SUBSTRATE WITH CELLULOSE ACETATE COATING
20190092960 ยท 2019-03-28
Inventors
- Michael COMBS (Pembroke, VA, US)
- Paul BUSBY (Blacksburg, VA, US)
- Melissa ALDRICH-WELCH (Rich Creek, VA, US)
Cpc classification
B05D1/28
PERFORMING OPERATIONS; TRANSPORTING
Y02P20/582
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
C09D5/00
CHEMISTRY; METALLURGY
Abstract
Disclosed are substrates coated with cellulose acetate and methods of forming the coated substrates. The coated substrate may be oil resistant and water resistant. The coated substrate may be used for food packaging.
Claims
1. A coated substrate, comprising: (a) a substrate having one or more surfaces; and (b) a coating layer disposed on at least one of the one or more surfaces, the coating layer comprising a cellulose acetate film having a glass transition temperature (Tg) of at least 140 C.
2. The substrate of claim 1, wherein the coating layer has a thickness from 0.1 to 500 microns.
3. The substrate of claim 1, wherein the coating layer is compostable.
4. The substrate of claim 1, wherein the substrate is compostable.
5. The substrate of claim 1, wherein the coating layer and the substrate are biodegradable.
6. The substrate of claim 1, wherein the substrate comprises cardboard, paper, plastic, fabric, paperboard, or a combination thereof.
7. The substrate of claim 1, wherein the coating layer is oil and water resistant.
8. The substrate of claim 1, wherein the coating layer has a pencil hardness from 6B to 3H.
9. The substrate of claim 1, wherein the substrate is coated with the coating layer on at least a top and bottom surface of the substrate.
10. The substrate of claim 1, wherein the coating layer has heat stability up to at least 150 C.
11. The substrate of claim 1, wherein the coating layer further comprises plasticizer.
12. A method of forming a coated substrate, the method comprising: a) combining cellulose acetate with a solvent to form a coating formulation; b) coating at least one surface of the substrate with the coating formulation; and c) fixing the coating formulation on the substrate to form a coated substrate.
13. The method of claim 12, wherein the coating formulation has a solids concentration from 0.1 to 80%.
14. The method of claim 12, wherein the coating step comprises coating the coating formulation on the substrate in a thickness from 0.1 to 500 microns.
15. The method of claim 12, wherein the coating formulation has a viscosity from 25 to 10000 cps.
16. The method of claim 12, wherein the solvent comprises acetone, n-butyl acetate, ethyl acetate, methyl ethyl ketone, ethyl lactate, methyl amyl ketone, methyl propyl ketone and dimethyl carbonate, aprotic glycol ether, aprotic glycol ether ester, dimethyl sulfoxide (DMSO), n-methyl pyrrolidone (NMP), dimethylacetamide (DMAC), and combinations thereof.
17. The method of claim 12, wherein the coating formulation is coated on the surface of the substrate using spray coating or brushing.
18. The method of claim 12, wherein the coating layer has heat stability up to at least 150 C.
19. The method of claim 12, wherein the coating layer is oil and water resistant.
20. A cellulose acetate coating formulation, the formulation comprising cellulose acetate and a solvent, wherein the formulation has a solids content from 0.1 to 80% and a viscosity from 50 to 10000 cps.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0013] The present invention will be better understood in view of the appended non-limiting figure, in which:
[0014]
[0015]
[0016]
[0017]
DETAILED DESCRIPTION OF THE INVENTION
I. Introduction
[0018] The present disclosure is directed to cellulose acetate coated substrates. The cellulose acetate coating may be disposed on at least one surface of the substrate. The cellulose acetate coating is a film comprising cellulose acetate having a glass transition temperature (Tg) of at least 140 C. The coated substrate may be formed by combining cellulose acetate with a solvent to form a coating formulation. At least one of surface of the substrate may then be coated with the coating formulation. The coating formulation is then fixed onto the substrate to form a coated substrate. The coating formulation may comprise cellulose acetate and a solvent. The formulation may have a solids content from 0.1 to 80% and a viscosity from 50 to 10,000 cps.
II. Cellulose Acetate
[0019] As described herein, the present disclosure involves film coatings comprising cellulose acetate. Cellulose acetate, as used herein, refers to cellulose diacetate. In some aspects, the cellulose acetate has a degree of substitution from 2 to 2.6.
[0020] Cellulose acetate may be prepared by known processes, including those disclosed in U.S. Pat. No. 2,740,775 and in U.S. Publication No. 2013/0096297, the entireties of which are incorporated herein by reference. Typically, acetylated cellulose is prepared by reacting cellulose with an acetylating agent in the presence of a suitable acidic catalyst and then de-esterifying.
[0021] The cellulose may be sourced from a variety of materials, including cotton linters, a softwood or from a hardwood. Softwood is a generic term typically used in reference to wood from conifers (i.e., needle-bearing trees from the order Pinales). Softwood-producing trees include pine, spruce, cedar, fir, larch, douglas-fir, hemlock, cypress, redwood and yew. Conversely, the term hardwood is typically used in reference to wood from broad-leaved or angiosperm trees. The terms softwood and hardwood do not necessarily describe the actual hardness of the wood. While, on average, hardwood is of higher density and hardness than softwood, there is considerable variation in actual wood hardness in both groups, and some softwood trees can actually produce wood that is harder than wood from hardwood trees. One feature separating hardwoods from softwoods is the presence of pores, or vessels, in hardwood trees, which are absent in softwood trees. On a microscopic level, softwood contains two types of cells, longitudinal wood fibers (or tracheids) and transverse ray cells. In softwood, water transport within the tree is via the tracheids rather than the pores of hardwoods. In some aspects, a hardwood cellulose is preferred for acetylating.
[0022] Acylating agents can include both carboxylic acid anhydrides (or simply anhydrides) and carboxylic acid halides, particularly carboxylic acid chlorides (or simply acid chlorides). Suitable acid chlorides can include, for example, acetyl chloride, propionyl chloride, butyryl chloride, benzoyl chloride and like acid chlorides. Suitable anhydrides can include, for example, acetic anhydride, propionic anhydride, butyric anhydride, benzoic anhydride and like anhydrides. Mixtures of these anhydrides or other acylating agents can also be used in order to introduce differing acyl groups to the cellulose. Mixed anhydrides such as, for example, acetic propionic anhydride, acetic butyric anhydride and the like can also be used for this purpose in some embodiments.
[0023] In most cases, the cellulose is exhaustively acetylated with the acetylating agent to produce a derivatized cellulose having a high degree of substitution (DS) value, such as from 2.5 to 3, e.g., about 3, along with some additional hydroxyl group substitution (e.g., sulfate esters) in some cases. Exhaustively acetylating the cellulose refers to an acetylation reaction that is driven toward completion such that as many hydroxyl groups as possible in cellulose undergo an acetylation reaction.
[0024] Suitable acidic catalysts for promoting the acetylation of cellulose often contain sulfuric acid or a mixture of sulfuric acid and at least one other acid. Other acidic catalysts not containing sulfuric acid can similarly be used to promote the acetylation reaction. In the case of sulfuric acid, at least some of the hydroxyl groups in the cellulose can become initially functionalized as sulfate esters during the acetylation reaction. Once exhaustively acetylated, the cellulose is then subjected to a controlled partial de-esterification step, generally in the presence of a de-esterification agent, also referred to as a controlled partial hydrolysis step.
[0025] De-esterification, as used herein, refers a chemical reaction during which one or more of the ester groups of the intermediate cellulosic ester are cleaved from the cellulose acetate and replaced with a hydroxyl group, resulting in a cellulose acetate product having a (second) DS of less than 3. De-esterifying agent, as used herein, refers to a chemical agent capable of reacting with one or more of the ester groups of the cellulose acetate to form hydroxyl groups on the intermediate cellulosic ester. Suitable de-esterifying agents include low molecular weight alcohols, such as methanol, ethanol, isopropyl alcohol, pentanol, ROH, wherein R is C.sub.1 to C.sub.20 alkyl group, and mixtures thereof. Water and a mixture of water and methanol may also be used as the de-esterifying agent. Typically, most of these sulfate esters are cleaved during the controlled partial hydrolysis used to reduce the amount of acetyl substitution. The reduced degree of substitution may range from 0.5 to 2.9, e.g., from 1.0 to 2.8, from 1.5 to 2.9, or from 2 to 2.6. The degree of substitution may be selected based on an organic solvent to be used with the cellulose acetate in the coating process. For example, when acetone is used as an organic solvent, the degree of substitution may range from 2.2 to 2.65.
[0026] The number average molecular weight of the cellulose acetate may range from 30,000 amu to 100,000 amu, e.g., from 50,000 amu to 80,000 amu and may have a polydispersity from 1.5 to 2.5, e.g., from 1.75 to 2.25 or from 1.8 to 2.2. All molecular weight recited herein, unless otherwise specified, are number average molecular weights. The molecular weight may be selected based on the desired hardness of the final wood filler composition. Although greater molecular weight leads to increased hardness, greater molecular weight also increases viscosity. The cellulose acetate may be provided in powder or flake form.
[0027] In some aspects, blends of different molecular weight cellulose acetate flake or powder may be used. Accordingly, a blend of high molecular weight cellulose acetate, e.g., a cellulose acetate having a molecular weight above 60,000 amu, may be blended with a low molecular weight cellulose acetate, e.g., a cellulose acetate having a molecular weight below 60,000 amu. The ratio of high molecular weight cellulose acetate to low molecular weight cellulose acetate may vary but may generally range from 1:10 to 10:1; e.g., from 1:5 to 5:1 or from 1:3 to 3:1.
III. Cellulose Acetate Coating and Preparation Thereof
[0028] The cellulose acetate described herein may be prepared as a film. In some embodiments, the film can have a thickness from 0.1 micron to 500 micron, e.g., from 0.5 to 500 micron, from 1 micron to 400 micron, from 1 to 300 micron, from 1 to 250 micron, from 1 to 100 micron, from 10 to 100 micron, from 0.5 to 100 micron, from 0.5 to 10 micron. Pure cellulose acetate is difficult to process as a raw material because its decomposition temperature is lower than melt-processing temperatures. One optional solution to this problem is to use plasticizers. Combining a plasticizer with cellulose acetate reduces interactions between segments of the cellulose acetate polymer chain and reduces the glass transition temperature, melt viscosity and elastic modulus of the cellulose acetate, making the plasticized cellulose acetate melt processable.
[0029] Generally, the cellulose acetate film comprises from 55 to 100 wt. % cellulose acetate, based on the total weight of the film, e.g., from 55 to 99.5 wt. %, from 60 to 95 wt. %, from 65 to 90 wt. %, or from 70 to 85 wt. %.
[0030] In some embodiments, the cellulose acetate film does not contain shellac. In some embodiments, the cellulose acetate film does not contain rosin. In some embodiments, the cellulose acetate film does not contain shellac or rosin. Thus, the cellulose acetate films in certain embodiments are not shellac or rosin based.
[0031] In embodiments, plasticizer may be present from 0 to 40 wt. % based on the total weight of the film, e.g., from 1 to 35 wt. %, from 5 to 30 wt. %, or from 10 to 25 wt. %. The percentage of plasticizer may vary depending on the method by which the cellulose acetate film is formed. Generally, a greater weight percentage of plasticizer is used to form the film by melt extrusion as compared to solvent casting, e.g., from 15 to 40 wt. %, from 20 to 40 wt. %, or from 25 to 35 wt. % for melt extrusion and from 0.5 to 25 wt. %, e.g., from 1 to 25 wt. %, from 5 to 25 wt. %, or from 10 to 25 wt. % for solvent casting.
[0032] Various plasticizers may be used to reduce the glass transition temperature of cellulose acetate. Manufacturers of cellulose acetate may choose the type and amount of plasticizer (e.g., the ratio of plasticizer to cellulose acetate) based on a number of factors including the desired properties of a final composition and/or chosen for compatibility with other components of a final composition. For example, some types of plasticizers may be selected because they are biodegradable, allowing for the plasticized cellulose acetate to be eco-friendly. The amount of plasticizer may be chosen to: (i) reduce the glass transition temperature of the cellulose acetate (e.g., too low a plasticizer content may not reduce the glass transition temperature enough to allow for melt processing) and (ii) maintain desirable mechanical properties of the cellulose acetate (e.g., too high a plasticizer content may reduce the tensile strength and/or the thermal stability of a final composition).
[0033] Although a wide variety of plasticizers are known for plasticizing cellulose acetate, including those described in US Pub. No. 2015/0351311, a food grade plasticizer is preferred. For example, phthalates, phosphorus, and chlorinated plasticizers may be prohibited. As used herein, the term food grade refers to a material that has been approved for contacting (directly or indirectly) food, which may be classified as based on the material's conformity to the requirements of the United States Pharmacopeia (USP-grade), the National Formulary (NF-grade), and/or the Food Chemicals Codex (FCC-grade) as of Apr. 30, 2017. Food grade plasticizers include triacetin, diacetin, tripropionin, trimethyl citrate, triethyl citrate, tributyl citrate, eugenol, cinnamyl alcohol, alkyl lactones (e.g., -valerolactone), methoxy hydroxy acetophenone (acetovanillone), vanillin, ethylvanillin, polyethylene glycols, 2-phenoxyethanol, glycol ethers, ethylene glycol ethers, propylene glycol ethers, polysorbate surfactants, sorbitan ester surfactants, polyethoxylated aromatic hydrocarbons, polyethoxylated fatty acids, polyethoxylated fatty alcohols, and combinations thereof. In further embodiments, the plasticizer is triacetin. In still further aspects, the plasticizer does not contain a phthalate (is phthalate-free). In some embodiments, no plasticizer is used. In some embodiments, an amide wax is used. Yet, in some embodiments, neither plasticizer nor amide wax is used.
[0034] As discussed, the film also optionally comprises a processing aid. When included, the processing aid may be present in an amount from 0.05 to 10 wt. % based on the total weight of the film, e.g., from 0.1 to 5 wt. % , or from 0.5 to 2.5 wt. %. The processing aid may be selected from the group consisting of titanium dioxide, aluminum oxide, zirconium oxide, silicon dioxide, calcium carbonate, calcium silicate, aluminum silicate, magnesium silicate, calcium phosphate and mixtures thereof. In some embodiments, the processing aid is silica. The average particle size of the processing aid may vary. In some aspects, the processing aid may have an average particle size from 0.01 to 50 m, e.g., from 0.02 microns to 40 microns, from, from 0.05 microns to 30 microns. The particle size may be determined, for example, by sieve analysis. In some embodiments, no processing aid is used.
[0035] A releasing agent may also be included in order to improve releasability of the film, once formed, from a backing sheet or substrate. When included, the releasing agent may be present from 0.01 to 10 wt. % based on the total weight of the film, e.g., from 0.05 to 5 wt. %, from 0.05 to 1 wt. %, or from 0.05 to 0.5 wt. %. The releasing agent is generally included when the film is solvent cast, and is added to the dope. In some embodiments, the releasing agent is a fatty acid, such as stearic acid. In some embodiments, no releasing agent is used. In some embodiments, no plasticizer, processing aid, or releasing agent is used.
[0036] Some embodiments contain other additives. For example, embodiments can contain any of dyes, pigments, fragrances, repellants, indicators, surface agents, adhesion promoters, and/or gloss enhancers.
[0037] In embodiments, the coating layer may be either biodegradable, compostable (for example according to EN 13432), or both. For example, in an embodiment, the coating layer is compostable at a thickness of less than 125 m, e.g., less than 100 m, less than 80 m, less than 50 m, less than 30 m.
[0038] In embodiments, the coating layer is water resistant, as determined by directly contacting the coating layer with liquid water. Substrate discoloration and/or breakthrough can be measured as a function of time. If the coated substrate does not show discoloration or breakthrough after 1 hour of exposure, the coating layer is considered to be water resistant. In embodiments, the coating layer is water resistant, as determined by direct contact with oil, for example corn oil. Substrate discoloration and/or breakthrough can be measured as a function of time. If the coated substrate does not show discoloration or breakthrough after 1 hour of exposure, the coating layer is considered to be oil resistant. In embodiments, the coating layer is both oil and water resistant.
[0039] In embodiments, the coating layer may maintain heat stability up to at least 150 C. In other embodiments, the coating layer may maintain heat stability up to at least 180 C. Heat stability means that the coating layer maintains integrity and function at the given temperature.
[0040] In embodiments, the film of the coating layer may have a glass transition temperature of at least 140 C. , e.g., at least 160 C., at least 180 C., at least 195 C., or at least 200 C., or from 140 C. to 200 C., or from 140 C. to 170 C., or from 140 C. to 150 C. In other embodiments, the film of the coating layer may be glossy or matte, as determined by visual inspection and by standard 20, 60 and 85 measurements. In some aspects, the film is glossy or high gloss. In other aspects, the film is matte. Without being bound by theory, it is believed that the surface area of the film is increased when the film is matte. In some embodiments, additional components may be added to the film. Such components include a matting agent, though such agent is not necessary to provide a matte film. In some aspects, the matte surface is imparted by the casting or extrusion process. In other aspects, an embossing roller may be used.
[0041] In embodiments, the coating layer may have a pencil hardness from 6B to 3H according to ASTM D3363 (2011). For example, the coating layer may have a pencil hardness of 6B, or of 5B, or of 4B, or of from 4B to 3H, or of 3B, or from 3B to 3H, or of 2B, or of from 2B to 2H, or of B, or of HB, or of from HB to 2H, or of from 6B to HB, or of F, or of from F to 3H, or of from 5B to F, or of H, or of from H to 3H, or of from 6B to H, or of 2H, or of from 5B to 2H, or of 3H.
[0042] The films and coatings of the present invention are can provide good hand feel and high visual appeal. In addition, the films and coatings can possess smoothness and not be cold to the touch.
[0043] The cellulose acetate film may be prepared by any film coating method known in the art. Examples of embodiments are is described below.
Melt Extrusion
[0044] For melt extrusion, cellulose acetate and any optional components, such as a plasticizer, and/or a processing aid, are combined. The mixture may be formed by combining cellulose acetate, in flake or powder form, with the optional plasticizer and/or processing aid. In some embodiments, the optional plasticizer and/or processing aid may be combined with the cellulose acetate using a spray distribution system during the mixing step. In other embodiments, the optional plasticizer and/or processing aid may be added to the cellulose acetate during the mixing step, either continuously or intermittently. In some embodiments, the powder form of cellulose acetate is preferred while in other embodiments cellulose acetate flake may be used. Without being bound by theory, it is believed that the powder form may lead to a sheet with improved plasticization and uniformity as compared to the flake form.
[0045] After forming the mixture comprising cellulose acetate, plasticizer and optional processing aid, the mixture may be melt extruded in a small hole die to form filaments which are then sent to a pelletizer to form pellets. The melt extrusion may be performed at a temperature from 165 to 230 C., e.g., from 165 to 220 C. or from 165 to 210 C. The melt extruder may be a twin screw feeder with co-rotating screws, and may be operated at a screw speed from 100 to 500 rpm, e.g., from 150 to 450 rpm, or from 250 to 350 rpm. The pellets may then be extruded to form a film. In an embodiment, the film can also be extruded directly onto the substrate. The film may then be dried. In another embodiment, once dried, the film may then be crimped using a crimper.
Solvent Based Preparations
[0046] Processes for preparing cellulose acetate films by using solvent, such as solvent casting, have been described in U.S. Pat. Nos. 2,232,012 and 3,528,833, the entireties of which are incorporated by reference herein. In general, a solvent process comprises preparing a mixture, also referred to as a dope, comprising cellulose acetate dissolved in a solvent, e.g., acetone and optionally plasticizer, processing aid, and/or releasing agent. The components of the mixture and the respective amounts determine the characteristics of the film, which is discussed herein.
[0047] As noted, the dope may be prepared by dissolving cellulose acetate in a solvent. In some embodiments, the solvent is acetone. In one embodiment, the solvent is selected from the group consisting of ethyl lactate, methyl ethyl ketone, and dichloromethane. In another embodiment, the solvent comprises acetone, ethyl acetate, methyl ethyl ketone, ethyl lactate, methyl amyl ketone, methyl propyl ketone and dimethyl carbonate, aprotic glycol ether, aprotic glycol ether ester, dimethyl sulfoxide (DMSO), n-methyl pyrrolidone (NMP), dimethylacetamide (DMAC), or combinations thereof. In embodiments, 2-propanol can be added to the solvent. To improve the solubility of cellulose acetate in the solvent, the cellulose acetate and the solvent may be continuously added to a first mixer. The mixture may then be sent to a second and/or third mixer to allow for full dissolution of the cellulose acetate in the solvent. The mixers may be continuous mixers that are used in series. It is understood that in some embodiments, one mixer may be sufficient to achieve cellulose acetate dissolution. In other embodiments, two, three, or more mixers (e.g., four mixers, five mixers, or greater than five mixers) may be used in series or in parallel. In yet other embodiments, the cellulose acetate, solvent, and other additives may be combined in one or more blenders, without the use of any mixers.
[0048] The dope may then be dried to evaporate the solvent to prepare a film. The dope can be cast directly on the substrate to form the coating. The inclusion of a releasing agent can improve the release of the film from the casting band. The film may dried and crimped as described above.
[0049] Thus, in one embodiment, a method of forming a coated substrate is to a) combine cellulose acetate with a solvent to form a dope or coating formulation, b) coating at least one surface of the substrate with the coating formulation, c) processing the coating formulation on the substrate to form the coated substrate.
[0050] In embodiments, the dope can have a solids concentration of 0 to 80%, e.g., 0 to 60%, 0 to 50%, 0 to 40%, 0.1 to 80%, 0.1 to 50%, 0.1 to 40%, 1 to 30%, 1 to 20%, 5 to 20%, 5 to 15%, or 15%.
[0051] In embodiments, the dope can have a viscosity from 25 to 10,000 centipoise (cps) (mPa.Math.s), e.g., 25 to 8,000 cps, 30 to 5,000 cps, 50 to 1,000 cps, or 100 to 500 cps. In one embodiment, the dope can have a solids concentration from 0.1 to 80% and a viscosity from 50 to 10,000 cps.
[0052] In addition to casting as described above, the mixed cellulose acetate dissolved in solvent (dope) can be applied as a coating using a number of methods. For example, the dope can be applied as a brush coating where the dope is applied on the surface of the substrate by means of brushes. In addition, the dope can be applied to the surface of the substrate as a spray coating by means of a spraying device. Other methods include roll coating and gravure coating where the dope is applied to the substrate using rollers (an engraved roller in the case of gravure coating). Another process that can be used is curtain coating, where an uninterrupted curtain of dope falls through from a gap onto the surface of the substrate. The speed of the substrate (for example, on a conveyor belt) is controlled to provide an even coat of the dope, if desired. Similarly, the coating can be formed by using a dip coating method. In this method the substrate is immersed in a tank of the dope and continuously moved through at a constant speed. A thin layer of the dope deposits on the substrate when it is withdrawn from the tank of dope. The thickness of the coating can be adjusted based on the speed of the substrate. In addition, if desired for the final product, the thickness can be varied across the substrate. For any of the above methods, the film can be dried to remove the solvent.
Substrate
[0053] In embodiments, the compositions of the present invention can be used in food related applications, such as to package, support, or contain food items. In other embodiments, the compositions of the present invention can be used in non-food related applications. In embodiments, the compositions of the present invention can be used where biodegradability or compostability is desired.
[0054] Substrates used in the invention can be chosen from a variety of materials. In embodiments, the substrate can be cardboard, paper, plastic, fabric, paperboard, or combinations thereof. In embodiments, the substrate can be made of Styrofoam. In embodiments, the substrate can be biodegradable. In embodiments, the substrate can be compostable, for example Home and Industrial compostable. In embodiments, the substrate can be made of recycled material(s). For example, the substrate can be made of recycled cardboard, recycled paper, recycled plastic, recycled paperboard, or combinations thereof. In one embodiment, the substrate can be made of recycled cardboard. However, in some embodiments, the substrate is neither compostable nor biodegradable.
[0055] Embodiments of the present invention can be used in direct or indirect food contact packaging applications requiring liquid barrier protection. In embodiments, the coated substrate can be used in food packaging or food containers. For example, in one embodiment, the coated substrate can be used in food trays. In embodiments, the coated substrate can be used in drink cups, fast food service containers, drink holders or coasters. In other embodiments, the coated substrates can be used in non-food applications. For example, the coated substrate can be used in posters and billboards, envelopes, or notebook covers.
[0056] The substrate can have one or more surfaces. The coating can be applied to at least one of the one or more surfaces. For example, the coating can be applied to a top surface or a bottom surface of the substrate.
[0057]
[0058]
[0059] In some embodiments, the coating can be of different thicknesses. For example, the coating can be thicker in some sections than others.
[0060] In some embodiments, the coating can be at least 10% thicker at the edges of the substrate than at the middle of the substrate, e.g., 10% thicker at the edges of the substrate than at the middle of the substrate, at least 20% thicker at the edges of the substrate than at the middle of the substrate, at least 30% thicker at the edges of the substrate than at the middle of the substrate, at least 50% thicker at the edges of the substrate than at the middle of the substrate, at least 80% thicker at the edges of the substrate than at the middle of the substrate, at least 100% thicker at the edges of the substrate than at the middle of the substrate, at least 200% thicker at the edges of the substrate than at the middle of the substrate, or between 10% and 200% thicker at the edges of the substrate than at the middle of the substrate.
[0061] In some embodiments, the coating can be applied to achieve at least a 2% gradient from its thinnest point to its thickest point, for example, at least a 3% gradient from its thinnest point to its thickest point, at least a 5% gradient from its thinnest point to its thickest point, at least an 8% gradient from its thinnest point to its thickest point, at least a 10% gradient from its thinnest point to its thickest point, at least a 15% gradient from its thinnest point to its thickest point, at least a 20% gradient from its thinnest point to its thickest point, at least a 30% gradient from its thinnest point to its thickest point, or from a 3% gradient to a 25% gradient from its thinnest point to its thickest point.
[0062] In certain embodiments, the coating layer does not penetrate into the substrate. In other embodiments, the coating layer does penetrate into the substrate. For example, the coating layer can penetrate into the substrate to a depth of 0.5 m to 800 m, e.g., 1 m to 500 m, 10 m to 500 m, 100 m to 500 m, or 100 m to 300 m.
[0063] The present invention will be better understood in view of the following non-limiting example.
EXAMPLE
Example 1
[0064] A solution of cellulose acetate in acetone with a 15% solids concentration was applied to a substrate of recycled cardboard and dried to form food trays. The color was observed as white to slight yellow. The coated food trays were exposed to direct contact with corn oil. Substrate discoloration and/or breakthrough were measured as a function of time. The coated food trays did not exhibit discoloration or breakthrough after 7 weeks of constant exposure. The food trays were also exposed to direct contact with liquid water. The food trays did not show any discoloration or breakthrough after 1 week of constant exposure. The coated food trays also had the following performance: Heat stability of up to 150 C. Tg of the coating of 195 C.
[0065] While the invention has been described in detail, modifications within the spirit and scope of the invention will be readily apparent to those of skill in the art. It should be understood that aspects of the invention and portions of various embodiments and various features recited above and/or in the appended claims may be combined or interchanged either in whole or in part. In the foregoing descriptions of the various embodiments, those embodiments which refer to another embodiment may be appropriately combined with other embodiments as will be appreciated by one of ordinary skill in the art. Furthermore, those of ordinary skill in the art will appreciate that the foregoing description is by way of example only, and is not intended to limit the invention. All US patents cited herein are incorporated by reference in their entirety.