WO2022269141A1 - Sheet-like product and method for its manufacture - Google Patents
Sheet-like product and method for its manufacture Download PDFInfo
- Publication number
- WO2022269141A1 WO2022269141A1 PCT/FI2022/050467 FI2022050467W WO2022269141A1 WO 2022269141 A1 WO2022269141 A1 WO 2022269141A1 FI 2022050467 W FI2022050467 W FI 2022050467W WO 2022269141 A1 WO2022269141 A1 WO 2022269141A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- coating layer
- polymer
- sheet
- coating
- melting point
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 17
- 238000004519 manufacturing process Methods 0.000 title description 7
- 239000011247 coating layer Substances 0.000 claims abstract description 115
- 229920000642 polymer Polymers 0.000 claims abstract description 85
- 238000002425 crystallisation Methods 0.000 claims abstract description 46
- 230000008025 crystallization Effects 0.000 claims abstract description 45
- 238000002844 melting Methods 0.000 claims abstract description 44
- 230000008018 melting Effects 0.000 claims abstract description 44
- 230000004888 barrier function Effects 0.000 claims abstract description 32
- 239000000758 substrate Substances 0.000 claims abstract description 28
- 239000011248 coating agent Substances 0.000 claims abstract description 26
- 238000000576 coating method Methods 0.000 claims abstract description 26
- 238000007766 curtain coating Methods 0.000 claims abstract description 9
- 239000010410 layer Substances 0.000 claims description 41
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 18
- 239000002245 particle Substances 0.000 claims description 18
- 229920013724 bio-based polymer Polymers 0.000 claims description 17
- 238000001035 drying Methods 0.000 claims description 17
- -1 polybutylene succinate Polymers 0.000 claims description 15
- 229920002988 biodegradable polymer Polymers 0.000 claims description 14
- 239000004621 biodegradable polymer Substances 0.000 claims description 14
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 11
- 229920001577 copolymer Polymers 0.000 claims description 9
- 239000000203 mixture Substances 0.000 claims description 8
- 239000005014 poly(hydroxyalkanoate) Substances 0.000 claims description 8
- 229920000903 polyhydroxyalkanoate Polymers 0.000 claims description 8
- 229920000728 polyester Polymers 0.000 claims description 7
- 239000004372 Polyvinyl alcohol Substances 0.000 claims description 5
- 239000010445 mica Substances 0.000 claims description 5
- 229910052618 mica group Inorganic materials 0.000 claims description 5
- 229920000747 poly(lactic acid) Polymers 0.000 claims description 5
- 229920002961 polybutylene succinate Polymers 0.000 claims description 5
- 239000004631 polybutylene succinate Substances 0.000 claims description 5
- 229920009537 polybutylene succinate adipate Polymers 0.000 claims description 5
- 229920001610 polycaprolactone Polymers 0.000 claims description 5
- 229920002451 polyvinyl alcohol Polymers 0.000 claims description 5
- 239000000454 talc Substances 0.000 claims description 5
- 229910052623 talc Inorganic materials 0.000 claims description 5
- 239000005995 Aluminium silicate Substances 0.000 claims description 4
- 229920002472 Starch Polymers 0.000 claims description 4
- 235000012211 aluminium silicate Nutrition 0.000 claims description 4
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 claims description 4
- 239000008107 starch Substances 0.000 claims description 4
- 235000019698 starch Nutrition 0.000 claims description 4
- 229920002134 Carboxymethyl cellulose Polymers 0.000 claims description 3
- 229920000331 Polyhydroxybutyrate Polymers 0.000 claims description 3
- 229920000229 biodegradable polyester Polymers 0.000 claims description 3
- 239000004622 biodegradable polyester Substances 0.000 claims description 3
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 3
- 239000001768 carboxy methyl cellulose Substances 0.000 claims description 3
- 235000010948 carboxy methyl cellulose Nutrition 0.000 claims description 3
- 239000008112 carboxymethyl-cellulose Substances 0.000 claims description 3
- 239000001913 cellulose Substances 0.000 claims description 3
- 229920002678 cellulose Polymers 0.000 claims description 3
- 239000005015 poly(hydroxybutyrate) Substances 0.000 claims description 3
- 229920000218 poly(hydroxyvalerate) Polymers 0.000 claims description 3
- 239000004632 polycaprolactone Substances 0.000 claims description 3
- 229920002792 polyhydroxyhexanoate Polymers 0.000 claims description 3
- 229920003048 styrene butadiene rubber Polymers 0.000 claims description 3
- 229920001059 synthetic polymer Polymers 0.000 claims description 3
- 239000004354 Hydroxyethyl cellulose Substances 0.000 claims description 2
- 239000004698 Polyethylene Substances 0.000 claims description 2
- 229920000954 Polyglycolide Polymers 0.000 claims description 2
- 239000004743 Polypropylene Substances 0.000 claims description 2
- DQXBYHZEEUGOBF-UHFFFAOYSA-N but-3-enoic acid;ethene Chemical compound C=C.OC(=O)CC=C DQXBYHZEEUGOBF-UHFFFAOYSA-N 0.000 claims description 2
- 229920003090 carboxymethyl hydroxyethyl cellulose Polymers 0.000 claims description 2
- 229920006242 ethylene acrylic acid copolymer Polymers 0.000 claims description 2
- 239000005038 ethylene vinyl acetate Substances 0.000 claims description 2
- 235000019447 hydroxyethyl cellulose Nutrition 0.000 claims description 2
- 229920003145 methacrylic acid copolymer Polymers 0.000 claims description 2
- 229920005615 natural polymer Polymers 0.000 claims description 2
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 claims description 2
- 229920000573 polyethylene Polymers 0.000 claims description 2
- 229920000139 polyethylene terephthalate Polymers 0.000 claims description 2
- 229920000098 polyolefin Polymers 0.000 claims description 2
- 229920001155 polypropylene Polymers 0.000 claims description 2
- 239000000047 product Substances 0.000 description 17
- 238000004806 packaging method and process Methods 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 229910001868 water Inorganic materials 0.000 description 7
- 230000009477 glass transition Effects 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 230000008569 process Effects 0.000 description 6
- 239000002344 surface layer Substances 0.000 description 6
- 238000003490 calendering Methods 0.000 description 5
- 230000000903 blocking effect Effects 0.000 description 4
- 235000010216 calcium carbonate Nutrition 0.000 description 4
- 238000001816 cooling Methods 0.000 description 4
- 238000000113 differential scanning calorimetry Methods 0.000 description 4
- 229920000126 latex Polymers 0.000 description 4
- 239000004816 latex Substances 0.000 description 4
- 229920006125 amorphous polymer Polymers 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 229920001222 biopolymer Polymers 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 239000004519 grease Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 238000007789 sealing Methods 0.000 description 3
- 238000004804 winding Methods 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 235000013361 beverage Nutrition 0.000 description 2
- 239000011230 binding agent Substances 0.000 description 2
- 230000005540 biological transmission Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000011109 contamination Methods 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000006185 dispersion Substances 0.000 description 2
- 239000002480 mineral oil Substances 0.000 description 2
- 235000010446 mineral oil Nutrition 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 239000003208 petroleum Substances 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 230000001681 protective effect Effects 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 238000003860 storage Methods 0.000 description 2
- 238000004381 surface treatment Methods 0.000 description 2
- NJVOHKFLBKQLIZ-UHFFFAOYSA-N (2-ethenylphenyl) prop-2-enoate Chemical compound C=CC(=O)OC1=CC=CC=C1C=C NJVOHKFLBKQLIZ-UHFFFAOYSA-N 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 241000195493 Cryptophyta Species 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 241000233866 Fungi Species 0.000 description 1
- 229920000426 Microplastic Polymers 0.000 description 1
- 239000002174 Styrene-butadiene Substances 0.000 description 1
- 238000013459 approach Methods 0.000 description 1
- 230000004071 biological effect Effects 0.000 description 1
- MTAZNLWOLGHBHU-UHFFFAOYSA-N butadiene-styrene rubber Chemical compound C=CC=C.C=CC1=CC=CC=C1 MTAZNLWOLGHBHU-UHFFFAOYSA-N 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 229910052570 clay Inorganic materials 0.000 description 1
- 239000008199 coating composition Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 239000007857 degradation product Substances 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 230000032798 delamination Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 239000000839 emulsion Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000002803 fossil fuel Substances 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 230000009931 harmful effect Effects 0.000 description 1
- 150000002484 inorganic compounds Chemical class 0.000 description 1
- 229910010272 inorganic material Inorganic materials 0.000 description 1
- 239000010954 inorganic particle Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000003475 lamination Methods 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000012764 mineral filler Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 230000006911 nucleation Effects 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 239000011846 petroleum-based material Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 239000011118 polyvinyl acetate Substances 0.000 description 1
- 229920002689 polyvinyl acetate Polymers 0.000 description 1
- 229940088417 precipitated calcium carbonate Drugs 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 238000004537 pulping Methods 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- WXMKPNITSTVMEF-UHFFFAOYSA-M sodium benzoate Chemical compound [Na+].[O-]C(=O)C1=CC=CC=C1 WXMKPNITSTVMEF-UHFFFAOYSA-M 0.000 description 1
- 239000004299 sodium benzoate Substances 0.000 description 1
- 235000010234 sodium benzoate Nutrition 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000011115 styrene butadiene Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 229920002725 thermoplastic elastomer Polymers 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- 238000012546 transfer 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
- D21H19/00—Coated paper; Coating material
- D21H19/80—Paper comprising more than one coating
- D21H19/82—Paper comprising more than one coating superposed
-
- 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
- D21H19/10—Coatings without pigments
- D21H19/14—Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12
- D21H19/24—Coatings without pigments applied in a form other than the aqueous solution defined in group D21H19/12 comprising macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
- D21H19/28—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
- 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
- D21H19/56—Macromolecular organic compounds or oligomers thereof 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
- D21H27/00—Special paper not otherwise provided for, e.g. made by multi-step processes
- D21H27/10—Packing paper
Definitions
- the present invention relates to a sheet-like product and to a method for its manufacture according to preambles of the enclosed independent claims.
- Cellulosic fibre based materials such as paper and board, are conventionally used for packaging various goods, including foodstuffs and beverages, as well as for disposable articles, such as cups, tableware and the like.
- the use of cellulosic fibre based materials is increasing, as there is a general desire to decrease or completely replace fossil fuel based plastics in packaging applications.
- the need to find sustainable and renewable packaging solutions is expanding the use of paper and board even to new areas, as the businesses and consumers become more aware about sustainability and environmental impact of the product packaging.
- Coating layers and/or surface size layers are applied on the surface of the paper and board in order to produce protective barrier layers, for example, against grease, water, water vapour, oxygen, aroma and/or mineral oil.
- protective barrier layers for example, against grease, water, water vapour, oxygen, aroma and/or mineral oil.
- Many of the conventional barrier layers are applied to the surface by extrusion or glue lamination, and they usually comprise one or more polymers which form a protective film on the surface of the paper or board, and prevents the interaction between the packaged goods and the environment.
- Crystalline polymers i.e. polymers with a high degree of crystallinity
- Crystalline polymers are generally known to be harder and more brittle than semi-crystalline or non-crystalline amorphous polymers.
- Surface layers comprising hard and brittle polymers easily break during folding, creasing and other converting steps, when the coated cellulosic substrate is formed into a final product. The damage caused to the surface layer during such converting steps will make the surface layer leak and reduce its barrier properties, as the layer will be easily penetrated by the grease, water, oxygen, etc.
- the higher degree of crystallinity usually also increases the film forming and melting temperature of the polymer, which makes their processability more demanding.
- polymers with a low degree of crystallinity would be advantageous in surface treatment of paper, board or the like.
- a low degree of crystallinity is, however, known to reduce the barrier properties of the final coating or surface sizing layer.
- use of amorphous polymers can make surface layers tacky, which easily leads to contamination of the processing equipment, such as leading rolls, fabrics and other machine elements.
- Amorphous polymers with low melting temperatures may also increase undesired blocking tendency of the coated paper or board, i.e. they cause unwanted sticking of the material to itself during winding and storage.
- biobased and/or biodegradable components there is an increasing trend and desire to use biobased and/or biodegradable components in manufacture of various products. This trend applies also to materials which are used for packaging of goods, especially with growing desired to reduce petroleum-based materials and the awareness of microplastics and their harmful effects to living organisms.
- suitable biobased and/or biodegradable polymers show a low degree of crystallinity, increasing the blocking tendency of the coated paper.
- the object of the present invention is to minimize or even eliminate the problems existing in the prior art.
- One non-limiting object of the present invention is to provide a sheet-like product which has good barrier properties, and which is easy to produce and process, even when a biobased and/or biodegradable polymer is used for providing at least one coating layer.
- a further non-limiting object of the present invention is to provide a method for manufacturing a coated sheet-like product without problems associated with surface layer tackiness.
- a typical sheet-like product according to the present invention such as paper, board or the like, comprises
- a substrate comprising cellulosic fibres and having a first large surface, wherein at least a first coating layer and a second coating layer are applied on the first large surface of the substrate by curtain coating to form a barrier coating, the second coating layer forming the surface of the sheet-like product,
- the first coating layer comprising a first polymer having a first crystallization degree and a first melting point
- the second coating layer comprising a second polymer having a second crystallization degree and a second melting point
- the first polymer is a biobased and/or biodegradable polymer
- the second crystallization degree and/or the second melting point of the second polymer is higher than the first crystallization degree and/or the first melting point of the first polymer
- a typical method according to the present invention for making a sheet-like product according to the invention comprises
- a barrier coating comprising at least a first coating layer and a second coating layer on a first large surface of a substrate comprising cellulosic fibres, such as paper, board or the like, by applying the first coating layer and the second coating layer simultaneously by curtain coating on the first large surface of the substrate, without an intermediate drying between the first coating layer and the second coating layer
- the first coating layer comprises a biobased and/or biodegradable first polymer which is a biobased and/or biodegradable polymer having a first crystallization degree and a first melting point
- the second coating layer comprises a second polymer having a second crystallization degree and a second melting point, which second crystallization degree and/or the second melting point is higher than the first crystallization degree and/or the first melting point of the first polymer, the second coating layer forming the surface of the sheet-like product, and
- the second coating layer which forms the surface of the coated product, has a higher crystallization degree and/or melting point temperature than the biobased and/or biodegradable first polymer of the coating layer underneath.
- the first polymer which is a biobased and/or biodegradable polymer with a lower crystallization degree and/or melting point, can be protected by a second coating layer, while it provides the first layer with the desired elasticity for the barrier coating.
- biobased polymer denotes a polymer which is produced from renewable nature derived raw materials directly or using mass- balance approach, excluding petroleum based raw materials.
- Biobased polymers comprise polymers derived from polysaccharides, such as sugar-based biopolymers, starch-based biopolymers, and cellulose-based biopolymers; polymers derived from proteins or lipids, as well as polymers obtained from microbiologically produced material, such as polyesters.
- Biobased polymers suitable for use in the present invention are preferable biodegradable.
- biodegradable polymer encompasses both biobased polymers and petroleum-based polymers as long as they are degradable by biological activity, e.g. by microorganisms, such as bacteria, fungi, algae, and/or enzymes, with the degradation accompanied by a lowering of the molar mass of the original polymer.
- the degradation products are non-toxic and environmentally acceptable, usually carbon dioxide, water and inorganic compounds.
- biodegradable polymers in the present context are compostable.
- crystallization degree is understood as the ratio between crystalline and amorphous parts of the polymer.
- crystallization degree can be determined by using differential scanning calorimetry (DCS), according to standard ISO 11357-1 :2016.
- the first polymer may be selected from biobased and/or biodegradable polyesters, such as polybutylene succinate, poly(butylene succinate-co-adipate), polyhydroxyalkanoates, polycaprolactones, polylactides, any of their mixtures and their copolymers.
- the first polymer may also be a copolymer of two or more said polyesters, or a mixture of two or more said polyesters.
- the first polymer may be a polyhydroxyalkanoate, such as polyhydroxybutyrate, polyhydroxyvalerate, polyhydroxyhexanoate or any of their copolymers.
- the first polymer may have a melting point in a range of 50 - 120 °C, preferably 60 - 110 °C.
- the melting point can be determined by using differential scanning calorimetry (DCS), according to standard ISO 11357-1 :2016.
- DCS differential scanning calorimetry
- the melting point of the first polymer provides optimal flexibility for the barrier layer and minimises the risk of leakage through cracking of the barrier layer.
- the first polymer may have a glass transition temperature T g ⁇ 0 °C, for example in a range from -40 °C to 0 °C.
- the glass transition temperature of the first polymer is lower than the first melting point temperature.
- the glass transition temperature can be determined by using differential scanning calorimetry (DCS), according to standard ISO 11357-1 :2016.
- the second polymer may be a thermoplastic elastomer.
- the second polymer may preferably be selected from a group comprising polyesters, such as polybutylene succinate, poly(butylene succinate-co-adipate), polyhydroxyalkanoates, polylactide or polycaprolactone; polyethyleneterephtalate; polyolefins, such as polyethylene or polypropylene; styrene acrylate copolymers; styrene butadiene copolymers; ethylene acrylic and methacrylic acid copolymers; poly(glycolic acid); butyl vinyl alcohol, polyvinyl alcohol; ethylene vinyl acetate and chitosane.
- polyesters such as polybutylene succinate, poly(butylene succinate-co-adipate), polyhydroxyalkanoates, polylactide or polycaprolactone
- polyethyleneterephtalate such as polyethylene or polypropylene
- styrene acrylate copolymers such as polyethylene or polypropylene
- the second polymer may be selected from biobased and/or biodegradable polyesters, such as polybutylene succinate, poly(butylene succinate-co-adipate), polyhydroxyalkanoate, polycaprolactone or polylactide.
- the second polymer may also be a copolymer of two or more said polyesters, or a mixture of two or more said polyesters.
- the second polymer may be a polyhydroxyalkanoate, such as polyhydroxybutyrate, polyhydroxyvalerate, polyhydroxyhexanoate or any of their copolymers.
- the second polymer may have a melting point in a range of 120 - 180 °C, preferably 80 - 170 °C or 80 - 140 °C.
- the melting point of the second polymer provides the coating with required flexibility while minimising the risk of blocking.
- the melting point of the second polymer also enables secure heat sealing of the sheet-like product, e.g. for manufacture of packages, hot and/or cold cups and the like.
- the second polymer may have a glass transition temperature T g >20 °C, for example in a range from 20 °C to 100 °C , preferably from 20 °C to 40 °C.
- the glass transition temperature of the second polymer is lower than the second melting point temperature.
- the glass transition temperature can be determined by using differential scanning calorimetry (DCS), according to standard ISO 11357-1 :2016.
- the first polymer and the second polymer may be different from each other.
- the second polymer may be a non-biodegradable and/or non-biobased polymer.
- the first polymer and second polymer are both biobased and/or biodegradable polymers. In this manner it is possible to maximize the amount of biobased and/or biodegradable polymer the barrier coating.
- the first polymer and second polymer may both be biobased and/or biodegradable polymers and they may be formed from same structural monomer units, as long as the second crystallization degree and/or the second melting point of the second polymer are higher than the first crystallization degree and/or the first melting point of the first polymer.
- Use of first and second polymer formed from same structural monomers units decreases the risk of repulsion and delamination between the different coating layers.
- the crystallization degree of the second polymer is higher than the crystallization degree of the first polymer.
- the second coating layer may comprise a crystallization promoter.
- the crystallization promoter may be finely- divided inorganic particle, such as mica or talc, or an organic salt, such as sodium benzoate.
- the crystallization promoter may provide effective nucleation and increase crystallization speed in the second coating layer during drying. Furthermore, use of crystallization promoter may generally improve the crystallization process in the second coating layer and reduce the operating challenges.
- the coating layer preferably comprises a crystallization promoter.
- the first coating layer and/or the second coating layer may further comprise inorganic mineral particles.
- the inorganic mineral particles may be selected from kaolin, talc, mica, calcium carbonate or any mixture thereof. Inorganic mineral particles may improve the barrier properties achieved.
- the first coating layer and/or the second coating layer may comprise ⁇ 50 weight-%, preferably ⁇ 25 weight-%, of inorganic mineral particles.
- the first coating layer and/or the second coating layer may comprise inorganic mineral particles in amount of 5 - 50 weight- %, preferably 10 - 25 weight-%, calculated from the dry weight of the coating layer.
- the first coating layer and/or second coating layer comprising inorganic mineral particles may be in form of an aqueous dispersion having solids content of 20 - 65 weight-%, preferably 30 - 60 weight-%, at the time of application.
- the amount of inorganic mineral particles in the first coating layer is higher than the amount of inorganic mineral particles in the second coating layer.
- the second coating layer is free of inorganic mineral particles.
- barrier coating with at least a first coating layer and a second coating layer that provides a barrier layer for grease, water, water vapour transmission, oxygen transmission, aroma and/or mineral oil.
- the sheet-like product is especially suitable for use in food and beverage packaging.
- the substrate for the sheet-like product comprises cellulosic fibres.
- the cellulosic fibres may be fibres obtained by chemical or mechanical pulping, or recycled fibres, or any mixture thereof.
- the substrate may be paper, board or the like.
- the substrate is usually in form of a moving cellulosic web, having a first large surface and a second large surface, which are parallel with each other.
- the substrate may have a basis weight or grammage from 40 g/m 2 to 550 g/m 2 , preferably from 80 g/m 2 to 450 g/m 2 .
- the substrate may have a basis weight or grammage from 175 g/m 2 to 400 g/m 2 , more preferably from 175 g/m 2 to 350 g/m 2 .
- the substrate may have a basis weight from 40 g/m 2 to 200 g/m 2 , preferably from 60 g/m 2 to 120 g/m 2 .
- At least a first coating layer and a second coating layer are applied simultaneously by curtain coating on the first large surface of the substrate, without an intermediate drying between the first coating layer and the second coating layer.
- the first and the second coating layer can be applied as aqueous dispersions or aqueous emulsions comprising the respective polymer.
- the coating layers are applied simultaneously from different, separate, slots. The laminar flows of the coating compositions from the different coating slots enable immiscibility of the applied coating layers.
- the first coating layer and the second coating layer are subjected to impingement drying with hot air for increasing the temperature of the second coating layer over the second melting point.
- the impingement drying with hot air ensures that the water is removed from the coating layers by heat transfer, which takes place from the outside inwards and the outer surface of second coating layer will be in direct contact with the hot drying air. This enables the formation of a temperature gradient through the coating layer.
- the second polymer in the second coating layer preferably rapidly reaches its melting point temperature for film forming. When the temperature of the second coating layer reaches the melting point of the second polymer, the temperature of the first layer may have at least partially increased over the melting point of the first polymer, as it is lower than the melting point of the second polymer.
- the more slowly crystallizing first polymer in the first coating layer will eventually reach its film forming temperature, without disturbing the process by its tackiness, since the first coating layer is protected by the second coating layer with the faster crystallizing second polymer, providing a non-tacky outer surface for the applied barrier coating.
- the temperature of the hot air in impingement drying may be at least 300 °C, preferably at least 400 °C, even more preferably at least 425 °C. High air temperatures in the impingement drying ensure fast crystallization of the second layer and minimize the risks for process problems caused by tacky coating surface.
- the temperature of the hot air in impingement drying may be adjusted according to the travel speed of the web to be coated. The higher the travel speed, the higher the temperature of the hot air should be in order to guarantee that the temperature of the second coating layer is increased over the second melting point.
- the second coating layer forms the surface of the sheet-like product.
- the crystallization degree of the second polymer is higher than the crystallization degree of the first polymer. In this manner it is possible to ensure that the surface of coated web does not contaminate process equipment during further processing.
- the sheet-like product may comprise two or more first coating layers. It is possible to apply more than one first coating layers simultaneously by curtain coating.
- the first polymers in the two or more first coating layers may be different from each other, or identical to each other, but each first polymer has first crystallization degree and/or first melting point, which is lower than the second crystallization degree and/or the second melting point of the second polymer in the second coating layer.
- the first coating layer preferably has a higher coat weight than the second coating layer.
- the first coating layer may have a coat weight >3 g/m 2 , preferably >5 g/m 2 .
- the first coating layer may have the coat weight in a range of 3 - 15 g/m 2 , preferably 5 - 12 g/m 2 , more preferably 5 - 10 g/m 2 . It is possible to apply a relatively thick first coating layer, as it is protected by the second coating layer.
- the second coating layer may have a coat weight ⁇ 6 g/m 2 , preferably ⁇ 5 g/m 2 or ⁇ 3 g/m 2 .
- the second coating layer may have the coat weight in a range of 0.5 - 6 g/m 2 , preferably 1 - 5 g/m 2 , more preferably 1 - 3 g/m 2 .
- the coat weight of the second coating layer is preferably as thin as possible to enable a fast film forming and crystallization, while still enabling a formation of a uniform coating layer on top of the first coating layer.
- the sheet-like product may comprise at least one precoat layer arranged between the surface of the substrate and the first coating layer of the barrier coating. This means that at least one precoat layer is applied on the surface of the substrate before forming the barrier coating.
- the precoat layer(s) reduce(s) the penetration of the first coating material into the cellulosic fibre web by sealing or closing the web surface and improves the coating hold-out.
- the precoat layer(s) may be applied by any conventional coating technique used in manufacture of paper and board. According to one preferable embodiment the precoat layer(s) may be applied by using a size press, a metered size press, a rod or blade coater. After the application the precoat layer(s) is/are preferably dried before the application of the first and the second coating layer. The drying may be performed by using an air dryer, infrared dryer, cylinder dryers or any combination of these.
- the precoat layer or one of the precoat layers may comprise a film forming natural or synthetic polymer, such as starch; a cellulose derivative, such as carboxymethyl cellulose or hydroxyethyl cellulose; and/or polyvinyl alcohol.
- the precoat layer may be thin, while it still effectively closes the surface of the substrate.
- the coat weight of the precoat layer may be ⁇ 5 g/m 2 , preferably ⁇ 4 g/m 2 or ⁇ 3 g/m 2 .
- the coat weight of the precoat layer may be in a range of 0.3 - 15.0 g/m 2 , preferably 0.3 - 5.0 g/m 2 , more preferably 0.5 - 4 g/m 2 , even more preferably 0.5 - 3.0 g/m 2 or 1 .0 - 2.0 g/m 2 .
- the precoat layer or one of the precoat layers may comprise inorganic mineral particles.
- the inorganic mineral particles may be selected from calcium carbonates, clay, talc, mica, kaolin or titanium dioxide. More preferably, the inorganic mineral filler particles may be selected from kaolin, talc, mica, calcium carbonates, such as ground calcium carbonate or precipitated calcium carbonate, or any mixture thereof.
- the precoat layer comprises further a binder, which binds the inorganic mineral particles to the precoat layer and to the substrate surface.
- the binder may be a synthetic polymer latex, such as styrene acrylate latex, styrene butadiene latex or polyvinyl acetate latex; polyvinyl alcohol; starch; or carboxymethyl cellulose.
- the precoat layer may have a coat weight ⁇ 30 g/m 2 , preferably ⁇ 20 g/m 2 , more preferably ⁇ 15 g/m 2 .
- the precoat layer comprising inorganic mineral particles may have a coat weight in a range of 4 - 30 g/m 2 , even more preferably 4 - 20 g/m 2 , more preferably 5 - 15 g/m 2 .
- the substrate is subjected to calendering after application of precoat layer.
- Calendering after application of the precoat improves the sealing and closure of the substrate surface by mechanically pressing the precoat layer at least partially within the substrate. Calendering reduces the porosity and improve the smoothness of the precoated substrate surface.
- Any suitable calendering unit may be used. Typical calendering units suitable for this purpose are heated or unheated, single or multinip, calenders with hard or soft rolls, shoe nip or metal belt calenders.
- one or more intermediate layers are arranged between the first coating layer and the second coating layer.
- the optional intermediate layers are applied simultaneously with the first coating layer and the second coating layer by curtain coating without any intermediate drying.
- the intermediate layer(s) may provide the formed coating with further functional properties, and/or improve its barrier properties.
- the second coating layer is arranged directly on the first coating layer without any intermediate layers.
- the cooling unit cools the coated web before winding into the jumbo reel.
- An appropriate reaction time should, however, be allowed between the impingement drying and the cooling unit, in order to allow desired film forming and crystallization in the coated layers, especially in the first coating layer.
- the cooling unit reduces the blocking risk during winding and the following storage.
- the method according to present invention is suitable for both on-line and off-line application.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Laminated Bodies (AREA)
Abstract
The invention relates to a sheet-like product, such as paper, board or the like, which comprises a substrate comprising cellulosic fibres and having a first large surface, wherein at least a first coating layer and a second coating layer are applied on the first large surface of the substrate by curtain coating to form a barrier coating. The second coating layer forms the surface of the sheet-like product. The first coating layer comprises a first polymer having a first crystallization degree and a first melting point, and the second coating layer comprises a second polymer having a second crystallization degree and a second melting point. The second crystallization degree and/or the second melting point is higher than the first crystallization degree and/or the first melting point of the first polymer.
Description
SHEET-LIKE PRODUCT AND METHOD FOR ITS MANUFACTURE
The present invention relates to a sheet-like product and to a method for its manufacture according to preambles of the enclosed independent claims.
Cellulosic fibre based materials, such as paper and board, are conventionally used for packaging various goods, including foodstuffs and beverages, as well as for disposable articles, such as cups, tableware and the like. The use of cellulosic fibre based materials is increasing, as there is a general desire to decrease or completely replace fossil fuel based plastics in packaging applications. The need to find sustainable and renewable packaging solutions is expanding the use of paper and board even to new areas, as the businesses and consumers become more aware about sustainability and environmental impact of the product packaging.
It is common to surface-treat paper and board in order to improve their barrier properties and to make them more suitable for various packaging applications. Coating layers and/or surface size layers are applied on the surface of the paper and board in order to produce protective barrier layers, for example, against grease, water, water vapour, oxygen, aroma and/or mineral oil. Many of the conventional barrier layers are applied to the surface by extrusion or glue lamination, and they usually comprise one or more polymers which form a protective film on the surface of the paper or board, and prevents the interaction between the packaged goods and the environment.
Polymers, which are used for surface treatment of paper and board, have different degrees of crystallinity. Crystalline polymers, i.e. polymers with a high degree of crystallinity, are generally known to be harder and more brittle than semi-crystalline or non-crystalline amorphous polymers. Surface layers comprising hard and brittle polymers easily break during folding, creasing and other converting steps, when the coated cellulosic substrate is formed into a final product. The damage caused to the surface layer during such converting steps will make the surface layer leak and reduce its barrier properties, as the layer will be easily penetrated by the grease, water, oxygen, etc. The higher degree of crystallinity usually also increases the film
forming and melting temperature of the polymer, which makes their processability more demanding. For these reasons, it would appear that the use of polymers with a low degree of crystallinity would be advantageous in surface treatment of paper, board or the like. A low degree of crystallinity is, however, known to reduce the barrier properties of the final coating or surface sizing layer. Furthermore, use of amorphous polymers can make surface layers tacky, which easily leads to contamination of the processing equipment, such as leading rolls, fabrics and other machine elements. Amorphous polymers with low melting temperatures may also increase undesired blocking tendency of the coated paper or board, i.e. they cause unwanted sticking of the material to itself during winding and storage.
There is an increasing trend and desire to use biobased and/or biodegradable components in manufacture of various products. This trend applies also to materials which are used for packaging of goods, especially with growing desired to reduce petroleum-based materials and the awareness of microplastics and their harmful effects to living organisms. Unfortunately, many of the suitable biobased and/or biodegradable polymers show a low degree of crystallinity, increasing the blocking tendency of the coated paper.
There is a need to increase the use of biobased and/or biodegradable polymers as well as overcome the problems associated with the different crystallisation degrees of the used polymers. On one hand, it is desired that the polymer will provide the surface layer with desired barrier properties, on the other hand it is desired that the polymer will not cause process problems, such as contamination of the equipment.
The object of the present invention is to minimize or even eliminate the problems existing in the prior art.
One non-limiting object of the present invention is to provide a sheet-like product which has good barrier properties, and which is easy to produce and process, even when a biobased and/or biodegradable polymer is used for providing at least one coating layer.
A further non-limiting object of the present invention is to provide a method for manufacturing a coated sheet-like product without problems associated with surface layer tackiness.
These objects are attained with the invention having the characteristics presented below in the characterising part of the independent claims. Some preferable embodiments are disclosed in the dependent claims.
The embodiments mentioned in this text relate, where applicable, to all aspects of the invention, even if this is not always separately mentioned.
A typical sheet-like product according to the present invention, such as paper, board or the like, comprises
- a substrate comprising cellulosic fibres and having a first large surface, wherein at least a first coating layer and a second coating layer are applied on the first large surface of the substrate by curtain coating to form a barrier coating, the second coating layer forming the surface of the sheet-like product,
- the first coating layer comprising a first polymer having a first crystallization degree and a first melting point, and
- the second coating layer comprising a second polymer having a second crystallization degree and a second melting point, wherein the first polymer is a biobased and/or biodegradable polymer, and wherein the second crystallization degree and/or the second melting point of the second polymer is higher than the first crystallization degree and/or the first melting point of the first polymer.
A typical method according to the present invention for making a sheet-like product according to the invention comprises
- forming a barrier coating comprising at least a first coating layer and a second coating layer on a first large surface of a substrate comprising cellulosic fibres, such as paper, board or the like, by applying the first coating layer and the second coating layer simultaneously by curtain coating on the first large surface of the substrate, without an intermediate drying between the first coating layer and the second
coating layer, wherein the first coating layer comprises a biobased and/or biodegradable first polymer which is a biobased and/or biodegradable polymer having a first crystallization degree and a first melting point, and the second coating layer comprises a second polymer having a second crystallization degree and a second melting point, which second crystallization degree and/or the second melting point is higher than the first crystallization degree and/or the first melting point of the first polymer, the second coating layer forming the surface of the sheet-like product, and
- subjecting the formed barrier coating to impingement drying with hot air for increasing the temperature of the second coating layer over the second melting point.
Now it has been surprisingly found that it is possible to circumvent the problems associated with tackiness of the biobased and/or biodegradable polymers and to obtain good barrier properties by simultaneous application of two or more coating layers by curtain coating, where the second coating layer, which forms the surface of the coated product, has a higher crystallization degree and/or melting point temperature than the biobased and/or biodegradable first polymer of the coating layer underneath. It was unexpectedly realised that the first polymer, which is a biobased and/or biodegradable polymer with a lower crystallization degree and/or melting point, can be protected by a second coating layer, while it provides the first layer with the desired elasticity for the barrier coating. In this way it is possible to form a barrier coating that has good barrier properties, is not brittle, and does not contaminate the machine parts. At the same time it is also possible to increase the amount of biobased/biodegradable constituents in the barrier coating and make the barrier coating more sustainable.
In the present context the term “biobased polymer” denotes a polymer which is produced from renewable nature derived raw materials directly or using mass- balance approach, excluding petroleum based raw materials. Biobased polymers comprise polymers derived from polysaccharides, such as sugar-based biopolymers, starch-based biopolymers, and cellulose-based biopolymers; polymers derived from proteins or lipids, as well as polymers obtained from
microbiologically produced material, such as polyesters. Biobased polymers suitable for use in the present invention are preferable biodegradable.
In the present context the term “biodegradable polymer” encompasses both biobased polymers and petroleum-based polymers as long as they are degradable by biological activity, e.g. by microorganisms, such as bacteria, fungi, algae, and/or enzymes, with the degradation accompanied by a lowering of the molar mass of the original polymer. The degradation products are non-toxic and environmentally acceptable, usually carbon dioxide, water and inorganic compounds. Preferably biodegradable polymers in the present context are compostable.
In the present context, the crystallization degree is understood as the ratio between crystalline and amorphous parts of the polymer. For the present purposes, crystallization degree can be determined by using differential scanning calorimetry (DCS), according to standard ISO 11357-1 :2016.
The first polymer may be selected from biobased and/or biodegradable polyesters, such as polybutylene succinate, poly(butylene succinate-co-adipate), polyhydroxyalkanoates, polycaprolactones, polylactides, any of their mixtures and their copolymers. The first polymer may also be a copolymer of two or more said polyesters, or a mixture of two or more said polyesters. According to one preferable embodiment, the first polymer may be a polyhydroxyalkanoate, such as polyhydroxybutyrate, polyhydroxyvalerate, polyhydroxyhexanoate or any of their copolymers.
The first polymer may have a melting point in a range of 50 - 120 °C, preferably 60 - 110 °C. The melting point can be determined by using differential scanning calorimetry (DCS), according to standard ISO 11357-1 :2016. The melting point of the first polymer provides optimal flexibility for the barrier layer and minimises the risk of leakage through cracking of the barrier layer.
The first polymer may have a glass transition temperature Tg <0 °C, for example in a range from -40 °C to 0 °C. The glass transition temperature of the first polymer is
lower than the first melting point temperature. The glass transition temperature can be determined by using differential scanning calorimetry (DCS), according to standard ISO 11357-1 :2016.
The second polymer may be a thermoplastic elastomer.
The second polymer may preferably be selected from a group comprising polyesters, such as polybutylene succinate, poly(butylene succinate-co-adipate), polyhydroxyalkanoates, polylactide or polycaprolactone; polyethyleneterephtalate; polyolefins, such as polyethylene or polypropylene; styrene acrylate copolymers; styrene butadiene copolymers; ethylene acrylic and methacrylic acid copolymers; poly(glycolic acid); butyl vinyl alcohol, polyvinyl alcohol; ethylene vinyl acetate and chitosane. According to one preferable embodiment, the second polymer may be selected from biobased and/or biodegradable polyesters, such as polybutylene succinate, poly(butylene succinate-co-adipate), polyhydroxyalkanoate, polycaprolactone or polylactide. The second polymer may also be a copolymer of two or more said polyesters, or a mixture of two or more said polyesters. According to one preferable embodiment the second polymer may be a polyhydroxyalkanoate, such as polyhydroxybutyrate, polyhydroxyvalerate, polyhydroxyhexanoate or any of their copolymers.
The second polymer may have a melting point in a range of 120 - 180 °C, preferably 80 - 170 °C or 80 - 140 °C. The melting point of the second polymer provides the coating with required flexibility while minimising the risk of blocking. The melting point of the second polymer also enables secure heat sealing of the sheet-like product, e.g. for manufacture of packages, hot and/or cold cups and the like.
The second polymer may have a glass transition temperature Tg >20 °C, for example in a range from 20 °C to 100 °C , preferably from 20 °C to 40 °C. The glass transition temperature of the second polymer is lower than the second melting point temperature. The glass transition temperature can be determined by using differential scanning calorimetry (DCS), according to standard ISO 11357-1 :2016.
The first polymer and the second polymer may be different from each other. For example, the second polymer may be a non-biodegradable and/or non-biobased polymer.
According to one embodiment, the first polymer and second polymer are both biobased and/or biodegradable polymers. In this manner it is possible to maximize the amount of biobased and/or biodegradable polymer the barrier coating. According to one preferable embodiment, the first polymer and second polymer may both be biobased and/or biodegradable polymers and they may be formed from same structural monomer units, as long as the second crystallization degree and/or the second melting point of the second polymer are higher than the first crystallization degree and/or the first melting point of the first polymer. Use of first and second polymer formed from same structural monomers units decreases the risk of repulsion and delamination between the different coating layers.
According to one preferable embodiment of the invention the crystallization degree of the second polymer is higher than the crystallization degree of the first polymer.
According to one embodiment of the invention the second coating layer may comprise a crystallization promoter. The crystallization promoter may be finely- divided inorganic particle, such as mica or talc, or an organic salt, such as sodium benzoate. The crystallization promoter may provide effective nucleation and increase crystallization speed in the second coating layer during drying. Furthermore, use of crystallization promoter may generally improve the crystallization process in the second coating layer and reduce the operating challenges. Especially, when the second coating layer comprises a biobased and/or biodegradable polymer, the coating layer preferably comprises a crystallization promoter.
The first coating layer and/or the second coating layer may further comprise inorganic mineral particles. The inorganic mineral particles may be selected from kaolin, talc, mica, calcium carbonate or any mixture thereof. Inorganic mineral particles may improve the barrier properties achieved. The first coating layer and/or
the second coating layer may comprise <50 weight-%, preferably <25 weight-%, of inorganic mineral particles. For example, the first coating layer and/or the second coating layer may comprise inorganic mineral particles in amount of 5 - 50 weight- %, preferably 10 - 25 weight-%, calculated from the dry weight of the coating layer. The first coating layer and/or second coating layer comprising inorganic mineral particles may be in form of an aqueous dispersion having solids content of 20 - 65 weight-%, preferably 30 - 60 weight-%, at the time of application. Preferably, the amount of inorganic mineral particles in the first coating layer is higher than the amount of inorganic mineral particles in the second coating layer. According to one preferable embodiment, the second coating layer is free of inorganic mineral particles.
According to the present invention it is thus possible to form barrier coating with at least a first coating layer and a second coating layer that provides a barrier layer for grease, water, water vapour transmission, oxygen transmission, aroma and/or mineral oil. The sheet-like product is especially suitable for use in food and beverage packaging.
In the present context the substrate for the sheet-like product comprises cellulosic fibres. The cellulosic fibres may be fibres obtained by chemical or mechanical pulping, or recycled fibres, or any mixture thereof. The substrate may be paper, board or the like. At the time of application of the first and the second coating layer, the substrate is usually in form of a moving cellulosic web, having a first large surface and a second large surface, which are parallel with each other. The substrate may have a basis weight or grammage from 40 g/m2 to 550 g/m2, preferably from 80 g/m2 to 450 g/m2. According to one preferable embodiment the substrate may have a basis weight or grammage from 175 g/m2 to 400 g/m2, more preferably from 175 g/m2 to 350 g/m2. According to another preferable embodiment the substrate may have a basis weight from 40 g/m2 to 200 g/m2, preferably from 60 g/m2 to 120 g/m2.
According to the present invention at least a first coating layer and a second coating layer are applied simultaneously by curtain coating on the first large surface of the
substrate, without an intermediate drying between the first coating layer and the second coating layer. The first and the second coating layer can be applied as aqueous dispersions or aqueous emulsions comprising the respective polymer. The coating layers are applied simultaneously from different, separate, slots. The laminar flows of the coating compositions from the different coating slots enable immiscibility of the applied coating layers.
The first coating layer and the second coating layer are subjected to impingement drying with hot air for increasing the temperature of the second coating layer over the second melting point. The impingement drying with hot air ensures that the water is removed from the coating layers by heat transfer, which takes place from the outside inwards and the outer surface of second coating layer will be in direct contact with the hot drying air. This enables the formation of a temperature gradient through the coating layer. The second polymer in the second coating layer preferably rapidly reaches its melting point temperature for film forming. When the temperature of the second coating layer reaches the melting point of the second polymer, the temperature of the first layer may have at least partially increased over the melting point of the first polymer, as it is lower than the melting point of the second polymer. The more slowly crystallizing first polymer in the first coating layer will eventually reach its film forming temperature, without disturbing the process by its tackiness, since the first coating layer is protected by the second coating layer with the faster crystallizing second polymer, providing a non-tacky outer surface for the applied barrier coating.
According to one preferable embodiment the temperature of the hot air in impingement drying may be at least 300 °C, preferably at least 400 °C, even more preferably at least 425 °C. High air temperatures in the impingement drying ensure fast crystallization of the second layer and minimize the risks for process problems caused by tacky coating surface.
The temperature of the hot air in impingement drying may be adjusted according to the travel speed of the web to be coated. The higher the travel speed, the higher the
temperature of the hot air should be in order to guarantee that the temperature of the second coating layer is increased over the second melting point.
As noted above, the second coating layer forms the surface of the sheet-like product. In this manner it is possible to avoid any problems that might be caused by tackiness of the first polymer in the first coating layer. According to one preferable embodiment the crystallization degree of the second polymer is higher than the crystallization degree of the first polymer. In this manner it is possible to ensure that the surface of coated web does not contaminate process equipment during further processing.
The sheet-like product may comprise two or more first coating layers. It is possible to apply more than one first coating layers simultaneously by curtain coating. The first polymers in the two or more first coating layers may be different from each other, or identical to each other, but each first polymer has first crystallization degree and/or first melting point, which is lower than the second crystallization degree and/or the second melting point of the second polymer in the second coating layer.
The first coating layer preferably has a higher coat weight than the second coating layer. According to one embodiment the first coating layer may have a coat weight >3 g/m2, preferably >5 g/m2. The first coating layer may have the coat weight in a range of 3 - 15 g/m2, preferably 5 - 12 g/m2, more preferably 5 - 10 g/m2. It is possible to apply a relatively thick first coating layer, as it is protected by the second coating layer. The second coating layer may have a coat weight <6 g/m2, preferably <5 g/m2 or <3 g/m2. The second coating layer may have the coat weight in a range of 0.5 - 6 g/m2, preferably 1 - 5 g/m2, more preferably 1 - 3 g/m2. The coat weight of the second coating layer is preferably as thin as possible to enable a fast film forming and crystallization, while still enabling a formation of a uniform coating layer on top of the first coating layer.
The sheet-like product may comprise at least one precoat layer arranged between the surface of the substrate and the first coating layer of the barrier coating. This means that at least one precoat layer is applied on the surface of the substrate
before forming the barrier coating. The precoat layer(s) reduce(s) the penetration of the first coating material into the cellulosic fibre web by sealing or closing the web surface and improves the coating hold-out. The precoat layer(s) may be applied by any conventional coating technique used in manufacture of paper and board. According to one preferable embodiment the precoat layer(s) may be applied by using a size press, a metered size press, a rod or blade coater. After the application the precoat layer(s) is/are preferably dried before the application of the first and the second coating layer. The drying may be performed by using an air dryer, infrared dryer, cylinder dryers or any combination of these.
According to one embodiment of the invention the precoat layer or one of the precoat layers may comprise a film forming natural or synthetic polymer, such as starch; a cellulose derivative, such as carboxymethyl cellulose or hydroxyethyl cellulose; and/or polyvinyl alcohol. The precoat layer may be thin, while it still effectively closes the surface of the substrate. The coat weight of the precoat layer may be <5 g/m2, preferably <4 g/m2 or <3 g/m2. For example, the coat weight of the precoat layer may be in a range of 0.3 - 15.0 g/m2, preferably 0.3 - 5.0 g/m2, more preferably 0.5 - 4 g/m2, even more preferably 0.5 - 3.0 g/m2 or 1 .0 - 2.0 g/m2.
According to another embodiment the precoat layer or one of the precoat layers may comprise inorganic mineral particles. The inorganic mineral particles may be selected from calcium carbonates, clay, talc, mica, kaolin or titanium dioxide. More preferably, the inorganic mineral filler particles may be selected from kaolin, talc, mica, calcium carbonates, such as ground calcium carbonate or precipitated calcium carbonate, or any mixture thereof. The precoat layer comprises further a binder, which binds the inorganic mineral particles to the precoat layer and to the substrate surface. The binder may be a synthetic polymer latex, such as styrene acrylate latex, styrene butadiene latex or polyvinyl acetate latex; polyvinyl alcohol; starch; or carboxymethyl cellulose. The precoat layer may have a coat weight <30 g/m2, preferably <20 g/m2, more preferably <15 g/m2. For example, the precoat layer comprising inorganic mineral particles may have a coat weight in a range of 4 - 30 g/m2, even more preferably 4 - 20 g/m2, more preferably 5 - 15 g/m2.
According to one embodiment the substrate is subjected to calendering after application of precoat layer. Calendering after application of the precoat improves the sealing and closure of the substrate surface by mechanically pressing the precoat layer at least partially within the substrate. Calendering reduces the porosity and improve the smoothness of the precoated substrate surface. Any suitable calendering unit may be used. Typical calendering units suitable for this purpose are heated or unheated, single or multinip, calenders with hard or soft rolls, shoe nip or metal belt calenders.
According to one embodiment, one or more intermediate layers are arranged between the first coating layer and the second coating layer. The optional intermediate layers are applied simultaneously with the first coating layer and the second coating layer by curtain coating without any intermediate drying. The intermediate layer(s) may provide the formed coating with further functional properties, and/or improve its barrier properties.
According to another embodiment the second coating layer is arranged directly on the first coating layer without any intermediate layers.
It is possible to arrange at least one cooling unit after the impingement drying. The cooling unit cools the coated web before winding into the jumbo reel. An appropriate reaction time should, however, be allowed between the impingement drying and the cooling unit, in order to allow desired film forming and crystallization in the coated layers, especially in the first coating layer. The cooling unit reduces the blocking risk during winding and the following storage.
The method according to present invention is suitable for both on-line and off-line application.
Even if the invention was described with reference to what at present seems to be the most practical and preferred embodiments, it is appreciated that the invention shall not be limited to the embodiments described above, but the invention is
intended to cover also different modifications and equivalent technical solutions within the scope of the enclosed claims.
Claims
1. A sheet-like product, such as paper, board or the like, comprising
- a substrate comprising cellulosic fibres and having a first large surface, wherein at least a first coating layer and a second coating layer are applied on the first large surface of the substrate by curtain coating to form a barrier coating, the second coating layer forming the surface of the sheet-like product,
- the first coating layer comprises a first polymer having a first crystallization degree and a first melting point, and - the second coating layer comprises a second polymer having a second crystallization degree and a second melting point, wherein the first polymer is a biobased and/or biodegradable polymer, and wherein the second crystallization degree and/or the second melting point of the second polymer is higher than the first crystallization degree and/or the first melting point of the first polymer.
2. Sheet-like product according to claim 1 , characterised in that the first polymer is selected from biodegradable polyesters, such as polybutylene succinate, poly(butylene succinate-co-adipate), polyhydroxyalkanoates, polycaprolactones, polylactides, any of their mixtures and copolymers.
3. Sheet-like product according to claim 2, characterised in that the first polymer is a polyhydroxyalkanoate, such as polyhydroxybutyrate, polyhydroxyvalerate, polyhydroxyhexanoate or any of their copolymers.
4. Sheet-like product according to any of preceding claims 1 - 3, characterised in that the crystallization degree of the second polymer is higher than the crystallization degree of the first polymer.
5. Sheet-like product according to any of preceding claims 1 - 4, characterised in that the second polymer is selected from a group comprising polyesters, such as polybutylene succinate, poly(butylene succinate-co-adipate), polyhydroxyalkanoates, polylactide or polycaprolactone; polyethyleneterephtalate;
polyolefins, such as polyethylene or polypropylene; styrene acrylate copolymers, styrene butadiene copolymers, ethylene acrylic and methacrylic acid copolymers, poly(glycolic acid); butyl vinyl alcohol; polyvinyl alcohol; ethylene vinyl acetate; and chitosane.
6. Sheet-like product according to any of preceding claims 1 - 5, characterised in that the first coating layer has a coat weight in a range of 3 - 15 g/m2, preferably 5 - 12 g/m2, more preferably 5 - 10 g/m2, and/or the second coating layer has a coat weight in a range of 0.5 - 6 g/m2, preferably 1 - 5 g/m2, more preferably 1 - 3 g/m2.
7. Sheet-like product according to any of preceding claims 1 - 6, characterised in that the sheet-like product comprises at least one precoat layer, arranged between the surface of the substrate and the first coating layer of the barrier coating.
8. Sheet-like product according to claim 7, characterised in that the precoat layer comprises a natural or synthetic polymer, such as starch; a cellulose derivative, such as carboxymethyl cellulose or hydroxyethyl cellulose; and/or polyvinyl alcohol.
9. Sheet-like product according to claim 7, characterised in that the precoat layer has a coat weight of 0.3 - 15 g/m2, preferably 0.3 - 5 g/m2, more preferably 0.5 - 4 g/m2.
10. Sheet-like product according to any of claims 7 - 9, characterised in that the precoat layer comprises inorganic mineral particles.
11. Sheet-like product according to any of claims 1 - 10, characterised in that the first coating layer and/or the second coating layer comprises inorganic mineral particles, preferably <50 weight-%, preferably <25 weight-%, of inorganic mineral particles.
12. Sheet-like product according to claim 10 or 11 characterised in that the inorganic mineral particles are selected from kaolin, talc, mica, calcium carbonate or any mixture thereof.
13. Sheet-like product according to any of preceding claims 1 - 12, characterised in that one or more intermediate layers are arranged between the first coating layer and the second coating layer.
14. Sheet-like product according to any of preceding claims 1 - 13, characterised in that the second coating layer comprises a crystallization promoter.
15. Method for making a sheet-like product according to any of claims 1 - 14, the method comprising
- forming a barrier coating comprising at least a first coating layer and a second coating layer on a first large surface of a substrate comprising cellulosic fibres, such as paper, board or the like, by applying the first coating layer and the second coating layer simultaneously by curtain coating on the first large surface of the substrate, without an intermediate drying between the first coating layer and the second coating layer, wherein the first coating layer comprises a biobased and/or biodegradable first polymer having a first crystallization degree and a first melting point, and the second coating layer comprises a second polymer having a second crystallization degree and a second melting point, which second crystallization degree and/or the second melting point is higher than the first crystallization degree and/or the first melting point of the first polymer, the second coating layer forming the surface of the sheet-like product, and
- subjecting the formed barrier coating to impingement drying with hot air for increasing the temperature of the second coating layer over the second melting point.
16. Method according to claim 15, characterised in applying at least one precoat layer on the surface of the substrate before forming the barrier coating.
17. Method according to claim 15 or 16, characterised in that the temperature of the hot air in the impingement drying is at least 300 °C, preferably at least 400 °C, even more preferably at least 425 °C.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| EP22757981.0A EP4359604A1 (en) | 2021-06-24 | 2022-06-23 | Sheet-like product and method for its manufacture |
| US18/573,092 US20240328092A1 (en) | 2021-06-24 | 2022-06-23 | Sheet-like product and method for its manufacture |
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FI20215756 | 2021-06-24 | ||
| FI20215756 | 2021-06-24 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2022269141A1 true WO2022269141A1 (en) | 2022-12-29 |
Family
ID=83005982
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/FI2022/050467 WO2022269141A1 (en) | 2021-06-24 | 2022-06-23 | Sheet-like product and method for its manufacture |
Country Status (3)
| Country | Link |
|---|---|
| US (1) | US20240328092A1 (en) |
| EP (1) | EP4359604A1 (en) |
| WO (1) | WO2022269141A1 (en) |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU761975B2 (en) * | 1997-05-23 | 2003-06-12 | Cargill Incorporated | Polylactide coated paper |
| WO2013182757A1 (en) * | 2012-06-08 | 2013-12-12 | Upm-Kymmene Corporation | A method and a system for manufacturing packaging material, as well as packaging material and a package |
| WO2014064335A1 (en) * | 2012-10-26 | 2014-05-01 | Stora Enso Oyj | A method for manufacturing biodegradable packaging material, biodegradable packaging material, and packages and containers made thereof |
-
2022
- 2022-06-23 WO PCT/FI2022/050467 patent/WO2022269141A1/en active Application Filing
- 2022-06-23 US US18/573,092 patent/US20240328092A1/en active Pending
- 2022-06-23 EP EP22757981.0A patent/EP4359604A1/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU761975B2 (en) * | 1997-05-23 | 2003-06-12 | Cargill Incorporated | Polylactide coated paper |
| WO2013182757A1 (en) * | 2012-06-08 | 2013-12-12 | Upm-Kymmene Corporation | A method and a system for manufacturing packaging material, as well as packaging material and a package |
| WO2014064335A1 (en) * | 2012-10-26 | 2014-05-01 | Stora Enso Oyj | A method for manufacturing biodegradable packaging material, biodegradable packaging material, and packages and containers made thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| EP4359604A1 (en) | 2024-05-01 |
| US20240328092A1 (en) | 2024-10-03 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP7093779B2 (en) | The method of manufacturing the packaging material and the packaging material produced by this method. | |
| US11458714B2 (en) | Heat-sealable packaging material | |
| US5654039A (en) | Recyclable and compostable coated paper stocks and related methods of manufacture | |
| JP2024519934A (en) | Coated paper for use as packaging material | |
| US11851821B2 (en) | Heat sealable paper-based substrate coated with water-based coatings, its process of manufacturing and uses thereof | |
| JP7485671B2 (en) | Repulpable packaging materials | |
| WO2022269141A1 (en) | Sheet-like product and method for its manufacture | |
| WO2021150404A1 (en) | Heat-sealable paperboard structures and methods | |
| US20240218601A1 (en) | Compostable Packaging Material | |
| TWI817592B (en) | Pulp molded, fabricating method thereof and use for containing ready-to-eat food that can be heated by oven or microwave | |
| EP4417325A1 (en) | Method for producing multilayer body | |
| SE2230443A1 (en) | A method for the manufacturing of a dispersion coated paperboard with at least two layers of pha having different cristallinity and a coated paperboard | |
| BR112020012442B1 (en) | HEAT SEALABLE PACKAGING MATERIAL | |
| AU2013226036A1 (en) | High viscosity blends and coatings of an ionomer and poly(vinyl alcohol) |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| 121 | Ep: the epo has been informed by wipo that ep was designated in this application |
Ref document number: 22757981 Country of ref document: EP Kind code of ref document: A1 |
|
| WWE | Wipo information: entry into national phase |
Ref document number: 18573092 Country of ref document: US |
|
| WWE | Wipo information: entry into national phase |
Ref document number: 2022757981 Country of ref document: EP |
|
| NENP | Non-entry into the national phase |
Ref country code: DE |
|
| ENP | Entry into the national phase |
Ref document number: 2022757981 Country of ref document: EP Effective date: 20240124 |