MULTI-LAYERED COMPOSITION BASED ON FOAMED RECYCLED POLYETHYLENE TEREPHTHALATE AND METHOD FOR PRODUCING SAME
20220234331 · 2022-07-28
Inventors
- Dmitrii Sergeevich RASTORGUEV (Moscow, RU)
- Sergei Sergeevich NIKITENKO (Moskovskaya oblast, g. Khimki, RU)
- Mikhail Valerevich TSIRKULEV (Moscow, RU)
Cpc classification
C08J2367/02
CHEMISTRY; METALLURGY
B32B2255/10
PERFORMING OPERATIONS; TRANSPORTING
B32B2553/00
PERFORMING OPERATIONS; TRANSPORTING
Y02W30/62
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
B32B2272/00
PERFORMING OPERATIONS; TRANSPORTING
B32B2307/4023
PERFORMING OPERATIONS; TRANSPORTING
C08J9/122
CHEMISTRY; METALLURGY
B32B5/18
PERFORMING OPERATIONS; TRANSPORTING
B32B38/0004
PERFORMING OPERATIONS; TRANSPORTING
B32B37/156
PERFORMING OPERATIONS; TRANSPORTING
B32B15/20
PERFORMING OPERATIONS; TRANSPORTING
B32B2255/102
PERFORMING OPERATIONS; TRANSPORTING
B32B3/30
PERFORMING OPERATIONS; TRANSPORTING
International classification
B32B15/04
PERFORMING OPERATIONS; TRANSPORTING
B32B15/20
PERFORMING OPERATIONS; TRANSPORTING
B32B27/06
PERFORMING OPERATIONS; TRANSPORTING
B32B37/00
PERFORMING OPERATIONS; TRANSPORTING
B32B38/00
PERFORMING OPERATIONS; TRANSPORTING
B32B5/18
PERFORMING OPERATIONS; TRANSPORTING
Abstract
The invention relates to a multi-layered structure intended for producing a packaging article for storage purposes and to a method for producing said structure. The essence of the invention is that a multi-layered composition based on foamed recycled polyethylene terephthalate comprises a printed layer, a layer of foamed recycled polyethylene terephthalate having a density of from 100 kg/m.sup.3 to 900 kg/m.sup.3 and an intrinsic viscosity of from 0.5 dl/g to 1.0 dl/g, and also a layer of polyethylene or a polyethylene copolymer, or a polyethylene terephthalate copolymer. A method for producing a multi-layered composition consists in cleaning polyethylene terephthalate waste, then grinding same into fractions, followed by melting it and subsequently extruding the melt, then producing granulated polyethylene terephthalate, then extruding the granulated polyethylene terephthalate, foaming the melt, subsequently cooling the foamed recycled polyethylene terephthalate, calendering it to a thickness of from 200 μm to 1000 μm.
Claims
1. A multi-layered composition based on expanded recycled polyethylene terephthalate, characterized in that the composition is comprising: a printed layer, a layer of expanded recycled polyethylene terephthalate having a density of 100 kg/m.sup.3 to 900 kg/m.sup.3 and an intrinsic viscosity of 0.5 dl/g to 1.0 dl/g, and a layer of polyethylene or polyethylene copolymer, or polyethylene terephthalate copolymer.
2. The multi-layered composition of claim 1, wherein the layer of expanded recycled polyethylene terephthalate has a thickness ranging from 200 μm to 1000 μm.
3. The multi-layered composition of claim 1, wherein the main layer of polyethylene or polyethylene copolymer, or polyethylene terephthalate copolymer has a thickness ranging from 10 μm to 40 μm.
4. The multi-layered composition of claim 1, wherein, instead of the layer of expanded recycled polyethylene terephthalate, a coextrusion or extrusion-cast layer of non-expanded recycled polyethylene terephthalate in combination with the layer of expanded recycled polyethylene terephthalate is used.
5. The multi-layered composition of claim 4, wherein the layer has a thickness ranging from 20 μm to 100 μm.
6. The multi-layered composition of claim 1, wherein a layer of polyethylene or polyethylene copolymer is added between the printed layer and the layer of expanded recycled polyethylene terephthalate.
7. The multi-layered composition of claim 6, wherein the added layer has a thickness ranging from 5 μm to 15 μm.
8. The multi-layered composition of claim 1, wherein a layer of aluminum foil is added after the layer of expanded recycled polyethylene terephthalate.
9. The multi-layered composition of claim 8, wherein the added layer of aluminum foil has a thickness ranging from 4 μm to 9 μm.
10. A method for producing a multi-layered composition based on expanded recycled polyethylene terephthalate, wherein a polyethylene terephthalate (PET) waste is washed, purified, then crushed to fractions from 1 mm to 20 mm in size, and separated according to polymer types and color; the PET is then melted, and a PET melt is extruded; the PET is next subjected to liquid-state polycondensation under vacuum to obtain granular PET having an intrinsic viscosity of 0.5 dl/g to 1.0 dl/g; the granular PET is further extruded, while simultaneously supplying nitrogen and/or carbon dioxide; the PET melt is subsequently expanded, whereupon the expanded secondary PET is cooled and calendered to a thickness of 200 μm to 1000 μm and wound into a roll; after that, by using an extrusion lamination line, a roll of a layer of expanded recycled polyethylene terephthalate or a roll of a layer of expanded recycled polyethylene terephthalate in combination with a coextrusion or extrusion-cast layer of non-expanded recycled polyethylene terephthalate is installed on a main unwinding station; at least one roll of a layer of polyethylene or polyethylene copolymer and a layer of aluminum foil are next installed on additional unwinding stations; the layer of polyethylene or polyethylene copolymer and the layer of aluminum foil are applied on the layer of expanded recycled polyethylene terephthalate or the layer of expanded recycled polyethylene terephthalate combined with the coextrusion layer of non-expanded recycled polyethylene terephthalate; the resulting material is temperature-controlled on outer rolls; a printed layer is applied on an outer surface and the multi-layered composition is then scored and cut into individual sheets.
11. The method for producing the multi-layered composition of claim 10, wherein the printed layer is applied by using rotogravure or offset, or flexographic printing, or any combination thereof.
12. The method for producing the multi-layered composition of claim 10, wherein bottles, fibers, filaments, sprues, flakes are used as the polyethylene terephthalate waste.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0007] The invention is explained by means of the drawings, in which:
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DETAILED DESCRIPTION OF THE INVENTION
[0019] A multi-layered composition based on expanded recycled (obtained from a polyethylene terephthalate waste) polyethylene terephthalate (shown in
[0020] In one embodiment (which is shown in
[0021] In one other embodiment (which is shown in
[0022] In one other embodiment (which is shown in
[0023] In one other embodiment (which is shown in
[0024] In one other embodiment (which is shown in
[0025] A method for producing the multi-layered composition based on polyethylene terephthalate is performed using a conventional extrusion lamination line that comprises: an unwinding station; a melt casting station; an extrusion lamination station; a printing station; a quality control station; a winding station. The method is performed as follows. At first, the layer 2 of expanded recycled polyethylene terephthalate is prepared. For this purpose, a polyethylene terephthalate waste 9 (bottles, fibers, filaments, sprues, polyethylene terephthalate flakes) are washed and purified from debris, labels, glue. Then, the polyethylene terephthalate waste is crushed to obtain fractions having a size from 1 mm to 20 mm and separated according to polymer types and color. Next, the separated polyethylene terephthalate waste is loaded into a hopper 10 and melted, and the polyethylene terephthalate melt is extruded on the extrusion line by using an extruder 10, while removing excess contaminants and moisture by means of vacuum pumps 11. After that, the liquid-state polycondensation of polyethylene terephthalate is performed in a reactor 12 under the action of vacuum pumps 13. The condensation leads to an increase in the intrinsic viscosity. High-efficiency vacuum effectively removes harmful chemical impurities from the material, making it possible for the recycled material to be used for 100% safe contact with food products. As the PET melt enters the vertical portion of the P:REACT (LSP reactor) 12, filaments are produced, which form a corresponding surface in volumetric relation. The material is then collected in a horizontal drum and slowly moved forward. The condensation process begins immediately after the production of the filaments and continues until the PET leaves the LSP reactor. An increase in the intrinsic viscosity is controlled by the residence time of the PET melt in the LSP reactor and the degree of vacuum in the LSP reactor and, therefore, may be set to a required level. Parameter settings allow a control unit to maintain a predetermined intrinsic viscosity level within a narrow tolerance range. The process of removing impurities is very effective as it is performed in the liquid state of polyethylene terephthalate. Not only the purification efficiency of the material that exceeds the limits set by food industry standards is provided, but also lubricants are effectively removed from the fibers during the purification process. An increase in the intrinsic viscosity may be measured at a level of about 0.01 dl/g per minute. The continuous operation of the LSP reactor provides a narrow intrinsic viscosity range of a granulate, which is suitable for high-end applications, such as fiber spinning or the production of sheets by extrusion. Fluctuations in the intrinsic viscosity during the mass production are simply ruled out. The separation of harmful impurities, such as lubricants or substances not intended for contact with food products, is performed under the vacuum pumps 13. The high removal rate of the impurities allows the LSP reactor to be utilized in a variety of applications, providing its high operational flexibility. The favorable conditions created in the LSP reactor (temperature/a melt surface-volume ratio/high-efficiency vacuum) allows the PET condensation process to be freely initiated. This leads to an increase in the intrinsic viscosity by about 0.01 dl/g per minute. Faster response times translate into faster achievement of required results and higher profitability. Polyethylene terephthalate granules are produced at the outlet of the LSP reactor. Then, the extrusion of the polyethylene terephthalate granules is performed, while simultaneously supplying nitrogen and/or carbon dioxide. In a connector in front of a die, in the die and at the outlet of the die, the polyethylene terephthalate melt is subjected to temperature- and pressure-controllable extrusion, whereupon the melt is fed from the die to calender rolls where it is cooled (temperature-controlled) and calendered to a thickness of 200 μm to 1000 μm. An additional station for extrusion-casting of either the polyethylene terephthalate melt 5 or the polyethylene or polyethylene copolymer melt 8 may be installed subsequently, and the repeated calendering, temperature control and winding of the film into rolls are performed. Next, the roll of the layer 2 of expanded recycled polyethylene terephthalate or the roll of the layer 2 of expanded recycled polyethylene terephthalate combined with the coextrusion or extrusion-cast layer 5 of non-expanded recycled polyethylene terephthalate or with the additional layer 8 of polyethylene or polyethylene copolymer is installed on the main unwinding station. Further, the roll of the main layer 3 of polyethylene or polyethylene copolymer is installed on additional unwinding stations. If required, the roll of the layer 7 of aluminum foil is also installed on additional unwinding stations. If required, the roll of the additional layer 8 of polyethylene or polyethylene copolymer is also installed on additional unwinding stations. Next, the layer 3 of polyethylene or polyethylene copolymer is applied on the layer 2 of expanded recycled polyethylene terephthalate or the layer 2 of expanded recycled polyethylene terephthalate combined with the coextrusion layer 5 of non-expanded recycled polyethylene terephthalate, and the resulting material is temperature-controlled on the calender rolls. After that, the printed layer is applied on the outer surface of the multi-layered composition based on expanded recycled polyethylene terephthalate by using rotogravure printing or offset printing, or flexographic printing, or any combination thereof. The resulting multi-layered composition is scored and cut into individual sheets.
INDUSTRIAL APPLICABILITY
[0026] The claimed invention makes it possible to: recycle a layer of expanded recycled polyethylene terephthalate similarly to cardboard; perform scoring for subsequent folding along a scoring line; perform finishing operations (e.g., printing); perform extrusion lamination with polyethylene terephthalate, polyethylene and polyethylene copolymers and aluminum foil. The claimed invention makes it possible to produce a packaging product consisting of the main carrier layer of recycled polyethylene terephthalate and fully recycle the wasted packaging product based on the multi-layered composition comprising the main carrier layer of expanded polyethylene terephthalate by means of crushing, aluminum filtration (when aluminum is used), and subsequent liquid-state polycondensation of polyethylene terephthalate, thereby restoring the properties of polyethylene terephthalate to those of primary raw materials. The claimed invention makes it possible to recycle multi-layered compositions comprising the main carrier layer of expanded polyethylene terephthalate as many times as one sees fit. In most cases, the claimed invention allows one to produce multi-layered compositions comprising a layer of expanded polyethylene terephthalate having physical and mechanical characteristics better than those of similar multi-layered compositions based on cardboard and/or paper. The claimed invention is 5%-30% cheaper in cost than cardboard or paper, depending on cardboard or paper brands and depending on a required expansion coefficient, and depending on the intrinsic viscosity of polyethylene terephthalate.