Method for Producing a Moulded Pulp Material for Packaging Unit and Such Packaging Unit
20230031748 · 2023-02-02
Inventors
Cpc classification
B65D85/324
PERFORMING OPERATIONS; TRANSPORTING
B65D65/466
PERFORMING OPERATIONS; TRANSPORTING
D21J3/00
TEXTILES; PAPER
D21J7/00
TEXTILES; PAPER
Y02W90/10
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
International classification
D21J3/00
TEXTILES; PAPER
B65D65/46
PERFORMING OPERATIONS; TRANSPORTING
Abstract
The present invention relates to a method for producing a moulded pulp material that is suitable for manufacturing of a packaging unit and such packaging unit. The method of the invention comprises the steps of: - preparing a raw moulded pulp material; - providing the raw moulded pulp material to an extruder; - extruding the raw moulded pulp material; - adding one or more additives; and - providing the moulded pulp material at the outlet of the extruder.
Claims
1-24. (canceled)
25. A method for producing a moulded pulp material for a packaging unit, the method comprising the steps of: preparing a raw moulded pulp material; providing the raw moulded pulp material to an extruder; extruding the raw moulded pulp material; adding one or more additives; and providing the moulded pulp material at the outlet of the extruder.
26. The method according to claim 25, wherein the additives comprise a pigment.
27. The method according to claim 26, wherein the pigment is added after adding a fixative.
28. The method according to claim 25, further comprising the step of selecting one or more dimethylamine polymers as fixative.
29. The method according to claim 25, wherein the weight ratio of additive to fixative is in the range of 2-25, preferably in the range of 3-20, and most preferably in the range of 4-19.
30. The method according to claim 25, wherein the raw moulded pulp material comprises a mixture of soft wood and hard wood, and/or comprising the step of providing an amount of natural and/or alternative fibers.
31. The method according to claim 25, further comprising the step of adding an amount of a biodegradable aliphatic polyester, wherein the amount of biodegradable aliphatic polyester in the moulded pulp material is preferably in the range of 0.5-20 wt.%, more preferably in the range of 1-15 wt.%, even more preferably in the range of 2-10 wt.%, even more preferably in the range of 5-9 wt.%, and most preferably in the range of 6.5-8 wt.%, wherein the biodegradable aliphatic polyester preferably comprises an amount of one or more of PBS, PHB, PHA, PCL, PGA, PHBH and PHBV.
32. The method according to claim 25, further comprising the step moulding a packaging unit, further comprising the step of: providing a laminated multi-layer comprising: an inner cover layer comprising an amount of a biodegradable aliphatic polyester; a first intermediate layer of a biodegradable material for connecting and/or sealing adjacent layers; a functional layer comprising a vinyl alcohol polymer; a second intermediate layer of a biodegradable material for connecting and/or sealing adjacent layers; and an outer cover layer comprising an amount of a biodegradable aliphatic polyester, and manufacturing the packaging unit with the laminated multi-layer to provide a food packaging unit that is a compostable packaging unit.
33. The method according to claim 32, further comprising the step of providing a biodegradable top seal film.
34. The method according to claim 32, further comprising the step of performing (dry) sterilisation and pasteurisation of the packaging units.
35. The method according to claim 32, further comprising the step of biodegrading the packaging unit, wherein the decomposing is performed at a temperature in the range of 5 to 40° C., preferably in the range of 10 to 30° C., more preferably in the range of 15 to 25° C., and most preferably at a temperature of about 20° C.
36. A packaging unit from a moulded pulp material, the packaging unit comprising a food receiving and/or carrying compartment, wherein the moulded pulp material is provided by a method according to claim 25.
37. The packaging unit according to claim 35, wherein the moulded pulp material comprises an amount of fibers, wherein at least 80% of the fibers has a length above 1.1 mm, preferably above 1.2 mm.
38. The packaging unit according to claim 35, wherein the moulded pulp material comprises a pigment and a fixative, wherein the weight ratio of pigment to fixative is in the range of 2-25, preferably in the range of 3-20, and most preferably in the range of 4-19.
39. The packaging unit according to claim 35, wherein the fixative comprise dimethylamine polymers.
40. The packaging unit according to claim 35, further comprising a biodegradable laminated multi-layer, with the multi-layer comprising: an inner cover layer comprising an amount of a biodegradable aliphatic polyester; a first intermediate layer of a biodegradable material for connecting and/or sealing adjacent layers; a functional layer comprising a vinyl alcohol polymer; a second intermediate layer of a biodegradable material for connecting and/or sealing adjacent layers; and an outer cover layer comprising an amount of a biodegradable aliphatic polyester, and wherein the packaging unit is a compostable packaging unit, wherein the thickness of the individual layers is within the range of 5-50 .Math.m, preferably in the range of 5-30 .Math.m, and wherein the total thickness of the laminated multi-layer is in the range of 20-150 .Math.m.
41. The packaging unit according to claim 40, wherein the laminated multi-layer is a co-extruded laminated multi-layer, wherein the laminated multi-layer is melted or fused with the compartment, wherein the packaging unit comprises a layer of biodegradable aliphatic polyester on a product contact surface to improve melting or fusing of the laminated multi-layer thereon, wherein the laminated multi-layer is melted in the moulded pulp material matrix.
42. The packaging unit according to claim 35, further comprising a biodegradable top seal film, wherein the packaging unit comprises a circumferential edge comprising a connecting surface for the top seal film that is substantially free of the laminated multi-layer, and wherein the top seal film comprising a biodegradable aliphatic polyester.
43. A method for producing a moulded pulp material for a packaging unit, the method comprising the steps of: preparing a raw moulded pulp material; providing the raw moulded pulp material to an extruder; extruding the raw moulded pulp material; adding one or more additives; and providing the moulded pulp material at the outlet of the extruder, wherein the additives comprise a pigment, wherein the pigment is added after adding a fixative, wherein the weight ratio of additive to fixation is in the range of 2-25.
44. The method according to claim 43, further comprising the step of adding an amount of a biodegradable aliphatic polyester, wherein the amount of biodegradable aliphatic polyester in the moulded pulp material is in the range of 0.5-20 wt.%.
Description
[0101] Further advantages, features and details of the invention are elucidated on the basis of preferred embodiments thereof, wherein reference is made to the accompanying drawings, in which:
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[0114] Stack 1 (
[0115] To produce units 3 with sufficient strength, method 1002 (
[0116] Next, some examples of packaging units that are manufactured from moulded pulp using method 1002 are shown.
[0117] Packaging unit 2 (
[0118] In the illustrated embodiment container 2 is provided with peelable top seal film 13a (
[0119] In the illustrated embodiment, laminated multi-layer 10 (
[0120] Packaging unit 22 (
[0121] Packaging unit 22 (
[0122] Laminated multi-layer 10 (
[0123] In another embodiment, plate 50 (
[0124] Packaging unit 102 (
[0125] In the illustrated embodiment, top surface 122 of cover part 104 is provided with groove 126 comprising a number of openings 128. Openings 128 are defined by two adjacent arch-shaped edges 130, 132 having a larger thickness as compared to the average thickness of cover part 104.
[0126] Side surfaces 118 of cover part 104 are provided with denest nocks or denest elements 134. In the illustrated embodiment, bottom part 106 is provided with similar elements 136 mirroring denest elements 134. Hinge 138 connects back surface 116 of cover part 104 with back surface 108 of bottom part 106. Lock 140 comprises nose-shaped lock element 142 that is connected to flap 144 of bottom part 106. Cover part 104 is provided with openings 146 that capture lock elements 142 therewith defining lock 140.
[0127] In the illustrated embodiment, bottom part 106 is provided with a number of product receiving compartments 148, cones 150 and separating walls 152. Cone 150 extends from the bottom of bottom part 106 in an upward direction. Cover part 104 comprises cone support 154. Inner surface 158 of packaging unit 102 may comprise PBS and/or other suitable biopolymer material, optionally as film layer or alternatively blended and/or integrated with the fibers of the moulded pulp material. Packaging unit 102 may also be configured to receive other products, such as tomatoes, kiwis.
[0128] Packaging unit 202 (
[0129] Packaging unit 202 has numerous applications, including but not limited to, airplane meals. Such meals are provided to the airplane after (dry) sterilisation and pasteurisation. In combination with the (O.sub.2)-barrier properties of the laminated multi-layer (and top seal film) the shelf-life of the food product is significantly improved. In addition, the O.sub.2-barrier prevents or at least reduces oxidation processes in the food and thereby contributes to the maintenance of food taste.
[0130] Meat dish 250 (
[0131] As a further example, bottle divider 302 (
[0132] A further example in accordance with the present invention is cover 402, for example for an ice cup (
[0133] It will be understood that other designs for packaging units in accordance with the invention can be envisaged. For example, containers 602, 702 (
[0134] Other examples of food packaging products may relate to cup carriers, cups, plates and other table ware etc.
[0135] When manufacturing a food packaging unit 2, 3, 50, 102, 202, 252, 302, 402, 502, 602 a moulded pulp material is prepared. Optionally, an amount of biodegradable aliphatic polyester, such as PBS and/or PHBH, is blended or mixed into the moulded pulp material and/or an amount of biodegradable aliphatic polyester, such as PBS and/or PHBH is included in a separate layer that is provided in or on unit 2, 3, 50, 102, 202, 252, 302, 402, 502, 602. Such separate layer may improve the contact with laminated multi-layer 10, 52, 101, 201, 251, 301, 401, 501, 601 optionally comprising a vinyl alcohol polymer, such as HAVOH and/or BVOH. Preferably, laminated multi-layer is co-extruded with the moulded pulp material and deep-drawn. In addition, or as an alternative, the raw unit is moulded. Optionally, the raw unit is dried in the mould applying an in-mould drying process. In such alternative embodiment laminated multi-layer 10, 52, 101, 201, 251, 301, 401, 501, 601 is provided in the mould and a heating step is performed. Optionally, an additional layer of biodegradable aliphatic polyester is provided to improve the contact between the packaging unit and the laminated multi-layer. Finally the product is released from the mould.
[0136] Several post-drawing or post-moulding operations may optionally be performed in relation to unit 2, 3, 50, 102, 202, 252, 302, 402, 502, 602 optionally including, but not limited to, labelling including in-mould labelling, marking including printing and digital printing, testing.
[0137] Experiments have been performed with one or more of the illustrated food packaging units that were manufactured from a moulded pulp that was provided involving an extrusion process.
[0138] In a first test a hardwood-softwood cellulose pulp mixture was used, using e.g. about 60% softwood cellulose pulp (spruce, pine), combined with about 40% hardwood cellulose pulp (like birch), both for the Twin Screw extrusion and the standard pulped and refined pulp. In the experiments a peristaltic pump was used. From the pulp hand sheets were made in both cases, and also 3-dimensional in-mould dried products.
TABLE-US-00001 Results of the hand sheets tests: Tensile index (Nm/g) E modulus (MPa) Taber stiffness (mN) Shopper Riegler (SR) Standard: 20 - 40 400 - 1000 1000- 1200 20 - 40 Extrusion: 20 - 43 400 - 950 1000 - 1250 25 - 45
[0139] Standard involved standard pulping follow by a disc refining process. The applied refining energy was 40-80 kWh/t.
[0140] Extrusion involved so-called twin screw extrusion.
[0141] From these hand sheet mechanical strength and freeness (SR relating to pulp freeness, dewatering) observations it can be concluded that the Twin Screw Extrusion can achieve a similar or slightly better result as when using a standard paper making set up using a pulper and disc refiner. The Twin Screw technology could therefore replace a pulper and refiner. Another observation during the tests was that the fibrillation of the fibers is better, i.e. leaving more open positions on the fibers to bind cationic additives like AKD sizing. Also the average fiber length of the extrusion process leads to a fiber length that is approximately 60% larger as when the same pulp/fibers are used in a conventional pulping and refining process. This may obviate the need for a conventional pulper and refiner combination. These larger fibers enhance the dewatering of a fiber slurry in a paper making process or in a moulded fiber process, both for an in-mould drying molded fiber process, where the paper slurry after the 1.sup.st forming step under vacuum is formed followed by one or more drying steps in a heated mould, and also in a conventional moulded fiber process where the paper slurry after the 1.sup.st forming step under vacuum is formed and then dried in a conventional drying process (like a gas heated and/or electrical heated drying oven).
[0142] Results of an in-mould drying process of a 3-dimensional packaging unit, using moulded pulp disclosed/refined in a Twin screw extrusion process show that the dryness of the pulp in the first forming step is 25 - 35%, where at the same machine with conventional refined pulp a dryness is achieved between 20 - 25% at low temperatures (ambient temperature). At higher process water temperatures the difference in dryness is slightly higher (2-3%), but remains in the same band width between the two refining technologies. This higher dryness leads to a faster machine speed to produce products. Also it saves energy to dry the products. Another observation of in-mould dried products that were refined in a Twin Screw Extruder system compared to conventional pulped and refined pulp is that the strength and stiffness of the in-mould dried products made out of the pulp is 40 - 70% better. For example, the Taber Stiffness was in the range of 40 -80% higher and also the compression strength of a 3D molded product is 40 - 80% higher.
[0143] The experiment showed that this way of refining a hardwood-softwood mixture in an extrusion process is therefore also enabling IMD moulded pulp product producers to make lighter weight products with remaining the same stiffness and strength properties leading also to lower drying energy levels, a better carbon footprint for the products. Depending on the application of the moulded pulp product in the market (like a meat tray used in a skin packaging where the tray needs to be very strong to avoid collapsing or warpage of the tray) this technology can also lead to stronger products, stiffer products.
[0144] Another observation from the experiments is that due to a different way of refining the fibers, leading to different fibrillation and creating more open spaces on the fibers, anionic charged, to bind cationic charged molecules like an AKD sizing or other cationic charged molecules like dyes or fixatives to bind pigments. To illustrate that effect: Twin screw refined pulp adding 2% AKD sizing, as received from suppliers (with ca 15% effective alkyl ketene dimer) lead to a Cobb (60 sec) of 10-20 g/m2, where the same pulp refined in the conventional way leads with same AKD sizing to a Cobb (60 sec) of 20-45 g/m.sup.2. It was shown that pigments could bind more easy to the fibers in the extrusion process. Furthermore, it was established that the process water in the extrusion process was less polluted with pigments as compared to conventionally adding pigments.
[0145] Other tests were performed to show the dual ovenable (oven and microwave) performance of the packaging unit according to the invention. In the experiments the laminated product was heated to a temperature of about 190° C. for about 30 minutes. Results show that the film layer remains intact and does not melt. No leakage was detected. Furthermore, the strength and stability of the packaging unit were not significantly affected. As a further effect, the packaging unit was more stable in view of twisting when removing the packaging unit from the oven as is often the case with conventional packaging units. Furthermore, the packaging unit of the invention showed a limited temperature increase to about 50-70° C., while the conventional units reached a temperature of about 90-100° C. under similar conditions. Other experiments with a (food) tray shows an even improved heat resistance when heating the tray to a temperature of 180-200° C., and in addition shows (an improved) oil, acid and moisture resistance/repellence.
[0146] Other tests were performed to show the performance of the packaging unit according to the invention by heating the packaging unit in an oven and/or microwave. In the experiments the laminated product, comprising a laminated layer with a total thickness of about 40 .Math.m, was heated to a temperature of about 180° C. for about 35 minutes. Results show that the film layer remains intact and does not melt. No leakage was detected. Furthermore, the strength and stability of the packaging unit were not significantly affected. As a further effect, the packaging unit was more stable in view of twisting when removing the packaging unit from the oven as is often the case with conventional packaging units. Leaking of the film layer was tested by using food simulantia such as 95% ethanol, modified polyphenylene oxide (MPPO), 2,2,4-trimethylpentane, and the like. Thus, this test showed a safe use of the laminate product as packaging, for example food packaging.
[0147] The present invention is by no means limited to the above described preferred embodiments thereof. The rights sought are defined by the following claims, within the scope of which many modifications can be envisaged. It is noted that this invention is not limited for cellulose fibers and not limited for smooth molded fiber processes but works for any biomass/fiber/ alternative fiber material, also in the rough molded fiber process. Also, this invention is not limited to 3D moulded fiber production and can also be applied to the flat paper production in paper mills facing similar challenges with coloured water treatment.