It is desirable, however, to create an even slurry of the fibers for use in paper-making machines and one way to achieve this effect is to run the fibers through a refiner or Jordan engine, as a slurry containing from say .1 to 5.0% by weight fibers.
- Other mixing devices may be used; for example, in making hand sheets for test purposes, a Waring Blendor and a Tappi Standard Disintegrator have both been used successfully.
- the conventional fibers may be beaten in a beater to the desired freeness (say 500 Canadian) and then the regenerated cellulose component added. After circulating through the beater just enough to disperse large concentrations of regenerated cellulose fiber, the mixture may be sent to a Jordan for further mixing and for further refining of the natural paper.
- the fiber concentration in the beater (after addition of regenerated cellulose) is about 1.0 to 6.0%. In the Jordan it is about one-half that.
- test sheets are made from a slurry having 'a fiber concentration of say 0.05 to 0.2% on a Standard British Sheet Mold. Usually, following Tappi Standard T205 M-53, a concentration of 0.15% is used.
- any conventional machine of the Fourdrinier type may be used.
- an aqueous slurry containing say 0.1 to 1.0% fiber is formed in the head box of the machine and is then poured onto a moving screen where the water is sucked off to form the paper.
- the paper may be pressed and dried as desired in accordance with conventional practice.
- sizes may be added to the fiber at any stage in the process, from the beater to the head box of the, paper-making machine.
- sizes may be applied to the paper after it has been formed. The character and quantity of the size depends on the use to which the paper is to be put, as will be understood by those skilled in the art.
- Paper made according to the invention is in general less dense and more porous than comparable paper made from paper pulp. It has, in general, lower tensile strength but greater tear strength, greater fold strength and greater bursting strength than similar papers made from wood pulp.
- the blanket is then dried and stored.
- the individual fibers are fiat, deflated tubes each having a cross-section in a plane perpendicular to its axis such that on the average one dimension is about ten times the other.
- the fibers made as above are used to make paper test sheets 6%" in diameter on a British Standard Sheet Mold.
- Four different types of sheets are made up.
- the sheets are made solely from pine paper pulp (500 freeness).
- the sheets contain 75% by weight pine paper pulp (500 freeness) and 25% of the regenerated cellulose fiber.
- the sheets consist of 50% regenerated cellulose fiber and 50% pine paper pulp (500 freeness).
- the sheets are regenerated cellulose.
- the regenerated cellulose fiber is opened by jets of water to form a slurry.
- This slurry is then put into a standard Tappi disintegrator with conventional pulp as appropriate and sufiicient water to bring the fiber concentration to about 1.75% by weight.
- the disintegrator is run for 300 counts to form a smooth dispersion.
- This dispersion is diluted to 0.15% by weight and the sheets are made on a Standard British Sheet Mold. They are given a first pressing of 50 p.s.i. for five minutes. They are then reversed on a dry blotter and repressed at 50 p.s.i. for two minutes. Finally, they are dried at 50% relative humidity and 23 C. (73 F.) until equilibrium is reached with the conditioning atmosphere.
- This procedure is in accordance with Tappi Standard T220 M-53.
- the sheets are then tested for tear factor, porosity (air), tensile strength, breaking length, stretch and fold strength. The results appear in Table I below:
- Example II Details of the tear factor test are found in Tappi Stand-' EXAMPLE II Example I is repeated except that the tow emerging from the spinning bath is subjected to the wash treat ments in that form. After drying it is cut by hand into staple fibers exactly 4" long. These fibers are then used to make up two types of test sheets using the procedure of Example I.
- Type A contains 25% regenerated cellulose and 75% pine paper pulp (500 freeness).
- Type B is a 50-50 blend of the same stocks. Test results are shown in Table II.
- Example III The procedure of Example I is repeated except that the viscose has the following composition: Cellulose percent by weight 7.5 NaOH do 6.0 Na CO do 25 TiO do 0.19 Total sulfur do 2.1 Salt index 6.0
- the staple fibers after washing and drying are found to have a cross-section in which, on the average, one dimension is 12 times the other.
- Hand sheets are made up as in Example I.
- Sheet A is 100% pine pulp (500 freeness)
- sheet B 25% regenerated cellulose and 75% pine pulp
- sheet C 50% regenerated cellulose and 50% pine pulp
- sheet D 100% regenerated cellulose. The characteristics of these sheets are shown in Table III.
- Table 111 Sample A B o D Percent Rayon (by weight) 0 25 50 100 Percent Pulp (1) weight) 100 75 50 0 Basis Wei ht Oven Dr 40.8 42.1 17.0 14.3 Caliper 3. 9 4. 2 4. 6 4. 3 Apparent Dens 10.5 10.1 10.4 10.4 Tear Factor 137 123 153 348 Air Porosity (sen/100 ee.) 11 18 18 Tensile Strength (lbs./% width 12.7 11.0 10.6 0.1 Breaking length meters) 7,020 7, 000 5, 620 3,473 Stretch (percent) 3.1 3.8 3.5 2.
- Paper comprising regenerated cellulose fibers, each of which has a cross-section in a plane perpendicular to its axis such that one dimension is between about 5 and about 15 times the other.
- the paper claimed in claim 1 wherein the regenerated cellulose fiber comprises between about 10% and 100% of the weight of the paper.
- Paper comprising regenerated cellulose fibers, each of said fibers having a cross-section in a plane perpendicular to its axis such that one dimension is between about 5 and about 15 times the other and containing be tween about 1.5% and about 4.0% by weight of an inert particulate material.
- Paper comprising regenerated cellulose staple fibers, each of said fibers being in the shape of a collapsed tube and having a cross-section in a plane perpendicular to its axis such that, on the average, one dimension is between about 5 and about 15 times the other.
- Paper comprising wood pulp and not less than 10% by weight regenerated cellulose fibers, each of said rcgenerated cellulose fibers having across section in a plane perpendicular to its axis such that one dimension of said cross-section is fi'om 5 to 15 times the other.
- Paper containing as its sole fibrous component regenerated cellulose fibers each of which is characterized in having a width from 5 to 15 times its thickness and in containing from about 1.5% to about 4.0% by weight titanium dioxide.
- Paper comprising regenerated cellulose fibers wherein a predominate portion of said fibers is composed of fibers, each of which has a cross-section in a plane perpendicular to its axis such that one dimension is between about 5 and about 15 times the other.
- Paper comprising regenerated cellulose fibers which have a ratio of width to thickness of from about 5:1 to about 15 :1.
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- Artificial Filaments (AREA)
- Paper (AREA)
Description
Claims (1)
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US820602A US3173830A (en) | 1959-06-16 | 1959-06-16 | Paper comprising collapsed regenerated cellulose fibers |
GB20965/60A GB945306A (en) | 1959-06-16 | 1960-06-15 | Paper and method of making same |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US820602A US3173830A (en) | 1959-06-16 | 1959-06-16 | Paper comprising collapsed regenerated cellulose fibers |
Publications (1)
Publication Number | Publication Date |
---|---|
US3173830A true US3173830A (en) | 1965-03-16 |
Family
ID=25231264
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US820602A Expired - Lifetime US3173830A (en) | 1959-06-16 | 1959-06-16 | Paper comprising collapsed regenerated cellulose fibers |
Country Status (2)
Country | Link |
---|---|
US (1) | US3173830A (en) |
GB (1) | GB945306A (en) |
Cited By (32)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3320117A (en) * | 1962-05-31 | 1967-05-16 | Tachikawa Res Inst | Process for the manufacture of rayon paper or non-woven fabric by the wet system |
US3359155A (en) * | 1963-10-28 | 1967-12-19 | Kurashiki Rayon Co | Process for preparing a viscose spinning solution, fibers formed therefrom and paper containing said fibers |
US20110265965A1 (en) * | 2006-03-21 | 2011-11-03 | Georgia-Pacific Consumer Products Lp | Absorbent Sheet Having Regenerated Cellulose Microfiber Network |
US8540846B2 (en) | 2009-01-28 | 2013-09-24 | Georgia-Pacific Consumer Products Lp | Belt-creped, variable local basis weight multi-ply sheet with cellulose microfiber prepared with perforated polymeric belt |
US20190194846A1 (en) * | 2010-09-14 | 2019-06-27 | Kelheim Fibres Gmbh | Method for strengthening a nonwoven fabric |
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 |
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 |
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 |
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 |
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 |
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 |
---|---|---|---|---|
US4182735A (en) | 1978-05-25 | 1980-01-08 | International Paper Company | Production of high crimp, high strength, hollow rayon fibers |
US4242411A (en) | 1978-05-25 | 1980-12-30 | International Paper Company | High crimp, high strength, hollow rayon fibers |
EP2599900A1 (en) | 2011-11-29 | 2013-06-05 | Kelheim Fibres GmbH | Regenerated cellulose fibre |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1464048A (en) * | 1921-10-13 | 1923-08-07 | Rousset Jules | Artificial textile filament and process of making same |
GB674577A (en) * | 1950-02-09 | 1952-06-25 | American Viscose Corp | Felt-like fibrous products and methods of making them |
GB687041A (en) * | 1950-03-20 | 1953-02-04 | American Viscose Corp | Paper making |
US2798283A (en) * | 1953-12-09 | 1957-07-09 | Du Pont | Condensation polymer filament |
-
1959
- 1959-06-16 US US820602A patent/US3173830A/en not_active Expired - Lifetime
-
1960
- 1960-06-15 GB GB20965/60A patent/GB945306A/en not_active Expired
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1464048A (en) * | 1921-10-13 | 1923-08-07 | Rousset Jules | Artificial textile filament and process of making same |
GB674577A (en) * | 1950-02-09 | 1952-06-25 | American Viscose Corp | Felt-like fibrous products and methods of making them |
GB687041A (en) * | 1950-03-20 | 1953-02-04 | American Viscose Corp | Paper making |
US2798283A (en) * | 1953-12-09 | 1957-07-09 | Du Pont | Condensation polymer filament |
Cited By (39)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3320117A (en) * | 1962-05-31 | 1967-05-16 | Tachikawa Res Inst | Process for the manufacture of rayon paper or non-woven fabric by the wet system |
US3359155A (en) * | 1963-10-28 | 1967-12-19 | Kurashiki Rayon Co | Process for preparing a viscose spinning solution, fibers formed therefrom and paper containing said fibers |
US20110265965A1 (en) * | 2006-03-21 | 2011-11-03 | Georgia-Pacific Consumer Products Lp | Absorbent Sheet Having Regenerated Cellulose Microfiber Network |
US8216425B2 (en) * | 2006-03-21 | 2012-07-10 | Georgia-Pacific Consumer Products Lp | Absorbent sheet having regenerated cellulose microfiber network |
US9051691B2 (en) | 2006-03-21 | 2015-06-09 | Georgia-Pacific Consumer Products Lp | Method of making a wiper/towel product with cellulosic microfibers |
US9057158B2 (en) | 2006-03-21 | 2015-06-16 | Georgia-Pacific Consumer Products Lp | Method of making a wiper/towel product with cellulosic microfibers |
US9382665B2 (en) | 2006-03-21 | 2016-07-05 | Georgia-Pacific Consumer Products Lp | Method of making a wiper/towel product with cellulosic microfibers |
US8540846B2 (en) | 2009-01-28 | 2013-09-24 | Georgia-Pacific Consumer Products Lp | Belt-creped, variable local basis weight multi-ply sheet with cellulose microfiber prepared with perforated polymeric belt |
US8632658B2 (en) | 2009-01-28 | 2014-01-21 | Georgia-Pacific Consumer Products Lp | Multi-ply wiper/towel product with cellulosic microfibers |
US8864945B2 (en) | 2009-01-28 | 2014-10-21 | Georgia-Pacific Consumer Products Lp | Method of making a multi-ply wiper/towel product with cellulosic microfibers |
US8864944B2 (en) | 2009-01-28 | 2014-10-21 | Georgia-Pacific Consumer Products Lp | Method of making a wiper/towel product with cellulosic microfibers |
US20190194846A1 (en) * | 2010-09-14 | 2019-06-27 | Kelheim Fibres Gmbh | Method for strengthening a nonwoven fabric |
US11390996B2 (en) | 2018-08-23 | 2022-07-19 | Eastman Chemical Company | Elongated tubular articles from wet-laid webs |
US11414818B2 (en) | 2018-08-23 | 2022-08-16 | Eastman Chemical Company | Dewatering in paper making 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 |
US11286619B2 (en) | 2018-08-23 | 2022-03-29 | Eastman Chemical Company | Bale of virgin cellulose and cellulose ester |
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 |
US11299854B2 (en) | 2018-08-23 | 2022-04-12 | Eastman Chemical Company | Paper product 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 |
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 |
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 |
Also Published As
Publication number | Publication date |
---|---|
GB945306A (en) | 1963-12-23 |
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