Patent Description:
Conventional approaches to preventing degradation, maintaining quality, and increasing the life of agricultural products include refrigeration and/or special packaging. Refrigeration requires capital-intensive equipment, demands constant energy expenditure, can cause damage or quality loss to the product if not carefully controlled, must be actively managed, and its benefits are lost upon interruption of a temperature-controlled supply chain. Special packaging can also require expensive equipment, consume packaging material, increase transportation costs, and require active management. Despite the benefits that can be afforded by refrigeration and special packaging, the handling and transportation of the agricultural products can cause surface abrasion or bruising that is aesthetically displeasing to the consumer and serves as points of ingress for bacteria and fungi. Moreover, the expenses associated with such approaches can add to the cost of the agricultural product.

The cells that form the aerial surface of most plants (such as higher plants) include an outer envelope or cuticle, which provides varying degrees of protection against water loss, oxidation, mechanical damage, photodegradation, and/or biotic stressors, depending upon the plant species and the plant organ (e.g., fruit, seeds, bark, flowers, leaves, stems, etc.). Cutin, which is a biopolyester derived from cellular lipids, forms the major structural component of the cuticle and serves to provide protection to the plant against environmental stressors (both abiotic and biotic). The thickness, density, as well as the composition of the cutin (i.e., the different types of monomers that form the cutin and their relative proportions) can vary by plant species, by plant organ within the same or different plant species, and by stage of plant maturity. The cutin-containing portion of the plant can also contain additional compounds (e.g., epicuticular waxes, phenolics, antioxidants, colored compounds, proteins, polysaccharides, etc.). This variation in the cutin composition as well as the thickness and density of the cutin layer between plant species and/or plant organs and/or a given plant at different stages of maturation can lead to varying degrees of resistance between plant species or plant organs to attack by environmental stressors (i.e., water loss, oxidation, mechanical injury, and light) and/or biotic stressors (e.g., fungi, bacteria, viruses, insects, etc.).

<CIT>) discloses the depolymerization of suberin and cutin using sulfuric acid and methanol to yield fatty acid esters.

The invention is set out in the appended claims and relates generally to methods to isolate cutin-derived monomers, oligomers, and/or their esters, and mixtures thereof, in particular for applications in agricultural coating formulations. More specifically, it is directed to methods of preparing compositions of fatty acid esters by treating crosslinked polyesters with an acid concurrently with an alcohol.

In particular, the invention provides a method of preparing a composition comprising fatty acid esters that includes providing a crosslinked polyester comprising polymerized fatty acids, treating the crosslinked polyester with an acid concurrently with an alcohol, at a temperature above <NUM> up to <NUM> and removing the acid and the alcohol to form a mixture comprising the fatty acid esters and purifying the mixture to form a purified isolate of fatty acid esters.

The crosslinked polyester can be naturally occurring. The crosslinked polyester can be derived from plant matter. The crosslinked polyester can be cutin. The cutin can be derived from plant skins. Treating the crosslinked polyester with the acid concurrently with the alcohol can include suspending or dissolving the crosslinked polyester and the acid in the alcohol to form a solution. The acid can be a strong acid. A concentration of the acid in the solution can be greater than <NUM>µmol/L. The solution can further comprise a non-reactive secondary solvent.

The crosslinked polyester can contain endogenous water. Heating the crosslinked polyester, the acid, and the alcohol at a temperature above <NUM> up to <NUM> can comprise refluxing the polyester, the acid, and the alcohol at the boiling point of the alcohol. The polyester, the acid, and the alcohol can be heated in a sealed vessel above the boiling point of the alcohol. The alcohol can comprise ethanol, methanol, propanol, glycerol, isopropanol, or combinations thereof. The alcohol can be a primary or secondary alcohol. Removing the acid can comprise neutralizing the acid. Removing the alcohol can comprise evaporating the alcohol.

The acid can be sulfuric acid, triflic acid, hydrochloric acid, hydrobromic acid, hydroiodic acid, para-toluenesulfonic acid, or a combination thereof. The acid can be catalytic. The acid can be utilized in superstoichiometric amounts. A molar ratio of the alcohol to the fatty acids can be greater than <NUM>. The fatty acids of the crosslinked polymer can comprise <NUM>-hydroxy hexadecanoic acid, <NUM>,<NUM>-dihydroxyhexadecanoic acid, <NUM>,<NUM>-dihydroxyhexadecanoic acid, <NUM>-hydroxysteric acid, <NUM>-hydroxy-(<NUM>)-octadec-<NUM>-enoic acid, <NUM>,<NUM>-epoxy-<NUM>-hydroxy octadecanoic acid, <NUM>,<NUM>,<NUM>-trihydroxyoctadecanoic acid, or a combination thereof. The resulting fatty acid esters can comprise ethyl <NUM>-hydroxyhexadecanoate, ethyl <NUM>,<NUM>-dihydroxyhexadecanoate, ethyl <NUM>,<NUM>-dihydroxyhexadecanoate, ethyl <NUM>-hydroxyoctadecanoate, ethyl <NUM>-hydroxy-(<NUM>)-octadec-<NUM>-enoate, ethyl <NUM>,<NUM>-epoxy-<NUM>-hydroxyoctadecanoate, ethyl <NUM>,<NUM>,<NUM>-trihydroxyoctadecanoate, or a combination thereof.

The method can be characterized as only requiring a single step to obtain the resulting fatty acid esters from the crosslinked polyester. The fatty acid esters formed can be applied to the surface of a substrate to form a protective coating. The substrate can be an edible substrate. The substrate can be a piece of produce. The substrate can be plant matter.

The biopolyester cutin forms the main structural component of the cuticle that composes the aerial surface of most land plants and plays a significant role in providing plants a protective barrier against both abiotic and biotic stressors. The thickness, density, as well as the composition of the cutin (i.e., the different types of monomers that form the cutin and their relative proportions) can vary by plant species, by plant organ within the same or different plant species, and by stage of plant maturity. These variations can define the amount, degree, or quality of protection (and degree of plasticity) offered by the cutin layer to the plant or plant organ against environmental and/or biotic stressors. Cutin is formed from a mixture of polymerized mono- and/or polyhydroxy fatty acids and embedded cuticular waxes. Among the hydroxy fatty acids, polyhydroxy fatty acids (e.g., dihydroxy fatty acids or trihydroxy fatty acids), once esterified, can in some cases form tightly bound networks with high crosslink density and lower permeability as compared to monohydroxy fatty acids and can thereby provide better protection against environmental stressors.

Described herein are methods of preparing plant extract compositions that include fatty acid esters (monomers and/or their oligomers) derived from cutin or other crosslinked polyesters. In particular, methods described herein allow for generation of fatty acid esters directly by treating a crosslinked polyester (e.g., cutin) which includes a mixture of polymerized mono- and/or polyhydroxy fatty acids with an acid concurrently with an alcohol. Compositions which include the resulting fatty esters can, for example, be subsequently applied to other plant or agricultural products in order to form a protective material (e.g., a coating) over the products, or to enhance or modify existing coatings (either naturally occurring or deposited coatings) which are on the outer surface of the products. The applied coatings can, for example, serve to protect the products from biotic stressors such as bacteria, fungi, viruses, and/or pests. The applied coatings can also (or alternatively) serve to increase the shelf life of produce without refrigeration, and/or to control the rate of ripening or respiration of produce.

Conventional methods for producing fatty acid esters typically involve performing a first step (or series of steps) to isolate fatty acids (e.g., fatty acid monomers and/or oligomers) and then subsequently perform a second step (or series of steps) to convert the fatty acids to esters, for example via Fischer esterification. Methods described herein provide for a process for generating fatty acid esters directly from a polyester such as cutin, without the need to first isolate the fatty acid monomers/oligomers. A method of preparing a composition comprising fatty acid esters in accordance with the invention includes (i) providing a crosslinked polyester (e.g., cutin) comprising polymerized fatty acids, (ii) treating the polyester with an acid concurrently with an alcohol, at a temperature above <NUM> up to <NUM> and (iii) removing the acid and alcohol to form a mixture comprising the fatty acid esters and purifying the mixture to form a purified isolate of fatty acid esters. In particular embodiments described herein, the crosslinked polyester is cutin derived from plant matter.

As used herein, "plant matter" refers to any portion of a plant, including, for example, fruits (in the botanical sense, including fruit peels and juice sacs), leaves, stems, barks, seeds, flowers, peels, or roots.

A first method <NUM> for treating (e.g., depolymerizing) cutin to obtain a plant extract composition is illustrated in <FIG>. Method <NUM> is intended to be illustrative only and is not part of the invention as claimed. The method <NUM> includes first treating plant matter to at least partially separate a cutin-containing portion from a non-cutin-containing portion of the plant matter (step <NUM>). Treating the plant matter can include, for example, thermal treating of the plant matter. The thermal treating can include, for example, heating the plant matter (e.g., with steam, in water or in another solvent), freezing the plant, subjecting the plant matter to cyclic thermal treatments, or drying. The plant matter can include any suitable plant matter or other agricultural product such as, for example, fruits (including fruit peels and juice sacs), leaves, stems, barks, seeds, flowers, peels, or roots. The plant matter can include agricultural waste products such as, for example, tomato peels, grape skins, apple peels, pepper peels, lemon peels, lemon leaf, lime peels, lime leaf, orange peels, orange leaf, orange fruit, clementine leaf, clementine fruit, mandarin leaf, mandarin fruit, pea seeds, grapefruit peels, grapefruit leaf, grapefruit seeds, papaya peels, cherry fruits, cranberry skins, coffee cherries, grass clippings, or any other plants or portions of plants that can yield any embodiment of the plant extract compositions described herein. The plant matter can be a fruit (e.g., a tomato, cranberry, or grape) and the cutin-containing portion can be a peel of the fruit (e.g., a tomato peel or cranberry skin or grape skin) such that the boiling can at least partially separate the peel from the fruit. The fruit can be washed to remove surface residue, waxes, or other debris before operation <NUM>. Furthermore, the fruit can be cut into halves, quarters, or small pieces or ground to finer pieces and then boiled until the peels or skins are visibly separated from the fruit pulp.

The method <NUM> can optionally include mechanically processing the plant matter to at least partially separate the cutin-containing portion from the non-cutin-containing portion of the plant matter (step <NUM>). The mechanical process can be performed before and/or after thermal treatment of the plant matter (i.e., <NUM>) (e.g., boiling of the plant matter in water) to facilitate separation of the cutin-containing portion from the non-cutin-containing portion of the plant matter. Suitable mechanical processes can include, for example, centrifugation, (ultra)sonication, pressing, ball milling, grinding, etc. Mechanical separation can include separating a fruit peel from the fruit pulp. Mechanical removal of the pulp might not be performed and the fruit skins (e.g., waste fruit skins left over after processing of the fruit) may be macerated, blended, cut, shredded, food processed, or otherwise subjected to some other mechanical treatment operation to physically break down the fruit skins into smaller or finer pieces. A plurality of intermediate mechanical processes can be used to obtain the plant extract composition. For example, a mechanical step can be used to separate the cutin from the non-cutin-containing portion, as described herein, or be used to augment any other operation included in the method <NUM>. Such mechanical processes can include any of the mechanical processes described herein such as, for example, centrifugation, sonication, (ultra)sonication, milling, grinding, filtration, etc..

The cutin-containing portion is then optionally heated (e.g., boiled) in a mixture of ammonium oxalate and oxalic acid to separate the cutin from the non-cutin-containing portion (step <NUM>). Optionally this process can also be achieved (or assisted) using enzymes capable of breaking down polysaccharides or pectin. For example, the cutin can include the cuticular layer of the plant matter. The heating in the ammonium oxalate and oxalic acid mixture disrupts the pectinaceous glue that attaches the cuticle to the underlying cells of the plant matter and helps release the cuticle. Furthermore, this step disrupts the pectinaceous glue that is found within primary cell walls and between plant cells (e.g., in the middle lamella that binds neighboring cells), aiding in the isolation of a cutin-containing portion. In this manner, the ammonium oxalate and oxalic acid solution can facilitate at least partial chemical detachment of remaining debris from the cutin-containing portion of the plant (e.g., removal of any remaining pulp from the fruit peel). The heating can be performed at any suitable temperature (e.g., <NUM> degrees Celsius, <NUM> degrees Celsius, <NUM> degrees Celsius, <NUM> degrees Celsius, <NUM> degrees Celsius, <NUM> degrees Celsius, <NUM> degrees Celsius, <NUM> degrees Celsius, <NUM> degrees Celsius, <NUM> degrees Celsius, <NUM> degrees Celsius, or <NUM> degrees Celsius, inclusive of all ranges and values therebetween) and for any suitable time (this process can be accelerated if carried out under elevated pressure). For example, the cutin-containing portion can be heated in the mixture of ammonium oxalate and oxalic acid at a temperature of about <NUM> degrees Celsius for about <NUM> hours. The portion of the plant, for example, the fruit peel, after treatment with the ammonium oxalate and oxalic acid solution, can be isolated by filtration and dried (e.g., air-dried under ambient conditions, oven-dried or freeze-dried) to remove any residual water.

The cutin can optionally be treated with an enzyme (step <NUM>). For example, the cutin can be treated with an enzyme such as a carbohydrate-hydrolyzing enzyme to digest or otherwise remove carbohydrates (e.g., cellulose or pectin) attached to or embedded within the cutin. Such enzymes can include, for example, naturally derived or synthetic cellulases, pectinases, and hemicellulases. The enzymatic degradation can be used before, after, or otherwise in place of step <NUM> to obtain the cutin from the non-cutin-containing portion. The reverse process may be employed, wherein the cutin is treated with an enzyme that can at least partially depolymerize the cutin to yield any combination of cutin-derived oligomers and cutin-derived monomers and to leave behind the non-cutin-containing components, which could be filtered out or otherwise separated. Such enzymes can include, for example, cutinases, esterases, or lipases.

Optionally, the cutin is refluxed or subjected to soxhlet extraction in at least one suitable solvent (e.g., chloroform and/or methanol) to remove soluble waxes or polar impurities from the cutin (step <NUM>). For example, the cutin can be refluxed or subjected to soxhlet extraction only in chloroform, refluxed or soxhlet extracted in chloroform followed by refluxing or soxhlet extraction in methanol, refluxed or subjected to soxhlet extraction only in methanol, or refluxed or subjected to soxhlet extraction in a mixture of chloroform and methanol, or any other suitable solvent(s) (or combinations thereof) in which the wax and/or polar components are soluble. The cutin can be refluxed in a dilute solution of a strong base (e.g., potassium hydroxide in water or in alcoholic solvent), or a solution of a moderately strong or weak base (e.g., potassium carbonate in water or in alcoholic solvent) to remove soluble pigmented impurities. Alternatively, removal of residual waxes and remaining soluble components can be achieved using supercritical CO<NUM> or supercritical H<NUM>O. The refluxing can be performed at any suitable temperature and for any suitable length of time. For example, the cutin can be refluxed in chloroform at about <NUM>-<NUM> degrees Celsius for about <NUM>-<NUM> hours to remove any wax and/or non-polar compounds embedded in the cutin. This can be followed by refluxing in methanol at <NUM>-<NUM> degrees Celsius for about <NUM>-<NUM> hours, for example, to remove any polar organic components (e.g., flavonoids and flavonoid glycosides) present in the cutin. The completion of the operation can be determined by the clarity of solvents. For example, the process can be monitored with instrumentation (e.g., NMR, GC-MS, React-IR, FTIR, spectrophotometry, etc.) configured to analyze the clarity of the solvents and can continue until a predetermined clarity is achieved. Each of the chloroform and/or methanol extraction processes can be performed in any apparatus capable of refluxing (i.e., recirculating and/or recycling) the solvents such as, for example, a reaction flask equipped with a condenser, a Soxhlet apparatus, a Kumagawa extractor, an ultrasound assisted extractor, a robot automated extractor, or any other suitable extraction apparatus. Such an apparatus can, for example, reduce the amount of solvent used in the extraction process. Any other solvent or combinations thereof (i.e., a binary or ternary mixture) can be used to wash out undesired impurities. Suitable solvents can include, for example, diethyl ether, dichloromethane, hexane, petroleum ether, ethyl acetate, acetone, isopropanol, ethanol, acetonitrile, supercritical carbon dioxide, supercritical water, water, and mixtures thereof. Multiple extraction steps in one or more solvents can also be performed. Intermediate enzymatic treatment steps can also be performed between the solvent extraction processes, for example, to liberate undesired compounds from the cutin. The solution obtained after operation <NUM> can include a relatively pure sample of the cutin included in the portion of the plant along with any residually attached or embedded polysaccharides (e.g., cellulose), plant metabolites (e.g., flavonoids), and/or proteins.

The cutin is then heated in a base solution (e.g., metal alkoxide or metal hydroxide dissolved in a solvent such as ethanol or methanol or water or combinations thereof) to at least partially depolymerize the cutin and obtain a plant extract including a plurality of cutin-derived monomers, oligomers, or combinations thereof (step <NUM>). The pH of the solution can, for example, be in a range of about <NUM> to <NUM>, for example in a range of <NUM> to <NUM>. The metal alkoxide can include, for example, sodium methoxide, sodium ethoxide, sodium iso-propoxide, sodium n-propoxide, sodium iso-butoxide, sodium n-butoxide, potassium methoxide, potassium ethoxide, potassium iso-propoxide, potassium n-propoxide, potassium iso-butoxide, or potassium n-butoxide. The metal hydroxide can include, for example, Group I or Group II metal hydroxides, such as lithium, sodium, potassium, calcium, rubidium, or cesium hydroxide. Also included are precursors or compounds that will generate alkoxide or hydroxide in a suitable reaction medium (such as neat metals (e.g., sodium metal) or oxides in methanol, or ammonia in water). Refluxing of the cutin in the presence of the metal alkoxide or metal hydroxide can be performed at any suitable temperature and for any suitable length of time such as, for example, at about <NUM> degrees Celsius for about <NUM> hours. The temperature and/or the refluxing time can be such that the cutin is only partially depolymerized to yield a predetermined combination of oligomers and monomers. The temperature and/or the refluxing time can be adjusted such that the cutin is mostly depolymerized by the metal alkoxide or metal hydroxide into a plurality of cutin-derived monomers and/or oligomers. The refluxing in the metal alkoxide or metal hydroxide can be performed in a mixture of the metal alkoxide or metal hydroxide and a solvent, for example, methanol, ethanol, hexane, toluene, etc. The solvent can include methanol. The concentration of metal alkoxide, solvent, and/or the pH of the solution can, for example, facilitate the preservation of the depolymerized cutin components in monomeric form, which can prevent oligomerization or repolymerization of the liberated cutin monomers included in the plant extract. Although an acid catalyst for the reaction (utilizing methods further described below) could be used in place of the base catalyst, base catalysts are commonly used for transesterification of oils, as in many cases the reaction rate can be higher than that for an acid catalyst.

In efforts to obtain fatty acid ester products (or oligomers thereof) from the depolymerization step <NUM> of method <NUM>, the refluxing of the cutin in the presence of the metal alkoxide was carried out by the inventors of the present disclosure in anhydrous reagents and anhydrous solvents (e.g., ethanol) in a closed, nitrogenous atmosphere. Specifically, cutin obtained from tomato pomace was refluxed in a solution comprising sodium ethoxide (prepared by dissolving sodium in ethanol) according to the process described in Example <NUM> below in order to favor ester formation over saponification and acid formation. The expected reaction is schematically represented in <FIG> for the case of an anhydrous solution comprising sodium ethoxide dissolved in ethanol. Referring to <FIG>, cutin <NUM> is represented by a crosslinked network of polyhydroxy fatty acids, where R and R' represent adjacent fatty acid units. Depolymerization of the cutin <NUM> by the sodium ethoxide present in the EtOH in the absence of water is expected to form isolated ethyl esters <NUM>, as shown in <FIG>.

<FIG> is a schematic representation of the depolymerization reaction for the case where water is present in the solution. In this case, the reaction produces both ethyl esters <NUM> and carboxylic acid <NUM>. As further shown in <FIG>, the base in the solution causes the carboxylic acid <NUM> to be converted to carboxylate <NUM>. If enough water is present in the solution, substantially all of the depolymerized product is driven to the carboxylic acid <NUM> and then converted to the carboxylate <NUM> by the base in the solution, such that no measurable concentration of ethyl esters <NUM> is present in the resulting composition.

Without wishing to be bound by theory, the inventors of the current disclosure observed that despite extensive drying and/or other efforts to ensure that no water was present in the reaction during cutin depolymerization according to Example <NUM>, the apparently dry cutin appeared to contain sufficient endogenous water to result in all of the depolymerized product being shunted to the carboxylate <NUM>. Consequently, no substantial concentration of esters <NUM> could be detected in the resulting extract composition.

A second method <NUM> for depolymerizing cutin to obtain a plant extract composition is illustrated in <FIG>. Steps <NUM>, <NUM>, <NUM>, <NUM>, and <NUM>, in which cutin is obtained from plant matter, are the same as steps <NUM>, <NUM>, <NUM>, <NUM>, and <NUM>, respectively, of method <NUM> in <FIG>. However, in step <NUM> of method <NUM>, the cutin is refluxed in an acid concurrently with an alcohol (rather than a base and an alcohol as in step <NUM> of method <NUM>) in order to obtain a plant extract composition including cutin-derived monomers and/or oligomers.

The specific reaction associated with the second method <NUM>, and specifically with step <NUM>, is schematically represented in <FIG> for the case of a solution comprising an acid dissolved in ethanol. The reaction in <FIG> assumes the presence of water in the solution (e.g., endogenous water contained within the cutin). Similar to <FIG>, in <FIG> cutin <NUM> is represented by a crosslinked network of polyhydroxy fatty acids, where R and R' represent adjacent fatty acid units. Depolymerization of the cutin <NUM> in the acidified solution in the presence of water is expected to form ethyl esters <NUM> and carboxylic acid <NUM> in a state of equilibrium with one another, thus producing a plant extract composition including fatty acid esters (e.g., ethyl esters <NUM>). In step <NUM> of method <NUM>, due to the absence of a base catalyst, the carboxylic acid <NUM> is not converted to a carboxylate, as in method <NUM> and corresponding <FIG>. Consequently, the reaction is expected to produce a composition comprising a mix of ethyl esters <NUM> and carboxylic acid <NUM>, where the product distribution approximately reflects the ratio of esterification partner to water.

In efforts to obtain a composition including fatty acid esters (or oligomers thereof) by way of method <NUM> (and in particular by utilizing step <NUM> of method <NUM>), the inventors of the subject matter in the current application refluxed cutin obtained from tomato pomace in a solution comprising sulfuric acid dissolved in ethanol according to the process described in Example <NUM> below. Results are illustrated in <FIG> and <FIG>. As shown in Example <NUM> and <FIG> and <FIG>, the process resulted in the production and isolation of ethyl <NUM>,<NUM>-dihydroxyhexdecanoate (herein "EtDHPA").

It was found through extensive experimentation that a larger amount of acid than predicted from catalytic calculations was needed to ensure high yields of products. For instance, under refluxing conditions, an increase in both crude isolate and purified isolate was seen when increasing the equivalence of sulfuric acid used from <NUM> to <NUM> to <NUM> to <NUM> to <NUM> equivalents, from negligible material to <NUM>% isolated yield, over the course of <NUM> hours. Furthermore, the reaction could additionally be accelerated by sealing the system to generate pressure, such that the reaction could be conducted above the atmospheric boiling point of the solvent (see Example <NUM>). A further increase in crude isolate and purified isolate yields was seen when the temperature was increased from reflux (<NUM>) to <NUM> to <NUM>, with one equivalent of acid, up to <NUM>% isolated yield. However, without wishing to be bound by theory, there appears to be an upper limit, after which the isolated yield appears to decrease, as seen in <FIG> and <FIG> (<NUM>, <NUM> eq. H<NUM>SO<NUM>, <NUM> hrs).

While EtDHPA <NUM> (in <FIG>) can be produced by method <NUM> of <FIG> with ethanol utilized as the alcohol and with a cutin source (or other crosslinked polymer) that includes <NUM>,<NUM>-dihydroxyhexadecanoic acid (or esters thereof) as a building block of the crosslinked network, other types of ethyl esters can be produced by method <NUM> using cutin from plant sources (or other crosslinked polymers/networks) that are formed of different molecular building blocks. For example, cutin from tomatoes tends to have a high proportion of C<NUM> fatty acids (e.g., fatty acids having a carbon chain length of <NUM>) such as that of <FIG>, <FIG>, <FIG>, and <FIG>, where <FIG> shows the chemical composition of <NUM>,<NUM>-dihydroxyhexadecanoic acid (<NUM> in <FIG>), <FIG> shows the chemical composition of <NUM>,<NUM>-dihydroxyhexadecanoic acid (<NUM> in <FIG>), <FIG> shows the chemical composition of <NUM>,<NUM>,<NUM>-trihydroxyhexadecanoic acid (<NUM> in <FIG>), and <FIG> shows the chemical composition of <NUM>,<NUM>-epoxy-<NUM>-hydroxyhexadecanoic acid (<NUM> in <FIG>). Accordingly, ethyl esters that can be produced by method <NUM> using cutin from tomatoes can include ethyl <NUM>,<NUM>-dihydroxyhexadecanoate (<NUM> in <FIG>), ethyl <NUM>,<NUM>-dihydroxyhexadecanoate (<NUM> in <FIG>), ethyl <NUM>,<NUM>,<NUM>-trihydroxyhexadecanoate (<NUM> in <FIG>), and/or ethyl <NUM>,<NUM>-epoxy-<NUM>-hydroxyhexadecanoate (<NUM> in <FIG>).

On the other hand, cutin from cranberries tends to have a high proportion of C<NUM> fatty acids (e.g., fatty acids having a carbon chain length of <NUM>) such as that of <FIG>, <FIG>, <FIG>, and <FIG>, where <FIG> shows the chemical composition of <NUM>,<NUM>-dihydroxyoctadecanoic acid (<NUM> in <FIG>), <FIG> shows the chemical composition of <NUM>,<NUM>-dihydroxyoctadecanoic acid (<NUM> in <FIG>), <FIG> shows the chemical composition of <NUM>,<NUM>,<NUM>-trihydroxyoctadecanoic acid (<NUM> in <FIG>), and <FIG> shows the chemical composition of <NUM>,<NUM>-epoxy-<NUM>-hydroxyoctadecanoic acid (<NUM> in <FIG>). Accordingly, ethyl esters that can be produced by method <NUM> using cutin from cranberries can include ethyl <NUM>,<NUM>-dihydroxyoctadecanoate (<NUM> in <FIG>), ethyl <NUM>,<NUM>-dihydroxyhexadecanoate (<NUM> in <FIG>), ethyl <NUM>,<NUM>,<NUM>-trihydroxyoctadecanoate (<NUM> in <FIG>), and/or ethyl <NUM>,<NUM>-epoxy-<NUM>-hydroxyoctadecanoate (<NUM> in <FIG>).

Furthermore, alcohols other than (or in addition to) ethanol can be used in the method <NUM> of <FIG>, which can result in other types of esters being produced. For example, using methanol as the alcohol can result in the production of methyl esters such as methyl <NUM>,<NUM>-dihydroxyhexadecanoate (<NUM> in <FIG>), methyl <NUM>,<NUM>-dihydroxyoctadecanoate (<NUM> in <FIG>), methyl <NUM>,<NUM>-dihydroxyhexadecanoate (<NUM> in <FIG>), methyl <NUM>,<NUM>-dihydroxyhexadecanoate (<NUM> in <FIG>), methyl <NUM>,<NUM>,<NUM>-trihydroxyhexadecanoate (<NUM> in <FIG>), methyl <NUM>,<NUM>,<NUM>-trihydroxyoctadecanoate (<NUM> in <FIG>), methyl <NUM>,<NUM>-epoxy-<NUM>-hydroxyhexadecanoate (<NUM> in <FIG>), and/or methyl <NUM>,<NUM>-epoxy-<NUM>-hydroxyoctadecanoate (<NUM> in <FIG>). Or, using glycerol as the alcohol can result in the production of glyceryl esters (e.g., <NUM>-glyceryl or <NUM>-glyceryl esters). For example, <NUM>-glyceryl esters that can be produced include <NUM>,<NUM>-dihydroxypropyl <NUM>,<NUM>-dihydroxyhexadecanoate (<NUM> in <FIG>), <NUM>,<NUM>-dihydroxypropyl <NUM>,<NUM>-dihydroxyoctadecanoate (<NUM> in <FIG>), <NUM>,<NUM>-dihydroxypropyl <NUM>,<NUM>-dihydroxyhexadecanoate (<NUM> in <FIG>), <NUM>,<NUM>-dihydroxypropyl <NUM>,<NUM>-dihydroxyhexadecanoate (<NUM> in <FIG>), <NUM>,<NUM>-dihydroxypropyl <NUM>,<NUM>,<NUM>-trihydroxyhexadecanoate (<NUM> in <FIG>), <NUM>,<NUM>-dihydroxypropyl <NUM>,<NUM>,<NUM>-trihydroxyoctadecanoate (<NUM> in <FIG>), <NUM>,<NUM>-dihydroxypropyl <NUM>,<NUM>-epoxy-<NUM>-hydroxyhexadecanoate (<NUM> in <FIG>), and/or <NUM>,<NUM>-dihydroxypropyl <NUM>,<NUM>-epoxy-<NUM>-hydroxyoctadecanoate (<NUM> in <FIG>). <NUM>-glyceryl esters that can be produced include <NUM>,<NUM>-dihydroxypropan-<NUM>-yl <NUM>,<NUM>-dihydroxyhexadecanoate (<NUM> in <FIG>), <NUM>,<NUM>-dihydroxypropan-<NUM>-yl <NUM>,<NUM>-dihydroxyoctadecanoate (<NUM> in <FIG>), <NUM>,<NUM>-dihydroxypropan-<NUM>-yl <NUM>,<NUM>-dihydroxyhexadecanoate (<NUM> in <FIG>), <NUM>,<NUM>-dihydroxypropan-<NUM>-yl <NUM>,<NUM>-dihydroxyhexadecanoate (<NUM> in <FIG>), <NUM>,<NUM>-dihydroxypropan-<NUM>-yl <NUM>,<NUM>,<NUM>-trihydroxyhexadecanoate (<NUM> in <FIG>), <NUM>,<NUM>-dihydroxypropan-<NUM>-yl <NUM>,<NUM>,<NUM>-trihydroxyoctadecanoate (<NUM> in <FIG>), <NUM>,<NUM>-dihydroxypropan-<NUM>-yl <NUM>,<NUM>-epoxy-<NUM>-hydroxyhexadecanoate (<NUM> in <FIG>), and/or <NUM>,<NUM>-dihydroxypropan-<NUM>-yl <NUM>,<NUM>-epoxy-<NUM>-hydroxyoctadecanoate (<NUM> in <FIG>).

In general, the method <NUM> in <FIG> can produce one or more compounds of Formula I:
<CHM>
wherein:.

In some implementations, R<NUM>, R<NUM>, R<NUM>, R<NUM>, R<NUM>, R<NUM>, R<NUM>, R<NUM>, R<NUM>, R<NUM>, and R<NUM> in Formula I are each H. Additionally, the method <NUM> in <FIG> can produce one or more compounds of Formula II:
<CHM>
wherein:.

R may be selected from -H, -CH<NUM>, or -CH<NUM>CH<NUM>. The method <NUM> described herein can be used to produce one or more of the following methyl ester compounds:
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
or
<CHM>.

The method <NUM> described herein can also be used to produce one or more of the following ethyl ester compounds:
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
or
<CHM>.

The method <NUM> described herein can also be used to produce one or more of the following <NUM>-glyceryl ester compounds:
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
<CHM>
or
<CHM>.

In some embodiments, the acid included in the solution used to depolymerize the crosslinked polyester is a strong acid. As used herein, a "strong acid" is one for which substantially all of the acid ionizes (dissociates) in a solution (provided there is sufficient solvent). A strong acid has a pKa < -<NUM>.

In some embodiments, the polyester, the acid, and the alcohol are heated in a sealed vessel above the atmospheric boiling point of the alcohol. This sealed vessel can allow higher temperatures to be reached, which can allow for shorter reaction times and/or less acid needed to obtain the product.

The fatty acid esters obtained by way of method <NUM> can be used in a variety of applications. For example, they can be applied directly to a plant or other agricultural product to form a protective coating, as further described below. Or, the esters may serve as starting material for further chemical transformations, for example for the production of free fatty acids. Although free fatty acids can be extracted from crosslinked polymers such as cutin using other methods (e.g., using method <NUM> of <FIG>), forming free fatty acids via transesterification of esters obtained by way of method <NUM> can result in more highly purified product. For example, when methods <NUM> and <NUM> are each used to depolymerize cutin, the resulting crude extract in both cases is an oil. However, purification of the extract obtained by method <NUM> results in product which is a solid powder with little or substantially no coloration, and when dissolved in a solvent produces a solution with a low viscosity. On the other hand, purification of the extract obtained by method <NUM> results in product which remains oily with substantial coloration, and when dissolved in a solvent produces a solution with a substantially higher viscosity.

A plant extract composition prepared by a method of the invention can be applied directly to a portion of a plant, e.g., to form a protective coating on the plant. The plant extract composition can be heated to modify the physical and/or chemical properties of the composition prior to and/or during and/or after the application process. The plant extract composition can be dissolved and/or suspended in a solvent, in aqueous solutions, or in a carrier liquid to form the coating. The solvent can include any polar, non-polar, protic, or aprotic solvents, including any combinations thereof. Examples of solvents that can be used to dissolve the plant extract compositions described herein include water, methanol, ethanol, isopropanol, butanol, acetone, ethyl acetate, chloroform, acetonitrile, tetrahydrofuran, diethyl ether, methyl tert-butyl ether, any other suitable solvent or a combination thereof. Aqueous solutions, suspensions, or emulsions of such plant extract compositions can be suitable for coating on agricultural products, for example, forming a coating on the agricultural product. For example, the aqueous solutions, suspensions, or emulsions can be applied to the surface of the agricultural product, after which the solvent can be removed (e.g., by evaporation or convective drying), leaving a protective coating formed from the plant extract composition on the surface of the agricultural product.

The coatings can be configured to change the surface energy of the agricultural product. Various properties of coatings described herein can be adjusted by tuning the crosslink density of the coating, its thickness, or its composition. This can, for example, be used to control the ripening of postharvest fruit or produce. For example, coatings formed of plant extract compositions that primarily include bifunctional or polyfunctional cutin monomer units can, for example, have higher crosslink densities than those that include monofunctional cutin monomer units. Thus, plant extract composition coatings formed from bifunctional or polyfunctional cutin monomer units can in some cases result in slower rates of ripening as compared to coatings formed from monofunctional monomer units.

An acid or a base can be added to the coating formulation to achieve a desired pH suitable for coating the agricultural product with the plant extract composition coating. Additives such as, for example, surfactants, emulsifiers, thickening agents, nonionic polymers, waxes, or salts can be included in the coating formulation. Weak acids, ions, or non-reactive molecules can be included in the coating formulation to control or adjust the properties of the resulting films or coatings. pH stabilizers or modifiers can also be included in the coating formulation. The coating formulation can include additional materials that are also transported to the surface with the coating, or are deposited separately and are subsequently encapsulated by the coating (e.g., the coating is formed at least partially around the additional material), or are deposited separately and are subsequently supported by the coating (e.g., the additional material is anchored to the external surface of the coating). Examples of such additional materials can include cells, biological signaling molecules, vitamins, minerals, pigments, aromas, enzymes, catalysts, antifungals, antimicrobials, and/or time-released drugs. The additional materials can be non-reactive with surface of the agricultural product and/or coating, or alternatively can be reactive with the surface and/or coating.

The coating can include an additive configured, for example, to modify the viscosity, vapor pressure, surface tension, or solubility of the coating. The additive can be configured to increase the chemical stability of the coating. For example, the additive can be an antioxidant configured to inhibit oxidation of the coating. The additive can be added to reduce or increase the melting temperature or the glass-transition temperature of the coating. The additive can be configured to reduce the diffusivity of water vapor, oxygen, CO<NUM>, or ethylene through the coating or enable the coating to absorb more ultra violet (UV) light, for example to protect the agricultural product (e.g., any of the products described herein). The additive can be configured to provide an intentional odor, for example a fragrance (e.g., smell of flowers, fruits, plants, freshness, scents, etc.). The additive can be configured to provide color and can include, for example, a dye or a US Food and Drug Administration (FDA) approved color additive. The additives can include sweeteners, color additives, flavors, spices, flavor enhancers, fat replacers, and components of formulations used to replace fats, nutrients, emulsifiers, bulking agents, cleansing agents, stabilizers, emulsion stabilizers, thickeners, flavor or fragrance, an ingredient of a flavor or fragrance, binders, texturizers, humectants, pH control agents, acidulants, leavening agents, anti-caking agents, antifungal agents, antimicrobial agents, antioxidants, and/or UV filters. The coating can include a photoinitiator, which can initiate crosslinking of the coating on exposure to an appropriate light source, for example, UV light.

Any of the plant extract composition coatings described herein can be flavorless or have high flavor thresholds, e.g. above <NUM> ppm, and can be odorless or have a high odor threshold. The materials included in any of the coatings described herein can be substantially transparent. For example, the plant extract composition, the solvent, and/or any other additives included in the coating can be selected so that they have substantially the same or similar indices of refraction. By matching their indices of refraction, they may be optically matched to reduce light scattering and improve light transmission. For example, by utilizing materials that have similar indices of refraction and have a clear, transparent property, a coating having substantially transparent characteristics can be formed.

Any of the coatings described herein can be disposed on the external surface of an agricultural product using any suitable means. For example, the agricultural product can be dip-coated in a bath of the coating formulation (e.g., an aqueous or mixed aqueous-organic or organic solution of the plant extract composition). The deposited coating can form a thin layer on the surface of an agricultural product, which can protect the agricultural product from biotic stressors, water loss, and/or oxidation. The deposited coating can have a thickness of less than about <NUM>, such that the coating is transparent to the naked eye. For example, the deposited coating can have a thickness of about <NUM>, about <NUM>, about <NUM>, about <NUM>, about <NUM>, about <NUM>, about <NUM>, about <NUM>, about <NUM>, about <NUM>, about <NUM>, about <NUM>, about <NUM>, about <NUM>, about <NUM>, about <NUM>, about <NUM>, about <NUM>, about <NUM>, about <NUM>, about <NUM>, about <NUM>, about <NUM>, <NUM>,<NUM>, about <NUM>,<NUM>, about <NUM>,<NUM>, about <NUM>,<NUM>, about <NUM>,<NUM>, or about <NUM>,<NUM>, inclusive of all ranges therebetween. The deposited coating can be uniformly deposited over the agricultural product and free of defects and/or pinholes. The dip-coating process can include sequential coating of the agricultural product in baths of coating precursors that can undergo self-assembly or covalent bonding on the agricultural product to form the coating. The coating can be deposited on agricultural products by passing the agricultural products under a stream of the coating formulation (e.g., a waterfall of the liquid coating). For example, the agricultural products can be disposed on a conveyor that passes through the stream of the coating formulation. The coating can be misted, vapor- or dry vapor-deposited on the surface of the agricultural product. The coating can be configured to be fixed on the surface of the agricultural product by UV crosslinking or by exposure to a reactive gas, for example, oxygen.

The plant extract composition coating can be spray-coated on the agricultural products. Commercially available sprayers can be used for spraying the coating or precursors of the coating onto the agricultural product. The coating formulation can be electrically charged in the sprayer before spray-coating on to the agricultural product, such that the deposited coating electrostatically and/or covalently bonds to the exterior surface of the agricultural product.

The coatings formed from plant extract compositions described herein can be configured to prevent water loss or other moisture loss from the coated portion of the plant, delay ripening, and/or prevent oxygen diffusion into the coated portion of the plant, for example, to reduce oxidation of the coated portion of the plant. The coating can also protect the coated portion of the plant against biotic stressors, such as, for example, bacteria, fungi, viruses, and/or pests that can infest and decompose the coated portion of the plant. Since bacteria, fungi and pests all identify food sources via recognition of specific molecules on the surface of the agricultural product, coating the agricultural products with the coating containing the plant extract compositions can deposit molecularly contrasting molecules on the surface of the portion of the plant, which can render the agricultural products unrecognizable. Furthermore, the coating can also alter the physical and/or chemical environment of the surface of the agricultural product making the surface unfavorable for bacteria, fungi or pests to grow. The coating can also be formulated to protect the surface of the portion of the plant from abrasion, bruising, or otherwise mechanical damage, and/or protect the portion of the plant from photodegradation. The portion of the plant can include, for example, a leaf, a stem, a shoot, a flower, a fruit, a root, etc. The coating can be used to coat fruits and, for example, delay ripening of the fruit.

Any of the coatings described herein can be disposed on the external surface of an agricultural product using any suitable means. For example, the agricultural product can be dip coated in a bath of the coating composition (e.g., an aqueous solution of hydrogen-bonding organic molecules). The coating can form a thin layer on the surface of agricultural product, which can protect the agricultural product from biotic stressors, water loss, and/or oxidation. The deposited coating can have a thickness of less than about <NUM> microns, for example less than <NUM> micron, less than <NUM>, less than <NUM>, less than <NUM>, less than <NUM>, less than <NUM>, less than <NUM>, less than <NUM>, less than <NUM>, or less than <NUM>, such that the coating is transparent to the naked eye. For example, the deposited coating can have a thickness of about <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, <NUM>, or about <NUM>,<NUM> inclusive of all ranges therebetween. The deposited coating can have a high degree of crystallinity to decrease permeability, such that the coating is conformally deposited over the agricultural product and is free of defects and/or pinholes. The dip coating process can include sequential coating of the agricultural product in baths of precursors that can undergo self-assembly or covalent bonding on the agricultural product to form the coating. The coatings can be deposited on agricultural products by passing the agricultural products under a stream of the coating (e.g., a waterfall of the liquid coating). For example, the agricultural products can be disposed on a conveyor that passes through the stream of the coating. The coating can be vapor deposited on the surface of the agricultural product. The coating can be formulated to be fixed on the surface of the agricultural product by UV cross-linking or by exposure to a reactive gas, for example, oxygen. The coating can be applied in the field before harvest as an alternative to pesticides.

The fatty acid esters and/or oligomers thereof can be dissolved in a suitable solvent (e.g., water, ethanol, or a combination thereof) prior to coating the agricultural product. The process of disposing the composition on the agricultural product may comprise dip-coating the agricultural product in a solution comprising the plurality of cutin-derived monomers, oligomers, or combinations thereof. Alternatively, the process of disposing the composition on the agricultural product may comprise spray-coating the produce with a solution comprising the plurality of fatty acid esters and/or oligomers thereof.

Any of the coatings can be spray coated on the agricultural products. Commercially available sprayers can be used for spraying the coating or precursors of the coating onto the agricultural product. The coatings can be electrically charged in the sprayer before spray coating on the agricultural product, such that the coating covalently bonds to the exterior surface of the agricultural product.

The coating can be deposited on the agricultural product such that the coating is unbound to the surface of the agricultural product. Alternatively, one or more components of the coating, for example, the hydrogen-bonding organic molecule, can be covalently (or hydrogen) bonded to at least a portion of the surface of the agricultural product. This can result in improved coating properties such as, for example, higher durability, tighter control of coating permeability and thickness. Multiple layers of the coating can be deposited on the surface of agricultural product to achieve a durable coating.

Any of the coatings described herein can be used to protect any agricultural product. The coating can be coated on an edible agricultural product, for example, fruits, vegetables, edible seeds and nuts, herbs, spices, produce, meat, eggs, dairy products, seafood, grains, or any other consumable item. The coating can include components that are non-toxic and safe for consumption by humans and/or animals. For example, the coating can include components that are U. Food and Drug Administration (FDA) approved direct or indirect food additives, FDA approved food contact substances, satisfy FDA regulatory requirements to be used as a food additive or food contact substance, and/or is an FDA Generally Recognized as Safe (GRAS) material. Examples of such materials can be found within the FDA Code of Federal Regulations Title <NUM>, located at "http://www. accessdata. gov/scripts/cdrh/cfdocs/cfcfr/cfrsearch. The components of the coating can include a dietary supplement or ingredient of a dietary supplement. The components of the coating can also include an FDA approved food additive or color additive. The coating can include components that are naturally derived, as described herein. The coating can be flavorless or have a high flavor threshold of below <NUM> ppm, are odorless or have a high odor threshold, and/or are substantially transparent. The coating can be configured to be washed off an edible agricultural product, for example, with water.

The coatings described herein can be formed on an inedible agricultural product. Such inedible agricultural products can include, for example, inedible flowers, seeds, shoots, stems, leaves, whole plants, and the like. The coating can include components that are non-toxic, but the threshold level for non-toxicity can be higher than that prescribed for edible products. The coating can include an FDA approved food contact substance, an FDA approved food additive, or an FDA approved drug ingredient, for example, any ingredient included in the FDA's database of approved drugs, which can be found at "http://www. accessdata. gov/scripts/cder/drugsatfda/index. The coating can include materials that satisfy FDA requirements to be used in drugs or are listed within the FDA's National Drug Discovery Code Directory, "http://www. accessdata. gov/scripts/cder/ndc/default. The materials can include inactive drug ingredients of an approved drug product as listed within the FDA's database, "http://www. accessdata. gov/scripts/cder/ndc/default.

The coatings described herein provide several advantages, including, for example: (<NUM>) the coatings can protect the agricultural products from biotic stressors, i.e. bacteria, viruses, fungi, or pests; (<NUM>) the coatings can prevent evaporation of water and/or diffusion of oxygen; (<NUM>) coating can help extend the shelf life of agricultural products, for example, post-harvest produce, without refrigeration; (<NUM>) the coatings can introduce mechanical stability to the surface of the agricultural products eliminating the need for expensive packaging designed to prevent the types of bruising which accelerate spoilage; (<NUM>) use of agricultural waste materials to obtain the coatings can help eliminate the breeding environments of bacteria, fungi, and pests; (<NUM>) the coatings can be used in place of pesticides to protect plants, thereby minimizing the harmful impact of pesticides to human health and the environment; (<NUM>) the coatings can be naturally derived and hence, safe for human consumption. Since the components of the coatings described herein can be obtained from agricultural waste, such coatings can be made at a relatively low cost. Therefore, the coatings can be particularly suited for small scale farmers, for example, by reducing the cost required to protect crops from pesticides and reducing post-harvest losses of agricultural products due to decomposition by biotic and/or environmental stressors.

The treating of the crosslinked polymer and/or forming of the plant extract composition can be carried out by a first party, while the application of the plant extract composition to an agricultural product to form a protective coating over the agricultural product can be carried out by a second party different from the first party. For example, a manufacturer of the plant extract compositions (i.e., a first party) can form the compositions by one or more of the methods described herein. The manufacturer can then sell or otherwise provide the resulting plant extract composition to a second party, for example a farmer, shipper, distributor, or retailer of produce, and the second party can apply the composition to one or more agricultural products to form a protective coating over the products. Alternatively, the manufacturer can sell or otherwise provide the resulting plant extract composition to an intermediary party, for example a wholesaler, who then sells or otherwise provides the plant extract composition to a second party such as a farmer, shipper, distributor, or retailer of produce, and the second party can apply the composition to one or more agricultural products to form a protective coating over the products.

In some cases where multiple parties are involved, the first party may optionally provide instructions or recommendations about the extract composition, either written or oral, indicating one or more of the following: (i) that the composition is intended to be applied to a product for the purpose of coating or protecting the product, to extend the life of the product, to reduce spoilage of the product, or to modify or improve the aesthetic appearance of the product; (ii) conditions and/or methods that are suitable for applying the compositions to the surfaces of products; and/or (iii) potential benefits (e.g., extended shelf life, reduced rate of mass loss, reduced rate of molding and/or spoilage, etc.) that can result from the application of the composition to a product. While the instructions or recommendations may be supplied by the first party directly with the plant extract composition (e.g., on packaging in which the composition is sold or distributed), the instructions or recommendations may alternatively be supplied separately, for example on a website owned or controlled by the first party, or in advertising or marketing material provided by or on behalf of the first party.

In view of the above, it is recognized that in some cases, a party that manufactures a plant extract composition according to one or more methods described herein (i.e., a first party) may not directly form a coating over a product from the extract composition, but can instead direct (e.g., can instruct or request) a second party to form a coating over a product from the extract composition. That is, even if the first party does not coat a product by the methods and compositions described herein, the first party may still cause the plant extract composition to be applied to the product to form a protective coating over the product by providing instructions or recommendations as described above. Accordingly, as used herein, the act of applying a plant extract composition to a product (e.g., a plant or agricultural product) also includes directing or instructing another party to apply the plant extract composition to the product, or causing the plant extract composition to be applied to the product.

The following examples describe plant extract compositions and methods for obtaining the same. These examples are only for illustrative purposes and are not meant to limit the scope of the present disclosure.

In each of the examples below, all reagents and solvents were purchased and used without further purification unless specified. All reactions were carried out under an atmosphere of nitrogen with commercial grade solvents unless otherwise stated. Reactions were monitored by thin layer chromatography (TLC) carried out on <NUM> E. Merck silica gel plates (<NUM>Å, F-<NUM>) using UV light as the visualizing agent and an acidic mixture of anisaldehyde, ceric ammonium molybdate, or basic aqueous potassium permanganate (KMnO<NUM>), and heat as developing agents. NMR spectra were recorded on a Bruker Avance <NUM> and/or Varian VNMRs <NUM> instruments and calibrated using residual un-deuterated solvent as an internal reference (eg. CHCl<NUM> @ <NUM> ppm <NUM>H NMR, <NUM> ppm <NUM>C NMR). The following abbreviations (or combinations thereof) were used to explain the multiplicities: s = singlet, d =doublet, t = triplet, q = quartet, m = multiplet, br = broad. Mass spectra (MS) were recorded on a Waters Xevo UPLC equipped with a C<NUM> column and a ESI TQD MS. Absolute ethanol was dried to low residual water according to the procedures in Purification of Laboratory Chemicals (<NUM>th ed.

Tomato pomace obtained from a commercial tomato processing facility was milled in a cutting mill, and sifted to give different particle size distributions (eg. ><NUM>, <NUM>-<NUM>, <NUM>-<NUM>, etc.). The fraction corresponding to <NUM>-<NUM> was sequentially extracted with CHCl<NUM> overnight in a Soxhlet extractor and with methanol overnight in a Soxhlet extractor to remove the surface waxes and other soluble components, followed by drying under vacuum (< <NUM> torr). The washed pomace was then lyophilized overnight (< <NUM> torr) to remove water, and then stored in a desiccator before use.

A general procedure for base catalyzed depolymerization is as follows. To depolymerize the dried and washed pomace, an ethanolic solution including a stoichiometric excess (relative to tomato pomace) of sodium ethoxide was prepared in an oven dried three neck round bottom by adding <NUM> eq. sodium metal (rel. to tomato pomace, assuming that the mass is entirely composed of cutin polymer) to <NUM> anhydrous ethanol under a nitrogen atmosphere. The mixture was stirred under nitrogen until the sodium had completely dissolved, after which <NUM> of the tomato pomace (<NUM>-<NUM> in size) was added against a counter-flow of nitrogen. The mixture was refluxed under nitrogen for <NUM> hours, followed by cooling the reaction to room temperature and quenching it with <NUM> glacial acetic acid to a pH of about <NUM>. The resulting solution was filtered using Grade <NUM> Whatman filter paper to remove any leftover solids and the filtrate was collected. Any excess solvent was removed from the filtered solution by rotary evaporation. The crude isolate was dried under high vacuum (< <NUM> torr), and was analyzed by UPLC and NMR. The crude isolate was found to contain (<NUM>)<NUM>,<NUM>-dihydroxypalmitic acid, with no evidence of ethyl ester formation.

To <NUM> of absolute ethanol was added sulfuric acid (<NUM>, <NUM>, <NUM> mmol) and tomato pomace (<NUM>, <NUM> - <NUM> in size) with stirring. The reaction was then heated to reflux for <NUM> hours. Once complete, the reaction was cooled and the solution neutralized to pH <NUM> with ~ <NUM> sat. NaHCO<NUM> (aq). The neutralized mixture was then filtered through a Buchner funnel and Grade <NUM> Whatman (<NUM>) filter paper. The filtrate was dried by sequential rotary evaporation and high vacuum (<<NUM> torr). When the crude material was dry, it was taken up in ethyl acetate (<NUM>) and three forward extractions were conducted with H<NUM>O (<NUM> x <NUM>) and brine (<NUM>). The organic layer was separated, and the combined aqueous phases were extracted with an additional <NUM> ethyl acetate, and the organic phases combined, and dried with MgSO<NUM>. The solvent was removed with rotary evaporation and high vacuum, yielding <NUM> (avg. ) of crude isolate.

The crude isolate from the ethanolysis was dissolved in methanol, and three times the mass of the crude isolate in Celite <NUM> was added. The methanol was removed by rotary evaporator and dried Celite admixture transferred to a cellulose extraction thimble. Glass wool was placed on top of the material to ensure it stayed in the thimble. The material was was extracted in a Soxhlet extractor for <NUM> hours under nitrogen with <NUM> of heptane. After <NUM> hours, the Soxhlet apparatus and contents were cooled. The Soxhlet apparatus was then dismantled, and the round bottom was placed in a fumehood overnight, which allowed a first crop of ethyl <NUM>,<NUM>-dihydroxyhexdecanoate (EtDHPA) to precipitate out of the heptane. The round bottom was then placed in a <NUM> fridge overnight, giving a second crop of EtDHPA. The second crop was then filtered and transferred to a scintillation vial. Both crops were dried by sequential treatment with a rotary evaporator and high vacuum (<<NUM> torr), resulting in a yellowish (first crop)/ white (second crop) powder. Both crops were analyzed by NMR and UPLC/ESI MS, matching the expected spectra for EtDHPA; yield (combined crops): <NUM>. <NUM>H NMR (<NUM>, Chloroform-d) δ <NUM> (q, J = <NUM>, <NUM>), <NUM> (t, J = <NUM>, <NUM>), <NUM> (s, <NUM>), <NUM> (t, J = <NUM>, <NUM>), <NUM> - <NUM> (m, <NUM>), <NUM> - <NUM> (m, <NUM>), <NUM> (t, J = <NUM>, <NUM>). See <FIG> (UPLC) and <FIG> (NMR).

To a thick-walled sealed tube containing <NUM> of absolute ethanol was added sulfuric acid (<NUM>, <NUM>, <NUM> mmol), followed by tomato pomace (<NUM>, <NUM> - <NUM> in size). The reaction was then heated to temperatures greater than the atmospheric boiling point of ethanol, such as <NUM> or <NUM> for <NUM> or <NUM> hours. Once complete, the reaction was cooled and the solution neutralized to pH <NUM> with <NUM> sat. NaHCO<NUM> (aq. The neutralized mixture was then filtered through a Buchner funnel and Grade <NUM> Whatman (<NUM>) filter paper. The filtrate was dried by sequential rotary evaporation and high vacuum (<<NUM> torr). When the crude material was dry, it was taken up in ethyl acetate (<NUM>), and three forward extractions were conducted with H<NUM>O (<NUM> x <NUM>) and brine (<NUM>). The organic layer was separated, and the combined aqueous phases were extracted with an additional <NUM> ethyl acetate, and the organic phases combined, and dried with MgSO<NUM>. The solvent was removed with rotary evaporation and high vacuum, yielding the crude isolate. The amounts of crude recovered at each of the different temperature and time conditions are plotted in <FIG>.

Claim 1:
A method of preparing a composition comprising fatty acid esters, the method comprising:
providing a crosslinked polyester comprising polymerized fatty acids;
treating the crosslinked polyester with an acid concurrently with an alcohol, at a temperature above <NUM> up to <NUM>; and
removing the acid and the alcohol to form a mixture comprising the fatty acid esters; and
purifying the mixture to form a purified isolate of fatty acid esters.