EP4234811A1 - Procédé de production d'un papier imprégné - Google Patents
Procédé de production d'un papier imprégné Download PDFInfo
- Publication number
- EP4234811A1 EP4234811A1 EP22167403.9A EP22167403A EP4234811A1 EP 4234811 A1 EP4234811 A1 EP 4234811A1 EP 22167403 A EP22167403 A EP 22167403A EP 4234811 A1 EP4234811 A1 EP 4234811A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- water
- based composition
- paper
- iso
- impregnated 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.)
- Pending
Links
- 238000000034 method Methods 0.000 title claims abstract description 22
- 239000000203 mixture Substances 0.000 claims abstract description 40
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 32
- 239000000835 fiber Substances 0.000 claims abstract description 16
- 229920002472 Starch Polymers 0.000 claims abstract description 14
- 235000019698 starch Nutrition 0.000 claims abstract description 14
- 239000008107 starch Substances 0.000 claims abstract description 14
- 239000011122 softwood Substances 0.000 claims abstract description 12
- 239000011121 hardwood Substances 0.000 claims abstract description 10
- 238000001035 drying Methods 0.000 claims abstract description 6
- 239000004971 Cross linker Substances 0.000 claims description 8
- 235000013808 oxidized starch Nutrition 0.000 claims description 7
- 239000001254 oxidized starch Substances 0.000 claims description 7
- 229920001353 Dextrin Polymers 0.000 claims description 5
- 239000004375 Dextrin Substances 0.000 claims description 5
- 229920002774 Maltodextrin Polymers 0.000 claims description 5
- 239000005913 Maltodextrin Substances 0.000 claims description 5
- 235000019425 dextrin Nutrition 0.000 claims description 5
- 229940035034 maltodextrin Drugs 0.000 claims description 5
- 239000011347 resin Substances 0.000 claims description 4
- 229920005989 resin Polymers 0.000 claims description 4
- 239000000123 paper Substances 0.000 description 65
- 230000004888 barrier function Effects 0.000 description 11
- 239000003921 oil Substances 0.000 description 9
- 230000003746 surface roughness Effects 0.000 description 6
- 239000011248 coating agent Substances 0.000 description 5
- 238000000576 coating method Methods 0.000 description 5
- 239000011436 cob Substances 0.000 description 5
- 239000004927 clay Substances 0.000 description 4
- 238000005470 impregnation Methods 0.000 description 4
- 239000000463 material Substances 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000003346 palm kernel oil Substances 0.000 description 3
- 235000019865 palm kernel oil Nutrition 0.000 description 3
- 125000002091 cationic group Chemical group 0.000 description 2
- 239000008199 coating composition Substances 0.000 description 2
- 239000004519 grease Substances 0.000 description 2
- 239000002655 kraft paper Substances 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- NGDLSKPZMOTRTR-OAPYJULQSA-N (4z)-4-heptadecylidene-3-hexadecyloxetan-2-one Chemical compound CCCCCCCCCCCCCCCC\C=C1/OC(=O)C1CCCCCCCCCCCCCCCC NGDLSKPZMOTRTR-OAPYJULQSA-N 0.000 description 1
- 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
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 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
- 238000010521 absorption reaction Methods 0.000 description 1
- 229940037003 alum Drugs 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000001143 conditioned effect Effects 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000007670 refining Methods 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
- 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
- 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
- D21H21/14—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 function or properties in or on the paper
- D21H21/16—Sizing or water-repelling agents
-
- 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
- D21H17/28—Starch
-
- 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
- D21H17/28—Starch
- D21H17/29—Starch cationic
-
- 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
- D21H17/54—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen
-
- 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
- D21H17/54—Synthetic macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen
- D21H17/55—Polyamides; Polyaminoamides; Polyester-amides
-
- 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
- D21H19/44—Coatings with pigments characterised by the other ingredients, e.g. the binder or dispersing agent
- D21H19/54—Starch
-
- 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
- D21H19/80—Paper comprising more than one coating
- D21H19/84—Paper comprising more than one coating on both sides of the substrate
-
- 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
- D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
- D21H23/02—Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
- D21H23/22—Addition to the formed paper
- D21H23/24—Addition to the formed paper during paper manufacture
- D21H23/26—Addition to the formed paper during paper manufacture by selecting point of addition or moisture content of the 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
- D21H23/00—Processes or apparatus for adding material to the pulp or to the paper
- D21H23/02—Processes or apparatus for adding material to the pulp or to the paper characterised by the manner in which substances are added
- D21H23/22—Addition to the formed paper
- D21H23/32—Addition to the formed paper by contacting paper with an excess of material, e.g. from a reservoir or in a manner necessitating removal of applied excess material from the paper
- D21H23/42—Paper being at least partly surrounded by the material on both sides
-
- 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
- D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
- D21H27/10—Packing paper
Definitions
- the present disclosure relates to the field of paper-based materials to be used in applications requiring barrier properties.
- An objective of the present disclosure is to provide a non-brittle fluorochemical-free paper that provides a grease barrier and/or enables formation of an efficient barrier coating thereon.
- the present disclosure provides a method of producing an impregnated paper, comprising the steps of:
- the present disclosure provides a method of producing an impregnated paper.
- the paper produced by this method obtains its beneficial properties without the addition of fluorochemicals.
- the impregnated paper of the present disclosure is preferably fluorochemical-free.
- the method comprising the steps of:
- step c the paper web was not impregnated to the same extent, which resulted in a more brittle paper product that broke during wind-up.
- a dry matter content of the water-based composition outside the range of 8-18 % results in less efficient impregnation.
- the dry matter content of the water-based composition is 10-15 %.
- a film press is used for the impregnation of the paper web in step c).
- the impregnated paper is an impregnated machine glazed (MG) paper.
- the Bendtsen surface roughness (measured according to ISO 8791-2:2013) of the glazed side of the impregnated paper is preferably below 200 ml/min, such as below 150 ml/min, such as below 120 ml/min.
- the lower limit for the Bendtsen surface roughness (ISO 8791-2:2013) of the glazed side may for example be 50 ml/min.
- the glazed side of an MG paper is particularly suitable for printing also without a pigmented coating thereon.
- the impregnated paper is an impregnated MG paper and the glazed side thereof is not pigment-coated, but printed.
- the non-glazed side may be provided with a barrier coating.
- the impregnated paper of this embodiment is preferably used for at least one wall of a package, wherein the glazed (and printed) side is facing outwards and the non-glazed (and barrier-coated) side is facing inwards.
- the furnish preferably comprises a mixture of hardwood fibres and softwood fibres.
- the dry weight ratio of hardwood fibers to softwood fibers is between 1:1 and 1:3.
- the dry weight ratio of hardwood fibers to softwood fibers is between 1:1.2 and 1:2.0, such as between 1:1.3 and 1:1.8.
- Such a relatively high proportion of softwood fibres is particularly preferred when the impregnated paper has an ash content of at least 3%, such as at least 5%.
- the starch of the water-based composition preferably comprises oxidized starch or dextrin, such as maltodextrin.
- water-based composition preferably comprises oxidized starch and dextrin, such as maltodextrin.
- Oxidized starch and/or dextrin may for example constitute at least 50% of the dry weight of the water-based composition, such as at least 75% of the dry weight of the water-based composition. In one embodiment, oxidized starch and dextrin constitute at least 85% of the dry weight of the water-based composition
- the water-based composition further comprises a crosslinker.
- this crosslinker is capable of crosslinking the starch.
- An example of such a crosslinker is a PAE resin.
- the amount of the crosslinker in the water-based composition may for example be 1-9 %, such as 3-7 %, based on the dry weight of starch.
- the dry amount of water-based composition applied in step c) is 0.4-3.0 g/m 2 , such as 0.6-3.0 g/m 2 . If a higher amount is applied, the risk of obtaining a brittle final product is greater (and brittleness may result in breakage during winding or converting). If the applied amount is too low, the oil barrier properties may be insufficient and/or it may be more difficult to form a continuous film on the surface of the paper product.
- the water-based composition is preferably applied to both sides of the paper web having the moisture content of 10-15 % in step c).
- the dry amount of water-based composition applied to each side is preferably 0.4-1.5 g/m 2 , such as 0.6-1.4 g/m 2 .
- the paper web having the moisture content of 10-15 % has a Gurley value when measured according to ISO 536:2019 of at least 75 s, such as at least 80 s, such as at least 85 s.
- the upper limit is typically 150 s. In one embodiment, the upper limit is 120 s. Such an embodiment maybe preferred since papermaking runnability problems may occur between 120 s and 150 s.
- the measurement according to ISO 536:2019 is carried out on a conditioned sample meaning that the moisture content is no longer 10-15 % when the Gurley value is determined.
- the above-mentioned Gurley values may be achieved by relatively extensive refining of the fibres prior to step a).
- the method of the present disclosure typically further comprises the step of drying the impregnated paper web from step c) to obtain the impregnated paper.
- the impregnation step typically results in a paper of very high air resistance, which reflects high resistance to oil breakthrough and/or low absorption of a barrier coating composition applied thereon.
- the impregnated paper preferably has a Gurley value (measured according to ISO 5636-5:2013) of at least 400 s, such as at least 500 s.
- the Bendtsen porosity (measured according to ISO 5636-3:2013) of the impregnated paper may for example be in the range of 10-50 ml/min.
- the basis weight of the impregnated paper may be 30-65 g/m 2 , such as 35-60 g/m 2 , preferably 35-55 g/m 2 . Higher basis weights are not needed (neither economically motivated) for the intended application. In the present application, basis weight is measured according to ISO 536:2019.
- the ash content of the impregnated paper is 3-9 %, such as 5-9 %, such as 5-8 %.
- a relatively high ash content is the consequence of addition of clay.
- the higher ash contents i.e. 5-9 %) are particularly preferred in case of lower grammages (i.e. 35-45 g/m 2 , such as 35-40 g/m 2 ).
- a reason for adding clay may be to increase opacity.
- clay reduces strength, which impairs runnability.
- Softwood pulp and cationic starch is typically included in the furnish to compensate for this strength reduction.
- the opacity of the impregnated paper is at least 47%, such as at least 53%.
- opacity is measured according to ISO 2471:2008. Strength values are discussed below.
- the burst strength of the impregnated paper is at least 100 kPa and/or the burst strength index is at least 3.3 kN/g, such as 3.3-5.0 kN/g.
- the burst strength is measured according to ISO 2758:2014.
- the tear strength in the machine direction (MD) of the impregnated paper is at least 150 mN and/or the tear strength index in the MD of the impregnated paper is at least 4.0 mNm 2 /g, such as 4.0-6.5 mNm 2 /g.
- the tear strength in the cross direction (CD) of the impregnated paper is at least 155 mN and/or the tear strength index in the CD of the impregnated paper is at least 4.3 mNm 2 /g, such as 4.3-6.8 mNm 2 /g.
- tear strength is measured according to ISO 1974:2012.
- At least one side of the impregnated paper has a Cobb 60 s value of less than 20 g/m 2 , such as less than 19 g/m 2 , such as less than 18.5 g/m 2 .
- both sides of the impregnated paper have a Cobb 60 s value below 21 g/m 2 , such as below 20 g/m 2 .
- the Cobb 60 s value is measured according to ISO 535:2014.
- the Bendtsen surface roughness (ISO 8791-2:2013) of a side of the impregnated paper is in the range of 200-500 ml/min. In case of an MG paper, this side is typically the non-glazed side.
- the tensile strength in the MD of the impregnated paper is preferably above 3.5 kN/m. Further, the tensile index in the MD of the impregnated paper is preferably in the range of 90-145 Nm/g.
- the tensile strength in the CD of the impregnated paper is preferably above 1.8 kN/m. Further, the tensile index in the CD of the impregnated paper is preferably in the range of 50-100 Nm/g, such as 50-85 Nm/g.
- tensile strength is measured according to ISO 1924-3:2005.
- the palm kernel oil breakthrough (measured according to ISO 16532-1) of at least one side of the impregnated paper is above 15 min, preferably above 18 min, such as above 20 min.
- the palm kernel oil breakthrough (measured according to ISO 16532-1) of both sides of the impregnated paper is above 15 min, preferably above 18 min, such as above 20 min.
- a furnish comprising softwood kraft fibres and hardwood kraft fibres in a 60:40 dry weight ratio was provided.
- the furnish contained clay in such an amount that the final ash content of the paper was 6.8%.
- the furnish contained 3.7 kg/tonne dry fibre of cationic starch, 2.5 kg/tonne dry fibre of rosin size and retention polymer.
- NaOH and alum was added to adjust the pH to 5.6.
- the furnish was refined to such an extent that the paper (before impregnation) had a Gurley value of 87 s.
- An MG paper was formed from the furnish on a full-scale paper machine equipped with a Yankee cylinder.
- the degree of drying was such that the paper web leaving the Yankee cylinder had a moisture content of 12%.
- This paper web having a moisture content of 12% was impregnated on both sides in a (full-scale) film press.
- the upper side of the paper web was impregnated with a first water-based composition comprising:
- the wire side (glazed side) of the paper web was impregnated with a second water-based composition comprising:
- the applied dry amount of the first water-based composition was 0.96 g/m 2 .
- the applied dry amount of the second water-based composition was 0.86 g/m 2 .
- the impregnated paper was then dried such that it had 6.2% moisture when rolled up.
- the basis weight at roll-up was 38 g/m 2 . Further properties are provided in table 1 below.
- Bags was formed from the paper of table 1. In the bags, the upper side was facing inwards. Freshly fried hash browns were placed in the bags. After containing the hash browns, the paper of the bags was evaluated and found to have a satisfactory grease barrier, comparatively low sogginess and no tack issues.
- the upper side of the impregnated paper is intended to be provided with a barrier coating, e.g. in an off-line coating operation, it may be preferred to omit the wax from the first water-based composition since it may otherwise be difficult to wet and hence efficiently coat the upper side with a water-based barrier coating composition.
- the wire side (glazed side) of the impregnated paper has low surface roughness and is thus particularly suitable for printing.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Paper (AREA)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP22159305.6A EP4234810B1 (fr) | 2022-02-28 | 2022-02-28 | Papier pare-graisse exempt de composés fluorés |
Publications (1)
Publication Number | Publication Date |
---|---|
EP4234811A1 true EP4234811A1 (fr) | 2023-08-30 |
Family
ID=80623430
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP22159305.6A Active EP4234810B1 (fr) | 2022-02-28 | 2022-02-28 | Papier pare-graisse exempt de composés fluorés |
EP22167403.9A Pending EP4234811A1 (fr) | 2022-02-28 | 2022-04-08 | Procédé de production d'un papier imprégné |
Family Applications Before (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP22159305.6A Active EP4234810B1 (fr) | 2022-02-28 | 2022-02-28 | Papier pare-graisse exempt de composés fluorés |
Country Status (3)
Country | Link |
---|---|
EP (2) | EP4234810B1 (fr) |
FI (1) | FI4234810T3 (fr) |
WO (1) | WO2023161351A1 (fr) |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0601562A1 (fr) * | 1992-12-09 | 1994-06-15 | Eastman Kodak Company | Support papier photographique encollé à l'amylose substituée par un groupe hydrophobe et élément photographique le contenant |
US20090297842A1 (en) * | 2005-04-27 | 2009-12-03 | Kousuke Akiyama | Oil-resistant sheet material |
DE102011001617A1 (de) * | 2011-03-29 | 2012-10-04 | Papierfabrik Hamburger Rieger GmbH & Co. KG | Vorrichtung und Verfahren zur Herstellung eines mehrlagigen Verpackungspapiers |
CN107988845A (zh) * | 2017-12-29 | 2018-05-04 | 安徽宏实光机电高科有限公司 | 一种纳米二氧化硅疏油增强复合壳聚糖施胶剂的制备方法 |
CN110093806A (zh) * | 2019-05-06 | 2019-08-06 | 浙江科技学院 | 一种无涂层数码喷墨转移印花原纸及其生产方法 |
CN110158364A (zh) * | 2019-05-30 | 2019-08-23 | 浙江恒达新材料股份有限公司 | 一种低定量涂布型食品包装原纸及其制备方法 |
CN112080964A (zh) * | 2020-09-10 | 2020-12-15 | 将军烟草集团有限公司济南包装材料分公司 | 一种防渗油涂布液及制备方法与应用 |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB9511482D0 (en) * | 1995-06-07 | 1995-08-02 | Wiggins Teape Group The Limite | Ink jet printing paper |
EP1176254A1 (fr) * | 2000-07-24 | 2002-01-30 | The Dow Chemical Company | Utilisation de dispersions d'amidon reticulé dans la fabrication du papier |
EP3202979B1 (fr) * | 2016-02-04 | 2018-08-22 | BillerudKorsnäs AB | Papier d'emballage de liquide |
US12037749B2 (en) * | 2016-07-26 | 2024-07-16 | Footprint International, LLC | Acrylate and non-acrylate based chemical compositions for selectively coating fiber-based food containers |
US20180030658A1 (en) * | 2016-07-26 | 2018-02-01 | Footprint International, LLC | Methods and Apparatus For Manufacturing Fiber-Based Produce Containers |
US10036126B2 (en) * | 2016-07-26 | 2018-07-31 | Footprint International, LLC | Methods for manufacturing fiber-based beverage lids |
-
2022
- 2022-02-28 EP EP22159305.6A patent/EP4234810B1/fr active Active
- 2022-02-28 FI FIEP22159305.6T patent/FI4234810T3/fi active
- 2022-04-08 EP EP22167403.9A patent/EP4234811A1/fr active Pending
-
2023
- 2023-02-23 WO PCT/EP2023/054574 patent/WO2023161351A1/fr unknown
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0601562A1 (fr) * | 1992-12-09 | 1994-06-15 | Eastman Kodak Company | Support papier photographique encollé à l'amylose substituée par un groupe hydrophobe et élément photographique le contenant |
US20090297842A1 (en) * | 2005-04-27 | 2009-12-03 | Kousuke Akiyama | Oil-resistant sheet material |
DE102011001617A1 (de) * | 2011-03-29 | 2012-10-04 | Papierfabrik Hamburger Rieger GmbH & Co. KG | Vorrichtung und Verfahren zur Herstellung eines mehrlagigen Verpackungspapiers |
CN107988845A (zh) * | 2017-12-29 | 2018-05-04 | 安徽宏实光机电高科有限公司 | 一种纳米二氧化硅疏油增强复合壳聚糖施胶剂的制备方法 |
CN110093806A (zh) * | 2019-05-06 | 2019-08-06 | 浙江科技学院 | 一种无涂层数码喷墨转移印花原纸及其生产方法 |
CN110158364A (zh) * | 2019-05-30 | 2019-08-23 | 浙江恒达新材料股份有限公司 | 一种低定量涂布型食品包装原纸及其制备方法 |
CN112080964A (zh) * | 2020-09-10 | 2020-12-15 | 将军烟草集团有限公司济南包装材料分公司 | 一种防渗油涂布液及制备方法与应用 |
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EP4234810A1 (fr) | 2023-08-30 |
EP4234810B1 (fr) | 2024-02-21 |
WO2023161351A1 (fr) | 2023-08-31 |
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