BARRIER-COATED CELLULOSE-BASED SUBSTRATE, LAMINATED PACKAGING MATERIAL AND PACKAGING CONTAINER COMPRISING THE CELLULOSE-BASED SUBSTRATE
20240025610 · 2024-01-25
Assignee
Inventors
Cpc classification
B32B2310/0806
PERFORMING OPERATIONS; TRANSPORTING
B32B2255/28
PERFORMING OPERATIONS; TRANSPORTING
D21H19/826
TEXTILES; PAPER
B32B27/16
PERFORMING OPERATIONS; TRANSPORTING
B32B37/24
PERFORMING OPERATIONS; TRANSPORTING
B32B7/12
PERFORMING OPERATIONS; TRANSPORTING
B65D65/42
PERFORMING OPERATIONS; TRANSPORTING
B65D65/40
PERFORMING OPERATIONS; TRANSPORTING
B32B2264/108
PERFORMING OPERATIONS; TRANSPORTING
B32B27/308
PERFORMING OPERATIONS; TRANSPORTING
B65D81/24
PERFORMING OPERATIONS; TRANSPORTING
International classification
B65D65/42
PERFORMING OPERATIONS; TRANSPORTING
B65D65/40
PERFORMING OPERATIONS; TRANSPORTING
B32B27/30
PERFORMING OPERATIONS; TRANSPORTING
B32B7/12
PERFORMING OPERATIONS; TRANSPORTING
B32B27/16
PERFORMING OPERATIONS; TRANSPORTING
B65D81/24
PERFORMING OPERATIONS; TRANSPORTING
B32B37/24
PERFORMING OPERATIONS; TRANSPORTING
Abstract
The present invention relates to a method for manufacturing a barrier-coated substrate web, coated with a layer of reduced graphene oxide. The invention further relates to laminated packaging materials comprising the barrier-coated substrate web, in particular intended for liquid carton food packaging, and to liquid carton packaging containers comprising the laminated packaging material.
Claims
1. Method for producing an oxygen barrier material for a packaging material, by coating a substrate material web with a layer of reduced graphene oxide, comprising the steps of a) providing and forwarding a substrate material web, b) providing an aqueous composition comprising graphene oxide including monolayer flakes of graphene oxide and multilayer graphene oxide platelets, having up to 20 stacked monolayer flakes of graphene oxide, c) coating the aqueous composition of graphene oxide onto the surface of the substrate material web while it is being forwarded, d) drying the wet coating of aqueous graphene oxide on the substrate material web, by forced evaporation, to obtain a first dry layer of layered graphene oxide particles or flakes, e) applying an aqueous solution of a reducing agent onto the first dry layer of graphene oxide on the substrate material web, f) directly following step e) drying the wet aqueous coating of the reducing agent, by forced evaporation, to obtain a second dry layer of reducing agent, and g) allowing the reducing agent of the second dry layer to reduce the graphene oxide of the underlying, first dry layer, during a minimum predetermined time at a minimum pre-determined temperature, to form a barrier-coated substrate material web with the dry layer of reduced graphene oxide.
2. Method according to claim 1, comprising a further step i) of coating or laminating the barrier-coated substrate material web to a further layer of a polymer, to cover the second dry layer of the reducing agent, to be performed before or after step g).
3. Method according to claim 1, comprising a further step h), of winding the coated and dried, barrier-coated substrate material web onto a reel, to be performed before or after step g).
4. Method according to claim 1, wherein the concentration of the aqueous composition of graphene oxide is from 0.1 to 15 weight %.
5. Method according to claim 1, wherein the wet coated thickness of the aqueous composition of graphene oxide is from 10 to 400 m.
6. Method according to claim 1, wherein the reducing agent is selected from the group consisting of sodium citrate, ascorbic acid (vitamin C), lemon juice, vinegar and green tea.
7. Method according to claim 1, wherein the reducing agent is ascorbic acid.
8. Method according to claim 1, wherein the concentration of the reducing agent is from 0.5 to 15 weight-%.
9. Method according to claim 1, wherein the dried, barrier-coated substrate material web from step f), before or during step g) is irradiated to accelerate the reduction reaction taking place between the applied first and second dry layers.
10. Method according to claim 1, wherein the substrate material web is continuously forwarded at a constant speed.
11. Barrier-coated substrate material web as obtained by the method of any claim 1, for use as an oxygen barrier material in a laminated packaging material for liquid food products, comprising a substrate material substrate web and applied onto it a dry layer from layered particles or flakes of reduced graphene oxide.
12. Barrier-coated substrate material web, according to claim 11, wherein the thickness of the dry layer from layered particles or flakes of reduced graphene oxide is from 50 to 1000 nm.
13. Barrier-coated substrate material web, according to claim 11, wherein the substrate material web is a polymer film web, a paper or other cellulose-based material web or a polymer-coated paper or other cellulose-based material web.
14. Barrier-coated substrate material web, according to claim 11, wherein the dry layer from layered particles or flakes of reduced graphene oxide is further coated with or laminated to an adjacent polymer layer.
15. Laminated packaging material comprising the barrier-coated substrate web as claimed in claim 11, and further comprising a first outermost protective material layer and a second innermost liquid tight, heat sealable material layer.
16. Laminated packaging material according to claim 15, further comprising a bulk layer of paper or paperboard or other cellulose-based material, a first outermost protective material layer, a second innermost liquid tight, heat sealable material layer and, arranged on the inner side of the bulk layer of paper or paperboard, between the bulk layer and the innermost layer, said barrier-coated substrate web.
17. Laminated packaging material according to claim 16, wherein the barrier-coated substrate web is bonded to the bulk layer by an intermediate bonding layer comprising a composition comprising a binder selected from the group consisting of acrylic polymers and copolymers, starch, cellulose and polysaccharide derivatives, polymers and copolymers of vinyl acetate and/or vinyl alcohol.
18. Packaging container comprising the laminated packaging material as defined in claim 15.
19. Method according to claim 1, wherein the multilayer graphene oxide platelets have 2-10 stacked monolayer flakes of graphene oxide.
Description
EXAMPLES AND DESCRIPTION OF PREFERRED EMBODIMENTS
[0097] In the following, preferred embodiments of the invention will be described with reference to the drawings, of which:
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EXAMPLES
Example 1
[0106] An aqueous dispersion of 1 weight-% of monolayer flakes of graphene oxide (pure quality, exfoliated to at least 95%, from Graphenea), was continuously stirred up to the moment of application onto a substrate. The well dispersed aqueous composition was thus applied onto a forward-moving web of paperboard pre-coated with polyethylene (liquid paperboard of 80 mN bending stiffness and a grammage of 200 g/m.sup.2) to a wet thickness of about 400 m, by means of a Hirano lab-coater. The water in the applied coating composition was evaporated off from the surface by air convection in a hot air dryer, at a web surface temperature of about 60 C. for about 1 minute. The resulting dry coating thickness of graphene oxide applied onto the PE-coated paper was measured to about 2.2 m.
[0107] The resulting substrate thus coated with a 2.2 m thin dry coating of layered graphene oxide exhibited an oxygen transmission of about 25 cc/m.sup.2, 24 h, 1 atm, 23 C./50% RH, 21% oxygen as measured by an Ox-Tran 2/21 Mocon instrument. The substrate coated with graphene oxide had a light brown colour.
[0108] The thus graphene-oxide coated web was subsequently further coated with an aqueous solution of 3 weight-% ascorbic acid, and dried again at about 60 C. surface temperature of the web during about 1 minute, cooled down to room temperature and finally wound onto a reel.
[0109] From the same coated and dried web of coated paperboard, samples were also taken to be continuously maintained at a higher surface temperature of 60 C. for 2 hours. In these samples, it was concluded that the graphene oxide at least in the surface portion of the coated graphene oxide had been completely reduced by a reduction reaction with the ascorbic acid added by the final coating after the time period at elevated temperature. The colour of the coated paperboard had changed from light brown to dark brown. The OTR was measured of these samples, in the same way as above, and found to be below 1 cc/m.sup.2, 24 h, 1 atm, 23 C./50% RH, 21% oxygen, two days later (the time it takes to condition the samples for OTR measurement). By this time, the samples had also turned completely black. The resulting dry coating thickness of the coating with this reduced graphene oxide was measured to be 530 nm, i.e. about 0.5 m. Thus the distance between the graphenic flakes had become lower by the reduction reaction of the graphene oxidic flakes, to provide the much improved barrier properties, and this reduction process thus happened within the dried coating of graphene oxide, and over time.
[0110] Consequently, by reducing the applied graphene oxide to graphene, even if only partially or at the surface of the coating, the oxygen barrier level was considerably improved to a level that is needed and desired in laminated packaging materials intended for aseptic liquid carton packaging, i.e. lower than 1 cc/m.sup.2, 24 h, 1 atm, 23 C./50% RH, 21% oxygen.
[0111] Before the 2 hours of such reduction reaction at elevated temperature, the samples did not exhibit a full reduction of the graphene oxide at the surface, indicated also by the coating colour being still light brown.
[0112] Further samples from the reel were also later taken after 1 and 2 weeks storage at ambient temperature (23 C.) and compared with the heat treated samples. After 1 week ambient storage, wound-up on the reel, the reduction reaction had progressed within the dry layer on the paper to a higher level, but still not to full reduction level. This was indicated by such samples having obtained a dark brown, almost black, colour and OTR in the order of about 10 cc/m.sup.2, 24 h, 1 atm, 23 C./50% RH, 21% oxygen.
[0113] After 2 weeks, the reduction seemed to be complete, by having obtained a black colour, as with the samples maintained at the elevated temperature for only 2 hours. This was concluded by measuring correspondingly low OTR values on samples from the reel, i.e. below 1 cc/m.sup.2, 24 h, 1 atm, 23 C./50% RH, 21% oxygen.
[0114] Accordingly, it seems that the Williams-Landel-Ferry model, or WLF for short, applies to the reduction reaction, and that the reduction reaction may be accelerated and controlled by increased temperature and/or increased reaction time. Most importantly, it seems the reduction reaction continues at the interface between the dried coatings of graphene oxide and ascorbic acid until full conversion degree, even after the drying of the coated web and after winding it up onto a reel for transport and storage.
[0115] Since a reaction time of 2 hours is barely feasible in an industrial coating and manufacturing process, this result is advantageous, because it means that the reduction to graphene in the applied coating of graphene oxide may still be continued to completion after the coating operation. It may thus be achieved merely by logistically planning for a pro-longed storage of the barrier-coated web, before further use. It is also possible to laminate the barrier-coated substrate web to further layers to form a finished packaging material, before the planned storage of the reels. In the case of lamination methods involving heat supply, such as polymer melt extrusion coating or polymer melt extrusion lamination, further acceleration of the reduction reaction may advantageously and conveniently be achieved. Further intermediate storage may be planned to take place partly also during transport, and partly before shipping and/or partly after shipping at a customer facility, depending on practical circumstances.
[0116] Further, relating to the attached figures:
[0117] In
[0118] The PET film is provided with a dry coating 12a of graphene oxide, applied by means of aqueous dispersion coating and subsequently heat dried to evaporate off the water. The dry weight of the graphene oxide coating thus applied is about 1.3 m. Further, the thus coated substrate material has a second dry coating layer 13a of ascorbic acid applied, as a 3 weight-% aqueous solution of ascorbic acid, onto the first dry coating layer of graphene oxide. The second dry coating layer 13a has also been applied as an aqueous solution coating and subsequently heat dried to evaporate off the water. The dry, thus coated substrate material web may be further heat treated for a period of time, or simply stored at ambient temperature for at least two weeks, whereafter the first dry barrier coating layer of graphene oxide has been reduced as far as possible to reduced graphene oxide, i.e. ideally to graphene. After the reduction reaction is as complete as possible, the thickness of the dry barrier coating 12a has been significantly reduced as well. Thus, in the example above, the dry graphene oxide layer had a thickness immediately after drying of about 1.3 m, while the final thickness of the reduced same graphene oxide was 300 nm, i.e. about 0.3 m. The OTR was measured to be 0,1 cc/m.sup.2, 24 h, 23 C./80% RH, 100% oxygen. If the same film substrate was coated with half the thickness on each side, i.e with 150 nm dry reduced graphene oxide on each side of the film, the OTR was instead 0,02 cc/m.sup.2, 24 h, 23 C./80% RH, 100% oxygen.
[0119] Furthermore, the robustness of the coatings of reduced graphene oxide can be illustrated by a test according to which the coated material is folded and unfolded once, twice and up to twenty times (according to a similar principle to a Flex-Gelbo test). After the first folding, the OTR increased to cc/m.sup.2, 24 h, 23 C./80% RH, 100% oxygen, but after 20 folding operations, it had not increased any further. Moreover, the reduced graphene oxide is not moisture sensitive, such that is loses its barrier properties at higher humidity, as would for example PVOH. Thus, the OTR at 80% RH would be the same for the barrier-coated film of this example.
[0120] In
[0121] A protective polymer coating 15a such as the one in
[0122] In
[0123] The bulk layer 21 is laminated to the barrier-coated PET film substrate material 25a; 10a of
[0124] The innermost heat sealable layer 23 may consist of one layer or alternatively of two or more part-layers of the same or different kinds of LDPE or LLDPE or blends thereof, and is well adhered to the surface of the barrier layer of the barrier-coated PET film substrate 10a; 25a, by an intermediate coextruded tie layer 24, e.g. of ethylene acrylic acid copolymer (EAA), which is thus bonding the innermost heat sealable layer(s) to the barrier surface of the barrier-coated substrate material web 10a, in applying the layers together in a single melt coextrusion coating step.
[0125] Alternatively, the barrier-coated PET film substrate 10a; 25a may be turned in the opposite direction in the laminate, i.e. with the barrier coating layer directed towards the bulk layer and the outside of the laminated material.
[0126] In
[0127] The bulk layer 21 is laminated to the uncoated side of the barrier-coated paper substrate 25b;10b, from
[0128] Thus, the amount of thermoplastic polymer can be significantly reduced in this lamination layer, in comparison to the conventional melt extrusion laminated bonding layer of polyethylene, described in
[0129] The innermost heat sealable layer 23 is applied at an amount of about 22 g/m.sup.2 onto the barrier-coated surface of the paper substrate material by an intermediate coextruded tie layer, e.g. of ethylene acrylic acid copolymer (EAA), which thus bonds the innermost heat sealable layer(s) 23 to the barrier coated paper substrate 10b, in applying the layers together in a single melt coextrusion coating step.
[0130] Alternatively, the innermost heat sealable and liquid-tight layer is a pre-manufactured, blown film 23b, comprising LDPE or LLDPE polymers in any blends thereof, and it may be laminated to the barrier-coated paper substrate, i.e. to the surface of its barrier coating, by means of an intermediate, melt extrusion laminated bonding layer 24b, comprising a thicker tie layer of EAA than the layer 24 used in
[0131] In an alternative embodiment, the pre-manufactured blown film 23b is laminated to the metallised coating by means of another wet lamination step, with an aqueous adhesive of an acrylic (co)polymer adhesive layer 24b, at ambient (cold) temperature, at an amount from 3 to 4 g/m.sup.2.
[0132] Further embodiments, having all the features as described and a melt extruded bulk layer lamination layer 26a of
[0133] A yet further embodiment, wherein the thin, wet, aqueous adhesive dispersion laminated layer 26a of
[0134] In
[0135] The resulting barrier pre-coated paper substrate web 34a is forwarded to cool off and is wound up onto a reel for intermediate storage and later further lamination operations.
[0136]
[0137] As explained in connection to
[0138] In
[0139] The non-laminated side of the bulk layer 21, i.e. its print side, is joined at a cooled roller nip 48a to a molten polymer curtain 46a of the LDPE, which is to form the outermost layer 22 of the laminated material, the LDPE being extruded from an extruder feedblock and die 47a. Subsequently, the paper pre-laminated web, now having the outermost layer 22 coated on its printed side, the outside, passes a second extruder feedblock and die 47b and a lamination nip 48b, where a molten polymer curtain 46b is joined and coated onto the other side of the pre-laminate, i.e. on uncoated, inner side of the barrier-coated substrate material web 10a; 10b; 25a;25b. Thus, the innermost heat sealable layer(s) 23 are coextrusion coated onto the inner side of the barrier-coated substrate material web, to form the finished laminated packaging material 49b, which is finally wound onto a storage reel, not shown.
[0140] These two coextrusion steps at lamination roller nips 48a and 48b, may alternatively be performed as two consecutive steps in the opposite order.
[0141] According to another embodiment, one or both of the outermost layers may instead be applied in a pre-lamination station, where the coextrusion coated layer is first applied to the outside of the (printed) bulk paperboard layer or onto the inner surface of the barrier-coated paper substrate, and thereafter the two pre-laminated paper webs may be joined to each other, as described above, in connection to
[0142] According to a further embodiment, the innermost layers of the heat sealable and liquid-tight thermoplastic layers may be applied in the form of a pre-manufactured film, which is laminated to the barrier-coated substrate material 10a; 10b.
[0143] As explained in connection to
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[0149] As a final remark, the invention is not limited by the embodiments shown and described above, but may be varied within the scope of the claims.