US20070284070A1 - Paper Manufacturing Process - Google Patents
- ️Thu Dec 13 2007
US20070284070A1 - Paper Manufacturing Process - Google Patents
Paper Manufacturing Process Download PDFInfo
-
Publication number
- US20070284070A1 US20070284070A1 US11/578,584 US57858405A US2007284070A1 US 20070284070 A1 US20070284070 A1 US 20070284070A1 US 57858405 A US57858405 A US 57858405A US 2007284070 A1 US2007284070 A1 US 2007284070A1 Authority
- US
- United States Prior art keywords
- fibres
- polymer
- wire
- man
- web Prior art date
- 2004-04-14 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.)
- Abandoned
Links
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 12
- 239000000835 fiber Substances 0.000 claims abstract description 22
- 238000000034 method Methods 0.000 claims abstract description 19
- 229920000642 polymer Polymers 0.000 claims abstract description 18
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 15
- 239000002023 wood Substances 0.000 claims abstract description 9
- 239000000725 suspension Substances 0.000 claims abstract description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 5
- 125000000129 anionic group Chemical group 0.000 claims description 5
- 229920002401 polyacrylamide Polymers 0.000 claims description 5
- 229920002134 Carboxymethyl cellulose Polymers 0.000 claims description 2
- 229920002907 Guar gum Polymers 0.000 claims description 2
- 239000000665 guar gum Substances 0.000 claims description 2
- 229960002154 guar gum Drugs 0.000 claims description 2
- 235000010417 guar gum Nutrition 0.000 claims description 2
- 239000001768 carboxy methyl cellulose Substances 0.000 claims 1
- 235000010948 carboxy methyl cellulose Nutrition 0.000 claims 1
- 239000008112 carboxymethyl-cellulose Substances 0.000 claims 1
- 230000000694 effects Effects 0.000 description 3
- 239000000853 adhesive Substances 0.000 description 2
- 230000016615 flocculation Effects 0.000 description 2
- 238000005189 flocculation Methods 0.000 description 2
- HRPVXLWXLXDGHG-UHFFFAOYSA-N Acrylamide Chemical compound NC(=O)C=C HRPVXLWXLXDGHG-UHFFFAOYSA-N 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 229920006184 cellulose methylcellulose Polymers 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 239000004745 nonwoven fabric Substances 0.000 description 1
- 230000010355 oscillation Effects 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 229920002994 synthetic fiber Polymers 0.000 description 1
Images
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
- D21H21/00—Non-fibrous material added to the pulp, characterised by its function, form or properties; Paper-impregnating or coating material, characterised by its function, form or properties
- D21H21/06—Paper forming aids
- D21H21/10—Retention agents or drainage improvers
-
- 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
-
- 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
- D21H17/20—Macromolecular organic compounds
- D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
- D21H17/24—Polysaccharides
- D21H17/25—Cellulose
- D21H17/26—Ethers thereof
-
- 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
- D21H17/20—Macromolecular organic compounds
- D21H17/21—Macromolecular organic compounds of natural origin; Derivatives thereof
- D21H17/24—Polysaccharides
- D21H17/31—Gums
- D21H17/32—Guar or other polygalactomannan gum
-
- 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
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/37—Polymers of unsaturated acids or derivatives thereof, e.g. polyacrylates
- D21H17/375—Poly(meth)acrylamide
-
- 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
- D21H17/20—Macromolecular organic compounds
- D21H17/33—Synthetic macromolecular compounds
- D21H17/34—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/41—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups
- D21H17/42—Synthetic macromolecular compounds obtained by reactions only involving carbon-to-carbon unsaturated bonds containing ionic groups anionic
- D21H17/43—Carboxyl groups or derivatives thereof
Definitions
- the present invention relates to a method for manufacturing a web comprising wood-based fibres and man-made fibres.
- man-made fibres i.e. synthetic fibres or regenerated fibres
- wood-based fibres While the wood-based fibres used have an average fibre length of 1.2 mm, the fibre length of man-made fibres used is usually in the order of 5 mm.
- problems are caused by different fibre lengths and also various other fibre properties.
- One problem is the flocculation of the fibres in the headbox, resulting in poor formation of the web. Long fibres adhere to each other, and they also capture short fibres in the fibre bundles of the long fibres.
- the flocculation tendency can be alleviated by reducing the consistency of the pulp, but the production parameters may thus become such that the production is not possible with conventional machinery and/or the machine speeds must be dropped so low that the production is not profitable.
- Attempts have also been made to manufacture multi-layered paper, wherein diluted pulps can be run at a relatively high speed.
- paper qualities of similar types have been shifted to be manufactured by wet web formation with machinery for non-woven fabrics. To sum up, it has been problematic to run webs comprising man-made fibres in paper machines, and attempts have been made to solve this problem for about 30 years.
- the method according to the invention is characterized in that a polymer is added to a fibre suspension comprising wood-based fibres and man-made fibres, to improve the web formation and to slow down the removal of water in the wire section of the paper machine.
- the above-mentioned problems can be reduced or eliminated by using a polymer mixed in the pulp to improve the web formation and to slow down the removal of water in the wire section of the paper machine.
- the web can be manufactured by utilizing a normal paper machine construction, because there is no need to lower the consistency of the pulp, and thus the size of the slice is sufficient for dosing the pulp onto the wire.
- the consistency is about 1% and the normal running speed is 800 m/min.
- the improvement in the web formation is manifested by the smoothness of the web.
- mechanical means can be used to have an effect on the placement of the fibres in the web.
- the mechanical means include, for example, the intrinsic improvement in the web formation during dewatering, due to the nature of the dewatering, because the fibres tend to move to locations with lower flow resistance and shear forces due to the speed difference between the headbox discharge and the wire.
- Other possible improving mechanisms include shearing forces generated by shaking of the wire and/or oscillation of the surface of the pulp layer.
- Further mechanical means include the effect of suction boxes underneath the forming wire, or it is possible to use a roll on the upper surface of the forming wire to prevent the formation of fibre bundles.
- the polymer to be used in the method according to the invention has a high molecular weight and is relatively unbranched.
- the polymer is preferably anionic.
- Suitable polymers to be used include, for example, anionic polyacrylamide, CMC, guargum, or compounds of these.
- An anionic polyacrylamide suitable for the purpose has a molecular weight of at least 10,000,000 g/mol and an electric charge density of about 30%, and it is dosed 0.2 to 2 kg per ton of fibre.
- CMC has a molecular weight of at least 750,000 g/mol, and it is dosed 2 to 8 kg per ton of fibre.
- the dosage of the polymer can be reduced, because the polymer hardly adheres to the fibre and is thus returned to use.
- the pH value, at which the method works, is neutral or alkaline.
- the pH of the fibre suspension is adjusted to at least 6.5, for the polymer to function in the process.
- the polymer does not function at too high a pH value either.
- the polymer is added either into the pulp mixing tank, before the machine screen, or after the machine screen.
- the method according to the invention is used primarily in the manufacture of wallpaper, particularly in connection with so-called paste-the-wall wallpapers (the adhesive agent is applied onto the wall to be papered and the dry wallpaper is placed onto the adhesive).
- the content of man-made fibres with a typical fibre length of 5 mm is often 10 weight-%, but in a wallpaper made by the method according to the invention, the content may be 15 to 50 weight-%.
- the man-made fibre to be used is polyester, because it has a density suitable for manufacturing with pulp fibres.
- the method is cost-efficient, as the paper can be made according to the conventional paper machine concept.
- the method according to the invention can be applied in products which are presently made by the wet web formation technique, such as filter papers, dust bags for vacuum cleaners, wet-strength towels, bed sheets and linen papers.
- FIG. 1 illustrates the formation (Ambertec formation) as a function of the consistency in the headbox.
- the dosage of anionic polyacrylamide was 1 to 2 kg per ton of fibre.
- the dosage of CMC was 5 to 10 kg per ton of fibre.
- the pH of the fibre suspension in connection with acrylamide was from 7 to 8.
- the pH of the fibre suspension in connection with CMC was from 7 to 8.
Landscapes
- Paper (AREA)
- Dry Formation Of Fiberboard And The Like (AREA)
Abstract
The invention relates to a method for manufacturing a web comprising wood-based fibres and man-made fibres. A polymer is added to a fibre suspension comprising wood-based fibres and man-made fibres to improve the web formation and to slow down the removal of water in the wire section of the paper machine.
Description
-
The present invention relates to a method for manufacturing a web comprising wood-based fibres and man-made fibres.
-
To improve the strength and/or dimensional stability of webs made of wood-based fibres, it is possible to admix man-made fibres, i.e. synthetic fibres or regenerated fibres, with wood-based fibres. While the wood-based fibres used have an average fibre length of 1.2 mm, the fibre length of man-made fibres used is usually in the order of 5 mm. In the manufacture of the fibre, problems are caused by different fibre lengths and also various other fibre properties. One problem is the flocculation of the fibres in the headbox, resulting in poor formation of the web. Long fibres adhere to each other, and they also capture short fibres in the fibre bundles of the long fibres.
-
The flocculation tendency can be alleviated by reducing the consistency of the pulp, but the production parameters may thus become such that the production is not possible with conventional machinery and/or the machine speeds must be dropped so low that the production is not profitable. Attempts have also been made to manufacture multi-layered paper, wherein diluted pulps can be run at a relatively high speed. Furthermore, paper qualities of similar types have been shifted to be manufactured by wet web formation with machinery for non-woven fabrics. To sum up, it has been problematic to run webs comprising man-made fibres in paper machines, and attempts have been made to solve this problem for about 30 years.
-
The method according to the invention is characterized in that a polymer is added to a fibre suspension comprising wood-based fibres and man-made fibres, to improve the web formation and to slow down the removal of water in the wire section of the paper machine.
-
The above-mentioned problems can be reduced or eliminated by using a polymer mixed in the pulp to improve the web formation and to slow down the removal of water in the wire section of the paper machine. The web can be manufactured by utilizing a normal paper machine construction, because there is no need to lower the consistency of the pulp, and thus the size of the slice is sufficient for dosing the pulp onto the wire. Typically, the consistency is about 1% and the normal running speed is 800 m/min.
-
The improvement in the web formation is manifested by the smoothness of the web. As the polymer slows down the exit of water, mechanical means can be used to have an effect on the placement of the fibres in the web. The mechanical means include, for example, the intrinsic improvement in the web formation during dewatering, due to the nature of the dewatering, because the fibres tend to move to locations with lower flow resistance and shear forces due to the speed difference between the headbox discharge and the wire. Other possible improving mechanisms include shearing forces generated by shaking of the wire and/or oscillation of the surface of the pulp layer. Further mechanical means include the effect of suction boxes underneath the forming wire, or it is possible to use a roll on the upper surface of the forming wire to prevent the formation of fibre bundles.
-
The polymer to be used in the method according to the invention has a high molecular weight and is relatively unbranched. The polymer is preferably anionic.
-
Suitable polymers to be used include, for example, anionic polyacrylamide, CMC, guargum, or compounds of these. An anionic polyacrylamide suitable for the purpose has a molecular weight of at least 10,000,000 g/mol and an electric charge density of about 30%, and it is dosed 0.2 to 2 kg per ton of fibre. CMC has a molecular weight of at least 750,000 g/mol, and it is dosed 2 to 8 kg per ton of fibre. During the process, the dosage of the polymer can be reduced, because the polymer hardly adheres to the fibre and is thus returned to use.
-
The pH value, at which the method works, is neutral or alkaline. The pH of the fibre suspension is adjusted to at least 6.5, for the polymer to function in the process. On the other hand, the polymer does not function at too high a pH value either. The polymer is added either into the pulp mixing tank, before the machine screen, or after the machine screen.
-
The method according to the invention is used primarily in the manufacture of wallpaper, particularly in connection with so-called paste-the-wall wallpapers (the adhesive agent is applied onto the wall to be papered and the dry wallpaper is placed onto the adhesive). In wallpaper, the content of man-made fibres with a typical fibre length of 5 mm is often 10 weight-%, but in a wallpaper made by the method according to the invention, the content may be 15 to 50 weight-%. Normally, the man-made fibre to be used is polyester, because it has a density suitable for manufacturing with pulp fibres. In the manufacture of wallpaper, the method is cost-efficient, as the paper can be made according to the conventional paper machine concept.
-
In addition to wallpaper, the method according to the invention can be applied in products which are presently made by the wet web formation technique, such as filter papers, dust bags for vacuum cleaners, wet-strength towels, bed sheets and linen papers.
-
In the following, the invention will be described with reference to an example and a figure. The figure illustrates the formation (Ambertec formation) as a function of the consistency in the headbox.
-
An experiment was made to find out the effect of polyacrylamide and CMC on the formation at different consistencies. The reference was a sample to which no polymer had been added to improve the formation and to slow down the dewatering.
-
The dosage of anionic polyacrylamide was 1 to 2 kg per ton of fibre. The dosage of CMC was 5 to 10 kg per ton of fibre. The pH of the fibre suspension in connection with acrylamide was from 7 to 8. The pH of the fibre suspension in connection with CMC was from 7 to 8.
-
The invention is not restricted to the description above, but it may vary within the scope of the claims.
Claims (6)
1. A method for the manufacture of a web comprising wood-based fibres and man-made fibres, the method comprising adding a polymer to a fibre suspension comprising the wood-based fibres and man-made fibres to improve the web formation and to slow down the removal of water in the wire section of the paper machine, characterized in that the fibre suspension is treated mechanically during the web formation on a wire by shaking the wire, allowing the surface of the pulp layer to oscillate, or using a roll on the upper surface of the wire.
2. The method according to
claim 1, characterized in that the polymer is an anionic polyacrylamide with a molecular weight of at least 10,000,000 g/mol.
3. The method according to
claim 1, characterized in that the polymer is carboxymethyl cellulose with a molecular weight of at least 750,000 g/mol.
4. The method according to
claim 1, characterized in that the polymer is guargum.
5. The method according to
claim 1, characterized in that the polymer is added into a pulp mixing tank, before the machine screen or after the machine screen.
6. The method according to
claim 1, characterized in that the pH of the fibre suspension is adjusted to at least 6.5.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI20045132 | 2004-04-14 | ||
FI20045132A FI20045132A (en) | 2004-04-14 | 2004-04-14 | Paper manufacturing process |
PCT/FI2005/050118 WO2005100689A1 (en) | 2004-04-14 | 2005-04-14 | Paper manufacturing process |
Publications (1)
Publication Number | Publication Date |
---|---|
US20070284070A1 true US20070284070A1 (en) | 2007-12-13 |
Family
ID=32104260
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US11/578,584 Abandoned US20070284070A1 (en) | 2004-04-14 | 2005-04-14 | Paper Manufacturing Process |
Country Status (7)
Country | Link |
---|---|
US (1) | US20070284070A1 (en) |
EP (1) | EP1735497A1 (en) |
JP (1) | JP2007532792A (en) |
CN (1) | CN1942630A (en) |
CA (1) | CA2561033A1 (en) |
FI (1) | FI20045132A (en) |
WO (1) | WO2005100689A1 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105786052B (en) * | 2014-12-16 | 2020-09-08 | 艺康美国股份有限公司 | Online control and reaction method for pH adjustment |
Citations (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2626214A (en) * | 1949-06-14 | 1953-01-20 | C H Dexter & Sons Inc | Paper from long synthetic fibers and partially water soluble sodium carboxymethylcellulose and method |
US3019157A (en) * | 1958-10-06 | 1962-01-30 | American Cyanamid Co | Web-forming fibrous suspensions of improved freeness |
US3391057A (en) * | 1965-07-06 | 1968-07-02 | Dow Chemical Co | Suspensions of synthetic polymer fibrous products containing acrylamide polymer and method of making a paper web therefrom |
US3794557A (en) * | 1969-03-26 | 1974-02-26 | Johnson & Johnson | Method of making isotropic fibrous webs containing textile length fibers |
US3808095A (en) * | 1971-05-13 | 1974-04-30 | Johnson & Johnson | Wet-formed nonwoven textile fabrics and methods of making the same |
US3834983A (en) * | 1973-03-15 | 1974-09-10 | Dexter C & Sons Inc | Process of forming wet laid tufted non-woven fibrous web from a viscous fibrous dispersion and product |
US4200488A (en) * | 1975-02-20 | 1980-04-29 | International Paper Company | Viscous dispersion for forming wet-laid, non-woven fabrics |
US4487657A (en) * | 1978-06-20 | 1984-12-11 | Soci/e/ t/e/ Anonyme dite: Arjomari-Prioux | Method for preparing a fibrous sheet |
US4822452A (en) * | 1987-04-06 | 1989-04-18 | James River Corporation Of Virginia | Manufacture of wet laid nonwoven webs |
US4925528A (en) * | 1987-04-06 | 1990-05-15 | James River Corporation Of Virginia | Manufacture of wetlaid nonwoven webs |
US5133835A (en) * | 1990-03-05 | 1992-07-28 | International Paper Company | Printable, high-strength, tear-resistant nonwoven material and related method of manufacture |
US5238534A (en) * | 1992-01-24 | 1993-08-24 | James River Corporation Of Virginia | Wetlaid nonwovens on high speed machines |
US5403444A (en) * | 1990-03-05 | 1995-04-04 | International Paper Company | Printable, high-strength, tear-resistant nonwoven material and related method of manufacture |
US6100322A (en) * | 1995-07-07 | 2000-08-08 | Eka Chemicals Ab | Process for the production of paper |
US6113741A (en) * | 1996-12-06 | 2000-09-05 | Eka Chemicals Ab | Process for the production of paper |
US6379497B1 (en) * | 1996-09-20 | 2002-04-30 | Fort James Corporation | Bulk enhanced paperboard and shaped products made therefrom |
US6511579B1 (en) * | 1998-06-12 | 2003-01-28 | Fort James Corporation | Method of making a paper web having a high internal void volume of secondary fibers and a product made by the process |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20040209058A1 (en) * | 2002-10-02 | 2004-10-21 | Chou Hung Liang | Paper products including surface treated thermally bondable fibers and methods of making the same |
-
2004
- 2004-04-14 FI FI20045132A patent/FI20045132A/en unknown
-
2005
- 2005-04-14 US US11/578,584 patent/US20070284070A1/en not_active Abandoned
- 2005-04-14 WO PCT/FI2005/050118 patent/WO2005100689A1/en active Application Filing
- 2005-04-14 EP EP05736333A patent/EP1735497A1/en not_active Withdrawn
- 2005-04-14 CA CA002561033A patent/CA2561033A1/en not_active Abandoned
- 2005-04-14 CN CNA200580011274XA patent/CN1942630A/en active Pending
- 2005-04-14 JP JP2007507808A patent/JP2007532792A/en active Pending
Patent Citations (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2626214A (en) * | 1949-06-14 | 1953-01-20 | C H Dexter & Sons Inc | Paper from long synthetic fibers and partially water soluble sodium carboxymethylcellulose and method |
US3019157A (en) * | 1958-10-06 | 1962-01-30 | American Cyanamid Co | Web-forming fibrous suspensions of improved freeness |
US3391057A (en) * | 1965-07-06 | 1968-07-02 | Dow Chemical Co | Suspensions of synthetic polymer fibrous products containing acrylamide polymer and method of making a paper web therefrom |
US3794557A (en) * | 1969-03-26 | 1974-02-26 | Johnson & Johnson | Method of making isotropic fibrous webs containing textile length fibers |
US3808095A (en) * | 1971-05-13 | 1974-04-30 | Johnson & Johnson | Wet-formed nonwoven textile fabrics and methods of making the same |
US3834983A (en) * | 1973-03-15 | 1974-09-10 | Dexter C & Sons Inc | Process of forming wet laid tufted non-woven fibrous web from a viscous fibrous dispersion and product |
US4200488A (en) * | 1975-02-20 | 1980-04-29 | International Paper Company | Viscous dispersion for forming wet-laid, non-woven fabrics |
US4487657A (en) * | 1978-06-20 | 1984-12-11 | Soci/e/ t/e/ Anonyme dite: Arjomari-Prioux | Method for preparing a fibrous sheet |
US4822452A (en) * | 1987-04-06 | 1989-04-18 | James River Corporation Of Virginia | Manufacture of wet laid nonwoven webs |
US4925528A (en) * | 1987-04-06 | 1990-05-15 | James River Corporation Of Virginia | Manufacture of wetlaid nonwoven webs |
US5133835A (en) * | 1990-03-05 | 1992-07-28 | International Paper Company | Printable, high-strength, tear-resistant nonwoven material and related method of manufacture |
US5403444A (en) * | 1990-03-05 | 1995-04-04 | International Paper Company | Printable, high-strength, tear-resistant nonwoven material and related method of manufacture |
US5238534A (en) * | 1992-01-24 | 1993-08-24 | James River Corporation Of Virginia | Wetlaid nonwovens on high speed machines |
US6100322A (en) * | 1995-07-07 | 2000-08-08 | Eka Chemicals Ab | Process for the production of paper |
US6379497B1 (en) * | 1996-09-20 | 2002-04-30 | Fort James Corporation | Bulk enhanced paperboard and shaped products made therefrom |
US6113741A (en) * | 1996-12-06 | 2000-09-05 | Eka Chemicals Ab | Process for the production of paper |
US6511579B1 (en) * | 1998-06-12 | 2003-01-28 | Fort James Corporation | Method of making a paper web having a high internal void volume of secondary fibers and a product made by the process |
Also Published As
Publication number | Publication date |
---|---|
CA2561033A1 (en) | 2005-10-27 |
EP1735497A1 (en) | 2006-12-27 |
WO2005100689A8 (en) | 2006-04-20 |
FI20045132A0 (en) | 2004-04-14 |
FI20045132A (en) | 2005-10-15 |
CN1942630A (en) | 2007-04-04 |
JP2007532792A (en) | 2007-11-15 |
WO2005100689A1 (en) | 2005-10-27 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US11525215B2 (en) | 2022-12-13 | Cellulose and cellulose ester film |
EP2622131B1 (en) | 2020-02-26 | Method for improving papermaking or board making process, use of a polysaccharide and paper |
US7258764B2 (en) | 2007-08-21 | Soft and strong webs from highly refined cellulosic fibres |
TWI589752B (en) | 2017-07-01 | Fibrous web of paper or board and method of making the same |
CN1439071A (en) | 2003-08-27 | Method for adding an adsorbable chemical additive to pulp during the pulp processing and products made by said method |
CA2781757C (en) | 2018-03-13 | A method and a system for making a fibre-containing product |
EP1583869B1 (en) | 2008-02-27 | Soft and strong webs from highly refined cellulosic fibres |
WO2020046628A2 (en) | 2020-03-05 | Composition of matter in stock preparation zone of wet-laid process |
CN111434853B (en) | 2022-10-11 | Paper comprising a multilayer sheet of old paper fibres and grass fibres |
US20070284070A1 (en) | 2007-12-13 | Paper Manufacturing Process |
US7406985B2 (en) | 2008-08-05 | Papermaking screen |
CN112424422A (en) | 2021-02-26 | Method for producing paper or paperboard, in particular label paper or paperboard suitable for use as packaging material for beverage containers, and paper or paperboard produced by the method |
US7585394B2 (en) | 2009-09-08 | Wire cloth, in particular paper making wire cloth |
NZ539024A (en) | 2006-06-30 | Papermaking furnish comprising solventless cationic polymer retention aid combined with phenolic resin and polyethylene oxide |
US7094319B2 (en) | 2006-08-22 | Additive for paper making |
WO2020041262A1 (en) | 2020-02-27 | Improved dewatering in paper making process and articles thereof |
GB2169323A (en) | 1986-07-09 | Making paper for wallboard |
Westman | 1989 | Cationic polyelectrolytes as retention aids in newsprint production |
Foster | 1973 | Water-Soluble Polymers as Flocculants in Papermaking |
Nordström et al. | 2017 | Effect of the ratio of softwood kraft pulp to recycled pulp on formation and strength efficiency in twin-wire roll forming |
EP4448865A1 (en) | 2024-10-23 | Cellulose-based gas barrier film |
McKinney | 1994 | 8 Manufacture of packaging grades from wastepaper |
Danielsson et al. | 2011 | Enhanced capabilities in wet-end paper machine clothing |
Bharati et al. | 1994 | The retention and drainage characteristics of Indian forming on Agriresidue Pulps |
JP2001072133A (en) | 2001-03-21 | Pulp mold |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
2009-11-09 | STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |