This application is based on, and Applicants claim priority from, Netherlands Patent Application No. NL 2016056 filed on Jan. 5, 2016, which is incorporated herein by reference.
The invention relates to a method for coating a product. The invention further relates to products coated and an apparatus and foil or laminate for coating products. The invention especially relates to such methods, apparatus or products wherein the product coated comprises at least a wall part having an at least partly open cell structure.
Products having a cell structure such as an at least partly open cell structure in at least part of a wall are known from the art. Such products are for example known from for example WO96/30186 or WO98/13184. Such products are produced and marketed under the name of PaperFoam®, a registered name of PaperFoam BV, Barneveld, The Netherlands. In these known methods a suspension of at least a natural polymer such as starch in a fluid, such as water, is gelatinized and then baked in a mould at a temperature sufficient to form a network of said natural polymers, wherein a blowing agent is used for forming a partly open celled structure by said network. The blowing agent can for example be water in which the natural polymer is suspended or another blowing agent. Similarly such products can be obtained using other materials and other methods for forming the same, such as for example expanded plastics, such as but not limited to EPS. In such the cells could be provided between mono- and/or polymer spheres or differently shaped mono- and/or polymer elements.
These products have an at least partly porous surface. Moreover at least the surface of such products may be susceptible to water or other fluids, may be prone to contamination and can be difficult to clean. Moreover such surfaces may be relatively soft and vulnerable to damage.
In WO00/39215 methods have been described for coating a surface of products having an at least partly open celled wall structure, such as known from but not limited to products as disclosed in for example WO96/30186 or WO98/13184. In this method a liquid coating is applied to a relevant surface area, which is then allowed to dry. The coating can for example be applied by spraying or dipping. This coating is relatively thin and may not be sufficiently resistant to external influences.
There is a need for a method and apparatus as well as a product for coating products having a wall which has at least a wall part having at least partly an cell structure. There is a need for a method and apparatus as well as a product for coating products having a wall which has at least a wall part having at least partly an open cell structure. There is furthermore a need for an alternative method for coating products. At least one of these goals is at least partly obtained by a method, product or apparatus or assembly according to this disclosure.
In an aspect a method according to the disclosure can be characterized in that pressure forming, such as vacuum forming and/or thermoforming is used for coating a product, said product preferably having a cell structure in al least part of a wall of the product, more preferably at least partly an open cell structure. Preferably a foil or laminate is pressure formed directly over and/or into said product by passing air through at least part of said product and/or wherein the foil or laminate is at least partly adhered to said product prior to or during said thermoforming and/or vacuum forming.
In an aspect this disclosure can be directed to a method for coating a product having a wall formed by at least a portion having at least partly a cell structure. A foil or foil laminate is pressure formed, for example thermoformed and/or vacuum formed over at least a part of at least one side of said wall, said foil or at least one layer of said laminate forming a coating of said part of the wall. In such method preferably a product having at least a wall part having at least partly an open cell structure is coated.
In an aspect this disclosure can be characterized by an assembly for coating a product, comprising a pressure forming unit, a mould or last and a foil or laminate. The product has a wall part having at least partly a cell structure, preferably at least partly an open cell structure, and wherein the product fits in/and or on the last or mould, such that at least the part of the wall having at least partly the cell structure is supported by said last or mould. The pressure forming unit comprises a suction device for sucking air through and/or along said part of the wall having said cell structure and preferably through and/or along said last or mould supporting said wall portion.
In further elucidation of the present disclosure embodiments of methods, materials and products, as well as assemblies for use will be described, with reference to the drawings, which are only shown in elucidation and should not be understood as limiting the disclosure in any way.
These figures and examples of embodiments are disclosed by way of example only and should by no means be interpreted as limiting in any way or form. In these drawings and description the same or similar reference signs are used for the same or similar aspects of the disclosure.
In this description wording like substantially should be understood as meaning that slight variations on a value, dimension or other property it refers to should also be considered allowable. For example but not limited to variations or deviations of up to 25% or at least up to 20%, such as but not limited to variations or deviations of up to 15%, more specifically up to 10%, such as for example up to 5%.
In this description a top side or a bottom side of a product or foil or laminate should not be understood as limiting the relevant element to a specific orientation. In use a bottom side of a product may face down or up or in another direction, as may a bottom side. Bottom side and top side should be understood as at least meaning opposite sides of a product or foil or laminate.
Products according to this description may be, but are by no means limited to shells or trays, having an at least partly open side, a peripheral wall and a substantially closed side opposite the at least partly open side, such that it can hold materials and/or artefacts, preferably even if that material is for example granular or fluid.
Products according to the present disclosure are preferably but are not limited to products made using bio degradable and/or natural, recyclable material, such as starch based and/or natural fiber based materials. In advantageous embodiments the products can be made of a suspension containing starch, such as but not limited to potato or tapioca starch, which has been baked in a mould, such that the starch is at least gelatinized and preferably heated such that cross linking of at least natural polymers in the material is obtained. A blowing agent such as water can form air pockets or cells in said material, which can in part be open cells. Natural fibers can be provided in the material, increasing the materials strength. Preferably the material is brought into the mould as a suspension at a temperature close to or below the gelatinization temperature of the natural polymers, which allows for easy an relatively low pressure filling. After baking, i.e. after cross linking of the natural polymers preferably the wall of the products has at least partly a cellular structure. The structure can be a foamed structure. The cells could be closed cells and/or open cells. Methods for manufacturing such products are for example known from WO96/30186 or WO98/13184, which applications are owned by the same applicant and are incorporated herein by reference, as an example of such manufacturing method and suspensions that could be used for the manufacture. Such processes are for example used for injection moulding products in heated moulds. Such processes are for example used for the manufacture of PaperFoam® products. Alternatively the products could be made from a different material, for example from plastic, especially recycled plastic, such as but not limited to foamed materials such as for example but not limited to EPS.
In this description pressure forming should be understood as at least including but not limited to thermoforming and/or vacuum forming. Pressure forming can be understood as a method in which a foil or laminate is applied and/or shaped by applying heat and/or pressure to the foil, especially a pressure difference on opposite sides of the foil or laminate, in order to apply the foil or laminate to a surface and/or shape the foil or laminate. Traditionally pressure forming, especially vacuum and/or thermo forming is used for forming three dimensional products such as cups, trays and the like, which are self supporting, by plastically deforming a flat sheet of foil or laminate into the desired shape using a last or mould which is pressed into the foil or laminate when heated to a plastifying temperature, and is removed after cooling. During such procedure in vacuum forming air can be sucked through the last or mould, from between the mould or last surface and the heated foil or laminate, creating an under pressure or vacuum there between relative to the surrounding pressure and thus drawing the foil or laminate over and into close contact with the surface of the mould or last. After cooling the mould or last is removed and the product has obtained the desired shape. In the present disclosure methods and apparatus are disclosed in which a foil or laminate is pressure formed, for example thermoformed and/or vacuum formed, onto a product as mould or last, such that after said pressure forming the foil or laminate stays on the product and is preferably intimately connected to the product or part thereof.
In this description a laminate should be understood as meaning a composite of at least two superimposed, interconnected layers of plastic, such as plastic foils, films or sheets. A laminate may for example be coextruded or formed by adhering two or more layers of foil or film to each other.
Products according to this disclosure can be used for for example packaging of articles, such as electronics, medicines, medical appliances and the like, but also for example as a product for packaging perishable goods, food, agricultural products and the like. The disclosure is however not limited to such products.
In this description products and methods shall be described in which the products are made at least in part using a biodegradable material, such as a starch based material. Biodegradable materials or products can be understood as meaning at least materials or products which are compostable, domestic or industrial, recyclable with paper and/or bio material based. Moreover disclosed are, by way of example, products having relatively thin walls with a cellular structure, which may have a closed cell configuration or an open cell configuration or a combination of both. By way of example products made of PaperFoam® are disclosed, made using for example a method and apparatus known from WO96/30186 or WO98/13184 as mentioned. It should however be clear that the disclosure is not limited to such products. They may be made of other materials, such as non-biodegradable materials, they may have different configurations and they can have different wall structures, preferably at least partly porous. Such as for example foamed plastic having a partly open structure, meaning that air can pass through it.
By way of example only embodiments of products and assemblies, as well as methods according to the description shall be discussed hereafter with reference to the drawings.
The injection-moulding apparatus 20 comprises a supply device 21 for a batter S, a nozzle 22 and a mould 23. The batter S is for instance supplied from a storage tank 24 utilizing a pump 25.
Provided in the mould 23 are a number of mould cavities 26, two of which are depicted. Different numbers of mould cavities can be provided, which are identical or different. The mould cavities 26 are connected to a gate 27 via mould channels 28. Connecting to the or each mould cavity 26 are one or more deaeration channels which are in communication with the environment. This communication is preferably free, but may also be adapted to be shut off, for instance by a pressure relief valve. The mould 23 has mould parts 23A, B and is suitably divisible along a plane V which intersects the or each mould cavity 26, in such a manner that products 1 formed in the or each mould cavity 26 can be simply removed therefrom. The mould 23 is entirely and/or locally heated utilizing heating means 29 incorporated therein.
The mould 23 may contain different heating means 29, which can for example be electric heating elements. It is noted that the mould parts 26A, B can also be heated indirectly. The temperature of the different heating elements 29 is preferably controllable individually, but several or all heating elements 29 may also be coupled. In addition, the mould 23 can be heated externally from one or more sides, for instance electrically or by steam or gas burners. Through the heating elements 29 and optional other means, the temperature of the mould 23 can be raised in such a manner that in the/each mould cavity 26 during use, as desired, at all times and at all points the desired high baking temperature is achieved and maintained.
The injection-moulding apparatus 20 can be used as follows.
The mould parts 23A, B are clamped against each other and an amount of batter S is pressed into the mould 23 and into the mould cavities 26 under pressure. In the mould cavities 26 the batter S is brought to the desired temperature, and maintained at that temperature for a “baking time” of, for instance, 2 minutes. As a result, gelatinization and subsequent cross-linking of the (natural) polymers occurs. In addition, the strongly heated water and/or other liquids evaporate from the batter, giving rise to the formation of bubbles. In the batter, bubbles are formed which are partly encapsulated by the cross-linked structure. This yields a foam structure, which can be further enhanced by adding extra blowing agent. In order to allow substantially all of the evaporating moisture to escape from the mould 23, a sufficiently large number of vents or aeration channels are provided. After the baking time, the mould 23 is opened and the products 1 are taken from the mould cavities 26 or pushed out of them using ejectors 30.
Upon sufficient heating of the suspension at least above the gas formation or vaporization temperature of the or a blowing agent, within the suspension gelatinization of the starch occurs and moreover bubble formation as a result of evaporation of the water. Upon further heating of the suspension, cross-linking of the polymers occurs, yielding a firm, relatively dense structure around cells that result from the evaporation of the water and optional other blowing agents.
The injection-moulded product 1 has a wall 2 with a skin 13, preferably on opposite sides 2A, 2B of the wall 2 and a foamy core 14 which comprises cells 15, for example open cells 15. In
In
In this description, “gelatinization” is understood to mean a change of a natural polymer from a slightly or complete loose granular or comparable granulate form into a cohesive form which may or may not be dry and/or foamed, in which stretched polymers are present which are mutually bonded to a limited extent, if at all. That is to say, a transition occurs from a solid substance, a colloidal solution or suspension to a more homogeneous fluid mass. Depending on the polymers used, “gelatinization” should therefore be understood to include, for instance, gelling, gellating and the like.
In foamed products where only gelatinization occurs, as a result of gas evolution, bubbles are formed in the mass to be foamed, substantially after gelatinization. This process occurs at relatively low temperatures and pressures. Over the entire cross section, such products can have approximately the same structure of relatively small cells with walls of substantially uncross-linked natural polymers.
In this description, “baking” is understood to mean a method in which both gelatinization and cross-linking occur. This may occur at relatively high temperature and/or pressure. As a result, the formation of gas arises relatively soon, so that bubbles are already formed prior to or during gelatinization. As a result of inter alia the high pressure adjacent strongly heated parts, the polymers cross-link quickly when using a mould or like baking form with a temperature at or above the baking temperature.
These baked products can have a core with relatively large cells, enclosed between skin parts with relatively small cells. By regulating the composition of the suspension and/or the heating conditions and pressure inside the mould the size of the cells and whether they are predominantly open or closed or a mixture thereof can be controlled.
Since the mould is heated, the temperatures in the mould can be properly controlled, both for the mould as a whole and for each separate portion thereof. As a result, products can be manufactured with different and varying wall thicknesses and with different mechanical properties. In fact, by heating more or less and/or for a longer or shorter period and adjusting, for instance, the pressure, for instance the extent of cross-linkage of the polymers can be controlled locally, so that the mechanical and physical properties are influenced. All this can be simply determined by those skilled in the art.
In this description foil or laminate has to be understood as at least including film or laminates of foil and/or film. Film can be understood as a synonym of or as a class of foil, especially a thin foil.
It should be noted that in an alternative embodiment the central portion may also be deformed plastically, for example by heating and sucking, without adhering it to the central portion 2C, for example by applying reduced pressure, by not wetting the relevant portion of the foil or laminate or the central portion 2C.
In stead of or additional to heating and/or wetting an adhesive could be added to the interface between the foil or laminate and the product surface, for example a heat or pressure activated adhesive, for further adhering the foil or laminate to the product.
The foil 5 can for example be formed by or comprise at least a layer of biodegradable aliphatic-aromatic (co)polyester based material, a polylactic, cellulose, lignin, starch and/or PHA based material, a material comprising 1.4-butanediol, adipic acid and/or terephtalic acid monomers in polymer chains. Such at least one layer can for example comprise or be formed by a polybutyrate (PBAT), which is for example marketed under the tradename Ecoflex®, a trademark of BASF, and/or an EVOH based material.
The foil or laminate is adhered to at least part of the wall, prior to or during pressure forming. The foil or laminate can be adhered to said wall by chemical bonding and/or by mechanical bonding. The bonding can be obtained for example by a bonding agent applied to one or both of the product 1 and the foil 5 or laminate 5. The bonding can be achieved prior to or during pressure forming.
As indicated, a foil or laminate can be formed by a film or laminate of foils and/or films, which may also be provided as sheets.
In embodiments a foil 5 can be used, for example as shown in
Without wanting to be bound to any theory it appears that by using a foil or a laminate with an outer layer of PBAT or similar biodegradable (co)polyester or other biodegradable plastics which is heated to become more flexible sufficient for thermo-vacuumforming, when the foil 5 is pressed against the product surface, especially when having a cell structure, such as PaperFoam®, the said foil or laminate will at least partly chemically bond to the product. When using a soluble foil or layer in a laminate, it has been found that by wetting the foil or layer and/or the surface of the product to be coated, part of the relevant foil or layer will dissolve and will led to a chemical and/or mechanical bonding of the foil or laminate to the surface of the product. Without wanting to be bound to any theory it appears that the plastic of the foil or layer will be allowed to be pressed into or flow into the inter cellular spaces between the cells and/or into the cells in the wall of the product. When drying out or when the solvent has evaporated it will mean a strong bond between the foil or laminate and the product. The said wetting can comprise applying at least one of water and a solvent, especially ethanol or a solvent comprising ethanol, or a mixture of water and such solvent. In embodiments said wetting can for example be done such that at least a surface layer of the relevant wall part and/or a surface layer of the foil or laminate at least partly dissolves or liquidifies, such that when pressed together the foil or laminate adheres to the wall.
As discussed with reference to the drawings examples of an assembly are disclosed for coating a product, comprising a pressure forming unit, a mould or last and a foil or laminate. The product has a wall part having at least partly a cell structure, preferably at least partly an open cell structure, and wherein the product fits in/and or on the last or mould, such that at least the part of the wall having at least partly the cell structure is supported by said last or mould. The pressure forming unit comprises a suction device for sucking air through and/or along said part of the wall having said cell structure and preferably through and/or along said last or mould supporting said wall portion.
In embodiments seeds P can be packed in a product 1 as shown for example in
Examples of batter that can be used for forming products according to this disclosure can for example be found in WO96/30186 or WO98/13184. Purely by way of example an embodiment is further discussed here below as an example. As indicated, this should by no means be understood as limiting for the disclosure.
1000 g potato starch was introduced into a Hobart mixer and under stirring at low speed (position 1) successively 2 g Kelzan S, 2 g hydroxyl apatite, 75 g China clay Spes and 75 g Hydrocarb 90 were added thereto. After all components had been added, mixing occurred for another 15 minutes (position 1). This mixture was introduced into a priorly measured and stirred composition of 1150 g mains water and 22 g rapeseed oil.
After all components had been stirred (position 2) to form a liquid batter, this was introduced into a supply device of an adapted injection-moulding machine. The injection-moulding machine used is of the type EPS-10, of the firm Thermoware of Barneveld. The injection-moulding machine used comprised a mould with ten mould cavities for forming trays, each tray having a size of 150*75*25 mm (L*B*H) and a wall thickness of 2.5 mm. The injection mould comprised electric heating elements and a plunger-injection device with a shut-off thermally uncoupled from the mould. Per mould cavity, approximately 15 cc batter was injected under a pressure of 2 bar and at a temperature of 20° C.
The mould was heated to 210 C, with a temperature tolerance of between 200° C. and 220° C. and the mould was closed with a force of 5 kN per mould cavity. The mould was closed for 120 s and maintained at the required temperature, so that each mould cavity was filled entirely with foamed product. During heating, 98% of the water escaped, substantially in the form of vapour, via vents in the mould, with the water functioning as blowing agent. After 120 s the mould was opened and the injection moulded products were pressed from the mould cavities using the ejectors. The thus formed products were directly ready for use.
Each product had a core of a thickness of approximately 2.4 mm, with an increased density towards opposite side surfaces. Each product had a moisture content of approximately 2% and a weight of 8 g.
In a first example the product 1 as described here above, shaped as a tray as shown in
After cooling of the product with the foil coating the foil was plastically deformed, fitting snugly against the surface of the product and firmly attached to the inside surface of the tray, and to the flange 9 thereof.
A tray as described was taken and a sealing foil was heat sealed over the open top side by heat sealing it to the foil coating on the flange. This packaging was found to be substantially air and moisture tight. The permeation for oxygen, measured after drying at 23° C. was a maximum of 1200 cm3/(m2*d*bar) wherein d is the thickness of the foil. The permeation to water vapor was a maximum of, measured at 23° C. and 85% RH, 135 g/(m2*d). The packaging including the foil was biodegradable.
In a second example a product was formed according to
The invention is by no means limited to the embodiments as shown and/or described in this description. Many variations thereof are possible within the scope of the claims, including at least all combinations of parts and elements of the embodiments and parts thereof shown, in any combination or permutation.
These and other alterations and modifications are supposed to be disclosed within the scope of the claims.
Number | Date | Country | Kind |
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2016056 | Jan 2016 | NL | national |