US20190037839A1 - Compositions for controlled release of active ingredients and methods of making same - Google Patents

Compositions for controlled release of active ingredients and methods of making same Download PDF

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Publication number
US20190037839A1
US20190037839A1 US15/999,302 US201715999302A US2019037839A1 US 20190037839 A1 US20190037839 A1 US 20190037839A1 US 201715999302 A US201715999302 A US 201715999302A US 2019037839 A1 US2019037839 A1 US 2019037839A1
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composition
active ingredient
hour
delivery material
release
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Adam Truett Preslar
Aidan R. Mouat
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Hazel Technologies Inc
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Hazel Technologies Inc
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Assigned to HAZEL TECHNOLOGIES, INC. reassignment HAZEL TECHNOLOGIES, INC. ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: MOUAT, AIDAN R., Preslar, Adam Truett
Publication of US20190037839A1 publication Critical patent/US20190037839A1/en
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    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01NPRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
    • A01N25/00Biocides, pest repellants or attractants, or plant growth regulators, characterised by their forms, or by their non-active ingredients or by their methods of application, e.g. seed treatment or sequential application; Substances for reducing the noxious effect of the active ingredients to organisms other than pests
    • A01N25/18Vapour or smoke emitting compositions with delayed or sustained release
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01NPRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
    • A01N25/00Biocides, pest repellants or attractants, or plant growth regulators, characterised by their forms, or by their non-active ingredients or by their methods of application, e.g. seed treatment or sequential application; Substances for reducing the noxious effect of the active ingredients to organisms other than pests
    • A01N25/02Biocides, pest repellants or attractants, or plant growth regulators, characterised by their forms, or by their non-active ingredients or by their methods of application, e.g. seed treatment or sequential application; Substances for reducing the noxious effect of the active ingredients to organisms other than pests containing liquids as carriers, diluents or solvents
    • A01N25/04Dispersions, emulsions, suspoemulsions, suspension concentrates or gels
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01NPRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
    • A01N25/00Biocides, pest repellants or attractants, or plant growth regulators, characterised by their forms, or by their non-active ingredients or by their methods of application, e.g. seed treatment or sequential application; Substances for reducing the noxious effect of the active ingredients to organisms other than pests
    • A01N25/12Powders or granules
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01NPRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
    • A01N27/00Biocides, pest repellants or attractants, or plant growth regulators containing hydrocarbons
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01NPRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
    • A01N31/00Biocides, pest repellants or attractants, or plant growth regulators containing organic oxygen or sulfur compounds
    • A01N31/02Acyclic compounds
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01NPRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
    • A01N31/00Biocides, pest repellants or attractants, or plant growth regulators containing organic oxygen or sulfur compounds
    • A01N31/08Oxygen or sulfur directly attached to an aromatic ring system
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01NPRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
    • A01N35/00Biocides, pest repellants or attractants, or plant growth regulators containing organic compounds containing a carbon atom having two bonds to hetero atoms with at the most one bond to halogen, e.g. aldehyde radical
    • A01N35/02Biocides, pest repellants or attractants, or plant growth regulators containing organic compounds containing a carbon atom having two bonds to hetero atoms with at the most one bond to halogen, e.g. aldehyde radical containing aliphatically bound aldehyde or keto groups, or thio analogues thereof; Derivatives thereof, e.g. acetals
    • AHUMAN NECESSITIES
    • A01AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
    • A01NPRESERVATION OF BODIES OF HUMANS OR ANIMALS OR PLANTS OR PARTS THEREOF; BIOCIDES, e.g. AS DISINFECTANTS, AS PESTICIDES OR AS HERBICIDES; PEST REPELLANTS OR ATTRACTANTS; PLANT GROWTH REGULATORS
    • A01N65/00Biocides, pest repellants or attractants, or plant growth regulators containing material from algae, lichens, bryophyta, multi-cellular fungi or plants, or extracts thereof
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B32/00Carbon; Compounds thereof
    • C01B32/30Active carbon
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/22Improving land use; Improving water use or availability; Controlling erosion
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/20Reduction of greenhouse gas [GHG] emissions in agriculture, e.g. CO2
    • Y02P60/21Dinitrogen oxide [N2O], e.g. using aquaponics, hydroponics or efficiency measures

Definitions

  • compositions for controlled release of active ingredients and methods of making same are generally provided.
  • Produce waste throughout the supply chain decreases agricultural productivity and reduces the availability of nutritious food sources.
  • Produce ages and eventually spoils due to, for example, one or more of the plant hormone ethylene, bacteria, microbes, fungus, and other pathogens.
  • Volatile or gaseous active ingredients including, but not limited to cyclopropenes, essential oils, terpenes, and terpenoids can be used to control produce spoilage, but their inherent volatility in the gas and vapor phase limit their usefulness. Accordingly, improved composition and methods are needed.
  • compositions for controlled release of active ingredients and methods of making same are generally provided.
  • a composition comprising a delivery material selected from among the group consisting of carbon materials and silicate materials; and a volatile or gaseous active ingredient useful for applications in at least one of agriculture, pest control, odor control, and food preservation present in the composition at a 0.01 wt % versus the total weight of the composition, wherein the composition is configured to control release the volatile or gaseous active ingredient.
  • a composition comprising a delivery material selected from the group consisting of carbon materials and silicate materials; and a cyclopropene present in the composition in at least about 0.05 wt % versus the total weight of the composition.
  • a composition comprising a silicate delivery material; and a cyclopropene present in the composition in at least about 0.01 wt % versus the total weight of the composition.
  • a composition comprising a delivery material selected from the group consisting of carbon materials and silicate materials; and a cyclopropene, wherein the composition is configured to control release the cyclopropene.
  • a composition comprising a cyclopropene, wherein the composition control releases the cyclopropene at a release rate of at least 0.0005 ⁇ L/g composition/hr at hour 22.
  • a composition comprising a cyclopropene, wherein a release rate of the cyclopropene from the composition at hour 22 is at least 0.1% of the release rate at hour 1.
  • a composition comprising a silicate material comprising a surface area greater than about 1 m 2 /g; and at least one active ingredient selected from the group consisting of essential oils, terpenes, terpenoids, carvone, thymol, hexanal, carvacrol, oregano oil, and thyme oil, and combinations thereof.
  • a method comprising exposing a composition as described herein to produce.
  • a method for controlled release of a cyclopropene comprising exposing produce to a composition or matrix comprising a cyclopropene associated with a delivery material, wherein the delivery material is selected from the group consisting of a carbon based material and a silicate material, and wherein the composition comprises between about 0.01-30 wt % cyclopropene versus the total weight of the composition.
  • a method of making a composition as described herein comprises modifying at least one of the hydrophobicity, hydrophilicity, chemical potential, zeta-potential, acidity, basicity, surface functionalization, and surface functional group density of a carbon material to make a delivery material; and associating the at least one active ingredient with the delivery material.
  • FIG. 1 is a cross-section of a delivery material in accordance with a non-limiting embodiment.
  • FIG. 2 is a cross-section of a composition in accordance with a non-limiting embodiment.
  • FIG. 3 is a perspective view of a delivery material in accordance with a non-limiting embodiment.
  • FIG. 4 is a schematic illustration of a complexing agent in accordance with a non-limiting an embodiment.
  • FIG. 5 is schematic illustration of a complexing agent in accordance with a non-limiting embodiment.
  • FIG. 6 is a perspective view inside a pore of a composition in accordance with a non-limiting embodiment.
  • FIG. 7 is a photograph of example results of a banana test using a composition of a non-limiting embodiment.
  • FIG. 8 is a photograph of example results of a test on strawberry pathogens using a composition of a non-limiting embodiment.
  • FIG. 9 is another photograph of example results from FIG. 8 from the test on strawberry pathogens using a composition of a non-limiting embodiment.
  • compositions comprising a delivery material and at least one active ingredient.
  • the composition may be configured to control release the active ingredient.
  • the active ingredient may be useful for applications in at least one of agriculture, pest control, odor control, and food preservation.
  • the active ingredient is a volatile or gaseous active ingredient. Additional details regarding each of the components of the composition and related methods will now be described in detail.
  • an “active ingredient” as used herein generally refers to a chemical, biological, or other function that helps directly in achieving a desired performance objective.
  • the active ingredient has sufficient volatility to be present in detectable concentrations (e.g. ⁇ 1 ppb) in the atmosphere surrounding the composition (e.g. the composition comprising the active ingredient and a delivery material) during (and often after) release of the active ingredient from the composition.
  • the compositions, the use of compositions, and methods of making compositions as described herein relate to the release or controlled-release delivery of vapor-phase or gas-phase active ingredients from a delivery material.
  • a “vapor-phase active ingredient” or “gas-phase active ingredient” is an active ingredient that is in the vapor-phase or gas phase, respectively, at the desired conditions (e.g. ambient room temperature (about 23° C.-25° C.) and atmospheric pressure).
  • an active ingredient may extend the shelf life of an agricultural product, and improve the overall quality of the agricultural product, and/or may provide control over the product ripeness.
  • active ingredients include, but are not limited to: ethylene inhibitors for the improvement of quality and shelf life in produce; ethylene production stimulating compounds for control over produce ripeness; phospholipase-D inhibitors for improving the shelf-life and quality of post-harvest produce; essential oils (e.g.
  • Active ingredients may include natural compositions, synthetic compositions, or a combination of both.
  • the composition may comprise a single active ingredient. In other embodiments, the composition may comprise more than one active ingredient, for example, two active ingredients, three active ingredients, four active ingredients, or more.
  • the composition may comprise any suitable amount of the active ingredient.
  • the active ingredient is present in the composition in at least about 0.01 wt %, at least about 0.1 wt %, at least about 0.5 wt %, at least about 1 wt %, at least about 1.5 wt %, at least about 2 wt %, at least about 3 wt %, at least about 4 wt %, at least about 5 wt %, at least about 6 wt %, at least about 7 wt %, at least about 8 wt %, at least about 9 wt %, at least about 10 wt %, or more, versus the total weight of the composition (e.g., the composition comprising the delivery material and the active ingredient).
  • the composition comprises active ingredient in a weight percent of at least about 0.01 wt %, at least about 0.05 wt %, at least about 0.1 wt %, at least about 0.5 wt %, at least about 1 wt %, at least about 1.5 wt %, at least about 2 wt %, at least about 3 wt %, at least about 4 wt %, at least about 5 wt %, at least about 6 wt %, at least about 7 wt %, at least about 8 wt %, at least about 9 wt %, at least about 10 wt %, or more, of the total weight of the composition (e.g., the composition comprising the delivery material and the active ingredient).
  • the composition comprising the delivery material and the active ingredient
  • the active ingredient is present in the composition at between about 0.01 wt % and about 30 wt %, between about 0.05 wt % and about 30 wt %, between about 0.1 wt % and about 30 wt %, between about 0.5 wt % and about 30 wt %, between about 1 wt % and about 30 wt %, between about 1.5 wt % and about 30 wt %, between about 2 wt % and about 30 wt %, or between about 5 wt % and about 30 wt %, between about 0.01 wt % and about 15 wt %, between about 0.01 wt % and about 10 wt %, between about 0.01 wt % and about 5 wt %, between about 0.1 wt % and about 10 wt %, between about 0.1 wt % and about 5 wt %, between about 1 wt % and about
  • compositions described herein may also be referred to as matrices (or a matrix).
  • a matrix comprises a delivery material and an active ingredient.
  • a matrix comprises a delivery material and an active ingredient, the active ingredient contained within the delivery material.
  • a matrix may be a composition comprising an active ingredient 20 and a delivery material 100 .
  • the matrix is configured for controlled release of an active ingredient.
  • the active ingredient is in the vapor phase or gas phase.
  • the release characteristics of an active ingredient from a composition can be assessed by measuring release of an active ingredient from the composition over time beginning at an hour zero.
  • hour zero is defined as the instant a matrix is exposed to a non-equilibrium condition.
  • a non-equilibrium condition occurs at all temperatures and pressures at which the active ingredient has vapor pressure.
  • the exposure of a matrix containing an active ingredient to an atmosphere containing zero (0) ppm of that active ingredient will trigger the release of the active ingredient until an equilibrium concentration of that active ingredient is reached between the composition and the atmosphere.
  • a non-equilibrium condition occurs when a composition comprising an active ingredient is exposed to an atmosphere containing zero (0) ppm of that active ingredient. In a non-limiting embodiment, a non-equilibrium condition occurs when a composition comprising an active ingredient is exposed to an atmosphere containing about one (1) ppb or less of the active ingredient. In a non-limiting embodiment, a non-equilibrium condition occurs when a composition comprising an active ingredient is exposed to an atmosphere containing about one (1) ppm or less of the active ingredient. In a non-limiting embodiment, a non-equilibrium condition occurs when a composition comprising an active ingredient is exposed to an atmosphere containing about ten (10) ppm or less of the active ingredient.
  • a non-equilibrium condition occurs when a composition comprising an active ingredient is exposed to an atmosphere containing about fifty (50) ppm or less of the active ingredient. In a non-limiting embodiment, a non-equilibrium condition occurs when a composition comprising an active ingredient is exposed to an atmosphere containing about one hundred (100) ppm or less of the active ingredient. In a non-limiting embodiment, a non-equilibrium condition occurs when a composition comprising an active ingredient is exposed to an atmosphere containing about one thousand (1000) ppm or less of the active ingredient.
  • a non-equilibrium condition occurs when a composition comprising an active ingredient is exposed to an atmosphere containing about ten thousand (10,000) ppm or less of the active ingredient. In a non-limiting embodiment, a non-equilibrium condition occurs when a composition comprising an active ingredient is exposed to an atmosphere containing about one (1) ppb-ten (10) ppm. In a non-limiting embodiment, a non-equilibrium condition occurs when a composition comprising an active ingredient is exposed to an atmosphere containing about one (1) ppb-one hundred (100) ppm.
  • a non-equilibrium condition occurs when a composition comprising an active ingredient is exposed to an atmosphere containing about one (1) ppb-one thousand (1000) ppm.
  • an active ingredient is released from the matrices described herein at all temperatures from 0° C. 40° C. at atmospheric pressure.
  • Non-limiting examples of “hour zero” include: immediately after the matrix material has been charged with active ingredient and exposed to a non-equilibrium condition, immediately after the matrix material has been removed from a low temperature (for example ⁇ 4° C. or lower) and transferred to a higher temperature (such as ambient room temperature) and a non-equilibrium condition, immediately after the matrix material has been removed from a very low temperature (for example ⁇ 20° C.
  • a higher temperature such as ambient room temperature
  • a non-equilibrium condition immediately after the matrix material is incorporated, sealed, or packaged in an structure or form factor and is exposed to a non-equilibrium condition, immediately after the structure or form factor containing the matrix is removed from a further outer packaging and exposed to a non-equilibrium condition, immediately after the matrix material has been removed from a hermetically sealed or gas impermeable container and exposed to a non-equilibrium condition, immediately after the matrix material is exposed to produce in a non-equilibrium condition.
  • the controlled release parameters of the matrices described herein are, unless otherwise stated, reported in relation to 1) the amount of active ingredient (e.g. as a volume or mass) released per gram of matrix per unit time, and/or 2) the percentage of the rate of release as compared to the rate of release at a particular time point (e.g. hour one (1)).
  • the control release parameters set forth below for the matrices described herein are, unless otherwise stated, given for conditions of matrix exposure at “hour zero” to a non-equilibrium condition.
  • Example non-equilibrium conditions for the controlled release parameters are matrix exposure to ambient room temperature (approximately 23-25° C.) and atmospheric pressure, with no active ingredient detected in the atmosphere prior to commencement of the release test. It should be understood that throughout the duration of the release test, temperature and atmospheric pressure around the matrix material has been kept substantially constant. It should be further understood that the atmospheric concentration of the active ingredient may vary throughout the duration of the release test as the active ingredient is released from the matrix into the surrounding atmosphere.
  • controlled release can be quantified as a rate, which may be reported as an amount of active ingredient (e.g. a volume or mass) released per gram of matrix per unit time. Equivalent to the amount of active ingredient (e.g. a volume or mass) released per gram of matrix per unit time is the amount of active ingredient (e.g. a volume or mass) released per gram of composition (e.g. the composition comprising a delivery material and the active ingredient) per unit time. In a non-limiting embodiment, the rate of release is reported on a per hour basis. The rate of release of active ingredient per gram of composition per hour may be determined for a particular hour (e.g.
  • hour 22 by measuring the amount of active ingredient released from the composition over a period of time (e.g. sixty (60) minutes) immediately preceding the particular hour (e.g. hour 22) at which the rate is reported.
  • the release rate on a per hour basis reported for hour 22 may be calculated based on the amount (e.g. as a volume or mass) of active ingredient released from a composition (e.g. comprising a delivery material and the active ingredient) during the sixty (60) minutes which commences at hour 21 and ending at hour 22.
  • the amount of active ingredient released from the composition e.g. calculated as a volume or a mass of active ingredient released during that period of sixty (60) minutes
  • the amount of active ingredient released from the composition is then divided by the total mass of the composition (e.g. as measured in grams immediately prior to hour zero of the release test) to arrive at a release rate as an amount of active ingredient released per gram of matrix per hour.
  • a non-limiting example of how to measure the release rate of an active ingredient from a composition (e.g. the composition comprising a delivery material and the active ingredient) at hour 1 is as follows.
  • the mass of the composition to be studied is measured (e.g. in grams).
  • the release study commences at hour zero when the matrix is exposed to a non-equilibrium condition, as discussed above.
  • the active ingredient released from the composition over the subsequent sixty (60) minutes is collected (e.g. in a sealed vial) and sampled (e.g. using conventional headspace methodologies) at hour 1, which occurs sixty (60) minutes after hour zero.
  • the sample of the active ingredient collected is then measured (e.g. using a gas chromatograph (GC)).
  • GC gas chromatograph
  • a non-limiting example of how to measure the release rate of an active ingredient from the same composition (e.g. during the same release test) at hour 22 is as follows. After the active ingredient collected over the sixty (60) minutes commencing at hour zero and ending at hour 1 is sampled at hour 1, the vial is left open to allow the active ingredient to escape. At sixty (60) minutes prior to the next sample time (e.g.
  • the vial is again sealed to allow the active ingredient to collect for one hour.
  • the vial is sealed at hour 21 in anticipation of a measurement sample to be taken at hour 22.
  • the active ingredient released from the composition during the sixty (60) minutes from hour 21 to hour 22 is collected and promptly sampled (e.g. using conventional headspace methodologies) at hour 22.
  • the sample of the active ingredient collected is then measured using GC analysis.
  • the amount (e.g. as a volume or mass) of active ingredient released as calculated from the GC measurement is then divided by the mass of the composition as initially measured (e.g. the same matrix mass used in the calculation for hour 1).
  • the resulting numerical figure is the amount (e.g. as a volume or mass) of active ingredient released per gram matrix per hour at hour 22.
  • a sample of the matrix comprising the active ingredient may be placed in a vial for analysis (e.g. at hour zero), and the vial may be sealed.
  • the rate of release may be calibrated based on the number of hours that the active ingredient is permitted to build up in the vial while the vial is sealed.
  • the vapor/gas phase active ingredient may be permitted to build up in the vial.
  • the vial may be left open to allow the active ingredient to escape.
  • the rate of release at a given timepoint can be calculated by sampling the headspace of the vial and injecting a sample volume (e.g. 100 ⁇ L to 300 ⁇ L) in a GC in accordance with methods known to those of ordinary skill in the art.
  • the area of the GC peak may be calibrated by comparison against an internal standard. For example, for calculating the controlled release of 1-methylcyclopropene (1-MCP) from a matrix, the area of the GC peak may be calibrated against known quantities of 1-MCP released from ETHYLBLOCTM (FLORALIFE®; Walterboro, S.C.).
  • 1-MCP in the form of ETHYLBLOCTM is obtainable as a 0.14 wt % solid powder.
  • the release of an essential oil active ingredient may be calculated based on headspace sampling of its component terpene(s) during a release test.
  • controlled release may be quantified as rate, which may be reported as an amount of active ingredient (as a volume or mass, for example) released per gram of matrix per hour ( ⁇ L active ingredient/g matrix/hr). Equivalent to that rate is the amount of active ingredient (e.g. as a volume or mass) released per gram of composition (e.g. the composition comprising a delivery material and the active ingredient) per hour. In some embodiments, the rate is reported is the amount (e.g. as a volume or mass) of active ingredient released per gram of matrix during the hour (e.g. sixty (60) minutes) leading up to the sample timepoint. In some embodiments, the rate of release of active ingredient at hour 22 is at least about 0.0005 ⁇ L/g matrix/hr.
  • the rate of release of active ingredient at hour 22 is at least about 0.001 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 22 is at least about 0.1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 22 is at least about 1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 22 is at least about 5 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 22 is at least about 10 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 22 is at least about 25 ⁇ L/g matrix/hr.
  • the rate of release of active ingredient at hour 22 is between about 0.0005 ⁇ L/g matrix/hr and about 25 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 22 is between about 0.001 ⁇ L/g matrix/hr and about 25 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 22 is between about 0.14/g matrix/hr and about 25 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 22 is between about 1 ⁇ L/g matrix/hr and about 22 ⁇ L/g matrix/hr.
  • the rate of release of active ingredient at hour 22 is between about 3 ⁇ L/g matrix/hr and about 22 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 22 is between about 5 ⁇ L/g matrix/hr and about 22 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 24 is at least about 0.001 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 24 is at least about 0.1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 24 is at least about 1 ⁇ L/g matrix/hr.
  • the rate of release of active ingredient at hour 24 is at least about 5 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 24 is at least about 10 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 24 is at least about 20 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 24 is at least about 30 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 24 is at least about 35 ⁇ L/g matrix/hr.
  • the rate of release of active ingredient at hour 24 is between about 0.0005 ⁇ L/g matrix/hr and about 35 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 24 is between about 0.001 ⁇ L/g matrix/hr and about 35 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 22 is between about 0.1 ⁇ L/g matrix/hr and about 35 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 24 is between about 1 ⁇ L/g matrix/hr and about 25 ⁇ L/g matrix/hr.
  • the rate of release of active ingredient at hour 24 is between about 3 ⁇ L/g matrix/hr and about 35 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 24 is between about 5 ⁇ L/g matrix/hr and about 35 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 48 is greater than zero ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 48 is at least about 0.01 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 48 is at least about 0.1 ⁇ L/g matrix/hr.
  • the rate of release of active ingredient at hour 48 at least about 1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 48 at least about 5 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 48 at least about 104/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 48 at least about 20 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 48 at least about 25 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 48 at least about 30 ⁇ L/g matrix/hr.
  • the rate of release of active ingredient at hour 48 is between about 0.1 ⁇ L/g matrix/hr and about 4 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 48 is between about 1 ⁇ L/g matrix/hr and about 5 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 48 is between about 0.01 ⁇ L/g matrix/hr and about 30 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 48 is between about 1 ⁇ L/g matrix/hr and about 30 ⁇ L/g matrix/hr.
  • the rate of release of active ingredient at hour 72 is greater than zero ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 72 is at least about 0.01 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 72 is at least about 0.1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 72 is at least about 1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 72 is at least about 3 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 72 is at least about 5 ⁇ L/g matrix/hr.
  • the rate of release of active ingredient at hour 72 is at least about 10 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 72 is at least about 15 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 72 is between about 0.01 ⁇ L/g matrix/hr and about 3 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 72 is between about 0.14/g matrix/hr and about 3 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 72 is between about 1 ⁇ L/g matrix/hr and about 34/g matrix/hr.
  • the rate of release of active ingredient at hour 72 is between about 0.01 ⁇ L/g matrix/hr and about 15 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 72 is between about 0.14/g matrix/hr and about 15 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 72 is between about 1 ⁇ L/g matrix/hr and about 15 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 96 is greater than zero ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 96 is at least about 0.01 ⁇ L/g matrix/hr.
  • the rate of release of active ingredient at hour 96 is at least about 0.1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 96 is at least 1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 96 is at least about 2 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 96 is between about 0.01 ⁇ L/g matrix/hr and about 24/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 96 is between about 0.14/g matrix/hr and about 2 ⁇ L/g matrix/hr.
  • the rate of release of active ingredient at hour 96 is between about 1 ⁇ L/g matrix/hr and about 2 ⁇ L/g matrix/hr. In some embodiments, the rate release of active ingredient at hour 120 is greater than zero ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 120 is at least about 0.01 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 120 is at least about 0.1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 120 is at least about 1 ⁇ L/g matrix/hr.
  • the rate of release of active ingredient at hour 120 is between about 0.01 ⁇ L/g matrix/hr and about 1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 120 is between about 0.1 ⁇ L/g matrix/hr and about 10 ⁇ L/g matrix/hr. In some embodiments, the rate release of active ingredient at hour 240 is greater than zero ⁇ L/g matrix/hr. In some embodiments, the rate release of active ingredient at hour 120 is greater than zero ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 168 is at least about 0.01 ⁇ L/g matrix/hr.
  • the rate of release of active ingredient at hour 168 is at least about 0.1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 168 is at least about 0.5 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 168 is at least about 2 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 168 is at least about 5 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 168 is at least about 10 s ⁇ L/g matrix/hr.
  • the rate of release of active ingredient at hour 168 is between about 0.01 ⁇ L/g matrix/hr and about 0.5 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 168 is between about 0.01 ⁇ L/g matrix/hr and about 3 ⁇ L/g matrix/hr In some embodiments, the rate of release of active ingredient at hour 168 is between about 0.01 ⁇ L/g matrix/hr and about 5 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 168 is between about 0.5 ⁇ L/g matrix/hr and about 13 ⁇ L/g matrix/hr.
  • the rate release of active ingredient at hour 240 is greater than zero ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 240 is at least about 0.01 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 240 is at least about 0.1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 240 is at least about 1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 240 is at least about 1.5 ⁇ L/g matrix/hr.
  • the rate of release of active ingredient at hour 240 is between about 0.01 ⁇ L/g matrix/hr and about 1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 240 is between about 0.1 ⁇ L/g matrix/hr and about 1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 240 is between about 0.1 ⁇ L/g matrix/hr and about 1.5 ⁇ L/g matrix/hr. In some embodiments, the rate release of active ingredient at hour 336 is greater than zero ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 336 is at least about 0.01 ⁇ L/g matrix/hr.
  • the rate of release of active ingredient at hour 336 is at least about 0.1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 336 is at least about 1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 336 is between about 0.01 ⁇ L/g matrix/hr and about 1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient at hour 336 is between about 0.1 ⁇ L/g matrix/hr and about 1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient sustained between hour 1 and hour 216 is at least about 14/g matrix/hr.
  • the rate of release of active ingredient sustained between hour 22 and hour 120 is at least about 1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient sustained between hour 22 and hour 120 is at least about 2 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient sustained between hour 22 and hour 96 is at least about 1 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient sustained between hour 22 and hour 96 is at least about 2 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient sustained between hour 22 and hour 72 is at least about 1 ⁇ L/g matrix/hr.
  • the rate of release of active ingredient sustained between hour 22 and hour 72 is at least about 4 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient sustained between hour 22 and hour 72 is at least about 10 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient sustained between hour 22 and hour 72 is at least about 15 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient sustained between hour 22 and hour 168 is at least about 5 ⁇ L/g matrix/hr. In some embodiments, the rate of release of active ingredient sustained between hour 22 and hour 168 is at least about 10 ⁇ L/g matrix/hr.
  • the release rate of the active ingredient between hour 22 and hour 120 is sustained within a range of about 0.1 and about 2 ⁇ L/g matrix/hr. In some embodiments, a release rate of the active ingredient between hour 22 and hour 120 is sustained within a range of about 1 and about 15 ⁇ L/g matrix/hr. In some embodiments, the release rates discussed above occur at ambient room temperature (approximately 23-25° C.) and at atmospheric pressure. In some embodiments, the release rates above relate to the release of ethylene inhibitor active ingredients, for example, cyclopropenes from a matrix. In a non-limiting embodiment, the controlled release parameters above relate to the release of at least one of an essential oil, a hexanal, a terpene and a terpenoid from a matrix.
  • Controlled release may alternatively be quantified as a percentage of the rate of release as compared to the rate of release at hour one (1), for example.
  • the rate of release of active ingredient at hour 22 is at least 0.1% of the release rate at hour 1.
  • the rate of release of active ingredient at hour 22 is at least 1% of the release rate at hour 1.
  • the rate of release of active ingredient at hour 22 at least 2.5% of the release rate at hour 1.
  • the rate of release of active ingredient at hour 22 is at least 10% of the release rate at hour 1.
  • the release of active ingredient at hour 22 is at least 20% of the rate of release at hour 1.
  • the rate of release of active ingredient at hour 48 is at least 0.1% of the release rate at hour 1. In some embodiments, the release of active ingredient at hour 48 is at least 1% of the release rate at hour 1. In some embodiments, the rate of release of active ingredient at hour 48 is at least 2% of the release rate at hour 1. In some embodiments, the rate of release of active ingredient at hour 48 is at least 10% of the release rate at hour 1. In some embodiments, the rate of release of active ingredient at hour 72 is at least 0.1% of the release rate at hour 1. In some embodiments, the rate of release of active ingredient at hour 72 is at least 1% of the rate of release at hour 1. In some embodiments, the rate of release of active ingredient at hour 72 is at least 10% of the release rate at hour 1.
  • the rate of release of active ingredient at hour 96 is at least 0.1% of the release rate at hour 1. In some embodiments, the rate of release of active ingredient at hour 96 is at least 1% of the release rate at hour 1. In some embodiments, the rate of release of active ingredient at hour 96 is at least 5% of the release rate at hour 1. In some embodiments, the rate of release of active ingredient at hour 168 is at least 0.1% of the rate of release at hour 1. In some embodiments, the rate of release of active ingredient at hour 168 is at least 1% of the release rate at hour 1. In some embodiments, the rate of release of active ingredient at hour 168 is at least 4% of the release rate at hour 1.
  • the rate of release of active ingredient at hour 240 is at least 0.1% of the release rate at hour 1. In some embodiments, the rate of release of active ingredient at hour 240 is at least 1% of the release rate at hour 1. In some embodiments, the rate of release of active ingredient at hour 336 is at least 0.1% of the rate of release rate at hour 1. In some embodiments, the rate of release of active ingredient at hour 336 is at least 1% of the release rate at hour 1. In some embodiments, the rate of release of active ingredient at hour 48 is at least 1% of the rate of release at hour 24. In some embodiments, the rate of release of active ingredient at hour 48 is at least 10% of the rate of release at hour 24.
  • the rate of release of active ingredient at hour 48 is at least 20% of the rate of release at hour 22. In some embodiments, the rate of release of active ingredient at hour 48 is at least 50% of the rate of release at hour 22. In some embodiments, the rate of release of active ingredient at hour 48 is at least 60% of the rate of release at hour 22. In some embodiments, the rate of release of active ingredient at hour 48 is at least 75% of the rate of release at hour 22. In some embodiments, the rate of release of active ingredient at hour 48 is at least 90% of the rate of release at hour 22. In some embodiments, the rate of release of active ingredient at hour 48 is at least 95% of the rate of release at hour 22.
  • the rate of release of active ingredient at hour 72 is at least 1% of the rate of release at hour 22. In some embodiments, the rate of release of active ingredient at hour 72 is at least 10% of the rate of release at hour 22. In some embodiments, the rate of release of active ingredient at hour 72 is at least 20% of the rate of release at hour 22. In some embodiments, the rate of release of active ingredient at hour 72 is at least 30% of the rate of release at hour 22. In some embodiments, the rate of release of active ingredient at hour 72 is at least 50% of the rate of release at hour 22. In some embodiments, the rate of release of active ingredient at hour 72 is at least 60% of the rate of release at hour 22.
  • the rate of release of active ingredient at hour 1 is between about 10 ⁇ L/g matrix/hr and about 1500 ⁇ L/g matrix/hr. In a non-limiting embodiment, the rate of release of active ingredient at hour 1 is between about 30 ⁇ L/g matrix/hr and about 1500 ⁇ L/g matrix/hr. In a non-limiting embodiment, the rate of release of active ingredient at hour 1 is between about 100 ⁇ L/g matrix/hr and about 1500 ⁇ L/g matrix/hr. In a non-limiting embodiment, the rate of release of active ingredient at hour 1 is between about 30 ⁇ L/g matrix/hr and about 500 ⁇ L/g matrix/hr.
  • the rate of release of active ingredient at hour 1 is between about 30 ⁇ L/g matrix/hr and about 1500 ⁇ L/g matrix/hr.
  • the release profiles discussed above occur at ambient room temperature (approximately 23-25° C.) and at atmospheric pressure.
  • the controlled release parameters above relate to the release of cyclopropenes from a matrix.
  • the controlled release parameters above relate to the release of at least one of an essential oil, a hexanal, a terpene and a terpenoid from a matrix.
  • compositions described herein can be used to improve the quality and shelf life of produce.
  • the quality and shelf life of produce may be improved, for example, by inhibiting the effects of ethylene, promoting the effects of ethylene, enhancing or maintaining shelf life, color, firmness, weight, sweetness, flavor, heat or chill temperature tolerance, resistance to microbes, fungi, or other pathogens, and/or humidity tolerance.
  • the products and processes described herein may be applied to either pre-harvest or post-harvest produce.
  • Processed produce refers to produce that has been altered by at least one mechanical, chemical, or physical process that modify the natural state or appearance of the produce. Mashed, cut, peeled, diced, squeezed, and chopped produce are non-limiting examples of processed produce. Produce also can refer to hydroponically-grown plants.
  • produce comprises berries.
  • a composition comprising a delivery material and at least one active ingredient may be used, for example, to extend the shelf life of berries, including but not limited to strawberries, raspberries, blueberries, blackberries, elderberries, gooseberries, golden berries, grapes, champagne grapes, Concord grapes, red grapes, black grapes, green grapes, and globe grapes.
  • the active ingredient in the vapor phase extends the shelf life of berries by optionally slowing or inhibiting the growth of, or optionally reducing the physical, physiological, biological, or cosmetic symptoms caused by, the action of one or more viruses, fungi, microbes, bacteria, pathogens, pests, or insects on the berries.
  • produce comprises vegetables.
  • vegetables that may be treated by the compositions described herein include, but are not limited to, leafy green vegetables such as lettuce (e.g., Lactuea sativa ), spinach ( Spinaca oleracea ) and cabbage ( Brassica oleracea ; various roots such as potatoes ( Solanum tuberosum ), carrots ( Daucus ); snapbeans ( Phaseolus vulgaris ), bulbs such as onions ( Allium sp.); herbs such as basil ( Ocimum basilicum ), oregano ( Origanum vulgare ) and dill ( Anethum graveolens ); as well as soybean ( Glycine max ), lima beans ( Phaseolus limensis ), peas ( Lathyrus sp.), corn ( Zea mays ), broccoli ( Brassica oleracea italica ), cauliflower ( Brassica oleracea botrytis ) and asparagus ( Asparagus officinalis
  • leafy green vegetables such as
  • produce comprises fruit.
  • fruits that may be treated by the compositions described herein include, but are not limited to, tomatoes ( Lycopersicon esculentum ), apples ( Malus domes tica ), bananas ( Musa sapientum ), cherries ( Prunus avium ), grapes ( Vitis vinifera ), pears ( Pyrus communis ), papaya ( Carica papya ), mangoes ( Mangifera indica ), peaches ( Prunus persica ), apricots ( Prunus armeniaca ), nectarines ( Prunus persica nectarina ), oranges ( Citrus sp.), lemons ( Citrus limonia ), limes ( Citrus aurantifolia ), grapefruit ( Citrus paradisi ), tangerines ( Citrus nobilis deliciosa ), kiwi ( Actinidia.
  • chinenus melons such as cantaloupes ( C. cantalupensis ) and musk melons ( C. melo ), honeydew, pineapples ( Aranae comosus ), persimmon ( Diospyros sp.) and raspberries (e.g., Fragaria or Rubus ursinus ), blueberries ( Vaccinium sp.), green beans ( Phaseolus vulgaris ), members of the genus Cucumis such as cucumber ( C. sativus ), starfruit, and avocados ( Persea americana ).
  • melons such as cantaloupes ( C. cantalupensis ) and musk melons ( C. melo ), honeydew, pineapples ( Aranae comosus ), persimmon ( Diospyros sp.) and raspberries (e.g., Fragaria or Rubus ursinus ), blueberries ( Vaccinium sp.), green beans ( Phaseolus vulgaris
  • produce comprises cut flowers or ornamental plants.
  • ornamental plants that may be treated by the compositions described herein include, but are not limited to, potted ornamentals and cut flowers.
  • Potted ornamentals and cut flowers which may be treated with the methods of the present invention include azalea ( Rhododendron spp.), hydrangea ( Macrophylla hydrangea ), hibiscus ( Hibiscus rosasanensis ), snapdragons ( Antirrhinum sp.), poinsettia ( Euphorbia pulcherima ), cactus (e.g., Cactaceae schlumbergera truncata ), begonias ( Begonia sp.), roses ( Rosa sp.), tulips ( Tulipa sp.), daffodils ( Narcissus sp.), petunias ( Petunia hybrida ), carnation ( Dianthus caryophyllus ), l
  • produce comprises plants.
  • plants that may be treated by the compositions described herein include, but are not limited to, cotton ( Gossypium spp.), pecans (Carva coffee ( Cofffea arabica ), and weeping fig ( Ficus henjamina ), as well as dormant seedlings such as various fruit trees including apple, ornamental plants, shrubbery, and tree seedlings.
  • shrubbery which may be treated with the compositions described herein include, but are not limited to, privet ( Ligustrum sp.), photinea ( Photina sp.), holly ( Ilex sp.), ferns of the family Polypodiaceae, schefflera ( Schefflera sp.), aglaonema ( Aglaonema sp.), Laceaster ( Cotoneaster sp.), barberry ( Berberris sp.), waxmyrtle ( Myrica sp.), abelia ( Abelia sp.), acacia ( Acacia sp.), and bromeliades of the family Bromeliaceae.
  • one or more active ingredients may be delivered to produce using the compositions described herein.
  • the active ingredient(s) may improve quality and/or extend shelf life of the produce.
  • Produce aging a process called senescence, negatively impacts the quality and shelf life of produce.
  • Senescence occurs, in part, due to a response to ethylene gas.
  • Ethylene activity causes wilting, erosion of flavor and aesthetics, and ultimately leads to spoilage of produce.
  • Senescence in produce can be slowed by the use of an ethylene inhibitor.
  • Ethylene inhibitors protect produce from ethylene damage, improving produce quality and shelf life, for example preserving texture, flavor, and aroma.
  • Ethylene inhibitors block the ethylene receptor sites in produce.
  • Known ethylene inhibitors useful for embodiments disclosed herein include, but are not limited to, cyclopentadiene, cyclopropene, diazocyclopentadiene, 1-methylcyclopropene (1-MCP), 3,3-dimethycyclopropene, methylenecyclopropane, trans-cyclooctene, cis-cyclooctene, 2,5-norbornadiene, 3,3-dipentylcyclopropene, 1-pent-2-enyl-2-pentyl-cyclopropene, 1-pent-2-enyl-3,3-dipentylcyclopropene, 4-(1-cyclopropenyl)-2-methylbutan-2-ol, 1-(n-amyl)-cyclopropene, 1-(5,5,5-trifluoropentyl)-cyclopropene, and 1,2-dipentyl-cyclopropene, and
  • the active ingredient is 1-methylcyclopropene (1-MCP).
  • the active ingredient may be a cyclopropene compound.
  • a cyclopropene compound also referred to herein as a cyclopropene, is any compound with the formula
  • R 1 , R 2 , R 3 and R 4 is independently selected from the group consisting of H and a chemical group of the formula:
  • each L is a bivalent radical
  • Z is a monovalent radical.
  • L groups include radicals containing one or more atoms selected from H, B, C, N, O, P, S, Si, or mixtures thereof. The atoms within an L group may be connected to each other by single bonds, double bonds, triple bonds, or mixtures thereof. Each L group may be linear, branched, cyclic, or a combination thereof. In any one R group (e.g., any one of R 1 , R 2 , R 3 and R 4 ) the total number of heteroatoms (e.g., atoms that are neither H nor C) is from 0 to 6.
  • any one R group the total number of non-hydrogen atoms is 50 or less.
  • Z groups are hydrogen, halo, cyano, nitro, nitroso, azido, chlorate, bromate, iodate, isocyanato, isocyanide, isothiocyanato, pentafluorothio, and a chemical group G, wherein G is a 3 to 14 membered ring system.
  • the R 1 , R 2 , R 3 , and R 4 groups are independently selected from the suitable groups.
  • the groups that are suitable for use as one or more of R 1 , R 2 , R 3 , and R 4 are, for example, aliphatic groups, aliphatic-oxy groups, alkylphosphonato groups, cycloaliphatic groups, cycloalkylsulfonyl groups, cycloalkylamino groups, heterocyclic groups, aryl groups, heteroaryl groups, halogens, silyl groups, other groups, and mixtures and combinations thereof.
  • Groups that are suitable for use as one or more of R 1 , R 2 , R 3 , and R 4 may be substituted or unsubstituted.
  • suitable R 1 , R 2 , R 3 , and R 4 groups are, for example, aliphatic groups.
  • suitable aliphatic groups include, for example, alkyl, alkenyl, and alkynyl groups.
  • Suitable aliphatic groups may be linear, branched, cyclic, or a combination thereof. Independently, suitable aliphatic groups may be substituted or unsubstituted.
  • a chemical group of interest is said to be “substituted” if one or more hydrogen atoms of the chemical group of interest is replaced by a substituent.
  • R 1 , R 2 , R 3 , and R 4 groups are, for example, substituted and unsubstituted heterocyclyl groups that are connected to the cyclopropene compound through an intervening oxy group, amino group, carbonyl group, or sulfonyl group; examples of such R 1 , R 2 , R 3 , and R 4 groups are heterocyclyloxy, heterocyclylcarbonyl, diheterocyclylamino, and diheterocyclylaminosulfonyl.
  • R 1 , R 2 , R 3 , and R 4 groups are, for example, substituted and unsubstituted heterocyclic groups that are connected to the cyclopropene compound through an intervening oxy group, amino group, carbonyl group, sulfonyl group, thioalkyl group, or ammosulfonyl group; examples of such R 1 , R 2 , R 3 , and R 4 groups are diheteroarylamino, heteroarylthioalkyl, and diheteroarylaminosulfonyl.
  • R 1 , R 2 , R 3 , and R 4 groups are, for example, hydrogen, fluoro, chloro, bromo, iodo, cyano, nitro, nitroso, azido, chlorato, bromato, iodato, isocyanato, isocyanido, isothiocyanato, pentafluorothio; acetoxy, carboethoxy, cyanato, nitrato, nitrito, perchlorato, allenyl, butylmercapto, diethylphosphonato, dimethylphenylsilyl, isoquinolyl, mercapto, naphthyl, phenoxy, phenyl, piperidino, pyridyl, quinolyl, triethylsilyl, trimethylsilyl; and substituted analogs thereof.
  • the chemical group G is a 3 to 14 membered ring system.
  • Ring systems suitable as chemical group G may be substituted or unsubstituted; they may be aromatic (including, for example, phenyl and napthyl) or aliphatic (including unsaturated aliphatic, partially saturated aliphatic, or saturated aliphatic); and they may be carbocyclic or heterocyclic.
  • heterocyclic G groups some suitable heteroatoms are, for example, nitrogen, sulfur, oxygen, and combinations thereof.
  • Ring systems suitable as chemical group G may be monocyclic, bicyclic, tricyclic, polycyclic, Spiro, or fused; among suitable chemical group G ring systems that are bicyclic, tricyclic, or fused, the various rings in a single chemical group G may be all the same type or may be of two or more types (for example, an aromatic ring may be fused with an aliphatic ring).
  • one or more of R 1 , R 2 , R 3 , and R 4 is hydrogen or (C 1 -C 10 ) alkyl. In another embodiment, each of R 1 , R 2 , R 3 , and R 4 is hydrogen or (C 1 -C 8 ) alkyl. In another embodiment, each of R 1 , R 2 , R 3 , and R 4 is hydrogen or (C 1 -C 4 ) alkyl. In another embodiment, each of R 1 , R 2 , R 3 , and R 4 is hydrogen or methyl. In another embodiment, is (C 1 -C 4 ) alkyl and each of R 2 , R 3 and R 4 is hydrogen. In another embodiment, R 1 is methyl and each of R 2 , R 3 , and R 4 is hydrogen, and the cyclopropene compound is known herein as 1-methylcyclopropene or “1-MCP.”
  • ethylene inhibitors useful for embodiments disclosed herein may also include: phosphonic acid compounds and derivatives thereof, for example, those disclosed in U.S. Pat. Nos. 3,879,188 and 6,562,758; diazocyclopentadiene and derivatives thereof, for example, those disclosed in U.S. Pat. No. 5,100,462; cyclopropene, 1.1.1. propellane, and derivatives thereof, for example, those disclosed in U.S. Pat. No. 5,518,988; and silver thiosulfate and derivatives thereof.
  • phosphonic acid compounds and derivatives thereof for example, those disclosed in U.S. Pat. Nos. 3,879,188 and 6,562,758
  • diazocyclopentadiene and derivatives thereof for example, those disclosed in U.S. Pat. No. 5,100,462
  • cyclopropene, 1.1.1. propellane and derivatives thereof, for example, those disclosed in U.S. Pat. No. 5,518,988
  • cyclopropenes comprise organic compounds containing any unsubstituted or substituted three-carbon cyclic ring with an unsaturated or olefinic bond (of the root formula C 3 H x ), or any organic compound containing a cyclopropene moiety.
  • the simplest example of this class of molecules is cyclopropene, the simplest cycloalkene.
  • the cyclopropene unit has a triangular structure.
  • Cyclopropenes also include cyclopropene derivatives, such as 1-methylcyclopropene (1-MCP; molecular formula C 4 H 6 ), or other cyclopropene derivatives (including, but not limited to borirenes, phosphirenes, and silirenes, which are boron-, phosphorus-, and silicon-substituted cyclopropenes respectively).
  • cyclopropene derivatives such as 1-methylcyclopropene (1-MCP; molecular formula C 4 H 6 )
  • other cyclopropene derivatives including, but not limited to borirenes, phosphirenes, and silirenes, which are boron-, phosphorus-, and silicon-substituted cyclopropenes respectively.
  • active ingredients useful for embodiments disclosed herein may include, for example, inhibitors of ethylene biosynthesis, including aminoethoxyvinylglycine, alpha-amino isobutyric acid, (aminooxy) acetic acid, methoxyvinylglycine, salicylic acid, acetylsalicylic acid, L-trans-2-amino-4-(2-acetamidoethoxy)-3-butenoic acid, among others, as disclosed in U.S. Pat. Nos. 8,603,524 and 6,153,559.
  • inhibitors of ethylene biosynthesis including aminoethoxyvinylglycine, alpha-amino isobutyric acid, (aminooxy) acetic acid, methoxyvinylglycine, salicylic acid, acetylsalicylic acid, L-trans-2-amino-4-(2-acetamidoethoxy)-3-butenoic acid, among others, as disclosed in U.S. Pat. Nos
  • Additional preservatives useful for embodiments disclosed herein may include agents that prevent the ripening of fruits and vegetables or the browning of cut fruits and vegetables, including inhibitors of fruit and vegetable membrane degrading phospholipases.
  • Inhibitors of fruit and vegetable membrane degrading phospholipases may include hexanal, lysophosphatidylethanolamine, and their derivatives.
  • Inhibitors of fruit and vegetable membrane degrading phospholipases may also include, for example, cytokines, such as N-(2-chloro-4-pyrridinyl)N-phenyl urea, as disclosed in U.S. Pat. No. 8,603,524. The U.S. patents mentioned in this paragraph are incorporated by reference in their entirety.
  • the active ingredient includes additional volatile plant hormones known to effect plant biological processes for the purpose of improving crop yield, quality, taste, or extending produce shelf-life, including but not limited to methyl salicylate, methyl jasmonate, (Z)-3hexenyl acetate, (z)-3-hexenal, (E)-beta-farnesene, (E)-beta-caryophyllene, (E)-beta-ocimene, Linalool, (E)-4,8-dimethyl-1,3,7-nonatriene, and (E,E)-4,8,12-trimethyl-1,3,7,11-tridecatetraene.
  • additional volatile plant hormones known to effect plant biological processes for the purpose of improving crop yield, quality, taste, or extending produce shelf-life, including but not limited to methyl salicylate, methyl jasmonate, (Z)-3hexenyl acetate, (z)-3-hexenal, (E)-beta-farnes
  • the active ingredient is another preservative for edible substances or foods to extend their freshness, shelf life, or suitability for consumption by living organisms.
  • These preservatives may include either natural or synthetic compositions that have anti-bacterial, anti-fungal, anti-viral, or other preventative or curative properties, such as having insecticidal and insect repellent properties.
  • the preservatives include essential oils or botanical extracts that have anti-bacterial, anti-fungal, anti-algae, anti-viral, mold inhibitors, or other preventative or curative properties such as having insecticidal and insect repellent properties.
  • the preservatives may include natural or synthetic compositions with anti-oxidant properties. These preservatives may be suitable for applications such as the packaging and preservation of perishable substances such as produce, meat products, dairy products, edible substances, non-edible substances, and other perishable substances.
  • active ingredients that can be incorporated into the matrices of the present application include, but are not limited to, limonene, proteases, xylanases, alpha-amylases, cellulases, ⁇ -glucanases, ⁇ -galactosidases, beta-mannases, polygalacturonases, arabinases, galactanases, arabinofuranosidases, feroyl esterases, and glucosidases, proteinase inhibitors, cryptoxanthin and derrivatives thereof, oregano oil and caprylic acid, aflatoxin B1, ochratoxin A (OTA), zearalenone, mycophenolic acid, cyclopiazonic acid, Fumonisin B 1, T-2 and patulin, vitamins A, C, and E, beta-carotene, hydroxylase phytases, lutein, zeaxanthin, beta-carotene, retinoids, retinal
  • the active ingredient is a compound or multiple compounds with efficacy in applications as an antiviral, antifungal, antimicrobial, antibacterial, antipathogenic, biocidal, pesticidal, or biopesticidal agent or agent(s).
  • the active ingredient may slow or inhibit the growth of one or more viruses, fungi, microbes, bacteria, pathogens, pests, or insects.
  • the active ingredient may reduce the spore count of produce by slowing or inhibiting the growth of one or more viruses, fungi, microbes, bacteria, pathogens, pests, or insects.
  • the active ingredient may reduce the physical, physiological, biological, or cosmetic symptoms caused by the action of one or more viruses, fungi, microbes, bacteria, pathogens, pests, or insects.
  • the active ingredient may extend the shelf life of produce by slowing or inhibiting the growth of, or optionally reducing the physical, physiological, biological, or cosmetic symptoms caused by, the action of one or more viruses, fungi, microbes, bacteria, pathogens, pests, or insects on the produce.
  • an active ingredient comprises an essential oil.
  • essential oils have detectable concentrations of terpenes and/or terpenoids that provide antibacterial and/or antifungal properties.
  • an active ingredient is a terpene or a terpenoid.
  • Non-limiting examples of terpenes include acyclic and cyclic terpenes, monoterpenes, diterpenes, oligoterpenes, and polyterpenes with any degree of substitution
  • an active ingredient is an essential oil comprising an extract from, for example, an herb, a plant, a trees, or a shrub.
  • an essential oil comprises at least one of a terpene, a terpenoid, a phenol, or a phenolic compounds.
  • essential oils and essential oil extracts include, thymol, curcumin, carvacrol, bay leaf oil, lemongrass oil, clove oil, peppermint oil, acacia oil, eucalyptol, limonene, eugenol, menthol, farnesol, carvone, hexanal, thyme oil, dill oil, oregano oil, neem oil, orange peel oil, lemon peel oil, rosemary oil, or cumin seed extract.
  • an active ingredient is at least one of oregano oil, thyme oil, hexanal, carvacrol, and thymol.
  • compositions comprise one or more terpenes and/or terpenoids.
  • the composition comprises an active ingredient selected from the group consisting of oregano oil, thyme oil, hexanal, carvacrol, and thymol, and combinations thereof.
  • an active ingredient comprises hydrogen peroxide in any concentration from 0.001%-100% by weight. In a non-limiting embodiment, an active ingredient comprises phenol.
  • the active ingredient is an ethylene production stimulating agent.
  • Ethylene generating agents such as ethephon, may be used to promote ripening, fruit coloring, and other known effects of ethylene.
  • Active ingredients including ethylene inhibiting active ingredients, compounds that inhibit or promote the ethylene response in produce, compounds that inhibit ethylene biosynthesis, phospholipase inhibitors, other compounds known to promote membrane or plant cell wall integrity, and other various preservatives may be used alone, or in combinations of two or more, in the compositions and structures described herein.
  • the composition comprises a delivery material.
  • the delivery material may be used to store and/or release the active ingredient.
  • Many of the above-described active ingredients may be in the vapor phase or gaseous, including cyclopropenes such as 1-MCP.
  • Complexes may be formed between the above-described active ingredients and a delivery material to overcome instability, handling, and shelf-life issues, among others.
  • 1-MCP for example, is a gas at room temperature and room pressure, and may be stabilized by complexation with a delivery material.
  • the terpenoid carvacrol is a liquid at ambient room temperature and atmospheric pressure with a boiling point >250° C.
  • carvacrol may be stored in a solid material and delivered in the vapor phase using a solid carrier.
  • the delivery material is a solid having a high surface area, as described in more detail herein.
  • the delivery material is porous.
  • the delivery material is nanoporous.
  • Non-limiting examples of porous materials are macroporous, mesoporous, and microporous materials.
  • the porous and/or nanoporous delivery material comprises one or more of macropores, mesopores, and micropores.
  • macropores are pores having a diameter greater than 50 nm.
  • macropores may have diameters of between 50 and 1000 nm.
  • mesopores are pores having a diameter between 2 nm and 50 nm.
  • micropores are pores having a diameter of less than 2 nm.
  • micropores may have diameters of between 0.2 and 2 nm. This comprising the delivery material and the active ingredient can be transported, for example, in hermetically sealed packing.
  • the active ingredient may be stabilized by, associated with, or impregnated in a delivery material by: i) covalent binding, dative binding, electrostatic binding, van der Waals binding, or chelative binding of an appropriate active ingredient at or within a moiety or chemically functionalized site immobilized on the internal and/or external chemical surface of the delivery material, ii) encapsulation of the active ingredient (the “guest”) using a chemical functionalization (“the host” in “host-guest” chemistry) that mimics an enzymatic site, “lock-and-key” structure, or other chelative interaction in which the chemical structure of the host holds a specific affinity for the chemical structure of the guest, iii) nonspecific physicochemical interactions with the inert internal and/or external chemical surface of the delivery material, in such a way as to manipulate adsorption/desorption equilibrium, or iv) a combination of various forms of adsorption/desorption
  • Unique combinations of chemical interactions and adsorption/desorption manipulations leading to unique loading and release parameters may be achieved by varying the concentration and chemical identity of immobilized functional groups in the delivery material, varying the hydrophobicity or hydrophilicity of the inert internal and/or external surface of the delivery material, varying the crystallinity of the delivery material, varying the pore dimensions and volume of the delivery material, and varying the total chemical surface area of the material.
  • the delivery material is a carbon material, also referred to herein as a carbon based delivery material.
  • a carbon material may be of various geometries and formations including, but not limited to, macroporous, mesoporous, and microporous carbon materials, monolithic carbon materials, extruded or pelletized carbon materials, steam-activated carbon materials, oxidized carbon materials, or acid- or base-treated carbon materials.
  • FIG. 1 shows a cross-section of an illustrative embodiment of a delivery material 100 .
  • delivery material 100 is a carbon based delivery material.
  • FIG. 1 shows a cross-section of an illustrative embodiment of a delivery material 100 .
  • delivery material 100 is a carbon based delivery material.
  • FIG. 1 shows a cross-section of an illustrative embodiment of a delivery material 100 .
  • delivery material 100 is a carbon based delivery material.
  • FIG. 1 shows a cross-section of an illustrative embodiment of a delivery material 100
  • delivery material 100 contains at least one macropore 10 , at least one mesopore 11 , and at least one micropore 12 .
  • a porous delivery material 100 contains only either one or both of macropores 10 and mesopores 11 .
  • a porous material does not contain internal micropores or mesopores, limiting the porosity to the macropores 10 .
  • a carbon delivery material may be commercially available carbon material which is offered are offered in a wide array of states with respect to surface areas, porosities, degrees of surface functionalization, degree of oxidation, acidity, basicity, and other chemical and physicochemical features.
  • the following commercial carbon materials may be used as delivery material for the compositions matrices described herein: carbon black (e.g. such as generally indicated by CAS No.: 1333-86-4) or lampblack carbon; activated carbon or activated charcoal (e.g.
  • carbon in powder, granule, film, or extrudate form such as generally indicated by CAS No.: 7440-44-0
  • carbon in powder, granule, film, or extrudate form optionally, carbon mixed with one or more adjuvants or diluents
  • Each of those carbons can be further modified to form other delivery materials 100 by operations including, but not limited to heat treating materials, oxidation, and/or acid- or base-treatment to arrive at other delivery materials and matrices described herein.
  • the delivery materials described herein combine chemical interactions between the delivery material and active ingredient with an adsorption/desorption equilibrium at the material surface. Characteristics of the delivery material can be modified to provide deliberately accelerated or deliberately decelerated release of the active ingredient as compared to the release rate of an active ingredient from a matrix comprising an unmodified delivery material. For example, hydrolyzing or oxidizing the hydrophobic carbon surface with adsorption-modifying functionalities to increase the polarity of the carbon surface can modify the hydrophobicity or hydrophilicity of a carbon material.
  • FIG. 3 illustrates a non-limiting embodiment of a portion of another delivery material 300 .
  • Delivery material 300 comprises a plurality of pores 30 . While pores 30 are shown in FIG. 3 to have a regular distribution in delivery material 300 , regularity in pore distribution is not necessary. Delivery material 300 may have pores 30 that are different sizes and/or are irregularly distributed in delivery material 300 . Delivery material 300 optionally comprises one or more complexing agents 40 .
  • FIG. 3 shows an example of an internal view of a pore 31 of delivery material 300 of delivery material 300 that comprises complexing agents 40 .
  • the delivery material may be a silicate material, also referred to herein as a silica based material.
  • a delivery material comprising a silicate material comprises silica.
  • Silicate materials are available from commercial sources in a wide array of states with respect to surface areas, porosities, degrees of surface functionalization, acidity, basicity, and other chemical and physicochemical features. Commercial silicates may be in the form of powder, granules, nanoscale particles, and porous particles.
  • delivery material 300 comprises silica gel.
  • delivery material 300 comprises one or more of macropores, mesopores, and micropores.
  • delivery material 300 comprises one or more of macroporous, mesoporous, and microporous silica.
  • delivery material 300 comprises precipitated, crystalline-free silica gel (such as generally indicated by CAS No. 112926-00-8).
  • material 300 comprises amorphous, fumed (crystalline free) silica (such as generally indicated by CAS No. 112945-52-5).
  • material 300 comprises mesostructured amorphous silica (such as generally indicated by CAS No. 7631-86-9).
  • a silicate delivery material comprises one or more of a polysiloxane, polyalkylsiloxane, and polyalkylenesiloxane materials; a polyoxoalkyelene material, metal oxide, and a zeolite.
  • the delivery material 300 may further comprise a complexing agent 40 .
  • the delivery material 300 comprises a porous material and a complexing agent 40 , the complexing agent embedded into at least one pore 31 of the porous material.
  • a complexing agent may be embedded into the delivery material via de novo synthesis, post-synthetic grafting, intercalation of the complexing agent into the macrostructure, or other techniques yielding immobilized complexing agents on the internal and/or external chemical surface of the delivery material.
  • complexing agents 40 may be used to further reduce and/or eliminate instability, handling, low vapor pressure of active ingredients, and/or shelf-life issues of volatile active ingredients.
  • a plurality of pores 30 may optionally be modified with complexing agents to produce pore 31 of delivery material 300 .
  • a complexing agent is a compound that has a lock and key structure, similar to an enzyme, whereby a substrate selectively fits into the encapsulation site.
  • the interaction between an active ingredient and a complexing agent may sometimes be characterized as “host-guest” chemistry, in which the active ingredient is the guest and the complexing agent is the host.
  • the complexing agent may be ⁇ -cyclodextrin, ⁇ -cyclodextrin, or ⁇ -cyclodextrin.
  • complexing agents may be mono-, oligo-, or polycarbohydrates, porphyrins, and phosphazenes.
  • the complexing agent may be selected from one or more of the following groups of compounds: cyclodextrins, substituted and/or modified cyclodextrins, crown ethers, substituted and/or modified crown ethers, calixarenes, and substituted and/or modified calixarenes.
  • a delivery material comprises more than one type of complexing agent.
  • pore 31 of FIG. 3 is illustrative only, and that complexing agents 40 are not required to be present in the delivery materials described herein.
  • the delivery material comprises a complexing agent in a concentration of 0-50 mol % of the delivery material (as measured determined from the empirical formula units in the ratio moles of complexing agent:moles of unmodified delivery material).
  • the complexing agent is cyclodextrin in a concentration of 0-20 mol % of the delivery material (as measured determined from the empirical formula units in the ratio moles of complexing agent:moles of unmodified delivery material, for example moles of SiO 2 ).
  • the complexing agent is ⁇ -cyclodextrin in a concentration of 0-20 mol % of the delivery material.
  • the complexing agent is ⁇ -cyclodextrin in a concentration of 0-20 mol. % of the delivery material. In a non-limiting embodiment, the complexing agent is substituted ⁇ -cycloderarin in a concentration of 0-20 mol % of the delivery material. In a non-limiting embodiment, the complexing agent is silyl-CD 44 ( FIG. 5 ) in a concentration of 0-20 mol % of the delivery material. In a non-limiting embodiment, the complexing agent is allyl-CD 45 ( FIG. 5 ) in a concentration of 0-20 mot % of the delivery material.
  • the complexing agent at 0-20 mol % concentration in the delivery material is embedded in a porous silicate material, the complexing agent together forming the delivery material.
  • the porous silicate material is a templated siliceous material approaching the composition SiO 2 .
  • the porous silicate material is also a high surface area material.
  • a delivery material comprises one of a complexing agent and an adsorption-modifying functionality.
  • a delivery material comprises a complexing agent and, optionally an adsorption-modifying functionality.
  • a delivery material comprises an adsorption-modifying functionality and, optionally a complexing agent.
  • An adsorption-modifying functionality is any chemical functionality that modifies the interaction between an active ingredient and a delivery material, such that the introduction of the chemical functionality (a) increases or decreases the storage capacity of a delivery material (with respect to the storage capacity of the delivery material absent that chemical functionality) for an active ingredient, or (b) accelerates or decelerates the release of an active ingredient from a delivery material (with respect to the release of active ingredient from the delivery material absent that chemical functionality).
  • Such modifiable interactions include, but are not limited to, covalent binding, dative binding, electrostatic binding, van der Waals binding, or chelative binding of an appropriate active ingredient.
  • an active ingredient and a matrix comprising a delivery material modified by an adsorption-modifying functionality or a complexing agent may sometimes be referred to herein as ensemble dynamic interactions.
  • ensemble dynamic interactions between the delivery material and the active ingredient allow the (e.g. modified) delivery materials herein to load active ingredient in excess of what would be expected for lock and key or host-guest interactions.
  • adsorption-modifying functionalities an example of an adsorption-modifying functionality is one or more hydrophobic groups, for instance trimethylsilyl-functionalities, incorporated in a delivery material via grafting.
  • compositions here are not limited to any particular theory or mechanism, it is contemplated that adsorption-modifying functionalities comprising hydrophobic or aliphatic groups in the pore space of the delivery material promote van der Waals interactions with hydrophobic active ingredients to help stabilize the hydrophobic active ingredients by via ensemble dynamic interactions.
  • a delivery material comprises more than one type of adsorption-modifying functionality.
  • Non-limiting examples of delivery materials and their methods of manufacture are provided below:
  • a silicate delivery material absent a complexing agent may be prepared in the following manner.
  • a typical synthetic procedure requires a molar ratio of 1.00 silica source to 114 H 2 O to 8.0 M NH 4 OH (35 wt % in water) to 0.12 cetyltrimethylammonium bromide (CTAB). Tetraethoxysilane (TEOS) and is used as a silica source.
  • CTAB (0.84 g, 2.3 mmol) is added to a solution of NH 4 OH (17.72 g, 30 wt %, 0.15 mmol) and deionized water (33.4 g, 1.86 mol), and the solution stirred for 30 minutes in a closed flask.
  • a delivery material can be prepared in the following manner.
  • a purely siliceous, periodic, high-surface area porous material is prepared according to the procedure described for Delivery Material A with no complexing agent embedded within it.
  • the surfactant (CTAB) is then removed from the material via calcination at 600° C. for 18 hours to yield a periodic, porous, high-surface-area delivery material.
  • the delivery material prepared by this method is sometimes referred to herein as “Delivery Material B”.
  • a delivery material comprising a complexing agent 40 , the complexing agent 40 being ⁇ -cyclodextrin can be prepared in the following manner.
  • a periodic, high-surface area porous material can be prepared from ⁇ -cyclodextrin depending on the mol % of content of complexing agent (in this case, ⁇ -cyclodextrin) desired.
  • the content ⁇ -cyclodextrin can vary, for example, by including 0-20 wt % of ⁇ -cyclodextrin.
  • a solution of NH 4 OH (17.72 g, 30 wt %, 0.15 mmol), deionized water (33.4 g, 1.86 mol), and ⁇ -cyclodextrin (0.4 g, 10 wt %) is prepared and stirred for 30 minutes in a closed flask.
  • TEOS (4 g, 19.2 mmol) is added slowly to the base/surfactant solution with gentle stirring. After stirring for 30 min, the solutions are aged at 80° C. for 4 days in a closed flask. The white solid is collected by filtration, washed with water, and dried in an oven at 100° C. Following this procedure, extracting the CTAB surfactant can further modify the surface area and pore size.
  • a delivery material that comprises a complexing agent 40 can be prepared according to the procedure described for Delivery Material A.
  • a purely siliceous, periodic, high-surface area porous material is prepared absent a complexing agent according to the previous procedure.
  • the surfactant (CTAB) is then extracted from the pores of the material in the manner described previously.
  • a quantity, of this material is suspended in water in which a complexing agent has been dissolved at a desired concentration.
  • 10 g, of the purely siliceous material may be suspended in 2 L of water, in which 1 g of complexing agent ⁇ -cyclodextrin (10 wt %) has been dissolved.
  • Complexing agents as described herein may be incorporated into porous commercial silica materials in the same fashion.
  • other complexing agents including but not limited to other cyclodextrins.
  • ⁇ -cyclodextrin and ⁇ -cyclodextrin can be substituted in the above methods to form matrices described herein.
  • Some cyclodextrins are available, for example, from Wacker Biochem Inc., Adrian, Mich. as well as other vendors.
  • a delivery material comprising a complexing agent, the complexing agent being a silyl-modified ⁇ -cyclodextrin (“silyl-CD” 44, as illustrated in FIG. 4 ) may be prepared by the following method, illustrated by FIG. 4 .
  • Tetradecakis-2,6-O-allylcycloheptaamylose is prepared from commercial B-cyclodextrin (Alfa-Aesar, 3 g, 2.3 mmole) allowed to react with an excess of allyl bromide, 21 g (0.31 mole), and with barium oxide, 15 g (0.09 mole), barium hydroxide octahydrate 15 g (0.09 mole) in dimethyl sulfoxide, 75 ml and dimethyl formamide, 75 ml, at room temperature for 48 hr under nitrogen. The reaction mixture is cooled, and 60 ml of ammonium hydroxide is added slowly with continual stirring.
  • Tetradecakis-2,6-di-O-(3-triethoxypropyl)cycloheptaamylose (hereafter referred to as “silyl-CD” 44) is prepared by first dissolving 2.57 g of tetradecakis-2,6-O-allylcycloheptaamylose in 50 mL of anhydrous THF and adding to this mixture 51.4 mL of triethoxysilane. To this mixture is added 2 mg of Cp 2 PtCl 2 catalyst in a 1 mg/mL solution in THF. The resulting solution is refluxed under nitrogen for 72 hours, and silyl-CD 44 is recovered by concentrating the reaction mixture in vacuo until no triethoxysilane remains. The resulting colorless oil silyl-CD 44 (illustrated in FIG. 4 ) is recovered in quantitative yield and used directly without further purification.
  • a periodic, high-surface area porous material can then be prepared from silyl-CD in the following a manner depending on the mol % of content of silyl-CD desired.
  • a typical synthetic procedure requires a molar ratio of 1.00 silica source to 114 H 2 O to 8.0 M NH 4 OH (35 wt % in water) to 0.12 cetyltrimethylammonium bromide (CTAB). Tetraethoxysilane and silyl-CD are used as silica sources. Delivery materials are prepared with TEOS to silyl-CD in Si mole ratios of 1/0, 0.9/0.1, 0.75/0.25, 0.50/0.50, and 0.25/0.75.
  • CTAB (0.84 g, 2.3 mmol) is added to a solution of NH 4 OH (17.72 g, 30 wt %, 0.15 mmol) and deionized water (33.4 g, 1.86 mol), and the solution stirred for 30 minutes in a closed flask.
  • the surface area and pore size can be further modified by extracting the CTAB surfactant.
  • 5 g of as-synthesized material is suspended in 170 mL methanol with 30 mL concentrated hydrochloric acid and refluxed with stirring for 48 hours. After extraction, the sample is collected via filtration, washed with methanol or a 0.05 M sodium bicarbonate solution, and dried in an oven at 100° C.
  • the delivery material prepared by this method is sometimes referred to herein as “Delivery Material C”.
  • a delivery material that comprises a complexing agent, the complexing agent being an allyl-modified ⁇ -cyclodextrin (“allyl-CD” 45 as illustrated in FIG. 5 ) can be prepared by the following method.
  • Tetradecalis-2,6-O-allylcycloheptaamylose is prepared from commercial ⁇ -cyclodextrin by stirring 5.68 g (5 mmol) ⁇ -cyclodextrin in 300 mL of a 1:1 mixture of DMF and DMSO with 29.25 mL (350 mmol) allyl bromide, 17.1 g of barium hydroxide (160 mmol) and 15.3 g barium oxide (160 mmol) for 48 hours at room temperature.
  • the oil is further purified by column chromatography on a silica column, first flushing with pure CHCl 3 and then collecting the pure tetradecakis-2,6-O-allylcycloheptaamylose fraction with 1:1 EtOac/CHCl 3 .
  • a yield of 43% of the pure compound is obtained after concentrating the eluent in vacuo.
  • the resulting compound is allyl-CD 45, as illustrated in FIG. 5 .
  • a periodic, high-surface area porous material can then be prepared from allyl-CD 45 in the following a manner depending on the mol % of content of allyl-CD desired.
  • the content of allyl-CD can vary, for example, by including 0 mol %, 2.5 mol % (0.48 mmol), or 10 mol % (1.92 mmol)) of allyl-CD.
  • a mixture of TEOS and allyl-CD corresponding to the desired mole fraction, with a total of 19.2 mmol of Si (for example, 4 g (19.2 mmol) of TEOS and 0.81 g (0.48 mmol) of allyl-CD for 2.5 mol % content) is added slowly to the base/surfactant solution with gentle stirring. After stirring for 30 min, the solutions re aged at 80° C. for 4 days in a closed flask.
  • the white solid is collected by filtration, washed with water, and dried in an oven at 100° C. Following this procedure, the surface area and pore size can be further modified by extracting the CTAB surfactant.
  • 5 g of as-synthesized material is suspended in 170 mL methanol with 30 mL concentrated hydrochloric acid and refluxed with stirring for 48 hours. After extraction, the sample is collected via filtration, washed with methanol or a 0.05 M sodium bicarbonate solution, and dried in an oven at 100° C.
  • a silica based delivery material comprising adsorption-modifying functionalities can be prepared in the following manner, the adsorption-modifying functionalities being trimethylsilyl functionalities.
  • a purely siliceous, periodic, high-surface area porous material is prepared according to the procedure described for Delivery Material A.
  • the surfactant (CTAB) is then extracted from the pores of the material in the manner described previously.
  • a quantity, 10 g, of this material is suspended in 250 mL of anhydrous toluene in a flask under an inert atmosphere. To this mixture is added 10 mL of trimethylchlorosilane, which may be purchased from Alfa-Aesar.
  • reaction mixture is refluxed for 18 hours to graft the trimethylsilyl functionalities to the silica.
  • the reaction mixture is then cooled and the solid recovered by filtration, washed with hexanes, and dried in an oven at 100° C.
  • This procedure therefore results in a material with similar pore size and surface area to the parent silica, but aliphatically modified walls, enabling ensemble dynamic interactions (including for example, a modified chemical potential) of the matrix with hydrophobic active ingredients such as 1-MCP as compared to its interaction with the unmodified parent material.
  • a carbon based delivery material modified with adsorption-modifying functionalities can be prepared in the following manner, resulting in a hydrophilically-modified delivery material.
  • a commercial activated carbon, NORIT A® may be purchased from Fisher Scientific. As received, the material has a surface area of 1146 m 2 /g. A quantity, 10 g, of this material is suspended in 100 mL of 70% nitric acid in water. The mixture is then refluxed for 18 hours, during which time reddish-brown gases evolve during the oxidation of the carbon surface. After the reaction is complete the solid is recovered by filtration and washed with water until the pH of the water wash is neutral. The solid is then dried at 100° C.
  • This procedure results in a material with a smaller pore size and surface area than the parent activated carbon, but with hydrophilically modified walls, enabling ensemble dynamic interactions (including for example, a modified chemical potential) of the matrix with hydrophobic active ingredients such as 1-MCP as compared to its interaction with the unmodified parent material.
  • the surface area after such a treatment was measured to be 1001 m 2 /g.
  • the delivery material may be comprised of a polymer, inorganic material, organic material, or hybrid thereof.
  • the polymer, inorganic, organic, or hybrid inorganic-organic material comprises 0-99.99 wt % of the matrix.
  • the polymer, inorganic material, organic material, or hybrid material of the matrix may be an inert material, which does not chemically interact with the active ingredient(s) of the matrix.
  • an active ingredient may experience significant physicochemical interactions with the inert chemical surface, internal and/or external, of an inert delivery material.
  • the polymer, inorganic material, organic material, or hybrid material of the matrix may be a chemically active material, which chemically interacts with the active ingredient(s) of the matrix.
  • templating agents or surfactants of this type include, but are not limited to, any tetraalkylammonium halide compound with alkyl groups from C 1 -C 18 , in which the halide is Cl, Br, or I; any tetraalkylammonium hydroxide compound with alkyl groups from C 1 -C 18 ; any alkylthiol compounds, typified by sodium dodecyl sulfate (SDS) with a thiol “head” and an alkyl “tail” from C 1 -C 18 ; any carboxylic acid or carboxylate salt, typified by sodium laurate, with a carboxylic acid or carboxylate “head” and an alkyl “tail” from C 1 -C 18 ; any bulky aliphatic amine or ammonium salt, typified by
  • the chemical surface area and pore structure will vary accordingly with the size and agglomerating effects of the individual templating agent or surfactant employed in the syntheses as described above.
  • the delivery material 100 is a solid material or solid carrier such as that typified by nanoporous, macroporous, mesoporous, and microporous carbon materials, templated organic materials of a type exemplified by mesoporous carbon, extruded or pelletized carbon materials, steam-activated carbon materials, oxidized carbon materials, or acid- or base-treated carbon materials.
  • the delivery material has an elemental composition indistinguishable from that of ash.
  • the delivery material having an elemental composition indistinguishable from that of ash stores and/or releases a vapor or gas.
  • the delivery material has an elemental composition indistinguishable from biochar, flue char, or soot.
  • the delivery material having an elemental composition indistinguishable from that of biochar, flue char, or soot stores and/or releases a vapor or gas.
  • a delivery material 300 may include, but is not limited to, nanoporous, macroporous, microporous, or mesoporous silicates, or organosilicate hybrids.
  • the delivery material has an elemental composition indistinguishable from that of sand.
  • the delivery material having an elemental composition indistinguishable from that of sand stores and/or releases a vapor or gas.
  • carbon based delivery materials and silicate delivery materials are combined, for example, by mixing a combination of two or more types of delivery materials.
  • the delivery materials 100 and 300 are solid materials. In a non-limiting embodiment porous delivery materials 100 and 300 are also high surface area materials.
  • a high-surface area material is a material with a total chemical surface area, internal and external, of at least about 1 m 2 /g. In some embodiments, a high-surface area material is a material with a total chemical surface area, internal and external, of at least about 10 m 2 /g. In some embodiments, a high-surface area material is a material with a total chemical surface area, internal and external, of at least about 50 m 2 /g.
  • a high-surface area material is a material with a total chemical surface area, internal and external, of at least about 90 m 2 /g. In some embodiments, a high-surface area material is a material with a total chemical surface area, internal and external, greater than about 400 m 2 /g. In some embodiments, a high-surface area material is a material with a total chemical surface area, internal and external, of at least about 500 m 2 /g. In some embodiments, a high-surface area material is a material with a total chemical surface area, internal and external, greater than about 1000 m 2 /g.
  • a high-surface area material is a material with a total chemical surface area, internal and external, greater than about 2000 m 2 /g.
  • total chemical surface area, internal and external refers to total chemical surface area, internal and external, greater than about 2000 m 2 /g.
  • total chemical surface area, internal and external refers to total chemical surface area, internal and external, greater than about 2000 m 2 /g.
  • a porous material is a material with a micropore diameter greater than about 0.1 nm. In a non-limiting embodiment, a porous material is a material with a micropore diameter greater than about 1 nm. In a non-limiting embodiment, a porous material is a material with a mesopore diameter between about 2 nm and about 5 nm. In some embodiments, a porous material is a material with an average pore diameter greater than 4 nm. In some embodiments, a porous material is a material with an average pore diameter greater than 6 nm. In a non-limiting embodiment, a porous delivery material is a material with an internal void volume greater than 0.1 cm 3 /g.
  • a porous delivery material is a material with an internal void volume greater than 0.5 cm 3 /g. In a non-limiting embodiment, a porous material is a material with an internal void volume greater than 1 cm 3 /g. In a non-limiting embodiment, a porous material is a material with an internal void volume greater than 1.5 cm 3 /g. As used herein, the terms “internal void volume” and “pore volume” may be used interchangeably.
  • a carbon based delivery material comprises one or more of the following properties: a density in the range of 0.1-3 g/cm 3 ; a pore volume in the range of 0.1-1.5 cm 3 /g; a surface area in the range of 500-4000 m 2 /g; moisture content in the range of 0-30%; and an iodine number in the range of 0-1200 mg/g.
  • a carbon based delivery material has a density in the range of about 0.1 to about 0.3 g/cm 3 .
  • a carbon based delivery material has a density in the range of about 0.3 to about 0.6 g/cm 3 .
  • a carbon based delivery material has a density in the range of about 0.6 to about 1.0 g/cm 3 . In a non-limiting embodiment, a carbon based delivery material has a density in the range of about 1 to about 3 g/cm 3 . In a non-limiting embodiment, a carbon based delivery material has a density in the range of about 0.3 to about 1.5 g/cm 3 . In a non-limiting embodiment, a carbon based delivery material has a density in the range of about 0.05 to about 0.15 cm 3 /g. In a non-limiting embodiment, a carbon based delivery material has a density in the range of about 0.15 to about 0.3 cm 3 /g.
  • a carbon based delivery material has a density in the range of about 0.3 to about 0.7 cm 3 /g. In a non-limiting embodiment, a carbon based delivery material has a density in the range of about 1 to about 1.5 cm 3 /g. In a non-limiting embodiment, a carbon based delivery material has a density in the range of about 0.5 to about 1.5 cm 3 /g. In a non-limiting embodiment, a carbon based delivery material has a surface area in the range of about 1 to about 3000 m 2 /g. In a non-limiting embodiment, a carbon based delivery material has a surface area in the range of about 1 to about 50 m 2 /g.
  • a carbon based delivery material has a surface area in the range of about 50 to about 500 m 2 /g. In a non-limiting embodiment, a carbon based delivery material has a surface area in the range of about 100 to about 1500 m 2 /g. In a non-limiting embodiment, a carbon based delivery material has a surface area in the range of about 500 to about 1500 m 2 /g. In a non-limiting embodiment, a carbon based delivery material has a surface area in the range of about 1000 to about 1500 m 2 /g. In a non-limiting embodiment, a carbon based delivery material has a surface area in the range of about 500 to about 2000 m 2 /g.
  • a carbon based delivery material has a surface area in the range of about 1000 to about 2500 m 2 /g. In a non-limiting embodiment, a carbon based delivery material has a surface area in the range of about 1000 to about 3000 m 2 /g. In a non-limiting embodiment, a carbon based delivery material has a surface area in the range of about 800 to about 1200 m 2 /g. In a non-limiting embodiment, a carbon based delivery material has a surface area in the range of about 800 to about 1500 m 2 /g. In a non-limiting embodiment, a carbon based delivery material has a moisture content in the range of 0 to about 2%.
  • a carbon based delivery material has a moisture content in the range of 2 to about 5%. In a non-limiting embodiment, a carbon based delivery material has a moisture content in the range of 5 to about 15%. In a non-limiting embodiment, a carbon based delivery material has a moisture content in the range of 15 to about 25%. In a non-limiting embodiment, a carbon based delivery material has a moisture content in the range of 25 to about 50%. In a non-limiting embodiment, a carbon based delivery material has a moisture content in the range of 50 to about 100%. In a non-limiting embodiment, a carbon based delivery material has an iodine number in the range of about 0-500.
  • a carbon based delivery material has an iodine number in the range of about 500-1000. In a non-limiting embodiment, a carbon based delivery material has an iodine number in the range of about 1000-1500. In a non-limiting embodiment, a carbon based delivery material has a pore volume of about 0.1 cm 3 /g to about 1.5 cm 3 /g. In a non-limiting embodiment, a carbon based delivery material has a pore volume of about 0.5 cm 3 /g to about 1.5 cm 3 /g. In a non-limiting embodiment, a carbon based delivery material has a pore volume of about 0.7 cm 3 /g to about 1.5 cm 3 /g. In a non-limiting embodiment, a carbon based delivery material has a pore volume of about 1 cm 3 /g to about 1.5 cm 3 /g.
  • a silicate delivery material comprises one or more of the following properties: a particle size of 5 nm to 5 mm, a pore volume of 0.5-5 cm 3 /g, a surface area of 0.01-2000 m 2 /g.
  • a silicate delivery material comprises one or more of the following properties: a pore size of 60 ⁇ , a mean particle diameter of 63-200 ⁇ m, a pore volume of 0.7-0.85 cm 3 /g, a surface area of 480 m 2 /g.
  • a silicate delivery material has a surface area in the range of about 0.01 to about 0.1 m 2 /g.
  • a silicate delivery material has a surface area in the range of about 0.1 to about 1 m 2 /g. In a non-limiting embodiment, a silicate delivery material has a surface area in the range of about 1 to about 50 m 2 /g. In a non-limiting embodiment, a silicate delivery material has a surface area in the range of about 50 to about 2500 m 2 /g. In a non-limiting embodiment, a silicate delivery material has a surface area in the range of about 50 to about 1500 m 2 /g. In a non-limiting embodiment, a silicate delivery material has a surface area in the range of about 100 to about 1500 m 2 /g.
  • a silicate delivery material has a surface area in the range of about 500 to about 1000 m 2 /g. In a non-limiting embodiment, a silicate delivery material has a surface area in the range of about 1000 to about 1500 m 2 /g. In a non-limiting embodiment, a silicate delivery material has a surface area in the range of about 1.500 to about 2500 m 2 /g. In a non-limiting embodiment, a silicate delivery material has a surface area in the range of about 100 to about 1500 m 2 /g. In a non-limiting embodiment, a silicate delivery material has a surface area in the range of about 500 to about 1500 m 2 /g.
  • a silicate delivery material has a particle size of about 5 nm to about 1000 nm. In a non-limiting embodiment, a silicate delivery material has a particle size of about 5 nm to about 500 nm. In a non-limiting embodiment, a silicate delivery material has a particle size of about 5 nm to about 1000 nm. In a non-limiting embodiment, a silicate delivery material has a particle size of about 50 nm to about 1000 nm. In a non-limiting embodiment, a silicate delivery material has a particle size of about 1 ⁇ m to about 10 m. In a non-limiting embodiment, a silicate delivery material has a particle size of about 10 ⁇ m to about 5 mm.
  • a silicate delivery material has a particle size of about 10 ⁇ m to about 0.5 mm. In a non-limiting embodiment, a silicate delivery material has a pore volume of about 0.1 cm 3 /g to about 10 cm 3 /g. In a non-limiting embodiment, a silicate delivery material has a pore volume of about 0.5 cm 3 /g to about 5 cm 3 /g. In a non-limiting embodiment, a silicate delivery material has a pore volume of about 0.5 cm 3 /g to about 2 cm 3 /g.
  • a silicate delivery material has a pore volume of about 0.5 cm 3 /g to about 2 cm 3 /g In a non-limiting embodiment, a silicate delivery material has a pore volume of about 0.5 cm 3 /g to about 10 cm 3 /g. In a non-limiting embodiment, a silicate delivery material has a D-spacing of about 3.5 ⁇ to 4.05 ⁇ . In a non-limiting embodiment, a silicate delivery material has a D-spacing of about 3.0 ⁇ to 4.5 ⁇ .
  • the storage and release parameters of the matrices described herein can be influenced by a combination of chemical and physicochemical interactions between the active ingredient and the delivery material.
  • the storage and release parameters are influenced by chemical interactions between an embedded complexing agent of the delivery material and the active ingredient and/or adsorption/desorption equilibria between the active ingredient and the inert chemical surface, internal or external, of the delivery material. Characteristics of the delivery material can also be modified to allow for different weight loadings of the active ingredient.
  • material properties including, but not limited to the specific chemical surface area, pore diameter, particle size, and pore volume of the delivery material influences and/or controls the weight capacity of matrix storage and rate of release from the matrix of the active ingredient. It is also contemplated herein that hydrophobicity, hydrophilicity, chemical potential, zeta-potential, acidity, basicity, surface functionalization, and surface functional group density of a delivery material influences and/or controls the weight capacity of matrix storage and rate of release from the matrix of the active ingredient. Delivery materials may be selected based on specific chemical surface area, pore diameter, and pore volume of the delivery material in order to control the weight capacity of matrix storage and rate of release from the matrix of the active ingredient.
  • complexing agents embedded in a delivery material may introduce specific chemical interactions between the complexing agent and the active ingredient that retard or accelerate the rate of release of the active ingredient, relative to the rate of release of active ingredient from a matrix comprising the active ingredient and an unmodified delivery material and/or relative to the rate of release of active ingredient from a complex of just the complexing agent and the active ingredient.
  • adsorption-modifying functionalities in the delivery material can modify the chemical potential of the delivery material (with respect to the chemical potential of a porous and/or high surface area material alone or with respect to the chemical potential of an adsorption-modifying functionality alone) by enabling ensemble dynamic interactions between the adsorption-modifying functionality and the active ingredient.
  • the sum of chemical and physicochemical interactions within a delivery material, modified or unmodified by either complexing agents or adsorption-modifying functionalities allows the delivery material to load active ingredient in excess of what would be expected for stoichiometric interactions between a complexing agent and an active ingredient.
  • a host-guest molecular interaction of ⁇ -cyclodextrin and 1-MCP has a binding constant >>1. These host-guest molecular complexes lock or partially retain the 1-MCP into the cage or cavity structure of the ⁇ -cyclodextrin, and cannot control release 1-MCP as do the matrices described herein.
  • a host-guest molecular complex of ⁇ -cyclodextrin and 1-MCP general has a 1:1 stoichiometry, whereas matrices described herein enable a higher loading capacity than what would be expected of merely a molecular complexation.
  • the modifications of (a) and (b) separately neither predict the weight capacity nor the active ingredient release rate of the matrix a priori.
  • the interaction of at least parameters (a) and (b) allows the advantage of providing a unique weight capacity and release rate of the active ingredient for unique compositions of the delivery material.
  • the delivery material can also be modified in other ways in order to control the storage and release of an active ingredient from the matrices described herein.
  • FIG. 2 shows a cross-section of a non-limiting illustrative embodiment of a matrix 200 comprising an active ingredient 20 and a delivery material 100 .
  • matrix 200 comprises a porous delivery material 100 and an active ingredient 20 .
  • matrix 200 contains at least one macropore 10 , at least one mesopore 11 , and at least one micropore 12 .
  • at least one of the macropore 10 , mesopore 11 , and micropore 12 stores active ingredient 20 .
  • the matrix 200 illustrates active ingredient 20 stored in macropores 10 and mesopores 11 of the matrix 200 .
  • Micropores 12 may also store active ingredient 20 .
  • active ingredient 20 in matrix 200 is a non-limiting example and is not drawn to scale, it should be noted that other storage concentrations of active ingredient 20 in matrix 200 can be achieved by the embodiments of the invention contemplated herein. Moreover, different positions of active ingredient 20 within the pores 10 , 11 , 12 of matrix 200 are also contemplated.
  • the active ingredient 20 is a cyclopropene. In a non-limiting embodiment, active ingredient 20 is 1-MCP.
  • FIG. 2 also illustrates active ingredient 21 .
  • Active ingredient 21 is the same active ingredient as active ingredient 20 ; however, active ingredient 21 has been released from matrix 200 .
  • an advantage of the matrix 200 disclosed herein is that it enables and/or can be configured for extended, accelerated, or controlled release of active ingredients.
  • a matrix 200 as described herein comprises a delivery material 100 and an active ingredient 20 .
  • the matrices described herein may allow access to new active ingredient release kinetics and increase material capacity for gaseous active ingredients as compared to, for example, previously known host-guest complexes and active ingredient adsorbates.
  • the matrices herein may be configured for controlled release of at least one active ingredient.
  • the at least one active ingredient is in the vapor phase or gas phase.
  • matrices comprising a delivery material and an active ingredient 20 can also be formed with delivery material 300 .
  • the matrix comprises a delivery material 300 , the delivery material comprising one or more complexing agents 40 in a concentration of 0-50 mol % of the total delivery material, the matrix further comprising at least one active ingredient 20 .
  • FIG. 6 shows an example of an internal view of a pore 61 of a matrix 600 , the matrix comprising a porous delivery material 300 (of FIG. 3 , for example), complexing agent 40 , and active ingredient 20 .
  • a complexing agent 40 encapsulating active ingredient 20 is shown as complex 42 .
  • the complexing agent is embedded into the porous delivery material 300 .
  • the delivery material 300 comprises a complexing agent 40 , a porous and high surface area material, at least one complexing agent 40 embedded onto a pore 61 of the porous and high surface area material.
  • the delivery material 30 is a high-surface area material.
  • Delivery materials comprising complexing agents 40 can combine the molecular host-guest interaction, for example, with an adsorption/desorption equilibrium at the material surface, resulting in unique storage and controllable release parameters. Characteristics of the delivery material, for example, an amount or weight percent of complexing agent comprising the delivery material can be modified to provide deliberately accelerated or deliberately decelerated release of the active ingredient. An advantage of the modifiable delivery material as disclosed herein is that the total rate of release of an active ingredient is unique to the chemical and physicochemical composition of the delivery material. With regard to complexing agents, however, it should be noted that FIG. 6 is illustrative only, and that complexes 42 are not necessarily present in the matrices described herein. In some embodiments, a matrix comprises a delivery material absent a complexing agent, and an active ingredient.
  • complexation of an active ingredient 20 with a complexing agent 40 may be accomplished using various clathrates, cage compounds, host-guest complexes, inclusion compounds, intercalation compounds, aromatic groups, aliphatic groups, templating surfactants, and adducts.
  • the clathrates, cage compounds, host-guest complexes, inclusion compounds, intercalation compounds, aromatic groups, templating surfactants, and adducts may be embedded into or onto a porous material such as macroporous, mesoporous, or microporous silica, or non-porous silica particles.
  • Complexes comprising a complexing agent and active ingredient may release an entrapped active ingredient (into the void of pore 61 , for example) of above a temperature at which the complex becomes unstable in some embodiments.
  • complexes may release an entrapped active ingredient (into the void of pore 61 and, possibly eventually out of the matrix, for example) upon dehydration, or when the complex falls below a given concentration of water.
  • the active ingredient may be present in the delivery material at up to about 25% by weight of the overall matrix.
  • the storage capacity for an active ingredient or ingredients can be uniquely tailored in the matrices described herein as a function of at least (a) the nature of the active ingredient employed, including, but not limited to hydrophobicity, molecular weight, and boiling point of the active ingredient; (b) the physicochemical characteristics of the delivery material, including but not limited to the hydrophobicity, chemical surface area, crystallinity, and/or pore size and volume within the delivery material; and (c) the chemical characteristics of the delivery material, including, but not limited to, the hydrophobicity or hydrophilicity of the delivery material, the degree of chemical functionalization of the delivery material (for instance by sulfonic, nitric, or carboxylic acid groups), the degree of oxidation of the delivery material, or the degree of aliphatic and aromatic functionalization of the delivery material.
  • delivery materials as described herein comprised of 75-100% carbon and having surface areas of 800-2000 m 2 /g can be charged with 0-25 wt % of 1-MCP via contact in either the liquid or gas phase with said active ingredient.
  • a delivery material with the chemical composition SiO 2 and with a chemical surface area of 846 m 2 /g may be impregnated with 10 wt % of carvacrol to yield a matrix that delivers the carvacrol in a controlled release fashion over time.
  • Preparation, loading, or charging of the delivery material with an active ingredient to produce a matrix can be performed by, for example and including, but not limited to, directly contacting the delivery material with the pure liquid active ingredient; directly contacting the delivery material with a solution of any kind containing the active ingredient; directly contacting the delivery material with an active ingredient in pure gas form; directly contacting the delivery material with a gas mixture containing the active ingredient; directly contacting the delivery material with an active ingredient in the vapor phase; directly contacting the delivery material with a gas mixture containing the active ingredient in the vapor phase.
  • the concentration of an active ingredient in the matrix may be controlled via the manner in which the active ingredient is introduced into the matrix.
  • An active ingredient with a high boiling point, for instance >100° C. may be dissolved in a compatible solvent with a low boiling point, for instance ⁇ 100° C., and slurried with a solid delivery material so as to evenly disperse the active ingredient over the total surface, internal and external, and throughout the total void volume of the delivery material.
  • the volume of a solution containing, for example, about 0.01-30 wt % of the active ingredient, relative to the weight of the delivery material may equal the total solid volume of the delivery material such that a “wicking” effect draws the active ingredient into pores of the delivery material, effectively distributing it throughout the matrix.
  • wicking Such a technique may sometimes be referred to herein as “incipient wetness impregnation.”
  • a low-boiling solvent may then be evaporated either through drying, heating, or dynamic vacuum.
  • the active ingredient may be incorporated into the delivery material via chemical grafting.
  • an active ingredient may be dissolved in a compatible solvent in a concentration from 0.01-25 wt %, relative to the delivery material.
  • the delivery material may then be slurried with this solution for a time, during which the active ingredient grafts to chemically available sites on the delivery material. Excess solution may be removed via filtration of the solid matrix, resulting in a matrix with a controlled concentration of the active ingredient.
  • Treatment of the prepared, loaded, or charged matrix after such a preparation can occur via, but is not limited to, removal of excess active ingredient by vacuum, distillation, evaporation, or blow-off; removal of excess solvent by vacuum, distillation, evaporation, or blow-off; isolation of the matrix under inert atmosphere, for instance nitrogen, to preserve the nature of the active ingredient; isolation of the matrix at low temperatures, for instance ⁇ 30° C., to preserve the nature of the active ingredient and/or prevent or retard release of the active ingredient from the matrix; steaming the matrix with water at an elevated temperature (20° C. or greater) to accelerate release of the active ingredient; and other methods. While such treatments may increase or decrease the inherent rate of release of the active ingredient from the matrix, these treatments do not destroy the fundamental advantages of the matrix.
  • the matrices may be incorporated into a structure, for example, non-wovens, wovens, knits, coated substrates, impregnated substrates, various forms of paper, cardboard, paper products, paper derivatives, fabrics, fibers, films, cloths, and coatings.
  • the matrices may also be incorporate into a structure such as wood, metal, clays, pulp, plastics, and other materials commonly used for planting, potting, shipping, harvesting, crating, storing, and supporting produce.
  • the structures may be formed from natural materials, synthetic materials, or a combination thereof. Other structures may include dispersions, froths, foams, powders, flakes, pellets, or the like.
  • the matrices may be incorporated into a structure through compression molding, extrusion, injection molding, blow molding, dry spinning, melt spinning, wet spinning, solution casting, spray drying, solution spinning, film blowing, calendaring, rotational molding, powder injection molding, thixomolding, and other various methods.
  • the matrices may be incorporated into a sachet, insert, paint, gel, coating, powder or encased in a capsule, pod, compartment, or container for the purpose of sale and ease of use for application.
  • These means of application may apply to any scale of treatment space or active ingredient application, and may be adapted to the particular compartment or container of target produce.
  • this material may be enclosed in a container, or “pod”, which upon breakage of a seal, would serve to release the active ingredient.
  • the pod may be plastic or another suitable material.
  • the matrix is incorporated into a structure or form factor by being sealed inside the structure or form factor.
  • the structure or form factor is comprised of a material that is one or more of food safe, non-absorptive, air permeable (but not necessarily porous).
  • the one or more of food safe, non-absorptive, air permeable (but not necessarily porous) structure comprises a sachet.
  • the sachet is porous.
  • the delivery material is charged with active ingredient prior to be deposited and sealed in a sachet.
  • the sachet may be prepared by depositing the composition in the sachet and then sealing the sachet.
  • a sachet material comprises one of a polypropylene material, polyethylene material (e.g. TYVEKTM), and a cellulose based material.
  • the Gurley Hill porosity measurement of a sachet material is 45-60 sec/100 cm 2 -in.
  • the structure comprising the matrix or the means of holding, encapsulating, encasing, or enrobing the material may further modulate active ingredient release properties.
  • the composition and/or the structure containing the matrix therein may be transported in hermetically sealed packaging.
  • compositions herein may be used as soil additives.
  • the matrices discussed herein can be used in or incorporated into refrigeration systems and other cold compartments, refrigeration filtration systems and the like.
  • the rate of release of the active ingredient(s) from the matrix disclosed herein may be controlled in various manners, some of which are discussed above.
  • the rate of release may also be affected, for example, by varying the concentration of the active ingredient in the matrix.
  • the rate of release may also be affected, for example, by modifying certain characteristics of the delivery material, for example, by varying the size of the delivery material's particles, by introducing a binder, oil, or other manner of encapsulation, including, but not limited to, encapsulation using a hydrogel or polymer, by varying the chemical structure, size, or composition of carbohydrates or other organic molecules that may be grafted into the delivery material, or by varying the nature or ratio of templating surfactants added to the material.
  • the rate of release may also be affected, for example, by mixing a combination of two or more delivery materials with different compositions with respect to any of the above variables.
  • the rate of release or amount of release may also be controlled by selecting a desired quantity of the delivery material or composition.
  • a user may select a smaller mass of composition for a smaller release of active ingredient, or a larger mass for a greater release of active ingredient.
  • the presence of additives may influence the rate of release of active ingredient.
  • adding a diluent material may modify the rate of release, amount of release, or concentration of active ingredient present in the total composition (e.g. including the diluent material).
  • a diluent material is combined, mixed with, or added to an already formed composition (e.g. comprising a delivery material impregnated with active ingredient).
  • the diluent material is a different material than the delivery material used in the composition. In some cases, the diluent material may be the same material as the delivery material used in the composition.
  • a diluent material may be a carbon based material which is mechanically mixed with a composition (e.g. comprising a carbon based delivery material impregnated with active ingredient) after the composition has been formed.
  • a diluent material may be an activated carbon which is mixed with a composition (e.g. comprising an activated carbon delivery material impregnated with active ingredient) after the composition has been formed.
  • a diluent material may be an silicate material which is mixed with a composition (e.g. comprising an silicate delivery material impregnated with active ingredient) after the composition has been formed.
  • the release of an active ingredient from the matrix can be accomplished passively, that is, without the addition of external wetting, hydrating, or chemically reactive agents in order to affect the release of the active ingredient from the delivery material.
  • an initial release of the active ingredient may be obtained within seconds or minutes of the matrix disclosed herein contacting water.
  • the release of an active ingredient from the matrix occurs as a function of temperature.
  • delayed release may be accomplished by storing the matrix at very low temperatures (e.g. approximately ⁇ 20° C. or lower) until release is required.
  • an initial release of the active ingredient may be delayed for several hours.
  • an initial release of the active ingredient may be delayed for several days, weeks, or months.
  • the active ingredient is liberated from the delivery material without the use of a solvent.
  • the active ingredient is liberated from the delivery material without the use of a solvent.
  • the active ingredient 1-MCP is liberated from the delivery material without the use of a solvent at temperatures between 0° C. and ambient room temperature, the release beginning essentially instantaneously after the delivery material is charged with 1-MCP to form the matrix.
  • the structure can be sized appropriately to control release of the active ingredient.
  • Discrete structures for example, pellets, flakes, and powders are advantageous for use in applications requiring a measurable or controllable dosage of the active ingredient.
  • Pellets and flakes may be advantageous for various dispersal methods, for example, where the pellets or flakes are scattered throughout a field during planting or prior to harvesting.
  • Films and sheets for example, may also provide measurable and controllable dosage due to the ability of the user to select a desired length of film or sheet. In other embodiments a smaller area or smaller volume of the structure may be selected for smaller release amounts of active ingredient.
  • the rate of release may be influenced based upon the rate in which the hygroscopic components used in forming the structure dissolve or swell in water. In other embodiments, the rate of release may be affected by the rate at which water diffuses through the structure and the location of the matrix within the structure.
  • compositions and structures described herein may provide for various modes of degradation, allowing for multiple releases or multiple release rates.
  • structures may provide for an initial release of active ingredient upon exposure to air, and a second release of active ingredient upon contact with moisture or humidity.
  • compositions and structures disclosed herein may provide an initial burst or high-concentration release of active ingredient, followed by a lower-concentration release over time.
  • compositions and structures disclosed herein may provide an initial low-concentration release over time, followed by a high-concentration release at a given time or condition.
  • Synthesis methods for generating 1-MCP are known in the art. Herein described are three examples of known methods for generating 1-MCP, appreciating that other methods for generating 1-MCP may also be employed.
  • 1-MCP is purchased in powder form as ETHYLBLOCTM (FLORALIFE®; Walterboro, S.C.), which contains 0.14% 1-MCP by weight.
  • ETHYLBLOCTM FLORALIFE®; Walterboro, S.C.
  • the ETHYLBLOCTM powder is weighed and placed in a glass flask holding distilled water as a solvent. The solution is then mixed and held at room temperature, for example, over time to develop the desired concentration of 1-MCP gas.
  • the glass flask holding the 1-MCP gas has a gas inlet and outlet port to allow continuous flow.
  • 1-MCP generation as extracted from ETHYLBLOCTM has been described in the art.
  • 1-MCP is generated from a 1-MCP-Li suspension in mineral oil, which is prepared by reacting lithium diisopropylamide (LDA) with 3-chloro-2-methylpropene under a nitrogen environment which is described in “Kinetics of Molecular Encapsulation of 1-Methylcyclopropene into ⁇ -Cyclodextrin,” Journal of Agricultural and Food Chemistry, 2007, 55(26): p. 11020-11026, which is incorporated herein by reference in its entirety. Table 1 summarizes the reaction conditions that can be used to synthesize 1-MCP in this manner.
  • LDA lithium diisopropylamide
  • nitrogen gas (99.95% pure) is pumped into a nitrogen vessel (351/2′′ ⁇ 28′′ ⁇ 32′′) containing either sodium amide powder (90%-NaNH 2 ) or lithium diisopropylamide powder (97%-[(CH 3 ) 2 CH] 2 NLi).
  • a separate powder addition vessel is also purged with the same nitrogen gas. Purging with nitrogen is necessary because of the reactivity of the above-mentioned Lewis bases with air, and to eliminate any contamination before conducting the synthesis reaction.
  • the sodium amide or an equivalent molar concentration of lithium diisopropylamide
  • To weigh the proper amount of the Lewis base all weighing is performed in a nitrogen box with nitrogen purging to eliminate oxygen and the threat of spontaneous ignition of the base. Special care is important when working with such bases for proper safety.
  • the openings in the powder addition vessel that were used for purging are sealed off to exclude air.
  • the powder addition vessel is attached to the main system.
  • the reaction vessel which already has been purged with nitrogen and has been partially evacuated, is opened to the powder addition vessel to allow the powder to fall into the reaction vessel with the aid of nitrogen flow. Nitrogen enters the powder addition vessel during transfer of the Lewis base.
  • the ball valve is closed.
  • a light mineral oil (dried with molecular sieves) or another equivalent solvent is added by opening the connecting ball valve and allowing it to pour into the reaction vessel with the aid of nitrogen flow.
  • the amount of oil added during the reaction can vary from 1-47 liters, with the higher amount 47 liters being preferred.
  • the reaction vessel is then purged and closed.
  • the reaction vessel temperature is adjusted to a temperature anywhere from 0° C. to 75° C., and preferably about 20° C. to start the reaction. The temperature can be raised or lowered by heating or chilling the jacket using a circulating pump. Should the holding capacity of the vessel be exceeded, the procedure is repeated.
  • the contents of the reaction vessel are stirred with a propeller mixer, but splashing of the contents should be avoided.
  • 3-chloro-2-methylpropene is added to the reaction vessel in an amount ranging from 0.15-1.0 liters.
  • the liquid reactant 3-chloro-2-methylpropene is added slowly over a period of 20 minutes.
  • the temperature of the reaction vessel is monitored and kept at less than 40° C.
  • the desired end-product methylcyclopropene
  • the nitrogen purge is stopped and water is added ranging from 0.00-1.47 liters by adding the water under positive pressure over a period of 1 hour.
  • a ball valve connecting the vessel with the condenser is opened and the headspace 1-MCP gas can be utilized.
  • 1-MCP generation in this fashion is described in U.S. Pat. No. 6,017,819, which is incorporated herein by reference in its entirety.
  • a stream of gaseous (or liquid) active ingredient at a known concentration is flowed through a tube of delivery material using an inert air stream (such as N 2 ) at a sufficient rate and duration to exhaust the desired amount of active ingredient into the tube of delivery material.
  • an inert air stream such as N 2
  • the temperature of the vessel containing the active ingredient may be adjusted to reduce impurities from loading into the delivery material. For example, if the active ingredient has a lower boiling point than impurities also contained in the vessel, the vessel containing the active ingredient (and impurities) may be chilled to a temperature below the boiling point of the active ingredient.
  • a chilled vessel (0° C. or less, for example) placed in an ice bath containing a desired amount of 1-MCP is connected to a packed bed column containing a desired amount delivery, for example, activated charcoal (available as DARCO® or other commercial charcoals).
  • a desired amount delivery for example, activated charcoal (available as DARCO® or other commercial charcoals).
  • inert air stream for example, N 2
  • a known concentration of 1-MCP vapor is forced through the packed bed column until a desired amount of 1-MCP has been exposed to the packed bed column in order to arrive at the desired weight loading.
  • the delivery materials described herein are efficient adsorbers of 1-MCP. Therefore, a skilled artisan will appreciate that the desired weight percent of 1-MCP in the matrix may be achieved, for example, by controlling the system variables such as the concentration of 1-MCP in the inert air stream and the mass of delivery material in the packed bed column.
  • Material weight gain may be measured after the charging process to assess the ultimate weight loading of 1-MCP in the matrix. If a lower weight loading is desired, diluent material (in the form of uncharged delivery material, for example) may be added.
  • the resulting matrix material may be packaged in form factors such as sachets or injection molded “pods” for example, for sales dress.
  • the resulting composition may be stored at cold temperatures (0° C. or less, for example) until release is desired.
  • compositions are provided below.
  • SAMPLE 1 A commercial carbon material (NORIT A®, Fisher Scientific) was obtained as an extrudate of 0.8 mm pellets. The carbon had a surface area of 1146 m 2 /g as determined by N 2 physisorption and BET analysis.
  • the delivery material was charged with 1-MCP (e.g. available in the form of ETHYLBLOCTM, from FloraLife®) in the vapor phase by slowly flowing a mixture of nitrogen and gaseous 1-MCP through a packed tube of the powder for 30 minutes. Thermogravimetric analysis of this matrix recovered a total of 14.7 wt % 1-MCP per gram of matrix (147 mg 1-MCP/g matrix).
  • 1-MCP e.g. available in the form of ETHYLBLOCTM, from FloraLife®
  • SAMPLE 2 A commercial carbon material (NORIT A®, Fisher Scientific) was obtained as an extrudate of 0.8 mm pellets.
  • the carbon had a surface area of 1146 m 2 /g as determined by N 2 physisorption and BET analysis.
  • the carbon was modified with 70% nitric acid by refluxing 10 g of carbon in 100 mL of 70% nitric acid for 18 hours, then isolating the solid by filtration and washing with water until the pH was neutral.
  • the surface area of the carbon after this treatment was 1001 m 2 /g.
  • the delivery material was charged with 1-MCP (e.g.
  • SAMPLE 3 A commercial carbon material (DARCO®, Sigma-Aldrich) was obtained as a powder with a particle size of 100 mesh. The carbon had a surface area of 843 m 2 /g as determined by N 2 physisorption and BET analysis.
  • the delivery material was charged with 1-MCP (e.g. available in the form of EthylBlocTM, from FloraLife®) in the vapor phase by slowly flowing a mixture of nitrogen and gaseous 1-MCP through a packed tube of the powder for 30 minutes. Thermogravimetric analysis of this sample recovered a total of 1.0 wt % of 1-MCP (10 mg 1-MCP/g matrix).
  • 1-MCP e.g. available in the form of EthylBlocTM, from FloraLife®
  • SAMPLE 4 A commercial carbon material (DARCO®, Sigma-Aldrich) was obtained as a powder with a particle size of 100 mesh. The carbon had a surface area of 843 m 2 /g as determined by N 2 physisorption and BET analysis. The carbon was modified with 70% nitric acid by refluxing 10 g of carbon in 100 mL of 70% nitric acid for 18 hours, then isolating the solid by filtration and washing with water until the pH was neutral. The surface area of the carbon after this treatment was 846 m 2 /g. The delivery material was charged with 1-MCP (e.g.
  • SAMPLE 5 A silicate material with the overall chemical formula SiO 2 was prepared according to the procedure previously described for Delivery Material A from tetraethylorthosilicate (TEOS, Acros Organics). Cetyltrimethylammonium bromide (CTAB, Acros Organics) was used as the surfactant and was not extracted from the silicate once the material was formed. The resulting delivery material had a specific surface area of 99 m 2 /g, a d-spacing of 4.08 ⁇ , and 0 mol % embedded complexing agent. The delivery material was charged with 1-MCP (e.g.
  • SAMPLE 6 A silicate material with the overall chemical formula SiO 2 was prepared according to the procedure previously described for Delivery Material A from tetraethylorthosilicate (TEOS, Acros Organics). Cetyltrimethylammonium bromide (CTAB, Acros Organics) was used as the surfactant and was extracted from the silicate once the material was formed by refluxing in methanol and concentrated hydrochloric acid for 48 hours. The resulting delivery material had a specific surface area of 1022 m 2 /g, a d-spacing of 4.02 ⁇ , and 0 mol % embedded complexing agent. The sample was charged with 1-MCP (e.g.
  • SAMPLE 7 A silicate material with the overall chemical formula SiO2 was prepared according to the procedure previously described for Delivery Material A from tetraethylorthosilicate (TEOS, Acros Organics). Cetyltrimethylammonium bromide (CTAB, Acros Organics) was used as the surfactant and was extracted from the silicate once the material was formed by refluxing in methanol and concentrated hydrochloric acid for 48 hours. The resulting delivery material had a specific surface area of 1022 m2/g, a d-spacing of 4.02 ⁇ , and 0 mol % embedded complexing agent. The delivery material was charged with 1-MCP (e.g.
  • SAMPLE 8 A silicate material with the overall chemical formula SiO 2 was prepared according to the procedure as described in for Delivery Material B from tetraethylorthosilicate (TEOS, Acros Organics). Cetyltrimethylammonium bromide (CTAB, Acros Organics) was used as the surfactant and was removed via calcination of the material at 600° C. in static air. The resulting delivery material had a specific surface area of 846 m 2 /g, a d-spacing of 4.02 ⁇ , and 0 wt % embedded adsorption-modifying functionalities or complexing agents.
  • TEOS tetraethylorthosilicate
  • CAB Cetyltrimethylammonium bromide
  • the delivery material was charged with carvacrol (Sigma-Aldrich, 98%) in a solution in acetone via incipient wetness impregnation.
  • the acetone was evaporated from the sample first under dynamic vacuum in a conventional rotovap apparatus at 20° C. for 30 minutes, then by heating in an oven at 150° C. for 30 minutes. This matrix contained 10 wt % of carvacrol per gram of matrix.
  • SAMPLE 9 A silicate delivery material with the overall chemical formula SiO 2 was prepared according to the procedure as described for Delivery Material B from tetraethylorthosilicate (TEOS, Acros Organics). Cetyltrimethylammonium bromide (CTAB, Acros Organics) was used as the surfactant and was removed via calcination of the material at 600° C. in static air. The resulting delivery material had a specific surface area of 846 m 2 /g, a d-spacing of 4.02 ⁇ , and 0 wt % embedded adsorption-modifying functionalities or complexing agents.
  • TEOS tetraethylorthosilicate
  • CAB Cetyltrimethylammonium bromide
  • the delivery material was charged with thyme oil (Sigma-Aldrich, white, FCC, FG) in a solution in acetone via incipient wetness impregnation.
  • thyme oil Sigma-Aldrich, white, FCC, FG
  • the acetone was evaporated from the sample first under dynamic vacuum in a conventional rotovap apparatus at 20° C. for 30 minutes, then by heating in an oven at 150° C. for 30 minutes.
  • This matrix contained 10 wt % of thyme oil per gram of matrix.
  • SAMPLE 10 A matrix material was prepared by mechanically mixing 1 g of Sample 8 with 1 g of Sample 9 to give a 1:1 ratio of the active ingredients.
  • the final composition of the matrix had the chemical formula SiO 2 and contained 0.050 g of carvacrol and 0.050 g of thyme oil per gram of matrix.
  • SAMPLE 11 A silicate delivery material with the overall chemical formula SiO 2 was prepared according to the procedure described for Delivery Material A from tetraethylorthosilicate (TEOS, Acros Organics). Cetyltrimethylammonium bromide (CTAB, Acros Organics) was used as the surfactant and was extracted from the silicate once the material was formed by refluxing in methanol and concentrated hydrochloric acid for 48 hours. The resulting delivery material had a specific surface area of 1022 m 2 /g, a d-spacing of 4.02 ⁇ , and 0 mol % embedded complexing agent. The delivery material was impregnated with D(+)-carvone (Acros Organics, 96%) in a methanol solution.
  • TEOS tetraethylorthosilicate
  • CAB Cetyltrimethylammonium bromide
  • SAMPLE 12 A silicate delivery material with a composition ratio of 10 mol % complexing agent to 90 mol % SiO 2 was prepared according to the procedure described for Delivery Material C from a mixture of tetraethylorthosilicate (TEOS, Acros Organics) and ⁇ -cyclodextrin (Alfa-Aesar) modified with silyl groups. As a molar ratio of Si, the mixture contained 10 mol % Si from silyl-modified ⁇ -cyclodextrin and 90% Si from TEOS.
  • TEOS tetraethylorthosilicate
  • Alfa-Aesar ⁇ -cyclodextrin
  • Cetyltrimethylammonium bromide (CTAB, Acros Organics) was used as the surfactant and was extracted from the silicate after it was formed by refluxing in methanol and concentrated hydrochloric acid for 48 hours.
  • the resulting delivery material had a specific surface area of 670 m 2 /g, a d-spacing of 3.85 ⁇ , and 10 mol % embedded complexing agent.
  • the delivery material was impregnated with D(+)-carvone (Acros Organics, 96%) in a methanol solution. For a 100 mg sample, 5 mg of carvone was dissolved in 1.5 mg methanol and added to the powder with stiffing for 30 min. The sample was then dried on a rotational evaporator for 30 mins and the sample further dried in the oven at 100° C. This matrix contained 5 wt % of carvone per gram of matrix.
  • SAMPLE 13 A silicate material with the overall chemical formula SiO 2 was prepared according to the procedure described for Delivery Material A from tetraethylorthosilicate (TEOS, Acros Organics). Cetyltrimethylammonium bromide (CTAB, Acros Organics) was used as the surfactant and was extracted from the silicate once the material was formed by refluxing in methanol and concentrated hydrochloric acid for 48 hours. The resulting delivery material had a specific surface area of 1022 m2/g, a d-spacing of 4.02 ⁇ , and 0 mol % complexing agent. The delivery material was impregnated with thymol (Acros Organics, 99%) in a methanol solution.
  • TEOS tetraethylorthosilicate
  • CAB Cetyltrimethylammonium bromide
  • SAMPLE 14 A silicate delivery material with a composition ratio of 10 mol % complexing agent to 90 mol % SiO 2 was prepared according to the procedure described for Delivery Material C from a mixture of tetraethylorthosilicate (TEOS, Acros Organics) and ⁇ -cyclodextrin (Alfa-Aesar) modified with silyl groups. As a molar ratio of Si, the mixture contained 10 mol % Si from silyl-modified ⁇ -cyclodextrin and 90% Si from TEOS.
  • TEOS tetraethylorthosilicate
  • Alfa-Aesar ⁇ -cyclodextrin
  • Cetyltrimethylammonium bromide (CTAB, Acros Organics) was used as the surfactant and was extracted from the silicate after it was formed by refluxing in methanol and concentrated hydrochloric acid for 48 hours.
  • the resulting delivery material had a specific surface area of 670 m2/g, a d-spacing of 3.85 ⁇ , and 10 mol % embedded complexing agent.
  • the delivery material was impregnated with thymol (Acros Organics, 99%) in a methanol solution. For a 100 mg sample, 5 mg of thymol was dissolved in 1.5 mg methanol and added to the powder with stirring for 30 min. The sample was then dried on a rotational evaporator for 30 mins and the sample further dried in the oven at 100° C. This matrix contained 5 wt % thymol per gram of matrix.
  • SAMPLE 15 A silicate delivery material with the overall chemical formula SiO2 was prepared according to the procedure described for Delivery Material A from tetraethylorthosilicate (TEOS, Acros Organics). Cetyltrimethylammonium bromide (CTAB, Acros Organics) was used as the surfactant and was extracted from the silicate once the material was formed by refluxing in methanol and concentrated hydrochloric acid for 48 hours. The resulting delivery material had a specific surface area of 1022 m 2 /g, a d-spacing of 4.02 ⁇ , and 0 mol % complexing agent. The delivery material was impregnated with hexanal (Acros Organics, 99%) in a hexanes solution.
  • TEOS tetraethylorthosilicate
  • CAB Cetyltrimethylammonium bromide
  • SAMPLE 16 A silicate material with a composition ratio of 2.5 mol % molecular complexing agent to 97.5% SiO2 was prepared according to the procedure described for Delivery Material C from a mixture of tetraethylorthosilicate (TEOS, Acros Organics) and ⁇ -cyclodextrin (Alfa-Aesar) modified with silyl groups. As a molar ratio of Si, the mixture contained 2.5 mol % Si from silyl-modified ⁇ -cyclodextrin and 97.5% Si from TEOS.
  • TEOS tetraethylorthosilicate
  • Alfa-Aesar ⁇ -cyclodextrin
  • Cetyltrimethylammonium bromide (CTAB, Acros Organics) was used as the surfactant and was extracted from the silicate after it was formed by refluxing in methanol and concentrated hydrochloric acid for 48 hours.
  • the resulting delivery material had a specific surface area of 988 m 2 /g, a d-spacing of 4.07 ⁇ , and 2.5 mol % embedded complexing agent.
  • the delivery material was impregnated with hexanal (Acros Organics, 99%) in a hexanes solution.
  • a 20 mg sample of powder was suspended in 1 mL of a 10 w/v % solution of hexanal in hexanes overnight. The sample was then left to dry in open air for 10 hours until all hexanes had evaporated. This matrix contained 5 wt % hexanal per gram of matrix.
  • Samples 1-9 and 11-16 above were measured using a commercial nitrogen physisorption and BET analyzer apparatus. The samples were outgassed at 120° C. for 24 h prior to physisorption measurements. The d-spacings of Samples 5-7 were measured using a sample packed onto a glass sample holder in a conventional powder X-ray diffraction apparatus equipped with a Cu K- ⁇ X-ray source.
  • Thermogravimetric analysis of Samples 1-4 was determined from one of two complementary methods.
  • the delivery material was loaded with 1-MCP as described, then ca. 1 g of the matrix was loaded into a glass vessel.
  • the exact mass of matrix was recorded to 0.1 mg accuracy, and the overall weight of the vessel was recorded to 0.1 mg accuracy.
  • the vessel was then subjected to vacuum at 50° C. in a conventional rotovap apparatus attached to an oil vacuum pump with a rotational speed of 250 RPM. Care was taken so that the sample did not dislodge into the rotovap.
  • the sample was thus evacuated for 30 minutes and the mass of the vessel taken again.
  • the difference in mass in the two samples is attributed to the loss of 1-MCP from the matrix and was normalized to a mass of 1-MCP per unit mass of matrix.
  • a ca. 1 g of matrix loaded with 1-MCP was placed in a tared vial. The total mass of the vial plus the sample was then recorded. The sample was placed overnight in an oven at 150° C. and left open to drive off any adsorbed volatiles. After 18 h, the sample was removed from the oven, cooled, and reweighed. The difference in sample mass is attributed to the loss of 1-MCP from the matrix and was normalized to a mass of 1-MCP per unit mass of matrix.
  • thermogravimetric analysis results are summarized in Table 2 below.
  • the mass uptake of 1-MCP was determined for Samples 5-7 by first loading 250 mg of the appropriate delivery material into a plastic tube atop a bed of quartz wool. A plug of quartz wool was packed over the top of the sample to keep the sample in place. The tube was then weighed on a precision balance and attached to a vapor-flow apparatus through tubing. A mixture of nitrogen and 1-MCP was flowed through the bed of delivery material for 30 minutes, then the tube was disengaged from the vapor-flow apparatus and reweighed. The mass difference is attributed to uptake of gaseous 1-MCP by the delivery material and represents the weight content of 1-MCP present in the matrix.
  • Mass difference methods were also used to determine the weight loading of various active ingredients in Samples 8, 9, and 11-16.
  • the mass difference before and after loading is attributed to uptake of the active ingredient by the delivery material and represents the weight content of the active ingredient present in the matrix.
  • the mass uptake analysis results for Samples 8, 9, and 11-16 are summarized in Table 4, below.
  • the release of active ingredient from Samples 1-4 and 8 and 9 was determined using headspace analysis of sealed vials containing 50 mg of the sample, as measured with a gas chromatograph equipped with a flame ionization detector. Active ingredient released out of Samples 1-4 was measured based on 1-MCP released from the composition. Active ingredient released out of Sample 8 was measured based on carvacrol release from the composition. Active ingredient released out of Sample 9 was measured based on thymol release from the composition, as thymol is the principal active terpene compound in in thyme oil.
  • the vials were 45 mm tall and 20 mm wide with a mouth of 15 mm, for a total internal volume of 8 mL.
  • a screw-cap with a TEFLONTM liner was screwed onto the vial and the vial sealed with paraffin wax to prevent leakage.
  • vials were left open to allow the active ingredients to escape freely.
  • the vial was sealed for 1 hour to allow gas to build up in the headspace of the vial, and a volume (e.g. 200 ⁇ L) was sampled from the headspace. In this way the rate of release at a given timepoint could be measured.
  • the GC oven temperature was set to 200° C.
  • the area of the GC peak was calibrated by comparison to known quantities of 1-MCP released from ETHYLBLOCTM.
  • the procedure was to place a quantity of ETHYLBLOCTM corresponding to the desired number of moles of 1-MCP in a sealed chromatograph vial, then inject 1 mL of the ETHYLBLOCTM buffer solution into the vial.
  • the vial was shaken to promote complete release of 1-MCP and a sample of the headspace injected in the gas chromatograph.
  • a linear calibration for GC peak area could be determined.
  • the location of the GC peaks were determined via comparison to authentic samples in the same GC.
  • the peak area was adjusted to the specific response factor of carvacrol and thymol using an Effective Carbon Number (ECN) adjustment.
  • ECN Effective Carbon Number
  • the calculated response factor for both carvacrol and thymol was determined to be 1.12.
  • the samples were stored at 25° C. at atmospheric pressure.
  • Rate of 1-MCP Release Time (hrs) ( ⁇ L 1-MCP/g matrix/hr) 1 189.9 22 22.1 48 4.3 72 1.7 96 1.2 120 0.8
  • Rate of 1-MCP Release Time (hrs) ( ⁇ L 1-MCP/g matrix/hr) 1 1228.7 22 3.5 48 0.3 72 0.0 96 0.0 120 0.0
  • Rate of 1-MCP Release Time (hrs) ( ⁇ L 1-MCP/g matrix/hr) 1 189.9 22 22.1 48 4.3 72 1.7 96 1.2 120 0.8
  • Rate of 1-MCP Release Time (hrs) ( ⁇ L 1-MCP/g matrix/hr) 1 1228.7 22 3.5 48 0.3 72 0.0 96 0.0 120 0.0
  • the release of 1-MCP from Samples 5-7 calculated in the unit of mg 1-MCP/g matrix was determined using an alternative headspace analysis method than the method discussed above, which was used to determine a the release rate of 1-MCP (e.g. ⁇ L 1-MCP ingredient/g matrix/hr).
  • a screw-cap with a TEFLONTM liner was screwed onto the vial and the vial sealed with paraffin wax to prevent leakage.
  • the GC oven temperature was set to 200° C.
  • the area of the GC peak was calibrated by comparison to known quantities of 1-MCP released from ETHYLBLOCTM. The procedure was to place a quantity of ETHYLBLOCTM corresponding to the desired number of moles of 1-MCP in a sealed chromatograph vial, then inject 1 mL of the ETHYLBLOCTM buffer solution into the vial. A vial was shaken to promote complete release of 1-MCP and a sample of the headspace injected in the gas chromatograph. By varying the amount of 1-MCP in each vial, a linear calibration for GC peak area could be determined. During the release experiments, the samples were stored at 25° C. at atmospheric pressure.
  • Rate of 1-MCP Release Time (hrs) ( ⁇ L 1-MCP/g matrix/hr) 1 189.9 22 22.1 48 4.3 72 1.7 96 1.2 120 0.8
  • Rate of 1-MCP Release Time (hrs) ( ⁇ L 1-MCP/g matrix/hr) 1 1228.7 22 3.5 48 0.3 72 0.0 96 0.0 120 0.0
  • the cumulative amount of active ingredient released over the test period can be measured and reported as a percentage of the total amount (e.g. as a mass) of active ingredient present in the sample initially. For example, based on the weight loading (e.g. 9.2 wt. %), the total amount of 1-MCP released over a period of 336 hours, and the initial mass of the sample tested, it was found that Sample 7 released 24.5% of its 1-MCP over the two (2) week test period.
  • Samples 11-16 were tested for the release of active ingredients. Specifically, D(+)-carvone (Samples 11 and 12), thymol (Samples 13 and 14), hexanal (Samples 15 and 16) were tested. Vials containing 20-50 mg of each sample were loosely sealed with a screw cap with a TEFLONTM liner so that air could flow in and out of them. The vials were 45 mm tall and 20 mm wide with a mouth of 15 mm, for a total internal volume of 8 mL. Each sample was tested by sampling the static headspace in the vial and injecting into a gas chromatograph with a flame ionization detector.
  • the GC peak areas were calibrated using an effective carbon number (ECN) calculation relative to the 1-MCP calibration as discussed previously.
  • ECN effective carbon number
  • the matrices disclosed herein are suitable to treat a wide variety of produce species, one technical advantage is that the matrices configured for controlled release are efficacious on produce with high respiration rates (for example, 20-40 mg CO 2 mg kg ⁇ 1 h ⁇ 1 or higher or as categorized in Wilson, L. G., M. D. Boyette, E. A. Estes. 1999 . Postharvest handling and cooling of fresh vegetables, and flowers for small farms . North Carolina Cooperative Extension Service.).
  • 1-MCP release technologies especially those operating in the absence of other treatments (for example 1-MCP technologies employed without the assistance of modified atmosphere packaging), have only limited efficacy on these varieties of produce. Bananas were treated with matrices comprising 1-MCP as described herein.
  • FIG. 7 illustrates a treated banana 71 versus an untreated banana 72 .
  • FIG. 7 displays at least the firmness retention in the treated banana 71 after 10 days of treatment, versus the untreated banana 72 after 10 days at ambient room temperature. After ten (10) days of treatment, the treated bananas displayed improved firmness retention and color as compared to the untreated bananas.
  • Broccoli was also treated with compositions as described herein comprising 1-MCP.
  • 0.5 g of matrix sealed in a TYVEKTM sachet was placed in each of five (5) treated cartons.
  • No treatment was used in the untreated cartons of broccoli.
  • the treated and untreated broccoli was kept as close to 0° C. as possible.
  • Relative humidity (RH) was approximately 95% for the duration of the study.
  • Matrices comprising 1-MCP as described herein have also been studied on other produce commodities, for example, honeydew and Donnie avocadoes.
  • honeydew study twenty-four (24) 301b cartons containing six honeydew melons each were studied. 0.5 g of matrix sealed in a TYVEKTM sachet was placed in each of twelve (12) treated cartons. No treatment was used in the untreated cartons of honeydew. The estimated brix of all melons in the sample size was 12-14 at time of packing.
  • the honeydew were stored for 28 days at 7.2° C. (45° F.) and 85% RH. Results of the study showed that the matrices used increased the treated honeydew shelf-life by least a 30% as compared to the untreated honeydew.
  • Donnie avocados are known as an early variety that ripens quickly and often gets basal dark decay.
  • six (6) boxes each containing ten (10) Donnie avocados were studied.
  • the treated and untreated Donnie avocados were also treated with Scholar fungicide prior to packing.
  • 0.5 g of matrix sealed in a TYVEKTM sachet was placed in each of three (3) treated cartons.
  • the results of the study showed that the R the matrices used increased the treated Donnie shelf-life by six (6) to nine (9) days as compared to the untreated avocados.
  • These non-limiting examples of produce tests indicate that the matrices described herein are effective at varying temperatures, varying humidities, and can improve the quality and shelf-life of a plethora of produce commodities.
  • compositions described herein are effective in extending the shelf-life of berries.
  • Compositions comprising terpenes as described herein were evaluated on cultivated microbes from strawberries.
  • the diseases cultivated included, for example, Botrytis (gray mold), Leak, Leather Rot, and Anthracnose. These diseases were cultivated in a single batch by macerating 8 oz. of affected strawberries and agitating them in 0.5 L of previously sterilized water for 3 hours. The resulting slurry was then filtered and placed in distinct individual drops upon sterilized, previously-prepared agar plates.
  • the agar plates were spherical with a 5.5 cm diameter, affording enough space for three distinct, non-contiguous sample spots approximately 0.5 cm in diameter apiece.
  • Ten plates were divided into two groups of 5. One group of 5 served as control plates 80 ( FIG. 8 ). To the second group of 5 served as active plates 90. For further emphasis, one control plate 81 and one active plate 91 from the experiment are placed side by side in FIG. 9 . To the active plates 90 was added 100 mg of matrix powder 900 (not labeled in every active plate), placed in a such a way as to avoid direct contact with any of the microbe colonies. The progress of the colony growth was then followed over time, noting that in control plates 80, growth of pathogen colonies was observed within 48 hours. The plates were left at room temperature and ambient conditions for 27 days to develop. Illustrative results of this experiment data are shown in FIG. 8 and FIG. 9 .
  • compositions described herein slowly release active ingredients over time. Furthermore, the release of these active ingredients has a statistically relevant impact in reducing the growth and development of multiple native diseases found in berries. Use of the compositions described herein on berries may result in a statistical improvement in the shelf life of berries.
  • the berries were left under ambient conditions at room temperature for 4 days, at which point they were removed from their clamshells and sorted according to visible pathogenic development. Visible signs of infection were denoted as visible discoloration ( Botrytis ), soft spots (Leak and Anthracnose), the development of brown flesh (Leather Rot), and collapse/loss of berry juice (Leak). Any strawberries visibly affected by pathogens were counted as “infected” whereas any strawberries displaying no visible symptoms were considered “uninfected.” Under the test conditions, the application of the composition comprising at least one terpene prevented 18% more strawberries from developing visible symptoms of natural strawberry diseases in comparison to the control sample strawberries. No impact on the odor or taste on the treated strawberries was observable, implying that the matrices described herein can be employed without introducing undesirable organoleptic effects.
  • the test above indicates that the matrices described herein reduce real infections in berries even at the end of the berry lifespan. Because advanced age increases the likelihood of pathogenic infection, the margin of infection reduction will likely be further increased by introducing the compositions described herein at an earlier point in the fruit's life cycle.
  • the use of a high surface area material enhances the vapor pressure of otherwise high-boiling antimicrobial agents (e.g. active ingredients not limited to carvacrol, which has a boiling point of 236° C.).
  • the loading of the active ingredient in the delivery material can be modified as desired using techniques, such as for example, incipient wetness impregnation as described herein.
  • the high surface area of the delivery material may reduce the physical volume and weight of matrix needed to deliver an effective concentration of the active ingredient.
  • compositions comprising powder or granular solid delivery materials permit the mechanical mixing of matrices comprising different active ingredients for precise combinations of active ingredients.
  • compositions described herein may reduce or prevent the presence of off-flavors and/or residue on food or produce, as opposed to dips, sprays, coatings, films, waxes, and other contact systems.
  • compositions disclosed herein enable and/or can be configured for extended, slow, or controlled release of active ingredients in the vapor phase. This is advantageous because direct contact of certain active ingredients with produce, for example, may adversely impact the flavor, texture, or aromatic qualities of the produce. Controlled delivery of a vapor phase active ingredient may help the commercial salability of the produce during and after treatment while extending the shelf life of the produce.
  • Another advantage of the matrices described herein is that the release of an active ingredient from the matrix can be accomplished passively, that is, without the addition of external wetting, hydrating, or chemically reactive agents in order to affect the release of the active ingredient from the delivery material. In an alternative embodiment, however, a matrix may release an active ingredient upon exposure to moisture.
  • Another advantage of the matrices disclosed herein is that they enable and/or can be configured for extended, accelerated, or controlled release of active ingredients in contrast to currently available technologies that cannot offer gradual, extended, or controlled release of active ingredients as can be provided by the matrices described herein.
  • Another advantage of the matrices described herein is that the matrix (in powder form, for example) does not need to be in direct contact with produce to be effective.
  • the matrix may release the active ingredient in the gaseous or vapor phase from the delivery material, wherein the produce is exposed to the active ingredient in the gaseous or vapor phase, and wherein the delivery material does not contact the produce. Furthermore, the matrix does not need to be sprayed onto produce to be effective.
  • a composition comprising a delivery material and an active ingredient is configured to extend the shelf life of produce without direct contact between the composition and the produce.
  • the delivery material of the matrix is recyclable (whereas competing cyclodextrin (CD) based polymers are not), which means that the matrix permits re-charging and re-use.
  • Additional advantages of the matrix disclosed herein are that the matrix is capable of high loading capacity (for example, 1-MCP loading of up to 25% by weight of the overall matrix), and the matrix is tunable across a range of parameters.
  • the tunable parameters including, but not limited to, pore-size, surface hydrophobicity, and the surface density of functional groups, surfactant extraction, affect the release kinetics of active ingredients stored in the matrix.
  • the ability to tune the parameters of the matrix permits tailoring of the matrix to be appropriate and possibly even optimized for a wide range of applications, such as different container sizes or different target produce, for example. This short list of advantages provided by the matrix disclosed herein is not exhaustive.
  • a reference to “A and/or B,” when used in conjunction with open-ended language such as “comprising” can refer, in one embodiment, to A without B (optionally including elements other than B); in another embodiment, to B without A (optionally including elements other than A); in yet another embodiment, to both A and B (optionally including other elements); etc.
  • the phrase “at least one,” in reference to a list of one or more elements, should be understood to mean at least one element selected from any one or more of the elements in the list of elements, but not necessarily including at least one of each and every element specifically listed within the list of elements and not excluding any combinations of elements in the list of elements.
  • This definition also allows that elements may optionally be present other than the elements specifically identified within the list of elements to which the phrase “at least one” refers, whether related or unrelated to those elements specifically identified.
  • “at least one of A and B” can refer, in one embodiment, to at least one, optionally including more than one, A, with no B present (and optionally including elements other than B); in another embodiment, to at least one, optionally including more than one, B, with no A present (and optionally including elements other than A); in yet another embodiment, to at least one, optionally including more than one, A, and at least one, optionally including more than one, B (and optionally including other elements); etc.

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Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN110898006A (zh) * 2019-11-07 2020-03-24 莆田学院 一种载药微米介孔硅、其透皮制剂及制备方法和应用
WO2021247958A1 (en) 2020-06-05 2021-12-09 Hazel Technologies, Inc. Devices and methods for release and delivery of active ingredients
US11278023B2 (en) 2016-02-19 2022-03-22 Hazel Technologies, Inc. Compositions for controlled release of active ingredients and methods of making same
WO2022072604A1 (en) 2020-10-01 2022-04-07 Hazel Technologies, Inc. Systems and methods for application of active ingredients to cannabis
WO2022241073A1 (en) * 2021-05-14 2022-11-17 Hazel Technologies, Inc. Systems and methods for dispersing active ingredients
WO2023096881A1 (en) * 2021-11-24 2023-06-01 Agrofresh Inc. Consumer applications for cyclopropene-containing compositions
WO2024076874A1 (en) * 2022-10-04 2024-04-11 Ryp Labs, Inc. Systems and methods for carrier systems for controlled release delivery in perishable goods

Families Citing this family (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20200396993A1 (en) * 2017-12-27 2020-12-24 Hazel Technologies, Inc. Compositions and methods for release of cyclopropenes
IL304085A (he) 2018-04-27 2023-08-01 Fresh Inset S A תכשירים ופריטים המכילים קומפלקסים של 1–מתילציקלופרופן ואלפא–ציקלודקסטרין
MX2021006689A (es) * 2018-12-07 2021-09-23 Hazel Tech Inc Composiciones activadas por humedad para la liberacion de antimicrobianos.
CN109588481A (zh) * 2019-02-15 2019-04-09 江苏莱顿博瑞生物科技有限公司 一种防止鲜切土豆褐变、延长贮藏时间的保鲜方法
CN110226600B (zh) * 2019-06-05 2021-05-11 甘肃省农业科学院农产品贮藏加工研究所 一种以羟丙基-β-环糊精为缓释载体的右旋香芹酮马铃薯抑芽剂
CN110235933A (zh) * 2019-07-08 2019-09-17 国家农产品保鲜工程技术研究中心(天津) 一种蓝莓鲜果采贮运销一体化保鲜方法及应用
US11730166B2 (en) 2020-02-03 2023-08-22 Fresh Inset S.A. Stable 1-methylcyclopropene compositions and uses thereof
CA3205120A1 (en) 2021-01-21 2022-07-28 Jp Laboratories, Inc. Materials and methods for extending shelf-life of foods
WO2023064294A1 (en) * 2021-10-11 2023-04-20 Strategia Project Management, LLC, an Illinois Limited Liability Company Method and composition for providing an engineered silica-based crystalline-like pathogen barrier on plants and produce
KR102430784B1 (ko) * 2021-10-12 2022-08-09 한국과학기술원 콩 휘발성유기화합물을 유효성분으로 함유하는 노린재 유인용 조성물 및 이의 용도
CN115943965B (zh) * 2022-12-01 2023-10-17 山东泉辉作物农业科技有限公司 一种杀虫除螨的生物农药杀虫剂及其制备方法

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20020018743A1 (en) * 2000-06-30 2002-02-14 Mitsubishi Chemical Corporation Silica gel
US20020198107A1 (en) * 2001-02-26 2002-12-26 Kostansek Edward Charles Delivery systems for cyclopropenes
US20050261132A1 (en) * 2004-05-19 2005-11-24 Kostansek Edward C Compositions with cyclopropenes and metal-complexing agents
US20060188572A1 (en) * 2005-02-23 2006-08-24 Sjogren Robert D Controlled release of S-methoprene and other active ingredients with activated carbon
CN102440237A (zh) * 2011-09-30 2012-05-09 西安鲜诺生物科技有限公司 一种1-甲基环丙烯制剂及其制备方法
WO2017091096A2 (en) * 2015-11-27 2017-06-01 Institutul National De Cercetare-Dezvoltare Pentru Chimie Şi Petrochimie Process for essential oils encapsulation into mesoporous silica systems and for their application as plant biostimulants

Family Cites Families (154)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3426011A (en) 1967-02-13 1969-02-04 Corn Products Co Cyclodextrins with anionic properties
US3879188A (en) 1969-10-24 1975-04-22 Amchem Prod Growth regulation process
JPS5542041B2 (he) 1973-09-25 1980-10-28
HU184066B (en) 1979-12-28 1984-06-28 Chinoin Gyogyszer Es Vegyeszet Plant growth regulating substance and process for preparing such compound
CA1264956A (en) 1984-10-30 1990-01-30 Seiwa Technological Laboratories Limited Preservation of foodstuffs, plants and plant materials and packaging material for use in this preservation
JPS62501771A (ja) 1985-01-07 1987-07-16 キノイン ギオギスゼル エス ベギエスゼチ テクメチク ギヤラ ア−ルテイ− シクロデキストリンを使うことにより植物保護剤の活性を促進する方法
US5102564A (en) 1989-04-12 1992-04-07 The Procter & Gamble Company Treatment of fabric with perfume/cyclodextrin complexes
US4888364A (en) 1989-01-26 1989-12-19 Dow Corning Corporation Solid gel dispensers for achieving controlled release of volatile liquid materials and method for preparing same
US4891389A (en) 1989-01-26 1990-01-02 Dow Corning Corporation Solid gel dispensers for achieving controlled release of volatile liquid materials and method for preparing same
US4891388A (en) 1989-01-26 1990-01-02 Dow Corning Corporation Solid gel dispensers for achieving controlled release of volatile liquid materials and method for preparing same
JP2849586B2 (ja) 1989-11-28 1999-01-20 昭和電工株式会社 青果物鮮度保持用合成樹脂フィルム及び鮮度保持方法
US5100462A (en) 1991-04-01 1992-03-31 North Carolina State University Method of counteracting ethylene response by treating plants with diazocyclopentadiene and derivatives thereof
US5165943A (en) 1991-06-21 1992-11-24 Wm. Wrigley Jr. Company Cooling agent/cyclodextrin complex for improved flavor release
US5321014A (en) 1991-06-28 1994-06-14 The United States Of America As Represented By The Department Of Health And Human Services Molecular encapsulation and delivery of alkenes alkynes and long chain alkanes, to living mammalian cells
JPH0551301A (ja) * 1991-08-23 1993-03-02 Osaka Gas Co Ltd 防菌・防黴性香気発生具
US5234611A (en) 1991-08-28 1993-08-10 The Procter & Gamble Company Fabric softener, preferably liquid, with protected, dryer-activated, cyclodextrin/perfume complex
US5324616A (en) 1992-04-01 1994-06-28 Xerox Corporation Encapsulated toner compositions and processes thereof
EP0572743A1 (en) 1992-06-05 1993-12-08 Ncsr "Demokritos" New inclusion complexes of cyclodextrin and their use in slow release formulation for the treatment of the olive pest Dacus oleae (GMEL).
US5472954A (en) 1992-07-14 1995-12-05 Cyclops H.F. Cyclodextrin complexation
JP3243866B2 (ja) * 1992-12-04 2002-01-07 ぺんてる株式会社 揮散性物質の粒体
US6375999B1 (en) 1993-10-07 2002-04-23 Darol Forsythe Methods for treating potatoes
US5518988A (en) 1994-06-03 1996-05-21 North Carolina State University Method of counteracting an ethylene response in plants
NO944131D0 (no) 1994-10-28 1994-10-28 Norsk Hydro As Fremgangsmåte og middel for å kontrollere insektsarter
US5958490A (en) * 1994-11-07 1999-09-28 The Unites States Of America, As Represented By The Secretary Of Agriculture Controlled release fumigation of harvested agricultural commodities
US5653971A (en) 1995-06-30 1997-08-05 The Gillette Company Shaving aid composite with an inclusion complex of a skin-soothing agent and a cyclodextrin
US6703672B1 (en) 1995-09-29 2004-03-09 Intel Corporation Polysilicon/amorphous silicon composite gate electrode
US6153559A (en) 1996-09-23 2000-11-28 Valent Biosciences, Inc. N-acetyl AVG and its use as an ethylene biosynthesis inhibitor
CN1291129A (zh) * 1998-02-20 2001-04-11 巴泰勒纪念研究所 保护贴近土壤的木结构的控制释放部件
US6048736A (en) 1998-04-29 2000-04-11 Kosak; Kenneth M. Cyclodextrin polymers for carrying and releasing drugs
ATE265138T1 (de) 1998-04-30 2004-05-15 Basf Ag Retardformulierungen von pflanzenschutzwirkstoffen
US6017849A (en) * 1998-08-20 2000-01-25 Biotechnologies For Horticulture, Inc. Synthesis methods, complexes and delivery methods for the safe and convenient storage, transport and application of compounds for inhibiting the ethylene response in plants
US7939091B2 (en) 1999-08-06 2011-05-10 Iowa State University Research Foundation, Inc. Biorational repellents obtained from terpenoids for use against arthropods
AU777916B2 (en) 1999-11-23 2004-11-04 North Carolina State University Blocking an ethylene response in plants using cyclopropene derivatives
US6194350B1 (en) 1999-11-23 2001-02-27 North Carolina State University Methods of blocking ethylene response in plants using cyclopropene derivatives
US6562758B1 (en) 1999-12-15 2003-05-13 Basf Corporation Methods and compositions to defoliate crop plants and minimize plant regrowth following defoliation
US6541560B1 (en) 2000-03-15 2003-04-01 Graphic Packaging Corporation Control of volatile carbonyl compound in compositions used in printing, printing methods and resulting printed structure
WO2001072129A1 (en) 2000-03-28 2001-10-04 Council Of Scientific And Industrial Research Acyclic monoterpenes as anti-sprouting agents for potato tubers
US6452060B2 (en) 2000-04-11 2002-09-17 Rohm And Haas Company Method to prepare cyclopropenes
CN1207335C (zh) 2000-04-17 2005-06-22 飘柔系统有限公司 湿度敏感性组合物
US6897185B1 (en) 2000-09-22 2005-05-24 Lytone Enterprise, Inc. Formulation for counteracting and ethylene response in plants, preparation process thereof, and method using the same
US6444619B1 (en) 2000-09-28 2002-09-03 Rohm And Haas Company Delivery system for cyclopropenes
IL145476A (he) 2000-09-29 2006-07-05 Rohm & Haas מערכות לשחרור ציקלופרופנים הדורשות פחות מים
US6953540B2 (en) 2000-09-29 2005-10-11 Rohm And Haas Company Continuous process for the preparation of encapsulated cyclopropenes
US6372220B1 (en) 2001-02-05 2002-04-16 Kavita Shukla Fenugreek impregnated material for the preservation of perishable substances
US6762153B2 (en) 2001-10-18 2004-07-13 Rohm And Haas Company Delivery system for cyclopropenes
US6821928B2 (en) * 2001-11-06 2004-11-23 Rodney Ruskin Method to reduce the rate of diffusion of slow-release materials through polymers and process for making drip irrigation devices with long-term control of root growth
JP4254097B2 (ja) 2001-11-28 2009-04-15 パナソニック株式会社 揮散性薬剤徐放部材とそれを用いた空気調和機
US20040072694A1 (en) 2002-02-25 2004-04-15 Jacobson Richard Martin Method to inhibit ethylene responses in plants
US7497623B2 (en) 2002-02-27 2009-03-03 Pactiv Corporation Packages with active agents
US7271259B1 (en) 2002-05-06 2007-09-18 Northwestern University Solid phase host compositions
TW200401609A (en) 2002-05-14 2004-02-01 Rohm & Haas Method and device for the generation of cyclopropene compounds
TWI339101B (en) 2002-08-06 2011-03-21 Rohm & Haas Stable ethylene inhibiting compounds and methods for their preparation
US20060003057A1 (en) 2002-10-21 2006-01-05 Kelly Robert C Gas-release packet with frangible sub-packet
US20040081727A1 (en) 2002-10-21 2004-04-29 Kelly Robert Charles Gas-release packet with frangible sub-packet
JP2004210661A (ja) 2002-12-27 2004-07-29 Japan Enviro Chemicals Ltd 殺シロアリ剤
US7138130B2 (en) * 2003-01-30 2006-11-21 S.C. Johnson & Son, Inc. Substrate for volatile delivery systems
US6770600B1 (en) 2003-02-28 2004-08-03 Rohm And Haas Company Delivery systems for cyclopropene compounds
US20070021300A1 (en) * 2003-05-09 2007-01-25 Jean-Pierre Farant Process for the production of activated carbon
US7041625B2 (en) 2003-08-21 2006-05-09 Rohm And Haas Company Method to inhibit ethylene responses in plants
US20050065033A1 (en) 2003-08-21 2005-03-24 Jacobson Richard Martin Method to inhibit ethylene responses in plants
JP2005307120A (ja) * 2004-04-26 2005-11-04 Mitsubishi Chemicals Corp 徐放剤及びそれを用いた徐放材
CA2504840C (en) 2004-05-05 2008-03-18 Rohm And Haas Company Humidity activated delivery systems for cyclopropenes
WO2005110592A1 (en) * 2004-05-17 2005-11-24 Yki, Ytkemiska Institutet Ab Mesoporous particles loaded with active substance
US20050260907A1 (en) 2004-05-18 2005-11-24 Chang William T H Laminate for counteraction an ethylene response in plants, method of making, or using the same
TW200538037A (en) 2004-05-19 2005-12-01 Rohm & Haas Compositions with cyclopropenes and adjuvants
US20090088323A1 (en) 2004-05-19 2009-04-02 Basel Richard M Compositions with cyclopropenes and adjuvants
AU2005250421A1 (en) 2004-05-27 2005-12-15 Perftech Inc. Packaging material and method for microwave and steam cooking of perishable food product
EP1609359A3 (en) 2004-06-24 2011-10-05 Rohm and Haas Company A method for treating plants or plant parts
CA2594495A1 (en) 2005-01-10 2006-07-13 Her Majesty The Queen In Right Of Canada As Represented By The Minister Of Agriculture And Agri-Food Compositions and methods to improve the storage quality of packaged plants
AU2007201831B8 (en) 2005-01-14 2013-02-21 Agrofresh Inc. Contacting crop plants with compositions
AU2005242218A1 (en) 2005-01-14 2006-08-03 Rohm And Haas Company Plant growth regulation
US20070000505A1 (en) 2005-02-24 2007-01-04 Philip Morris Usa Inc. Smoking article with tobacco beads
WO2007041272A2 (en) * 2005-09-30 2007-04-12 Maxam Industries, Inc. Long lasting natural anti-pest additive
CA2565427A1 (en) 2005-11-08 2007-05-08 Rohm And Haas Company Compositions with cyclopropenes and non-hydrocarbon oils
US20070117720A1 (en) 2005-11-18 2007-05-24 Jacobson Richard M Compositions with cyclopropenes
KR100823872B1 (ko) 2005-11-18 2008-04-21 유상구 농산물의 숙성 과정을 조절하기 위한 시클로프로펜유도체의 발생장치
CN100340172C (zh) 2006-04-17 2007-10-03 西安交通大学 用于果蔬花卉保鲜的1-甲基环丙烯稳定包结物的制备
US20070265167A1 (en) 2006-05-15 2007-11-15 Todd Edgington Treating horticultural crops
US8691728B2 (en) 2006-11-09 2014-04-08 Rohm And Haas Company Cyclopropene compositions
ZA200904974B (en) 2007-01-17 2010-09-29 Dow Agrosciences Llc Delivery of ethylene blocking and/or promoting agents
MX2008002145A (es) 2007-02-22 2009-02-25 Rohm & Haas Metodo para elaborar un complejo.
EP1967545A1 (en) 2007-03-09 2008-09-10 Rohm and Haas France SAS Cationic polymer latex
US20150282479A1 (en) 2007-05-10 2015-10-08 Dow Agrosciences Llc Methods of treating crop plants
GB2449876B (en) 2007-06-06 2009-05-06 Post Harvest Solutions Ltd Active packaging materials incorporating micro-porous solids and essential oils
CA2631186A1 (en) 2007-06-19 2008-12-19 Rohm And Haas Company Safening of pesticides with cyclopropenes
AU2008269161B2 (en) 2007-06-22 2013-10-03 North Carolina State University Methods of inhibiting ethylene responses in plants using cyclopropene amine compounds
JP5128392B2 (ja) 2007-08-03 2013-01-23 ローム アンド ハース カンパニー 油配合物
US9012515B2 (en) 2007-08-03 2015-04-21 Rohm And Haas Company Oil formulations with thickeners
JP5097069B2 (ja) 2007-11-06 2012-12-12 ローム アンド ハース カンパニー 封入複合体の製造法
JP5342774B2 (ja) * 2007-12-25 2013-11-13 花王株式会社 複合メソポーラスシリカ粒子
JP5080513B2 (ja) 2008-03-13 2012-11-21 ローム アンド ハース カンパニー シクロプロペン複合体組成物
US8343261B2 (en) 2008-03-17 2013-01-01 Basf Se Use of formate-based porous metal organic frameworks for methane storage
CN101297659A (zh) 2008-06-13 2008-11-05 西安交通大学 一种环丙烯类包结物胶囊及其制备方法
KR20100004516A (ko) * 2008-07-04 2010-01-13 이수진 활성탄을 이용한 1-메틸사이클로프로펜과메틸렌사이클로프로판의 저장과 방출 방법
US20140066310A1 (en) 2008-08-25 2014-03-06 Rohm And Haas Company Methods and systems for banana yield protection and enhancement
ES2371603T3 (es) 2008-08-25 2012-01-05 Rohm And Haas Company Tratamiento de platanos.
KR101605677B1 (ko) 2008-09-25 2016-03-25 (주)이룸바이오테크놀러지 1-메틸시클로프로펜을 제조하여 식물에 부가하는 방법
EP2408684B1 (de) 2009-03-20 2013-08-21 Basf Se Biologisch abbaubares material aus einem polymer enthaltenden porösen metallorganischen gerüstmaterial
ES2400355T3 (es) 2009-03-20 2013-04-09 Basf Se Obtención exenta de disolvente de material estructural organometálico poroso basado en formiato de magnesio
JP5430987B2 (ja) 2009-03-23 2014-03-05 クラレケミカル株式会社 高機能造粒炭
JP2011045363A (ja) 2009-08-06 2011-03-10 Rohm & Haas Co 観賞植物の処理
EP2296171A3 (de) 2009-09-10 2016-04-06 Basf Se Verwendung von metallorganischen gerüstmaterialien zur herstellung von mikroelektronischen bauteilen
TWI445500B (zh) 2009-10-16 2014-07-21 Lytone Enterprise Inc 用於抑制植物中乙烯反應之微膠囊組合物,製備微膠囊之方法及使用微膠囊組合物之方法
US8461086B2 (en) 2009-10-16 2013-06-11 Lytone Enterprise, Inc. Microcapsule composition for inhibiting an ethylene response in plants, method for preparing microcapsules, and method using the microcapsule composition
US9155299B2 (en) * 2009-11-18 2015-10-13 Agrofresh Inc. Bonded fiber matrix containing encapsulation complex
CA2692211C (en) 2009-12-14 2011-09-13 Cellresin Technologies, Llc Maturation or ripening inhibitor release from polymer, fiber, film, sheet or packaging
KR101663184B1 (ko) 2009-12-15 2016-10-06 삼성전자주식회사 하이브리드 다공성 물질 및 그의 제조방법
DE202009017307U1 (de) 2009-12-18 2010-03-18 Basf Se Verwendung mindestens eines porösen metallorganischen Gerüstmaterials (MOF) zur Reduktion des Methangasanteils und zur Erhöhung der Gesamtgasausbeute in Tierfutter
US20110150995A1 (en) 2009-12-22 2011-06-23 Hemant Narahar Joshi Solid Dosage Forms of Essential Oils
CA2780728C (en) 2009-12-28 2015-04-07 Rohm And Haas Company Method of handling bananas
WO2011133575A1 (en) 2010-04-19 2011-10-27 Freshtec, Inc. Treatment of modified atmosphere packaging
KR101429554B1 (ko) * 2010-04-22 2014-08-14 (주)이룸바이오테크놀러지 시클로프로펜 화합물 및 이를 농작물에 부가하는 방법
WO2011143564A1 (en) 2010-05-13 2011-11-17 Paper-Pak Industries Treatment system to prolong life of cut flowers
CN102933077B (zh) 2010-06-07 2016-01-20 先正达参股股份有限公司 环丙烯组合物
CA2743758C (en) 2010-07-02 2013-01-08 Rohm And Haas Company Coated powder particles
CN101926387B (zh) 2010-09-17 2012-11-28 天津农科食品生物科技有限公司 无公害葡萄保鲜垫及其制备方法
CN101971875B (zh) 2010-10-19 2012-11-28 西安交通大学 果蔬花卉保鲜用1-甲基环丙烯包结物及其制备方法
US20130345060A1 (en) * 2010-12-07 2013-12-26 Agrofresh Inc. Methods and compositions of granule formulations
US20120142534A1 (en) 2010-12-07 2012-06-07 Mark Linden Dahmer Granular compositions
CN102119718B (zh) * 2010-12-10 2013-06-19 山东营养源食品科技有限公司 一种环丙烯类保鲜剂及其制备方法
CN102119719B (zh) 2010-12-10 2013-06-19 山东营养源食品科技有限公司 一种环丙烯类保鲜剂及其制备和包装方法
PT2976946T (pt) 2011-03-27 2017-06-26 Cellresin Tech Llc Composições de ciclodextrina, artigos e métodos
KR101877419B1 (ko) 2011-03-30 2018-07-11 (주)이룸바이오테크놀러지 1-메틸시클로프로펜 발생 장치
JP5562992B2 (ja) * 2011-04-05 2014-07-30 ローム アンド ハース カンパニー 制御放出組成物
WO2012177969A2 (en) 2011-06-22 2012-12-27 1,4 Group, Inc. Cipc vapor treatment
TWI583309B (zh) 2011-06-29 2017-05-21 羅門哈斯公司 處理芒果之方法
JP5953733B2 (ja) 2011-12-19 2016-07-20 住友化学株式会社 固形農薬製剤
WO2013126047A1 (en) 2012-02-21 2013-08-29 Empire Technology Development Llc Food-preservation devices and methods of use
EP2839525B1 (en) 2012-04-18 2020-06-03 King Abdullah University Of Science And Technology Electrode separator
NZ704099A (en) 2012-07-25 2016-12-23 Agrofresh Inc Methods of handling avocados and system
US20140080711A1 (en) 2012-09-17 2014-03-20 Agrofresh Inc. Suspension of particles comprising cyclopropene complexes dispersed in a resin matrix
US20140080712A1 (en) * 2012-09-17 2014-03-20 Agrofresh Inc. Compositions and methods for double encapsulation of a volatile compound
AU2013314957B2 (en) 2012-09-17 2016-06-09 Agrofresh Inc. Compositions and methods for double encapsulation of a volatile compound
CN104822750A (zh) * 2012-09-17 2015-08-05 农鲜股份有限公司 用于将挥发性化合物双重封装的组合物和方法
CN202807462U (zh) 2012-09-18 2013-03-20 西安鲜诺生物科技有限公司 一种果蔬保鲜药包
CN102862361B (zh) 2012-09-26 2015-05-13 北京印刷学院 一种可释放1-甲基环丙烯的果蔬保鲜包装材料及制备方法
CN102964615B (zh) 2012-10-09 2017-09-22 新疆农业科学院农产品贮藏加工研究所 一种环丙烯保鲜纸的制备方法
NZ706839A (en) 2012-10-10 2018-05-25 Univ Queensland Encapsulation of gases within cyclodextrins
AU2013329131B2 (en) 2012-10-11 2016-10-13 Agrofresh Inc. Yield enhancement for stress-susceptible plants
US9591847B2 (en) * 2012-10-29 2017-03-14 Washington State University Control of ripening and senescence in pre-harvest and post-harvest plants and plant materials by manipulating alternative oxidase activity
US9210938B2 (en) 2012-11-28 2015-12-15 Elwha Llc Methods for modulating photosynthetic activity
CN104936447B (zh) * 2012-11-30 2018-03-06 塞尔瑞星技术有限公司 控制释放组合物及使用方法
US9320288B2 (en) 2012-11-30 2016-04-26 Cellresin Technologies, Llc Controlled release compositions and methods of using
EP2989164A4 (en) 2013-04-26 2016-11-02 Agrofresh Inc METHOD AND COMPOSITIONS FOR POLYMER CONDENSATION SYNTHETIZED POLYMER MATRIX
US8802140B2 (en) 2013-05-05 2014-08-12 Nazir Mir Situ mixing and application of hydrocolloid systems for pre- and post harvest use on agricultural crops
US8822382B2 (en) 2013-05-05 2014-09-02 Nazir Mir Hydrocolloid systems for reducing loss of volatile active compounds from their liquid formulations for pre- and post harvest use on agricultural crops
TW201503831A (zh) 2013-07-11 2015-02-01 Agrofresh Inc 用於揮發性化合物之濕度活化的調配物
US9992995B2 (en) 2013-09-25 2018-06-12 Agrofresh Inc. Systems and methods for solvent-free delivery of volatile compounds
US9421793B2 (en) 2014-06-26 2016-08-23 Cellresin Technologies, Llc Electrostatic printing of cyclodextrin compositions
ES2815650T3 (es) 2014-09-05 2021-03-30 Basf Corp Sistema de almacenamiento de alimentos que comprende un recipiente y un material adsorbente, y procedimiento para extender la vida comercial de un producto
US9394216B2 (en) * 2014-11-10 2016-07-19 Mirtech, Inc. Complexes of 1-methylcyclopropene with metal coordination polymer networks
CN108366555A (zh) 2015-10-13 2018-08-03 博凯普有限公司 用于处理作物的腐败阻滞剂组合物
ES2820879R1 (es) 2016-02-19 2021-06-21 Hazel Tech Inc Composiciones para la liberación controlada de ingredientes activos y métodos de preparación de las mismas
US20200396993A1 (en) 2017-12-27 2020-12-24 Hazel Technologies, Inc. Compositions and methods for release of cyclopropenes

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20020018743A1 (en) * 2000-06-30 2002-02-14 Mitsubishi Chemical Corporation Silica gel
US20020198107A1 (en) * 2001-02-26 2002-12-26 Kostansek Edward Charles Delivery systems for cyclopropenes
US20050261132A1 (en) * 2004-05-19 2005-11-24 Kostansek Edward C Compositions with cyclopropenes and metal-complexing agents
US20060188572A1 (en) * 2005-02-23 2006-08-24 Sjogren Robert D Controlled release of S-methoprene and other active ingredients with activated carbon
CN102440237A (zh) * 2011-09-30 2012-05-09 西安鲜诺生物科技有限公司 一种1-甲基环丙烯制剂及其制备方法
WO2017091096A2 (en) * 2015-11-27 2017-06-01 Institutul National De Cercetare-Dezvoltare Pentru Chimie Şi Petrochimie Process for essential oils encapsulation into mesoporous silica systems and for their application as plant biostimulants

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11278023B2 (en) 2016-02-19 2022-03-22 Hazel Technologies, Inc. Compositions for controlled release of active ingredients and methods of making same
CN110898006A (zh) * 2019-11-07 2020-03-24 莆田学院 一种载药微米介孔硅、其透皮制剂及制备方法和应用
CN110898006B (zh) * 2019-11-07 2021-11-05 莆田学院 一种载药微米介孔硅、其透皮制剂及制备方法和应用
WO2021247958A1 (en) 2020-06-05 2021-12-09 Hazel Technologies, Inc. Devices and methods for release and delivery of active ingredients
WO2022072604A1 (en) 2020-10-01 2022-04-07 Hazel Technologies, Inc. Systems and methods for application of active ingredients to cannabis
WO2022241073A1 (en) * 2021-05-14 2022-11-17 Hazel Technologies, Inc. Systems and methods for dispersing active ingredients
WO2023096881A1 (en) * 2021-11-24 2023-06-01 Agrofresh Inc. Consumer applications for cyclopropene-containing compositions
WO2024076874A1 (en) * 2022-10-04 2024-04-11 Ryp Labs, Inc. Systems and methods for carrier systems for controlled release delivery in perishable goods

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