EP2876207A1 - Trockenpulpe für aushärtungsgeformtes Papier - Google Patents
Trockenpulpe für aushärtungsgeformtes Papier Download PDFInfo
- Publication number
- EP2876207A1 EP2876207A1 EP13194313.6A EP13194313A EP2876207A1 EP 2876207 A1 EP2876207 A1 EP 2876207A1 EP 13194313 A EP13194313 A EP 13194313A EP 2876207 A1 EP2876207 A1 EP 2876207A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- process according
- sheet
- fibres
- solvent
- paper
- 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.)
- Ceased
Links
- 238000000034 method Methods 0.000 claims abstract description 38
- 230000008569 process Effects 0.000 claims abstract description 36
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 15
- 239000011347 resin Substances 0.000 claims description 19
- 229920005989 resin Polymers 0.000 claims description 19
- 239000000835 fiber Substances 0.000 claims description 15
- 239000002904 solvent Substances 0.000 claims description 14
- 239000000725 suspension Substances 0.000 claims description 11
- 238000003825 pressing Methods 0.000 claims description 8
- 239000007789 gas Substances 0.000 claims description 7
- 239000000126 substance Substances 0.000 claims description 5
- 150000001413 amino acids Chemical class 0.000 claims description 3
- 239000000654 additive Substances 0.000 claims description 2
- 238000010894 electron beam technology Methods 0.000 claims description 2
- 239000003094 microcapsule Substances 0.000 claims description 2
- 239000000178 monomer Substances 0.000 claims description 2
- 230000005855 radiation Effects 0.000 claims description 2
- 229920000642 polymer Polymers 0.000 claims 1
- 238000005516 engineering process Methods 0.000 abstract description 13
- 239000007788 liquid Substances 0.000 abstract description 8
- 229920003043 Cellulose fiber Polymers 0.000 abstract description 4
- 239000010410 layer Substances 0.000 description 9
- 230000009467 reduction Effects 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 7
- UIIMBOGNXHQVGW-UHFFFAOYSA-M Sodium bicarbonate Chemical compound [Na+].OC([O-])=O UIIMBOGNXHQVGW-UHFFFAOYSA-M 0.000 description 6
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 5
- 238000001035 drying Methods 0.000 description 5
- 238000005189 flocculation Methods 0.000 description 5
- 230000016615 flocculation Effects 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 229910002092 carbon dioxide Inorganic materials 0.000 description 4
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012545 processing Methods 0.000 description 3
- 229910000030 sodium bicarbonate Inorganic materials 0.000 description 3
- 235000017557 sodium bicarbonate Nutrition 0.000 description 3
- 239000002253 acid Substances 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 230000001627 detrimental effect Effects 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 238000007306 functionalization reaction Methods 0.000 description 2
- 230000001050 lubricating effect Effects 0.000 description 2
- 238000004806 packaging method and process Methods 0.000 description 2
- 239000000049 pigment Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 230000001681 protective effect Effects 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- RSWGJHLUYNHPMX-UHFFFAOYSA-N Abietic-Saeure Natural products C12CCC(C(C)C)=CC2=CCC2C1(C)CCCC2(C)C(O)=O RSWGJHLUYNHPMX-UHFFFAOYSA-N 0.000 description 1
- 239000002028 Biomass Substances 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 239000004859 Copal Substances 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- 241000782205 Guibourtia conjugata Species 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- KHPCPRHQVVSZAH-HUOMCSJISA-N Rosin Natural products O(C/C=C/c1ccccc1)[C@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 KHPCPRHQVVSZAH-HUOMCSJISA-N 0.000 description 1
- 229920002522 Wood fibre Polymers 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 229920013724 bio-based polymer Polymers 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000011247 coating layer Substances 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 125000003700 epoxy group Chemical group 0.000 description 1
- 230000007717 exclusion Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 239000000976 ink Substances 0.000 description 1
- 230000001678 irradiating effect Effects 0.000 description 1
- 239000004922 lacquer Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000003032 molecular docking Methods 0.000 description 1
- 239000000025 natural resin Substances 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- -1 polyethylene Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001296 polysiloxane Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 238000007639 printing Methods 0.000 description 1
- 239000011241 protective layer Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000010125 resin casting Methods 0.000 description 1
- 238000000518 rheometry Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 239000012815 thermoplastic material Substances 0.000 description 1
- 229920001187 thermosetting polymer Polymers 0.000 description 1
- KHPCPRHQVVSZAH-UHFFFAOYSA-N trans-cinnamyl beta-D-glucopyranoside Natural products OC1C(O)C(O)C(CO)OC1OCC=CC1=CC=CC=C1 KHPCPRHQVVSZAH-UHFFFAOYSA-N 0.000 description 1
- 239000002966 varnish Substances 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 239000011345 viscous material Substances 0.000 description 1
- 238000004804 winding Methods 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
- D21H25/00—After-treatment of paper not provided for in groups D21H17/00 - D21H23/00
- D21H25/04—Physical treatment, e.g. heating, irradiating
- D21H25/06—Physical treatment, e.g. heating, irradiating of impregnated or coated paper
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/03—Non-macromolecular organic compounds
- D21H17/05—Non-macromolecular organic compounds containing elements other than carbon and hydrogen only
- D21H17/07—Nitrogen-containing compounds
-
- 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
-
- 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
-
- 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
-
- 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
-
- 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
- D21H17/35—Polyalkenes, e.g. polystyrene
-
- 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
- D21H17/46—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
-
- 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
- D21H17/46—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/52—Epoxy resins
-
- 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
- D21H17/46—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- D21H17/53—Polyethers; Polyesters
-
- 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
- D21H17/63—Inorganic compounds
- D21H17/70—Inorganic compounds forming new compounds in situ, e.g. within the pulp or paper, by chemical reaction with other substances added separately
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B27—WORKING OR PRESERVING WOOD OR SIMILAR MATERIAL; NAILING OR STAPLING MACHINES IN GENERAL
- B27N—MANUFACTURE BY DRY PROCESSES OF ARTICLES, WITH OR WITHOUT ORGANIC BINDING AGENTS, MADE FROM PARTICLES OR FIBRES CONSISTING OF WOOD OR OTHER LIGNOCELLULOSIC OR LIKE ORGANIC MATERIAL
- B27N3/00—Manufacture of substantially flat articles, e.g. boards, from particles or fibres
- B27N3/04—Manufacture of substantially flat articles, e.g. boards, from particles or fibres from fibres
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- 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
- D21H21/50—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 characterised by form
- D21H21/52—Additives of definite length or shape
- D21H21/54—Additives of definite length or shape being spherical, e.g. microcapsules, beads
Definitions
- the present invention relates to a process comprising a non-water sheet forming technology using high concentration of cellulose fibres suspended in a high viscosity liquid.
- fibre flocs[1] The dominant feature of a suspension composed of wood fibres and water is its inherent propensity to form bundles of mechanically entangled fibres, i.e. fibre flocs[1]. This is a feature closely connected to the concentration of fibres in water [2,3], which lies between 0.5-3% since higher concentration are not technically possible.
- the present invention therefore provides a process for producing paper comprising
- paper will be made by applying an innovative non-water sheet forming technology using high concentration of cellulose fibres suspended in a high viscosity liquid.
- the biggest energy saving impact may result from eliminating not only the drying section, but also the needs for refining, vacuums in the process and huge flows in the white water recirculation. This would mean 28% energy saving and 61% CO 2 saving.
- This process enables single or multi-layer structure, thus opening new opportunities for functionalization of paper as well as with significantly reduced capital investments.
- resin as used herein relates to any liquid, solid, semisolid or viscous substances of plant origin, such as copal, rosin, and amber, used principally in lacquers, varnishes, inks, adhesives, synthetic plastics, and pharmaceuticals and any physically similar synthetics, or chemically modified natural resins including thermoplastic materials such as polyvinyl, polystyrene, and polyethylene and thermosetting materials such as polyesters, epoxies, and silicones that may be used with fillers, stabilizers, pigments, and other components to form plastics.
- thermoplastic materials such as polyvinyl, polystyrene, and polyethylene
- thermosetting materials such as polyesters, epoxies, and silicones that may be used with fillers, stabilizers, pigments, and other components to form plastics.
- a "viscous solvent” is a solvent having a dynamic viscosity of 0.01 to 1 kg/ms (Pa. s) measured with a viscometer at 20 °C.
- the invention provides a process for producing paper comprising
- the invention provides a process for producing paper comprising
- a "shear reduction layer” or a drag-reducing (lubricating) layer is implemented to protect the fibres from shear. This may be done by creating a low viscosity layer surrounding the fibre suspended in a high viscosity liquid that will prevent flocculation and allow processing at high concentration.
- the application relates to the use of two main technologies that are combined with the generic process of layered material structures:
- the first technology starts with dry (preferably ⁇ 10% water content) fibres.
- the fibres used in step (i) have a water content of 0 to 20 wt%, preferably 5 to 15 wt%, and more preferably 10 to 12 wt%.
- the fibres used in step (i) may be obtained from recycled or from virgin pulp.
- the fibres are mixed into a high viscosity liquid, i.e. a resin, at high fibre concentration (up to 40% of fibres).
- a high viscosity liquid i.e. a resin
- the suspension obtained in step (ii) may have a fibre concentration of 10 and 45 wt.-%, preferably 20 to 40 wt.-% and more preferably 30 to 40 wt.-%.
- the liquid/resin may be constituted of a bio-based polymer, oligomer or monomer, which can be cross-linked during the curing process in order to form a fixed structure.
- the resin should be seen as a generic technology platform. Similarly to the possibility to choose fibres raw material, the resin will be available in many variants targeted at different needs (bulk, opacity, moldability, printing, barrier properties %) that all fulfils the base requirement for being able to be used to form a sheet structure at very high fibre concentrations without excessive flocculation and without detrimental effects on the fibres.
- the fibres may be modified chemically such that they will give rise to the protective "shear reduction layer" closest to the fibre surface.
- the possibility of modifying the resin to allow processing has been exploited for processing within other areas such as e.g. in paints with excessive concentration of pigments or in biomass extrusion[5].
- the resin and the fibres thus form a compatible system, which is called "DryPulp".
- amino acids may be used to protect the fibres from shear.
- one possible embodiment of this application is to use bio-based substances such as amino acids to functionalize the surface of the cellulosic fibre. These will modify the docking points and introduce bulky side chains that push the individual fibres apart. This will modify the viscosity of the medium in the proximity of the fibres.
- the DryPulp will allow forming of a thin sheet without excessive flocculation due to the high viscosity of the resin.
- a fibre network similar to paper that is made today can be formed with up to 40% fibre content.
- the DryPulp is formed as a sheet, containing up to 40% fibres.
- the solvent is removed.
- the solvent is removed by pressing the sheet e.g. subjected the sheet to a pressing stage where resin is removed similarly to today's pressing operation where water is removed.
- the sheet has a fibre concentration of 50 and 90 wt.-%, preferably 60 to 85 wt.-% and more preferably 70 to 80 wt.-%.
- the web may contain up to 80% fibres.
- the curing may be carried out by chemical additives, ultraviolet radiation, electron beam, heat or any combination thereof.
- the curing may cause cross-linking within the resin as well as between resin and the cellulose fibres. Curing can be made in several steps affecting different properties such as the resin only or the resin-protective layer interface.
- the resin-protective layer-fibre system will allow reversal of the curing, which will allow recycling of the resin as well as of the fibres.
- the use of air or other gases as expanding elements within the sheet may be applied. This could be achieved either by having micro-capsules of air and gas within the resin that are activated during treatment in the pressing (crushed) or through substances that generates gas bubbles under the influence of the curing process or some other external forcing.
- One possibility is to use Sodium Bicarbonate to form gas bubbles[6]. This activation will generate carbon dioxide and the sheet will expand generating a bulky material. This is already used in speciality paper grades where an active energy beam is irradiated onto a foamable composition containing an acid generating agent and Sodium Bicarbonate. The irradiating energy generates an acid that activates the Sodium Bicarbonate that, in turn, generates the bubbles/foam.
- the sheet may be formed as a layered product.
- the layered product is formed by first forming simultaneously, e.g. in one nozzle, or separately at least two layers and then bringing the layers together. This will allow optimization towards desired product properties as well as addition of new functionalities. As an example, if a smooth surface is required, the expansion can be limited to take place within the middle layer of a three layered sheet, i.e. coating will be achieved during the forming process. Micro-bubbles may also be used in the final sheet in order to achieve opacity, which would remove the need for fillers.
- This process for paper and board products will contribute to decarbonisation through the energy savings gained from the elimination of the excessive need for vacuum, the friction losses in pressing and the drying of the base paper as well as drying of coating layers.
- the drying process in paper making alone consumes about half of the energy and today has the largest CO 2 impact.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Paper (AREA)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP13194313.6A EP2876207A1 (de) | 2013-11-25 | 2013-11-25 | Trockenpulpe für aushärtungsgeformtes Papier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP13194313.6A EP2876207A1 (de) | 2013-11-25 | 2013-11-25 | Trockenpulpe für aushärtungsgeformtes Papier |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| EP2876207A1 true EP2876207A1 (de) | 2015-05-27 |
Family
ID=49639781
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP13194313.6A Ceased EP2876207A1 (de) | 2013-11-25 | 2013-11-25 | Trockenpulpe für aushärtungsgeformtes Papier |
Country Status (1)
| Country | Link |
|---|---|
| EP (1) | EP2876207A1 (de) |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4413619A1 (de) * | 1993-12-02 | 1995-06-08 | Wkp Wuerttembergische Kunststo | Verfahren zum Herstellen von Papier |
| US6582648B1 (en) * | 1997-09-05 | 2003-06-24 | Fritz Egger Gmbh & Co. | Method for manufacturing moulded bodies from crushed material and a binder hardenable by electron radiation |
| WO2011001791A1 (ja) | 2009-06-29 | 2011-01-06 | Komatsu Michio | 木粉含有樹脂成形体及びその製造方法 |
| WO2012084846A2 (en) * | 2010-12-22 | 2012-06-28 | Bayer Materialscience Ag | Process for the production of sized and/or wet-strength papers, paperboards and cardboards |
| US20130078437A1 (en) * | 2011-09-28 | 2013-03-28 | Trespa International B.V. | Method for producing a decorative film, as well as a decorative panel |
-
2013
- 2013-11-25 EP EP13194313.6A patent/EP2876207A1/de not_active Ceased
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE4413619A1 (de) * | 1993-12-02 | 1995-06-08 | Wkp Wuerttembergische Kunststo | Verfahren zum Herstellen von Papier |
| US6582648B1 (en) * | 1997-09-05 | 2003-06-24 | Fritz Egger Gmbh & Co. | Method for manufacturing moulded bodies from crushed material and a binder hardenable by electron radiation |
| WO2011001791A1 (ja) | 2009-06-29 | 2011-01-06 | Komatsu Michio | 木粉含有樹脂成形体及びその製造方法 |
| WO2012084846A2 (en) * | 2010-12-22 | 2012-06-28 | Bayer Materialscience Ag | Process for the production of sized and/or wet-strength papers, paperboards and cardboards |
| US20130078437A1 (en) * | 2011-09-28 | 2013-03-28 | Trespa International B.V. | Method for producing a decorative film, as well as a decorative panel |
Non-Patent Citations (5)
| Title |
|---|
| KEREKES: "Rheology of fibre suspensions in papermaking: An overview of recent research", NORDIC PULP AND PAPER RESEARCH JOURNAL, vol. 21, no. 5, 2009, pages 598 - 612 |
| MASON, S.G.: "The Flocculation of Cellulose Fibre Suspensions", PULP PAPER MAG. CAN., 1948, pages 99 - 104 |
| SCHMID, C.F.; KLINGENBERG, D.J.: "Mechanical Flocculation in Flowing Fiber Suspensions", PHYSICAL REVIEW LETTERS, vol. 84, no. 2, 2000, pages 290 - 293 |
| SCOTT, C.T.; SAMANIUK, J.R.; KLINGENBERG, D.J.: "Rheology and extrusion of high- solids biomass", TAPPI JOURNAL, vol. 10, no. 5, 2011, pages 47 - 53 |
| SUZUKI, K.; OKUMURA, H.; KITAGAWA, K.; SATO, S.; NAKAGAITO, A.N.; YANO, H.: "Development of continuous process enabling nanofibrillation of pulp and melt compounding", CELLULOSE, vol. 20, no. 1, 2013, pages 201 - 210 |
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