US2006209A - Dull finish coated paper - Google Patents
Dull finish coated paper Download PDFInfo
- Publication number
- US2006209A US2006209A US672906A US67290633A US2006209A US 2006209 A US2006209 A US 2006209A US 672906 A US672906 A US 672906A US 67290633 A US67290633 A US 67290633A US 2006209 A US2006209 A US 2006209A
- Authority
- US
- United States
- Prior art keywords
- paper
- coated paper
- coating
- dull finish
- moistening
- 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
- 239000011248 coating agent Substances 0.000 description 14
- 238000000576 coating method Methods 0.000 description 14
- 229920002472 Starch Polymers 0.000 description 11
- 239000008107 starch Substances 0.000 description 11
- 235000019698 starch Nutrition 0.000 description 11
- 229920002678 cellulose Polymers 0.000 description 9
- 239000001913 cellulose Substances 0.000 description 9
- 239000008199 coating composition Substances 0.000 description 8
- 239000000049 pigment Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 238000001035 drying Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 238000003490 calendering Methods 0.000 description 4
- 229910052500 inorganic mineral Inorganic materials 0.000 description 4
- 239000011707 mineral Substances 0.000 description 4
- 239000007921 spray Substances 0.000 description 3
- 230000008961 swelling Effects 0.000 description 3
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 229920003043 Cellulose fiber Polymers 0.000 description 2
- 229920001131 Pulp (paper) Polymers 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 239000005018 casein Substances 0.000 description 2
- BECPQYXYKAMYBN-UHFFFAOYSA-N casein, tech. Chemical compound NCCCCC(C(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(CC(C)C)N=C(O)C(CCC(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(C(C)O)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(COP(O)(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(N)CC1=CC=CC=C1 BECPQYXYKAMYBN-UHFFFAOYSA-N 0.000 description 2
- 235000021240 caseins Nutrition 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- 238000010981 drying operation Methods 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 1
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 235000014510 cooky Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000009499 grossing Methods 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 229920005610 lignin Polymers 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000010002 mechanical finishing Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 238000007788 roughening Methods 0.000 description 1
- -1 satin white Substances 0.000 description 1
- 238000012216 screening Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
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
- D21H19/00—Coated paper; Coating material
- D21H19/36—Coatings with pigments
- D21H19/38—Coatings with pigments characterised by the pigments
- D21H19/42—Coatings with pigments characterised by the pigments at least partly organic
-
- 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
- Y10T428/31—Surface property or characteristic of web, sheet or block
-
- 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
- Y10T428/31504—Composite [nonstructural laminate]
- Y10T428/31971—Of carbohydrate
- Y10T428/31975—Of cellulosic next to another carbohydrate
- Y10T428/31978—Cellulosic next to another cellulosic
- Y10T428/31982—Wood or paper
Definitions
- dull finish coated paper is preferred from an artistic standpoint, but as prepared in the past by the use of crystalline mineral pigment of relatively large grain size, it has had certain faults from the standpoint of printing, e. g. it absorbs too much ink'and unevenly so that half tone impressions are apt to appear muddy and solid colors are apt to lack brilliance and be of uneven tone or "spotty.
- an aqueous coating composition is prepared consisting essentially of a suitable adhesive, such as casein or cooked starch, and a pigment consisting wholly or in part of uncooked starch.
- a suitable adhesive such as casein or cooked starch
- a pigment consisting wholly or in part of uncooked starch.
- This coat-- ing is applied to the paper and dried and calendered. in the customary way and thereafter moistened.
- the calendering of the coated paper is carried out without regard to the character of the finish, whether dull or glossy, but so as to produce the desired degree of smoothness of the surface.
- the subsequent moistening of the coating apparently serves to swell the starch composition
- the proportions of uncooked starch and mineralpigment may vary with the character of the pigment and the degree of dull finish desired in the product. In general the 55 greater the relative proportion of uncooked grains and to yield a dull finish due to the difiEu-" starch the greater will be the degree of dullness. of the finish and vice versa.
- the uncooked starch may constitute any desired proportion of the pigment component of the composition, but generally does not exceed 50%.
- the subsequent moistening of the coating, followed by drying, if necessary, to develop the dull finish may be accomplished in a variety of ways, it being necessary only that the moistening be uniform and not excessive.
- the paper may-be passed over'a roll carrying a'film of water, or it may be contacted with a fine spray or mist, or with wet steam or a humid or moistureladen atmosphere. If too much water isapplied there is a tendency for the paper to cookie and this tendency may be minimized by holding the paper taut during the moistening operation. .Under some conditions the application of a. special drying operation to the paper after the moistening is unnecessary, e. g. when it has been moistened by means of a humid atmosphere.
- the dulling effect of the moistening may be regulated by varying the rapidity of the drying operation, since not only the amount of water applied but the time that it is allowed to act, determine the degree of swelling of the starch granules. It is generally preferred to dry the paper by means of .a blast of warm air.
- the present invention resides essentially in the substitution of pulverized cellulose for uncooked starch in the process of my application Serial No. 590,315, briefly described above.
- the pulverized cellulose may be obtained from any suitable raw material, such as cotton, sulflte-, kraft-, soda or other chemical wood pulp; rag pulp, etc. Wood itself may be used, but generally is not desirable on account of its color, lignin, resin and other non-cellulosic content which tend to impair the stability of the paper. Bleached sulfite wood pulp is a suitable material from which to obtain the pulverized cellulose.
- the present invention is not concerned with the manner in which the pulverized cellulose is prepared, but for completeness it may be said that a suitable product may be obtained by subjecting thoroughly dried fiber to a ball mill operation until it is reduced to an impalpable powder and then screening through a 200-mesh screen.
- the pulverized cellulose is incorporated in a suitable coating composition with or without mineral pigment, such as clay, satin white, etc., and a suitable adhesive such as casein, cooked starch, etc., the only requisite in this respect being that the mineral pigment must not be in such proportion with respect to the pulverized cellulose that the efi'ect of the latter in dulli'ng the finish upon subsequent moistening of the coating is completely masked.
- the coating composition is applied to the paper, smoothed, dried and supercalendered to the desired smoothness of surface in accordance with the well known practice and then moistened in any of a variety of ways, e. g. by passing the paper over a wet roll or in contact with a spray or mist or steam jets or a humid or moisture-laden atmosphere. In this operation it is desirable to apply the minimum of water 'to avoid cockling of v the paper and the paper preferably is moistened under tension to minimim this tendency.
- the paper is then dried or not, as required, depending upon the method of moistening used. When using a humid atmosphere, drying generally is unnecessary, but when water is applied by means of a roll or spray, it is generally desirable to dry the paper, e. g.
- Process of making dull finish coated paper which comprises coating paper with an aqueous coating composition comprising pulverized cellulosejdrying the coating, calendering the coating to the desired surface smoothness and thereafter moistening' the coating.
- Dull finish coated paper having a supercalendered surface, the coating of which contains pulverized cellulose which has been swelled by moistening in situ.
- Dull finish coated paper obtained by .coating paper with an aqueous coating composition comprising pulverized cellulose, drying and me-. chanically finishing the coating to the .desired smoothness and thereafter mois'tening 'the coating, the coated paper product being characterized by smoothness and printing properties corresponding to the mechanical finishing applied and
Landscapes
- Paper (AREA)
Description
Patented June 25, 1935 PATENT OFFICE 2,008,209 I DULL FINISH COATED PAPER Donald B. Bradner, Oxford, Ohio, assignor to The Champion Coated Paper Company, Hamilton, Ohio, a corporation of Ohio No Drawing. Application May 25, 1933, Serial No. 672,906
3 Claims. (Cl. ci-cs) In my application Serial No. 590,315, filed February 1, 1932, of which this application is a continuation-in-part, I have described dull finish coated paper and a process of preparing it in- 5 volving the use of a coating composition containing or comprising uncooked starch.
As is explained in said application, dull finish coated paperis preferred from an artistic standpoint, but as prepared in the past by the use of crystalline mineral pigment of relatively large grain size, it has had certain faults from the standpoint of printing, e. g. it absorbs too much ink'and unevenly so that half tone impressions are apt to appear muddy and solid colors are apt to lack brilliance and be of uneven tone or "spotty.
Since the process of the present invention is analogous to the process of said application, excepting that pulverized cellulose is substituted for uncooked starch in the coating composition, the process of said application will be briefly described. In accordance therewith an aqueous coating composition is prepared consisting essentially of a suitable adhesive, such as casein or cooked starch, and a pigment consisting wholly or in part of uncooked starch. This coat-- ing is applied to the paper and dried and calendered. in the customary way and thereafter moistened. The calendering of the coated paper is carried out without regard to the character of the finish, whether dull or glossy, but so as to produce the desired degree of smoothness of the surface. The subsequent moistening of the coating apparently serves to swell the starch composition may contain as a part of the pig ment component thereof the well known mineral pigments such as satin white, clay, calcium carbonate or the like. The proportions of uncooked starch and mineralpigment may vary with the character of the pigment and the degree of dull finish desired in the product. In general the 55 greater the relative proportion of uncooked grains and to yield a dull finish due to the difiEu-" starch the greater will be the degree of dullness. of the finish and vice versa. The uncooked starch may constitute any desired proportion of the pigment component of the composition, but generally does not exceed 50%.
The application of the coating composition, the smoothing of this coating on the paper stock, the drying and the calendering of the coating are, as stated, all carried out in accordance with known practice.
The subsequent moistening of the coating, followed by drying, if necessary, to develop the dull finish, may be accomplished in a variety of ways, it being necessary only that the moistening be uniform and not excessive. For example, the paper may-be passed over'a roll carrying a'film of water, or it may be contacted with a fine spray or mist, or with wet steam or a humid or moistureladen atmosphere. If too much water isapplied there is a tendency for the paper to cookie and this tendency may be minimized by holding the paper taut during the moistening operation. .Under some conditions the application of a. special drying operation to the paper after the moistening is unnecessary, e. g. when it has been moistened by means of a humid atmosphere. The dulling effect of the moistening may be regulated by varying the rapidity of the drying operation, since not only the amount of water applied but the time that it is allowed to act, determine the degree of swelling of the starch granules. It is generally preferred to dry the paper by means of .a blast of warm air.
The present invention resides essentially in the substitution of pulverized cellulose for uncooked starch in the process of my application Serial No. 590,315, briefly described above. The pulverized cellulose may be obtained from any suitable raw material, such as cotton, sulflte-, kraft-, soda or other chemical wood pulp; rag pulp, etc. Wood itself may be used, but generally is not desirable on account of its color, lignin, resin and other non-cellulosic content which tend to impair the stability of the paper. Bleached sulfite wood pulp is a suitable material from which to obtain the pulverized cellulose.
The present invention is not concerned with the manner in which the pulverized cellulose is prepared, but for completeness it may be said that a suitable product may be obtained by subjecting thoroughly dried fiber to a ball mill operation until it is reduced to an impalpable powder and then screening through a 200-mesh screen.
The pulverized cellulose is incorporated in a suitable coating composition with or without mineral pigment, such as clay, satin white, etc., and a suitable adhesive such as casein, cooked starch, etc., the only requisite in this respect being that the mineral pigment must not be in such proportion with respect to the pulverized cellulose that the efi'ect of the latter in dulli'ng the finish upon subsequent moistening of the coating is completely masked.
The coating composition is applied to the paper, smoothed, dried and supercalendered to the desired smoothness of surface in accordance with the well known practice and then moistened in any of a variety of ways, e. g. by passing the paper over a wet roll or in contact with a spray or mist or steam jets or a humid or moisture-laden atmosphere. In this operation it is desirable to apply the minimum of water 'to avoid cockling of v the paper and the paper preferably is moistened under tension to minimim this tendency. The paper is then dried or not, as required, depending upon the method of moistening used. When using a humid atmosphere, drying generally is unnecessary, but when water is applied by means of a roll or spray, it is generally desirable to dry the paper, e. g. by contacting it with a blast of warm air. The drying serves to prevent excessive swelling of the cellulose fibers. It appears that 'the production of the dull finish is the result of a swelling of the cellulose fibers probably accompanied by a microscopic roughening of the surface which does not" detrimentall'y afie'ct 'the' course be uniform.
I claim:
1. Process of making dull finish coated paper which comprises coating paper with an aqueous coating composition comprising pulverized cellulosejdrying the coating, calendering the coating to the desired surface smoothness and thereafter moistening' the coating.
2. Dull finish coated paper, having a supercalendered surface, the coating of which contains pulverized cellulose which has been swelled by moistening in situ. I
3. Dull finish coated paper obtained by .coating paper with an aqueous coating composition comprising pulverized cellulose, drying and me-. chanically finishing the coating to the .desired smoothness and thereafter mois'tening 'the coating, the coated paper product being characterized by smoothness and printing properties corresponding to the mechanical finishing applied and
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US672906A US2006209A (en) | 1933-05-25 | 1933-05-25 | Dull finish coated paper |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US672906A US2006209A (en) | 1933-05-25 | 1933-05-25 | Dull finish coated paper |
Publications (1)
Publication Number | Publication Date |
---|---|
US2006209A true US2006209A (en) | 1935-06-25 |
Family
ID=24700516
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US672906A Expired - Lifetime US2006209A (en) | 1933-05-25 | 1933-05-25 | Dull finish coated paper |
Country Status (1)
Country | Link |
---|---|
US (1) | US2006209A (en) |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2780563A (en) * | 1952-12-08 | 1957-02-05 | Warren S D Co | Method for cast calendering supercalendered coated paper |
US20080060774A1 (en) * | 2006-09-12 | 2008-03-13 | Zuraw Paul J | Paperboard containing microplatelet cellulose particles |
US8231764B2 (en) | 2009-05-15 | 2012-07-31 | Imerys Minerals, Limited | Paper filler method |
US10053817B2 (en) | 2010-04-27 | 2018-08-21 | Fiberlean Technologies Limited | Process for the manufacture of structured materials using nano-fibrillar cellulose gels |
US10214859B2 (en) | 2016-04-05 | 2019-02-26 | Fiberlean Technologies Limited | Paper and paperboard products |
US10253457B2 (en) | 2010-11-15 | 2019-04-09 | Fiberlean Technologies Limited | Compositions |
US10294371B2 (en) | 2009-03-30 | 2019-05-21 | Fiberlean Technologies Limited | Process for the production of nano-fibrillar cellulose gels |
US10301774B2 (en) | 2009-03-30 | 2019-05-28 | Fiberlean Technologies Limited | Process for the production of nano-fibrillar cellulose suspensions |
US10577469B2 (en) | 2015-10-14 | 2020-03-03 | Fiberlean Technologies Limited | 3D-formable sheet material |
US10794006B2 (en) | 2016-04-22 | 2020-10-06 | Fiberlean Technologies Limited | Compositions comprising microfibrilated cellulose and polymers and methods of manufacturing fibres and nonwoven materials therefrom |
US11155697B2 (en) | 2010-04-27 | 2021-10-26 | Fiberlean Technologies Limited | Process for the production of gel-based composite materials |
US11846072B2 (en) | 2016-04-05 | 2023-12-19 | Fiberlean Technologies Limited | Process of making paper and paperboard products |
-
1933
- 1933-05-25 US US672906A patent/US2006209A/en not_active Expired - Lifetime
Cited By (33)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2780563A (en) * | 1952-12-08 | 1957-02-05 | Warren S D Co | Method for cast calendering supercalendered coated paper |
US20080060774A1 (en) * | 2006-09-12 | 2008-03-13 | Zuraw Paul J | Paperboard containing microplatelet cellulose particles |
WO2008033283A1 (en) * | 2006-09-12 | 2008-03-20 | Meadwestvaco Corporation | Paperboard containing microplatelet cellulose particles |
RU2374374C1 (en) * | 2006-09-12 | 2009-11-27 | Мидвествако Корпорейшн | Carton containing micro-lamellate cellulose particles |
US10294371B2 (en) | 2009-03-30 | 2019-05-21 | Fiberlean Technologies Limited | Process for the production of nano-fibrillar cellulose gels |
US10982387B2 (en) | 2009-03-30 | 2021-04-20 | Fiberlean Technologies Limited | Process for the production of nano-fibrillar cellulose suspensions |
US10975242B2 (en) | 2009-03-30 | 2021-04-13 | Fiberlean Technologies Limited | Process for the production of nano-fibrillar cellulose gels |
US10301774B2 (en) | 2009-03-30 | 2019-05-28 | Fiberlean Technologies Limited | Process for the production of nano-fibrillar cellulose suspensions |
US8231764B2 (en) | 2009-05-15 | 2012-07-31 | Imerys Minerals, Limited | Paper filler method |
US11970817B2 (en) | 2009-05-15 | 2024-04-30 | Fiberlean Technologies Limited | Paper filler composition |
US11377791B2 (en) | 2009-05-15 | 2022-07-05 | Fiberlean Technologies Limited | Paper filler composition |
US10100464B2 (en) | 2009-05-15 | 2018-10-16 | Fiberlean Technologies Limited | Paper filler composition |
US11732411B2 (en) | 2009-05-15 | 2023-08-22 | Fiberlean Technologies Limited | Paper filler composition |
US11162219B2 (en) | 2009-05-15 | 2021-11-02 | Fiberlean Technologies Limited | Paper filler composition |
US9127405B2 (en) | 2009-05-15 | 2015-09-08 | Imerys Minerals, Limited | Paper filler composition |
US10100467B2 (en) | 2010-04-27 | 2018-10-16 | Fiberlean Technologies Limited | Process for the manufacture of structured materials using nano-fibrillar cellulose gels |
US10633796B2 (en) | 2010-04-27 | 2020-04-28 | Fiberlean Technologies Limited | Process for the manufacture of structured materials using nano-fibrillar cellulose gels |
US10053817B2 (en) | 2010-04-27 | 2018-08-21 | Fiberlean Technologies Limited | Process for the manufacture of structured materials using nano-fibrillar cellulose gels |
US11155697B2 (en) | 2010-04-27 | 2021-10-26 | Fiberlean Technologies Limited | Process for the production of gel-based composite materials |
US10253457B2 (en) | 2010-11-15 | 2019-04-09 | Fiberlean Technologies Limited | Compositions |
US11136721B2 (en) | 2010-11-15 | 2021-10-05 | Fiberlean Technologies Limited | Compositions |
US11655594B2 (en) | 2010-11-15 | 2023-05-23 | Fiberlean Technologies Limited | Compositions |
US11384210B2 (en) | 2015-10-14 | 2022-07-12 | Fiberlean Technologies Limited | 3-D formable sheet material |
US10577469B2 (en) | 2015-10-14 | 2020-03-03 | Fiberlean Technologies Limited | 3D-formable sheet material |
US11932740B2 (en) | 2015-10-14 | 2024-03-19 | Fiberlean Technologies Limited | 3D-formable sheet material |
US11274399B2 (en) | 2016-04-05 | 2022-03-15 | Fiberlean Technologies Limited | Paper and paperboard products |
US10801162B2 (en) | 2016-04-05 | 2020-10-13 | Fiberlean Technologies Limited | Paper and paperboard products |
US11732421B2 (en) | 2016-04-05 | 2023-08-22 | Fiberlean Technologies Limited | Method of making paper or board products |
US11846072B2 (en) | 2016-04-05 | 2023-12-19 | Fiberlean Technologies Limited | Process of making paper and paperboard products |
US10214859B2 (en) | 2016-04-05 | 2019-02-26 | Fiberlean Technologies Limited | Paper and paperboard products |
US12203223B2 (en) | 2016-04-05 | 2025-01-21 | Fiberlean Technologies, Ltd. | Method of making paper or board products |
US11572659B2 (en) | 2016-04-22 | 2023-02-07 | Fiberlean Technologies Limited | Compositions comprising microfibrillated cellulose and polymers and methods of manufacturing fibres and nonwoven materials therefrom |
US10794006B2 (en) | 2016-04-22 | 2020-10-06 | Fiberlean Technologies Limited | Compositions comprising microfibrilated cellulose and polymers and methods of manufacturing fibres and nonwoven materials therefrom |
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