WO2024010072A2 - Ornamental plant production method and ornamental plant - Google Patents

Ornamental plant production method and ornamental plant Download PDF

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Publication number
WO2024010072A2
WO2024010072A2 PCT/JP2023/025178 JP2023025178W WO2024010072A2 WO 2024010072 A2 WO2024010072 A2 WO 2024010072A2 JP 2023025178 W JP2023025178 W JP 2023025178W WO 2024010072 A2 WO2024010072 A2 WO 2024010072A2
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WO
WIPO (PCT)
Prior art keywords
film
plant
dried
drying
paint
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PCT/JP2023/025178
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French (fr)
Japanese (ja)
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WO2024010072A3 (en
Inventor
美和子 堺
Original Assignee
美和子 堺
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Application filed by 美和子 堺 filed Critical 美和子 堺
Publication of WO2024010072A2 publication Critical patent/WO2024010072A2/en
Publication of WO2024010072A3 publication Critical patent/WO2024010072A3/en

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Classifications

    • 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
    • A01N3/00Preservation of plants or parts thereof, e.g. inhibiting evaporation, improvement of the appearance of leaves or protection against physical influences such as UV radiation using chemical compositions; Grafting wax
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/08Processes
    • C08G18/10Prepolymer processes involving reaction of isocyanates or isothiocyanates with compounds having active hydrogen in a first reaction step
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/30Low-molecular-weight compounds
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/28Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the compounds used containing active hydrogen
    • C08G18/40High-molecular-weight compounds
    • C08G18/42Polycondensates having carboxylic or carbonic ester groups in the main chain
    • C08G18/44Polycarbonates
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00Polymeric products of isocyanates or isothiocyanates
    • C08G18/06Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/70Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/72Polyisocyanates or polyisothiocyanates
    • C08G18/74Polyisocyanates or polyisothiocyanates cyclic
    • C08G18/75Polyisocyanates or polyisothiocyanates cyclic cycloaliphatic
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D175/00Coating compositions based on polyureas or polyurethanes; Coating compositions based on derivatives of such polymers
    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09DCOATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D7/00Features of coating compositions, not provided for in group C09D5/00; Processes for incorporating ingredients in coating compositions
    • C09D7/20Diluents or solvents

Definitions

  • the present invention relates to a method for producing an ornamental plant and an ornamental plant.
  • Patent Document 1 describes a step of putting a plant into a container, a step of putting into the container a ceramic body obtained by applying silica gel, shirasu, and glaze to a spherical ceramic and a desiccant containing oil, and a step of putting the entire container into the container.
  • a method for producing a dried ornamental plant is disclosed, which includes the step of drying at 27 to 32°C.
  • the present invention aims to suppress damage to dried ornamental plants.
  • the technology disclosed herein includes a drying step of drying a plant, and a film forming step of forming a film of a resin composition on the surface of the dried plant.
  • the polyol component is a liquid carbonate polyol having a functional group number of 2 and a number average molecular weight of 2,000 to 3,000, and has an active hydroxy group at the terminal
  • the polyisocyanate component is an alicyclic polyisocyanate having two functional groups and has an isocyanate group at the terminal, and the hydroxyl equivalent (OH) of the polyol component (A) is equal to that of the polyisocyanate component (B).
  • the polyol component of (A) and the polyisocyanate component of (B) are reacted in the presence of (C) a catalyst (D) in a solvent (E)
  • a film of the paint (E) is formed on the surface of the dried plant, and the paint is exposed to air. This is a method for producing ornamental plants in which a urea bond is formed by reacting with water vapor.
  • the equivalent ratio (NCO/OH) between the hydroxyl equivalent (OH) of the polyol component (A) and the isocyanate equivalent (NCO) of the polyisocyanate component (B) is 1.95 to 2.5.
  • the alicyclic polyisocyanate is preferably methylene bis(4,1-cyclohexylene) diisocyanate or isophorone diisocyanate.
  • the film of the resin composition has a tensile stress at 100% elongation of 1.0 to 1.1 MPa, a tensile elongation at break of 1,000% or more, and a tensile strength at break of 17.6 to 18.7 MPa. It would be good if it were.
  • the paint (E) be dry to the touch within 30 seconds after forming a film of the paint on the dried plant.
  • the solvent (D) is preferably an ethyl acetate solvent, and the resin concentration of the paint used in the touch drying step is preferably 5 to 10%.
  • the step of drying to the touch is performed by placing the dried plants on an absorbent body that absorbs the paint of (E), and after the step of drying to the touch, the dried plants are hung to absorb the paint. It is advisable to further dry the membrane. It is also preferable that the plant is provided with a flower receptacle, and that the frozen plant is vacuum-dried in the drying step. Furthermore, it is preferable that the plant is dried in the drying step without being pressed into a flat shape after being harvested.
  • the technology disclosed in this specification includes a drying step of freezing and vacuum drying a plant provided with flower receptacles, and a film forming step of forming a film of a resin composition on the surface of the dried plant.
  • the polyol component is a liquid carbonate polyol having a functional group number of 2, a molecular weight of 2,000 to 3,000, and an active hydroxyl group at the end, and (B) a polyol component.
  • the isocyanate component is methylene bis(4,1-cyclohexylene) diisocyanate or isophorone diisocyanate having two functional groups and an isocyanate group at the terminal, and the hydroxyl equivalent (OH) of the polyol component (A) and the polyol component (B) are The equivalent ratio (NCO/OH) of the isocyanate component to the isocyanate equivalent (NCO) is 1.95 to 2.5, and the polyol component of (A) and the polyisocyanate component of (B) are combined into (C) It is a coating of a prepolymer solution having an active isocyanate group at the end, which is composed of (E) a polyurethane resin reacted in (D) an ethyl acetate solvent in the presence of a catalyst, and in the film forming step, the drying A film of the paint of (E) is formed on the surface of the dried plant, and is reacted with water vapor in the air to form a urea bond
  • the film of the resin composition is dry to the touch within 30 seconds after being applied, and the film of the resin composition has a 100% elongation tensile stress of 1.0 to 1.1 MPa, and a tensile elongation at break of 1,000% or more.
  • This is a method for producing an ornamental plant having a tensile strength at break of 17.6 to 18.7 MPa.
  • the technology disclosed herein is an ornamental plant produced by the above production method.
  • the technology disclosed herein includes a dried plant and a film of a resin composition formed on the surface of the plant, and the film of the resin composition has a It is an ornamental plant having a % elongation tensile stress of 1.0 to 1.1 MPa, a tensile elongation at break of 1,000% or more, and a tensile strength at break of 17.6 to 18.7 MPa.
  • FIG. 1 is a schematic configuration diagram of a dried flower to which this embodiment is applied. It is a figure showing the manufacturing process of dried flowers.
  • (A) is a flowchart showing a manufacturing process of dried flowers
  • (B) is a flowchart showing another manufacturing process of dried flowers.
  • FIG. 1 is a schematic configuration diagram of a dried flower 10 to which this embodiment is applied.
  • the dried flower 10 includes a plant body 20 and a resin film 30 that is a protective layer formed on the surface of the plant body 20.
  • the plant body 20 is not particularly limited as long as it is a plant that can be subjected to drying treatment or resin forming treatment, which will be described later.
  • the plant body 20 is an ornamental plant such as a rose, a carnation, a viola, a snapdragon, a julienne, a pentus denfare (orchid), a dianthus (diana), a cherry blossom, a cosmos, a carrot leaf, a basil, or a chervil.
  • the plant body 20 has a stem 11, a leaf blade 13, petals 15, a flower receptacle 17, and a calyx 19.
  • the plant body 20 in the illustrated example is a rose.
  • dried flowers refer to ornamental plants that have been subjected to drying treatment.
  • the moisture content of the plant body 20 is, for example, 20% or less, preferably 10% or less, and more preferably 5% or less.
  • dried flowers include not only petals and leaf blades, but also dried stems, fruits, and the like.
  • the plant body 20 has a three-dimensional shape.
  • the plant body 20 is not a so-called pressed flower.
  • pressed flowers are harvested flowers and leaves that are pressed into a flat shape and dried.
  • the plant body 20 is manufactured without being pressed into a flat shape from the harvested state.
  • dried flowers such as the plant body 20 have been subjected to a drying process, they are easily damaged when subjected to external pressure. Therefore, in the past, dried flowers were sometimes reinforced by applying resin or the like to the surface of the dried flowers. However, when the resin is applied, a so-called shine or luster occurs, and the appearance of the dried flowers becomes different from the natural texture before the resin is applied. To explain further, if the entire resin is formed thickly in a thin part such as a flower petal, gloss may occur and the appearance may differ from the natural finish.
  • the thickness of the resin film 30 can be suppressed by using a resin liquid to be described later. As a result, even when the resin film 30 is formed on the surface of the plant body 20, gloss is suppressed, and an ornamental plant with a natural-looking finish can be formed.
  • the illustrated resin film 30 is flexible. Therefore, even with the resin film 30 formed, deformation of the plant body 20 can be allowed, and it is possible to suppress deformation and cracking of the dried flower 10. In other words, in this embodiment, the durability of the dried flowers 10 is improved, and the dried flowers 10 can be made to last for a long time.
  • the dried flowers 10 can be made to last for a long time even when the dried flowers 10 are displayed in a humid environment, for example. Further, since the resin film 30 reflects light such as ultraviolet rays, it becomes possible to maintain bright colors for a long period of time.
  • the resin film 30 on the surface of the plant body 20, it is possible to suppress a portion of the dried flower 10, that is, a petal or a leaf blade, from falling.
  • the deformable resin film 30 can be formed on the surface of the plant body 20. This can prevent the dried flowers 10 from collapsing even when external force is applied.
  • the resin film 30 is formed on the surface of the plant body 20 in a shape corresponding to the irregularities of the plant body 20.
  • the resin film 30 is formed to smooth the surface of the plant body 20.
  • the resin film 30 is formed in a thick film part 31 formed in the concave part 18 of the plant body 20 and a thick film part 31 formed in the convex part 16 of the plant body 20. It has a thin film portion 33 with a small thickness. By having different thicknesses of the resin film 30, generation of gloss due to the resin film 30 can be suppressed.
  • FIG. 2 is a diagram showing a manufacturing process of dried flower 10.
  • the manufacturing process of the dried flower 10 will be explained with reference to FIG. 2.
  • drying treatment, dipping treatment, temporary drying treatment, and main drying treatment are performed.
  • the dipping treatment, temporary drying treatment, and main drying treatment are resin forming treatments that form the resin film 30 on the surface of the plant body 20.
  • the plant body 20 is dried.
  • the plant body 20 and the desiccant 4 are placed in the drying container 3, and the plant body 20 is dried.
  • a predetermined amount of desiccant 4 is placed at the bottom of the drying container 3, for example.
  • the plant body 20 is placed on the desiccant 4, and the desiccant 4 is further added into the drying container 3.
  • the outer periphery of the plant body 20 is covered with the desiccant 4.
  • the plant body 20 is dried over a predetermined period (for example, 3 days to 1 week).
  • the drying container 3 may be placed in a dryer to control the drying of the plant body 20.
  • the type of desiccant 4 that can be used in this embodiment, but examples include silica gel, calcium chloride, and magnesium chloride.
  • a resin film 30 is formed on the surface of the dried plant body 20.
  • the dried plant body 20 is immersed in a resin liquid 6 (described later) contained in a resin container 5.
  • the time for immersing the plant body 20 in the resin liquid 6 may be any length that allows the resin liquid 6 to adhere to the entire surface of the plant body 20.
  • the immersion time is, for example, 1 second to 60 seconds.
  • the resin liquid 6 adhering to the plant body 20 is temporarily dried.
  • the plant body 20 with the resin liquid 6 adhered to its entire surface is placed on a nonwoven fabric 7 that is an absorbent body.
  • the temporary drying time may be long enough for the resin liquid 6 attached to the plant body 20 to be dry to the touch.
  • the temporary drying time is, for example, 3 seconds to 3 hours.
  • drying to the touch refers to touching the surface of the resin liquid 6 (resin film 30) adhering to the plant body 20 with a fingertip so that the resin liquid 6 does not stick to the fingertip.
  • formation of an excessive resin film 30 on the plant body 20 is suppressed.
  • formation of a pool of the resin liquid 6 on the lower side of the plant body 20 and formation of an excessive resin film 30 on the plant body 20 is suppressed.
  • the resin liquid 6 adhering to the plant body 20 is dried.
  • the main drying time may be long enough for the resin liquid 6 attached to the plant body 20 to be completely dried.
  • the main drying time is, for example, 2 hours to 5 days.
  • main drying refers to pressing the surface of the resin liquid 6 (resin film 30) with a fingertip to make it free from fingerprints.
  • main drying is a process for bringing the resin of the resin film 30 into a more stable state than drying to the touch.
  • the main drying process when performing decorations using the dried flowers 10, etc., it is preferable to perform the main drying process to stabilize the resin film 30. For example, by performing the main drying process for 24 hours, damage to the dried flowers 10 is suppressed. Further, for example, by performing the main drying treatment for 24 hours, the odor of the resin liquid 6 can be reduced.
  • the posture in which the plant body 20 is hung by the hanging tool 9 in the main drying process is such that the plant body 20 is in the opposite growth state in the vertical direction, that is, the petals 15 are on the lower side. Place it like this. This makes it easier for the excess resin film 30 adhering to the plant body 20 to fall from the plant body 20. Moreover, it becomes possible to make the thickness of the resin film 30 formed on the plant body 20 uniform.
  • the plant body 20 such as a flower is dried, and an ornamental plant such as a dried flower can be manufactured.
  • the method of disposing the resin liquid 6 on the surface of the plant body 20 may be other methods such as spraying or hand painting. Note that by immersing the entire plant body 20 in the resin liquid 6 as shown in FIG. 2(B), it is possible to suppress the occurrence of uncoated resin liquid 6 and unevenness in the film thickness of the resin liquid 6.
  • FIG. 3(A) is a flowchart showing the manufacturing process for the dried flower 10
  • FIG. 3(B) is a flowchart showing another manufacturing step for the dried flower 10.
  • drying treatment dipping treatment, temporary drying treatment, and main drying treatment are performed
  • the present invention is not limited thereto.
  • some of these processes may be omitted.
  • an embodiment may be adopted in which either the temporary drying process or the main drying process is omitted.
  • a well-known drying process method such as a hanging method, dry-in-water method, freeze-vacuum drying, vacuum drying, or hot air drying may be used.
  • the following processing is performed. Specifically, first, the plant body 20 is subjected to a drying process (S311). In this drying process, a desiccant 4 (see FIG. 2(A)) is used. The plant body 20 dried by the desiccant 4 is then frozen by a freezing device (not shown) (S312). Then, the frozen plant body 20 is vacuum dried by a vacuum drying device (not shown) (S313). That is, in this manufacturing process, the plant body 20 is dried in two stages: a drying process using the desiccant 4 and a freeze-vacuum drying process.
  • the plant body 20 that has been vacuum dried is subjected to a dipping treatment (S314).
  • the plant body 20 is immersed in the resin liquid 6 (see FIG. 2(C)).
  • the main drying process is performed on the plant body 20 to which the resin liquid 6 has adhered (S315).
  • the plant body 20 is held in a suspended state (see FIG. 2(D)).
  • the temperature inside the refrigerator is set to -80° C. to -60° C. and maintained for 12 hours to 24 hours. This ensures that the plant body 20 is frozen.
  • the internal temperature of the freezing device (-80°C to -60°C) and the freezing period (3 hours to 24 hours) required for the freezing process are based on the appearance of the plant body 20 after the vacuum drying process. This is derived from the test results that determine pass/fail.
  • the vacuum drying process (see S313) is performed by, for example, keeping the interior of the vacuum drying device at room temperature for 12 hours to 3 days. To explain further, holding at a temperature of 40° C. or less, preferably 30° C. or less, more preferably 20° C. or less at a pressure of 50 Pa or less, preferably 5 Pa or less, more preferably 1 Pa or less for about 12 hours to 3 days. is executed. This ensures that the plant body 20 is dried. The moisture content of the plant body 20 becomes, for example, 5% or less after vacuum drying.
  • the pressure inside the vacuum drying device decreases as time passes in the vacuum drying process, but the plant body 20 may be dried when the pressure inside the storage becomes 5 Pa or less. .
  • the plant body 20 includes the flower receptacles 17 and calyxes 19 (see FIG. 1), so that the flower receptacles 17 and calyxes 19 support the petals 15, and deformation of the petals 15 is suppressed.
  • the flower receptacle 17 (see FIG. 1) is a portion with a large diameter in the plant body 20, and is a portion in which it is difficult to dry water in the plant body 20 compared to other portions. For such a portion, it is preferable to perform freeze-vacuum drying treatment as shown in FIG. 3(B). This allows the plant body 20 to be dried more reliably. Additionally, by making the drying more reliable, the occurrence of mold on the dried flowers 10 can be suppressed.
  • freeze-vacuum drying treatment may be performed together with drying treatment using desiccant material 4, or unlike FIG. 3(B), drying treatment using desiccant material 4 is not performed. may be subjected to freeze-vacuum drying treatment.
  • the plant body 20 is suppressed from changing its appearance such as color and shape due to the freeze-vacuum drying process, and has an appearance and flexibility similar to that of a fresh flower.
  • the resin film 30 formed on the plant body 20 is thin and deformable. This makes it possible to give the dried flower 10 the appearance and feel of a fresh flower.
  • the resin film 30 has, for example, the following properties.
  • the resin film 30 is soft and has a tensile stress of 1.0 to 1.1 MPa at 100% elongation. Furthermore, the resin film 30 has a tensile elongation at break of 1,000% or more and is excellent in displacement followability. Further, the resin film 30 has a tensile strength at break of 17.6 to 18.7 MPa.
  • the resin film 30 is a soft coating or a coating composition.
  • non-yellowing soft paint a method is known in which two liquids, a specific polyol component and a specific isocyanate component for imparting flexibility, are mixed in a solvent and applied.
  • the coating workability of this two-liquid mixed reaction type paint sometimes depends on the reaction rate.
  • this two-component mixed reaction type coating material imparts softness, the toughness (tensile elongation or tensile strength) of the coating film sometimes decreases.
  • the resin liquid 6 of this embodiment is a one-component moisture-curable non-yellowing soft paint
  • the resin film 30 is soft with low elongation and tensile stress at 100%, and has excellent tensile elongation at break. It can form a tough coating film with excellent displacement followability and high tensile strength at break.
  • the resin liquid 6 described above in FIG. 2(B) is a one-component moisture-curable non-yellowing soft paint.
  • This resin liquid 6 is a solvent solution of a prepolymer having active isocyanate groups at the terminals obtained from the reaction of a less than stoichiometric amount of a specific polyol component and a stoichiometric amount of a specific polyisocyanate compound component.
  • the hydroxyl equivalent (OH) of the polyol component is smaller than the isocyanate equivalent (NCO) of the polyisocyanate compound component.
  • This resin liquid 6 is applied as a paint to the surface of the plant body 20 as an adherend, and in parallel with the volatilization of the solvent, it reacts with water vapor in the air to form urea bonds, thereby forming a resin film 30. is formed as.
  • the polyol component (A) is a carbonate polyol with a functional group number of 2 and a number average molecular weight of 2,000 to 3,000, and has an active hydroxyl group at the terminal
  • the polyisocyanate component is an alicyclic polyisocyanate having two functional groups and has an isocyanate group at the terminal
  • the hydroxyl equivalent (OH) of the polyol component of (A) above is the same as the polyisocyanate component of (B) above.
  • the polyol component (A) is a liquid carbonate polyol having two functional groups, a molecular weight of 2,000 to 3,000, and an active hydroxyl group at the end.
  • the number of functional groups is 2, it becomes easier to obtain a linear polymer.
  • the composition tends to be uncured.
  • the number of functional groups is larger than 2, a network-like crosslinked structure is created in the polymer structure, which is not preferable because the tensile elongation rate of the coating film decreases.
  • the number of functional groups is less than 2, it is not preferable because the liquid viscosity of the (E) prepolymer solution increases or the prepolymer solution gels.
  • the molecular weight is less than 2,000, the tensile elongation at break will be small and the displacement followability will be poor. If the molecular weight is greater than 3,000, the liquid viscosity becomes high, and the liquid viscosity of the prepolymer solution (E) becomes high, which is not preferable.
  • the polyol component (A) known carbonate polyols that are liquid at room temperature are preferred from the viewpoint of achieving the desired properties of the coating film, long-term stability, and adjusting the liquid viscosity, molecular weight, and number of functional groups. That is, the liquid carbonate polyol can maintain the resin of the coating film in an amorphous state, that is, as a transparent coating film, because of its structure of repeating alkyl carbonate bonds having branches such as methyl groups.
  • a carbonate-bonded coating film has excellent weather resistance, thermal history and heat shock resistance, and is therefore preferable for a coating film with a linear structure that is soft and stretches well, such as this coating film.
  • the liquid carbonate polyol can be obtained, for example, by a known method by polycondensation reaction of diphenyl carbonate and 3-methyl-1,5-pentanediol in the presence of a transesterification catalyst.
  • a transesterification catalyst for example, Clapol C3090 (manufactured by Kuraray Co., Ltd.) may be used.
  • known carbonate polyols, ⁇ -caprolactone polyols, polytetramethylene polyoxyglycol, ⁇ -methyl- ⁇ -valerolactone polyols, etc. may be used, or two of these polyols may be used. The above may be used in combination.
  • the polyisocyanate component is an alicyclic polyisocyanate having two functional groups and an isocyanate group at the terminal. Since the number of functional groups is 2, it becomes easier to obtain a coating film of a linear polymer. When the number of functional groups is less than 2, the composition tends to be uncured. If the number of functional groups is greater than 2, it is not preferable because a network-like crosslinked structure is created in the polymer structure, resulting in a decrease in the tensile elongation rate of the coating film. Further, (E) is not preferable because the liquid viscosity of the prepolymer solution increases and the prepolymer solution gels.
  • polyisocyanate component a general alicyclic compound can be used.
  • methylene bis(4,1-cyclohexylene) diisocyanate or the like may be used as the polyisocyanate component, or two or more of these may be used in combination.
  • known hexamethylene diisocyanate (HDI) or its derivatives, xylidene diisocyanate, norbornene diisocyanate, etc. may be used, or two or more of these may be used in combination.
  • the catalyst causes a urethanization reaction between the isocyanate component (B) and a less than stoichiometric amount of the polyol component (A) to obtain a prepolymer having an active isocyanate group at the end and is composed of a polyurethane resin.
  • a predetermined urethanization catalyst can be used.
  • this urethanization catalyst known catalysts such as tertiary amine compounds and organometallic compounds can be used.
  • urethanation catalysts include triethylenediamine, N,N-dimethylhexamethylenediamine, N,N-dimethylbutanediamine, diazabicyclo(5,4,0)-7-undecene (DBU) and DBU salt, bismuth Preferred are tris(2-ethylhexanoate), diisopropoxybis(ethyl acetoacetate)titanium, lead octylate, dibutyltin laurate, and the like.
  • DBU diazabicyclo(5,4,0)-7-undecene
  • bismuth Preferred are tris(2-ethylhexanoate), diisopropoxybis(ethyl acetoacetate)titanium, lead octylate, dibutyltin laurate, and the like.
  • Solvents include ester solvents, ketone solvents, aromatic hydrocarbon solvents, halogenated hydrocarbon solvents, and polyhydric alcohol derivatives, preferably ester solvents, ketone solvents, and polyhydric alcohol derivatives. Derivatives of alcohols are preferred because of their low toxicity.
  • ester solvents include ethyl acetate, butyl acetate, etc.
  • ketone solvents include acetone, methyl ethyl ketone, etc.
  • polyhydric alcohol derivatives include propylene glycol monomethyl ether acetate.
  • the reaction ratio between the isocyanate component (B) and the polyol component (A), which is 1/2 of the theoretical amount, is The equivalent ratio of the isocyanate groups (NCO) of the prepolymer to the hydroxyl groups (OH) of the polyol, that is, the NCO/OH ratio, is 1.95 to 2.5, more preferably 2.0 to 2.1. If this equivalent ratio exceeds 2.5, a large amount of unreacted active isocyanate remains in the coating material (E), which is undesirable because dryness to the touch after coating becomes slow.
  • this equivalent ratio is less than 1.95, the viscosity of (E) the paint becomes high, and the workability of (E) the manufacturing and coating operations of the paint may deteriorate.
  • this equivalent ratio is 2.0 to 2.1, all of the (B) isocyanate components react and become a prepolymer, and there is no unreacted (B) isocyanate component in the paint, so the (E) paint Ingredient safety is increased.
  • the prepolymer solution coating composed of polyurethane resin and having an active isocyanate group at the end can be used alone, but the following components can be added.
  • pigments can be added.
  • the amount of this pigment is preferably less than 5 parts by weight, preferably less than 1 part by weight, per 100 parts by weight of the total amount of the isocyanate component (B) and the polyol component (A) as main components.
  • the hardness of the resulting coating film decreases as the amount added increases.
  • the pigment there is no particular limitation as long as it is a pigment for urethane resin, but a paste in which the pigment is kneaded using a polyol as a vehicle is preferred for use.
  • each color of the paste coloring agent FTR manufactured by Dainichiseika Chemical Co., Ltd.
  • one type of stabilizer such as a heat stabilizer, antioxidant, ultraviolet absorber, ultraviolet stabilizer, filler, etc.
  • a heat stabilizer such as a heat stabilizer, antioxidant, ultraviolet absorber, ultraviolet stabilizer, filler, etc.
  • two or more kinds can be mixed and used.
  • pigments, dyes, flame retardants, antifoaming agents, dispersants, surface modifiers, water adsorbents, etc. can also be added as appropriate.
  • a solvent is put into a reaction tank equipped with a mixing device, then (A) polyol component used as a raw material is added and mixed and dispersed in the solvent, (B) polyisocyanate component is added and mixed and dispersed, and then ( C) After adding the catalyst and mixing and dispersing it, stirring is continued under a nitrogen atmosphere, and the urethanization reaction is carried out for a predetermined time at room temperature or in a heated state, respectively. (E) Active isocyanate is added to the terminals composed of polyurethane resin A coating of prepolymer solution with groups is obtained.
  • mixing additives they may be mixed with the polyol component in advance, or may be added at the time of mixing the main components.
  • a one-component moisture-curable non-yellowing soft paint is obtained. This can be achieved by diluting the obtained paint with a solvent or the like and adjusting the resin concentration in the paint depending on the purpose of finishing the paint film to be "glossy” or “non-glossy.”
  • the above-obtained paint (E) is quick-drying and can be dry to the touch in about 30 seconds.
  • it can be applied to a polypropylene plate (PP plate), and after reacting with water vapor, the coating film can be peeled off from the PP plate and taken out.
  • PP plate polypropylene plate
  • Example 1 350 g of dehydrated ethyl acetate was added to a four-necked separable flask equipped with a stirring blade, a reflux device, and a heating device in a nitrogen gas atmosphere, and then methylene bis(4,1- 17.86 g (0.139 equivalents) of cyclohexylene diisocyanate were added, and then 100 g (0.067 g. Then, 0.1 g of dibutyl-tin-laurate as a reaction catalyst was charged into the reaction tank, and the reaction was carried out for 4 hours while the temperature of the reaction solution was maintained at 40° C. or lower. Then, the mixture was refluxed at 80° C. for 4 hours.
  • Example-1 After the reaction was completed, when the reaction solution was returned to room temperature, 0.9 g of dibutyl-tin-laurate was added and mixed with stirring to obtain a prepolymer solution coating composed of polyurethane resin and having active isocyanate groups at the terminals. Ta.
  • the obtained coating material was a liquid having a viscosity of 0.3 Pa ⁇ s at 25°C. This is indicated by the symbol “Example-1”.
  • the obtained paint (E) of "Example-1” was applied to a PP board, and the solvent quickly evaporated and the paint film was dry to the touch after 30 seconds. Furthermore, by leaving it at room temperature for 2 hours, a reaction with water vapor is caused, after which the paint becomes a soft, tough, transparent coating.
  • This coating film was left at room temperature for 3 days and then peeled off from the PP board to obtain a soft, tough and transparent film.
  • the coating film has a soft tensile stress of 1.1 MPa at 100% elongation (for example, natural rubber 0.5 MPa), a tensile strength of 18.7 MPa (for example, natural rubber 5 MPa), and a tensile elongation rate of 1,300% (for example, natural rubber 5 MPa). 600% rubber) and strong.
  • this coating film was exposed for 10 days in a constant temperature bath at 100° C., no change was observed in the appearance of the coating film and it exhibited excellent durability (natural rubber melted due to decomposition within one
  • Example 2 A coating material of a prepolymer solution was obtained in the same manner as in Example 1 except that 15.26 g (0.139 equivalents) of isophorone diisocyanate was added.
  • the obtained coating material was a liquid having a viscosity of 0.2 Pa ⁇ s at 25°C.
  • the coating film has a soft tensile stress of 1.0 MPa at 100% elongation, and is strong with a tensile strength of 17.6 MPa and a tensile elongation rate of 1,200%. When this coating film was exposed for 10 days in a constant temperature bath at 100° C., no change was observed in the appearance of the coating film, and it showed excellent durability. (Natural rubber melts due to decomposition within one day).
  • Example 3 100 g of the obtained (E) paint of "Example-1" (resin concentration (NV) 25%) and 150 g of ethyl acetate solvent were added and mixed to obtain a diluted paint (NV 10%).
  • NV 10% resin concentration
  • Ta. Dried flowers were dipped in this diluted solution and air-dried for 30 seconds to dry to the touch to obtain shiny coated dried flowers.
  • This dried flower was confirmed to be flexible.
  • this dried flower had a glossy (glossy) appearance compared to before coating.
  • the growth of mold was suppressed in this dried flower compared to when it was not coated.
  • Example 4 300 g of ethyl acetate solvent was added to 100 g (resin concentration 25%) of the obtained paint (E) of "Example-1" and mixed to obtain a diluted paint (NV 5%). Dried flowers were dipped in this diluted solution and air-dried for 30 seconds to dry to the touch to obtain matte coated dried flowers. This dried flower was confirmed to be flexible. Additionally, this dried flower had an appearance with no significant change in gloss compared to before coating. In addition, the growth of mold was suppressed in this dried flower compared to when it was not coated.
  • Example 5 0.5 g of pigment (FTR Red; manufactured by Dainichiseika Kaisha, Ltd.) and 300 g of ethyl acetate solvent were added to 100 g (NV 25%) of the obtained (E) paint of "Example-1" and mixed. A red colored diluted paint (NV5%) was obtained. Dried rose flowers were dipped in this diluted solution and air-dried for 30 seconds to dry to the touch to obtain a matte coated dried flower colored red. This dried flower was confirmed to be flexible. Furthermore, compared to before coating, this dried flower had a reddish appearance with no significant change in glossiness. In addition, the growth of mold was suppressed in this dried flower compared to when it was not coated.
  • FTR Red manufactured by Dainichiseika Kaisha, Ltd.
  • liquid viscosity is the numerical value measured using a BH type liquid viscometer, and the coating limit is set to 8/Pa ⁇ s or less, and a viscosity higher than that is considered difficult to coat. .
  • elongation tensile stress "tensile strength”, and "tensile elongation rate” are determined by performing a tensile test using a dumbbell-shaped No. 3 test piece according to JIS K6301, and calculating the stress at 100% elongation. (unit: MPa), stress at break (unit: MPa), and elongation at break (unit: %).
  • the one-component, moisture-curable, non-yellowing soft paint of the present invention dries quickly to the touch in 30 seconds after application, and has excellent workability.It reacts with water vapor to create a soft, tough coating with excellent displacement followability. A transparent coating can be provided.
  • a soft composition deforms under load and easily breaks due to stress concentration, but it would be extremely advantageous if it were covered with a strong coating that is soft and has excellent displacement followability.
  • a strong coating that is soft and has excellent displacement followability.
  • the resin film 30 is formed on the entire surface of the plant body 20, but the present invention is not limited to this.
  • the resin film 30 may be formed on a part of the surface of the plant body 20, such as only on the petal portion of the plant body 20.
  • the plant body 20 is an example of a plant.
  • the dipping treatment, the temporary drying treatment, and the main drying treatment are examples of film forming steps.
  • the nonwoven fabric 7 is an example of an absorbent material.

Abstract

An ornamental plant production method according to the present invention comprises a drying step for drying a plant and a film formation step for forming a film of a resin composition on the surface of the dried plant. The resin composition is a coating material consisting of a prepolymer solution that is composed of a (E) polyurethane resin and has active isocyanate terminal groups, said (E) polyurethane resin being obtained by reacting a (A) polyol component and a (B) polyisocyanate component in a (D) solvent in the presence of a (C) catalyst. The (A) polyol component is a liquid carbonate polyol having two functional groups and a number average molecular weight of 2,000-3,000, and has active hydroxyl terminal groups. The (B) polyisocyanate component is an alicyclic polyisocyanate having two functional groups, and has isocyanate terminal groups. The hydroxyl equivalent (OH) of the (A) polyol component is less than the isocyanate equivalent (NCO) of the (B) polyisocyanate component. In the film formation step, a film of the (E) coating material is formed on the surface of the dried plant, and reacts with water vapor in the air to form urea bonds.

Description

観賞用植物の製造方法および観賞用植物Ornamental plant manufacturing method and ornamental plants
本発明は、観賞用植物の製造方法および観賞用植物に関する。 The present invention relates to a method for producing an ornamental plant and an ornamental plant.
特許文献1には、容器に植物を入れる工程と、容器に、シリカゲル、シラス、釉薬を球状のセラミックに塗布して焼成されたセラミック体及び油分を含む乾燥剤を入れる工程と、容器の全体を27~32℃にて乾燥させる工程と、を含む観賞用乾燥植物の製造方法が開示されている。 Patent Document 1 describes a step of putting a plant into a container, a step of putting into the container a ceramic body obtained by applying silica gel, shirasu, and glaze to a spherical ceramic and a desiccant containing oil, and a step of putting the entire container into the container. A method for producing a dried ornamental plant is disclosed, which includes the step of drying at 27 to 32°C.
特許第5564142号公報Patent No. 5564142
ところで、例えば花や葉などの観賞用植物の観賞可能な期間を延ばすため、観賞用植物に乾燥処理を施し所謂ドライフラワーとすることがある。しかしながら、乾燥させた観賞用植物は、乾燥にともない柔軟性が低下し、例えば外部から圧力を受けると破損しやすくなることがあった。  By the way, in order to extend the period during which ornamental plants such as flowers and leaves can be admired, the ornamental plants are sometimes subjected to a drying treatment to produce so-called dried flowers. However, as dried ornamental plants dry, their flexibility decreases, and for example, they tend to break when subjected to external pressure. 
そこで、本発明では、乾燥させた観賞用植物の破損を抑制することを目的とする。 Therefore, the present invention aims to suppress damage to dried ornamental plants.
かかる目的のもと、本明細書に開示される技術は、植物を乾燥させる乾燥工程と、前記乾燥させた植物の表面に樹脂組成物の膜を形成する膜形成工程と、を有し、前記樹脂組成物は、(A)ポリオール成分が、官能基数2であって、数平均分子量2,000~3,000の液状カーボネート系ポリオールであり、かつ末端に活性ヒドロキシ基を有し、(B)ポリイソシアネート成分が、官能基数2である脂環式ポリイソシアネートであり、かつ末端にイソシアネート基を有し、前記(A)のポリオール成分のヒドロキシル当量(OH)は、前記(B)のポリイソシアネート成分のイソシアネート当量(NCO)よりも小さく、前記(A)のポリオール成分と前記(B)のポリイソシアネート成分とを、(C)触媒の存在下で(D)溶剤中にて反応させた(E)ポリウレタン樹脂から構成された末端に活性イソシアネート基を有するプレポリマー溶液の塗料であり、前記膜形成工程においては、前記乾燥させた植物の表面に前記(E)の塗料の膜を形成し、空気中の水蒸気と反応させてウレア結合を形成する観賞用植物の製造方法である。  For this purpose, the technology disclosed herein includes a drying step of drying a plant, and a film forming step of forming a film of a resin composition on the surface of the dried plant. In the resin composition, (A) the polyol component is a liquid carbonate polyol having a functional group number of 2 and a number average molecular weight of 2,000 to 3,000, and has an active hydroxy group at the terminal, and (B) The polyisocyanate component is an alicyclic polyisocyanate having two functional groups and has an isocyanate group at the terminal, and the hydroxyl equivalent (OH) of the polyol component (A) is equal to that of the polyisocyanate component (B). The polyol component of (A) and the polyisocyanate component of (B) are reacted in the presence of (C) a catalyst (D) in a solvent (E) This is a prepolymer solution paint composed of polyurethane resin and having active isocyanate groups at the end. In the film forming step, a film of the paint (E) is formed on the surface of the dried plant, and the paint is exposed to air. This is a method for producing ornamental plants in which a urea bond is formed by reacting with water vapor. 
ここで、前記(A)のポリオール成分のヒドロキシル当量(OH)と前記(B)のポリイソシアネート成分のイソシアネート当量(NCO)との当量比率(NCO/OH)は1.95~2.5であるとよい。 また、前記脂環式ポリイソシアネートは、メチレンビス(4,1-シクロヘキシレン)ジイソシアネートまたはイソホロンジイソシアネートであるとよい。 また、前記樹脂組成物の膜は、100%伸び引張応力が1.0~1.1MPaであり、引張破断伸びが1,000%以上であり、引張破断強さが17.6~18.7MPaであるとよい。 また、前記(E)の塗料は、前記乾燥させた植物に前記塗料の膜を形成してから30秒以内に指触乾燥を来すとよい。 また、前記(D)の溶剤は、酢酸エチル溶剤であり、前記指触乾燥の工程に用いる塗料の樹脂分濃度が5~10%であるとよい。 また、前記指触乾燥の工程は前記乾燥させた植物を前記(E)の塗料を吸収する吸収体に配置して行い、前記指触乾燥の工程の後に前記乾燥させた植物を吊るし前記塗料の膜をさらに乾燥させるとよい。 また、前記植物は、花托を備え、前記乾燥工程において、冷凍された前記植物を真空乾燥させるとよい。 また、前記植物は、収穫されてから平面状に押し付けられることなく、前記乾燥工程において乾燥されるとよい。  Here, the equivalent ratio (NCO/OH) between the hydroxyl equivalent (OH) of the polyol component (A) and the isocyanate equivalent (NCO) of the polyisocyanate component (B) is 1.95 to 2.5. Good. Furthermore, the alicyclic polyisocyanate is preferably methylene bis(4,1-cyclohexylene) diisocyanate or isophorone diisocyanate. Further, the film of the resin composition has a tensile stress at 100% elongation of 1.0 to 1.1 MPa, a tensile elongation at break of 1,000% or more, and a tensile strength at break of 17.6 to 18.7 MPa. It would be good if it were. Furthermore, it is preferable that the paint (E) be dry to the touch within 30 seconds after forming a film of the paint on the dried plant. Further, the solvent (D) is preferably an ethyl acetate solvent, and the resin concentration of the paint used in the touch drying step is preferably 5 to 10%. Further, the step of drying to the touch is performed by placing the dried plants on an absorbent body that absorbs the paint of (E), and after the step of drying to the touch, the dried plants are hung to absorb the paint. It is advisable to further dry the membrane. It is also preferable that the plant is provided with a flower receptacle, and that the frozen plant is vacuum-dried in the drying step. Furthermore, it is preferable that the plant is dried in the drying step without being pressed into a flat shape after being harvested. 
他の観点から捉えると、本明細書に開示される技術は、花托を備える植物を冷凍し真空乾燥させる乾燥工程と、前記乾燥させた植物の表面に樹脂組成物の膜を形成する膜形成工程と、を有し、前記樹脂組成物は、(A)ポリオール成分が、官能基数2、分子量2,000~3,000の末端に活性ヒドロキシ基を有する液状カーボネート系ポリオールであり、(B)ポリイソシアネート成分が、官能基数2の末端にイソシアネート基を有するメチレンビス(4,1-シクロヘキシレン)ジイソシアネートまたはイソホロンジイソシアネートであり、前記(A)のポリオール成分のヒドロキシル当量(OH)と前記(B)のポリイソシアネート成分のイソシアネート当量(NCO)との当量比率(NCO/OH)は1.95~2.5であり、前記(A)のポリオール成分と前記(B)のポリイソシアネート成分とを、(C)触媒の存在下で(D)酢酸エチル溶剤中にて反応させた(E)ポリウレタン樹脂から構成された末端に活性イソシアネート基を有するプレポリマー溶液の塗料であり、前記膜形成工程においては、前記乾燥させた植物の表面に前記(E)の塗料の膜を形成し、空気中の水蒸気と反応させてウレア結合を形成し、前記(E)の塗料は、前記乾燥させた植物に前記膜を形成してから30秒以内に指触乾燥を来し、前記樹脂組成物の膜は、100%伸び引張応力が1.0~1.1MPaであり、引張破断伸びが1,000%以上であり、引張破断強さが17.6~18.7MPaである観賞用植物の製造方法である。  From another perspective, the technology disclosed in this specification includes a drying step of freezing and vacuum drying a plant provided with flower receptacles, and a film forming step of forming a film of a resin composition on the surface of the dried plant. and, in the resin composition, (A) the polyol component is a liquid carbonate polyol having a functional group number of 2, a molecular weight of 2,000 to 3,000, and an active hydroxyl group at the end, and (B) a polyol component. The isocyanate component is methylene bis(4,1-cyclohexylene) diisocyanate or isophorone diisocyanate having two functional groups and an isocyanate group at the terminal, and the hydroxyl equivalent (OH) of the polyol component (A) and the polyol component (B) are The equivalent ratio (NCO/OH) of the isocyanate component to the isocyanate equivalent (NCO) is 1.95 to 2.5, and the polyol component of (A) and the polyisocyanate component of (B) are combined into (C) It is a coating of a prepolymer solution having an active isocyanate group at the end, which is composed of (E) a polyurethane resin reacted in (D) an ethyl acetate solvent in the presence of a catalyst, and in the film forming step, the drying A film of the paint of (E) is formed on the surface of the dried plant, and is reacted with water vapor in the air to form a urea bond, and the paint of (E) forms the film on the dried plant. The film of the resin composition is dry to the touch within 30 seconds after being applied, and the film of the resin composition has a 100% elongation tensile stress of 1.0 to 1.1 MPa, and a tensile elongation at break of 1,000% or more. This is a method for producing an ornamental plant having a tensile strength at break of 17.6 to 18.7 MPa. 
さらに他の観点から捉えると、本明細書に開示される技術は、上記製造方法によって形成されてなる、観賞用植物である。  Viewed from another perspective, the technology disclosed herein is an ornamental plant produced by the above production method. 
さらに他の観点から捉えると、本明細書に開示される技術は、乾燥した植物と、前記植物の表面に形成された樹脂組成物の膜とを有し、前記樹脂組成物の膜は、100%伸び引張応力が1.0~1.1MPaであり、引張破断伸びが1,000%以上であり、引張破断強さが17.6~18.7MPaである観賞用植物である。 Viewed from yet another perspective, the technology disclosed herein includes a dried plant and a film of a resin composition formed on the surface of the plant, and the film of the resin composition has a It is an ornamental plant having a % elongation tensile stress of 1.0 to 1.1 MPa, a tensile elongation at break of 1,000% or more, and a tensile strength at break of 17.6 to 18.7 MPa.
本発明によれば、乾燥させた観賞用植物の破損を抑制することができる。 According to the present invention, damage to dried ornamental plants can be suppressed.
本実施の形態が適用されるドライフラワーの概略構成図である。FIG. 1 is a schematic configuration diagram of a dried flower to which this embodiment is applied. ドライフラワーの製造工程を示す図である。It is a figure showing the manufacturing process of dried flowers. (A)はドライフラワーの製造工程を示すフロチャートであり、(B)はドライフラワーの他の製造工程を示すフロチャートである。(A) is a flowchart showing a manufacturing process of dried flowers, and (B) is a flowchart showing another manufacturing process of dried flowers.
以下、添付図面を参照して、本発明の実施の形態について説明する。<ドライフラワー10> 図1は、本実施の形態が適用されるドライフラワー10の概略構成図である。 図1(A)および(B)に示すように、ドライフラワー10は、植物本体20と、植物本体20の表面に形成された保護層である樹脂膜30とを有する。  Embodiments of the present invention will be described below with reference to the accompanying drawings. <Dried Flower 10> FIG. 1 is a schematic configuration diagram of a dried flower 10 to which this embodiment is applied. As shown in FIGS. 1A and 1B, the dried flower 10 includes a plant body 20 and a resin film 30 that is a protective layer formed on the surface of the plant body 20. 
植物本体20は、後述する乾燥処理や樹脂形成処理が可能な植物であれば特に限定されない。例えば、植物本体20は、バラ、カーネーション、ビオラ、スナップドラゴン、ジュリアン、ペンタスデンファレ(ラン)、なでしこ(ダイアナ)、さくら草、コスモス、キャロットリーフ、バジル、チャービルなどの観賞用の植物である。植物本体20は、茎11、葉身13、花弁15、花托17、がく19を有する。  The plant body 20 is not particularly limited as long as it is a plant that can be subjected to drying treatment or resin forming treatment, which will be described later. For example, the plant body 20 is an ornamental plant such as a rose, a carnation, a viola, a snapdragon, a julienne, a pentus denfare (orchid), a dianthus (diana), a cherry blossom, a cosmos, a carrot leaf, a basil, or a chervil. The plant body 20 has a stem 11, a leaf blade 13, petals 15, a flower receptacle 17, and a calyx 19. 
なお、図示の例の植物本体20はバラである。ここで、ドライフラワーとは、乾燥処理が施された観賞用の植物をいう。例えば、植物本体20の水分率は、例えば20%以下、好ましくは10%以下、より好ましくは5%以下である。付言すると、ドライフラワーは、花弁、葉身だけでなく、茎、果実等を乾燥させたものを含む。  Note that the plant body 20 in the illustrated example is a rose. Here, dried flowers refer to ornamental plants that have been subjected to drying treatment. For example, the moisture content of the plant body 20 is, for example, 20% or less, preferably 10% or less, and more preferably 5% or less. Additionally, dried flowers include not only petals and leaf blades, but also dried stems, fruits, and the like. 
また、植物本体20は、立体的な形状を有している。言い替えると、植物本体20は、所謂押し花ではない。ここで、押し花とは、収穫された花や葉を平面状に押し付けて乾燥させたものである。付言すると、植物本体20は、収穫された状態から平面状に押し付けられることなく製造される。  Moreover, the plant body 20 has a three-dimensional shape. In other words, the plant body 20 is not a so-called pressed flower. Here, pressed flowers are harvested flowers and leaves that are pressed into a flat shape and dried. In addition, the plant body 20 is manufactured without being pressed into a flat shape from the harvested state. 
ここで、植物本体20のようなドライフラワーは、乾燥処理が施されているため、外圧を受けると破損しやすい。そこで、従来、樹脂等をドライフラワーの表面に塗布することでドライフラワーが補強されることがあった。しかしながら、この樹脂の塗布にともない、所謂テカリやツヤと呼ばれる光沢が出ると、ドライフラワーの外観が、樹脂の塗布前の自然な風合いと異なるものとなる。さらに説明をすると、例えば花弁のように厚みが薄い部分において、樹脂が全体に厚く形成されると、光沢が発生して自然な仕上がりと異なる外観となることがある。  Here, since dried flowers such as the plant body 20 have been subjected to a drying process, they are easily damaged when subjected to external pressure. Therefore, in the past, dried flowers were sometimes reinforced by applying resin or the like to the surface of the dried flowers. However, when the resin is applied, a so-called shine or luster occurs, and the appearance of the dried flowers becomes different from the natural texture before the resin is applied. To explain further, if the entire resin is formed thickly in a thin part such as a flower petal, gloss may occur and the appearance may differ from the natural finish. 
また、例えばいわゆるフリーズドライと呼ばれる冷凍真空乾燥処理によって、柔軟性を残し生花などに近い形で観賞用植物を乾燥させたとしても、剛性の高い樹脂を塗布することにより、樹脂とともに観賞用植物が崩れやすくなる(脆くなる)ことがあった。  In addition, even if ornamental plants are dried in a form similar to fresh flowers while retaining their flexibility, for example by freeze-drying (freeze-drying), the ornamental plants can be dried along with the resin by applying a highly rigid resin. There were times when it became easy to crumble (become brittle). 
本実施の形態においては、後述の樹脂液を用いることで樹脂膜30の膜厚が抑制され得る。このことにより、樹脂膜30を植物本体20の表面に形成した状態であっても、光沢が抑制され、外観上自然な仕上がりの観賞用植物が形成され得る。  In this embodiment, the thickness of the resin film 30 can be suppressed by using a resin liquid to be described later. As a result, even when the resin film 30 is formed on the surface of the plant body 20, gloss is suppressed, and an ornamental plant with a natural-looking finish can be formed. 
また、図示の樹脂膜30は、柔軟性がある。したがって、樹脂膜30を形成した状態であっても、植物本体20の変形を許容することができ、ドライフラワー10の形状の崩れや、ひび割れを抑制することが可能である。言い替えると、本実施の形態においては、ドライフラワー10の耐久性が向上し、ドライフラワー10を長持ちさせ得る。  Further, the illustrated resin film 30 is flexible. Therefore, even with the resin film 30 formed, deformation of the plant body 20 can be allowed, and it is possible to suppress deformation and cracking of the dried flower 10. In other words, in this embodiment, the durability of the dried flowers 10 is improved, and the dried flowers 10 can be made to last for a long time. 
また、樹脂膜30が形成されることにより、例えば、湿度が高い環境にドライフラワー10を飾る場合においても、ドライフラワー10を長持ちさせ得る。また、樹脂膜30が紫外線等の光を反射させることにより、鮮やかな色を長期間保つことが可能となる。  Further, by forming the resin film 30, the dried flowers 10 can be made to last for a long time even when the dried flowers 10 are displayed in a humid environment, for example. Further, since the resin film 30 reflects light such as ultraviolet rays, it becomes possible to maintain bright colors for a long period of time. 
また、本実施の形態においては、植物本体20の表面に樹脂膜30を形成することで、ドライフラワー10の一部、すなわち花弁や葉身が落下することが抑制され得る。  Furthermore, in this embodiment, by forming the resin film 30 on the surface of the plant body 20, it is possible to suppress a portion of the dried flower 10, that is, a petal or a leaf blade, from falling. 
また、本実施の形態においては、変形可能な樹脂膜30を植物本体20の表面に形成し得る。このことにより、外部からの力が加わった場合においても、ドライフラワー10が崩れることは回避され得る。  Further, in this embodiment, the deformable resin film 30 can be formed on the surface of the plant body 20. This can prevent the dried flowers 10 from collapsing even when external force is applied. 
また、本実施の形態においては、樹脂膜30は、植物本体20の凹凸に対応する形で植物本体20の表面に形成されている。言い替えると、樹脂膜30は、植物本体20の表面を滑らかにする形で形成されている。さらに説明をすると、図1(B)に示すように、樹脂膜30は、植物本体20の凹部18に形成され膜厚が厚い膜厚部31と、植物本体20の凸部16に形成され膜厚が薄い膜薄部33とを有する。樹脂膜30の膜厚が異なることにより、樹脂膜30による光沢の発生が抑制され得る。  Further, in this embodiment, the resin film 30 is formed on the surface of the plant body 20 in a shape corresponding to the irregularities of the plant body 20. In other words, the resin film 30 is formed to smooth the surface of the plant body 20. To explain further, as shown in FIG. 1(B), the resin film 30 is formed in a thick film part 31 formed in the concave part 18 of the plant body 20 and a thick film part 31 formed in the convex part 16 of the plant body 20. It has a thin film portion 33 with a small thickness. By having different thicknesses of the resin film 30, generation of gloss due to the resin film 30 can be suppressed. 
<ドライフラワー10の製造工程> 図2は、ドライフラワー10の製造工程を示す図である。 次に、図2を参照しながら、ドライフラワー10の製造工程について説明をする。 図2(A)乃至(D)に示すように、この製造工程においては、乾燥処理、浸漬処理、仮乾燥処理および本乾燥処理が施される。ここで、浸漬処理、仮乾燥処理および本乾燥処理は、植物本体20の表面に樹脂膜30を形成する樹脂形成処理である。  <Manufacturing process of dried flower 10> FIG. 2 is a diagram showing a manufacturing process of dried flower 10. Next, the manufacturing process of the dried flower 10 will be explained with reference to FIG. 2. As shown in FIGS. 2(A) to 2(D), in this manufacturing process, drying treatment, dipping treatment, temporary drying treatment, and main drying treatment are performed. Here, the dipping treatment, temporary drying treatment, and main drying treatment are resin forming treatments that form the resin film 30 on the surface of the plant body 20. 
まず、図2(A)に示すように、植物本体20の乾燥処理が行われる。図示の乾燥処理においては、乾燥用容器3内に植物本体20と乾燥剤4とを配置し、植物本体20を乾燥させる。さらに説明をすると、例えば乾燥用容器3の底部に所定量の乾燥剤4を配置する。そして、乾燥剤4の上に植物本体20を静置し、乾燥用容器3内にさらに乾燥剤4を加える。このことにより、植物本体20の外周が乾燥剤4に覆われた状態となる。この状態において、所定期間(例えば3日~1週間)かけて植物本体20を乾燥させる。なお、乾燥用容器3を乾燥機の中に配置して植物本体20の乾燥を制御してもよい。本実施形態において利用できる乾燥剤4の種類に特に限定はないが、例えば、シリカゲル、塩化カルシウム、塩化マグネシウムなどが挙げらる。  First, as shown in FIG. 2(A), the plant body 20 is dried. In the illustrated drying process, the plant body 20 and the desiccant 4 are placed in the drying container 3, and the plant body 20 is dried. To explain further, a predetermined amount of desiccant 4 is placed at the bottom of the drying container 3, for example. Then, the plant body 20 is placed on the desiccant 4, and the desiccant 4 is further added into the drying container 3. As a result, the outer periphery of the plant body 20 is covered with the desiccant 4. In this state, the plant body 20 is dried over a predetermined period (for example, 3 days to 1 week). Note that the drying container 3 may be placed in a dryer to control the drying of the plant body 20. There is no particular limitation on the type of desiccant 4 that can be used in this embodiment, but examples include silica gel, calcium chloride, and magnesium chloride. 
次に、図2(B)に示すように、乾燥処理が施された植物本体20の表面に樹脂膜30を形成する。さらに説明をすると、樹脂容器5に収容された樹脂液6(後述)に乾燥処理が施された植物本体20を浸漬する。樹脂液6に植物本体20を浸漬する時間は、植物本体20の表面全体に樹脂液
6が付着することを許容する長さであればよい。浸漬する時間は、例えば1秒~60秒である。 
Next, as shown in FIG. 2(B), a resin film 30 is formed on the surface of the dried plant body 20. To explain further, the dried plant body 20 is immersed in a resin liquid 6 (described later) contained in a resin container 5. The time for immersing the plant body 20 in the resin liquid 6 may be any length that allows the resin liquid 6 to adhere to the entire surface of the plant body 20. The immersion time is, for example, 1 second to 60 seconds.
次に、図2(C)に示すように、植物本体20に付着した樹脂液6を仮乾燥させる。さらに説明をすると、表面全体に樹脂液6が付着した植物本体20を、吸収体である不織布7上に配置する。仮乾燥する時間は、植物本体20に付着した樹脂液6が指触乾燥するのに十分な長さであればよい。仮乾燥する時間は、例えば3秒~3時間である。なお、指触乾燥とは、植物本体20に付着した樹脂液6(樹脂膜30)の表面を指先で触れて、樹脂液6が指先につかなくなる状態とすることを言う。また、不織布7上で仮乾燥をさせることにより、植物本体20に過剰な樹脂膜30が形成されることが抑制される。さらに説明をすると、例えば植物本体20の下側に樹脂液6の液だまりができて、植物本体20に過剰な樹脂膜30が形成されることなどが抑制される。  Next, as shown in FIG. 2(C), the resin liquid 6 adhering to the plant body 20 is temporarily dried. To explain further, the plant body 20 with the resin liquid 6 adhered to its entire surface is placed on a nonwoven fabric 7 that is an absorbent body. The temporary drying time may be long enough for the resin liquid 6 attached to the plant body 20 to be dry to the touch. The temporary drying time is, for example, 3 seconds to 3 hours. Note that drying to the touch refers to touching the surface of the resin liquid 6 (resin film 30) adhering to the plant body 20 with a fingertip so that the resin liquid 6 does not stick to the fingertip. Further, by temporarily drying on the nonwoven fabric 7, formation of an excessive resin film 30 on the plant body 20 is suppressed. To explain further, for example, formation of a pool of the resin liquid 6 on the lower side of the plant body 20 and formation of an excessive resin film 30 on the plant body 20 is suppressed. 
次に、図2(D)に示すように、植物本体20に付着した樹脂液6を本乾燥させる。さらに説明をすると、表面全体に樹脂液6が付着した植物本体20を、吊下具9によって吊り下げる。本乾燥する時間は、植物本体20に付着した樹脂液6が本乾燥するのに十分な長さであればよい。本乾燥する時間は、例えば2時間~5日である。なお、本乾燥とは、樹脂液6(樹脂膜30)の表面を指先で押さえて指紋がつかなくなる状態とすることを言う。言い替えると、本乾燥とは、指触乾燥よりも樹脂膜30の樹脂が安定した状態にするための処理である。  Next, as shown in FIG. 2(D), the resin liquid 6 adhering to the plant body 20 is dried. To explain further, the plant body 20 with the resin liquid 6 adhered to its entire surface is suspended by the hanging tool 9. The main drying time may be long enough for the resin liquid 6 attached to the plant body 20 to be completely dried. The main drying time is, for example, 2 hours to 5 days. Note that main drying refers to pressing the surface of the resin liquid 6 (resin film 30) with a fingertip to make it free from fingerprints. In other words, main drying is a process for bringing the resin of the resin film 30 into a more stable state than drying to the touch. 
さて、ドライフラワー10を用いた装飾などを行う場合などにおいては、樹脂膜30が安定する本乾燥処理後に行うとよい。例えば、本乾燥処理を24時間行うことにより、ドライフラワー10が損傷を受けることが抑制される。また、例えば本乾燥処理を24時間行うことにより、樹脂液6の臭いが低減され得る。  Now, when performing decorations using the dried flowers 10, etc., it is preferable to perform the main drying process to stabilize the resin film 30. For example, by performing the main drying process for 24 hours, damage to the dried flowers 10 is suppressed. Further, for example, by performing the main drying treatment for 24 hours, the odor of the resin liquid 6 can be reduced. 
また、図2(D)に示すように、本乾燥処理において吊下具9により植物本体20を吊り下げる姿勢は、上下方向において植物本体20が生育状態と反対、すなわち花弁15が下側となるように配置する。このことにより、植物本体20に付着した過剰な樹脂膜30を植物本体20から落下させやすくなる。また、植物本体20に形成される樹脂膜30の膜厚を均一化させることが可能となる。  Furthermore, as shown in FIG. 2(D), the posture in which the plant body 20 is hung by the hanging tool 9 in the main drying process is such that the plant body 20 is in the opposite growth state in the vertical direction, that is, the petals 15 are on the lower side. Place it like this. This makes it easier for the excess resin film 30 adhering to the plant body 20 to fall from the plant body 20. Moreover, it becomes possible to make the thickness of the resin film 30 formed on the plant body 20 uniform. 
本実施の形態における観賞用乾燥植物の製造工程(製造方法)では、草花等の植物本体20を乾燥させ、例えばドライフラワーのような観賞用植物を製造できる。ここで、樹脂液6を植物本体20の表面に配置する方法は、スプレーや手塗りなど、他の方法であってもよい。なお、図2(B)に示すように樹脂液6の中に植物本体20全体を浸すことによって、樹脂液6の塗り残しや、樹脂液6の膜厚のムラの発生を抑制し得る。  In the manufacturing process (manufacturing method) of a dried ornamental plant in the present embodiment, the plant body 20 such as a flower is dried, and an ornamental plant such as a dried flower can be manufactured. Here, the method of disposing the resin liquid 6 on the surface of the plant body 20 may be other methods such as spraying or hand painting. Note that by immersing the entire plant body 20 in the resin liquid 6 as shown in FIG. 2(B), it is possible to suppress the occurrence of uncoated resin liquid 6 and unevenness in the film thickness of the resin liquid 6. 
<ドライフラワー10の他の製造工程> 図3(A)はドライフラワー10の製造工程を示すフロチャートであり、図3(B)はドライフラワー10の他の製造工程を示すフロチャートである。  <Other manufacturing steps for the dried flower 10> FIG. 3(A) is a flowchart showing the manufacturing process for the dried flower 10, and FIG. 3(B) is a flowchart showing another manufacturing step for the dried flower 10. 
上記においては、乾燥処理、浸漬処理、仮乾燥処理および本乾燥処理が施されることを説明したが、これに限定されない。例えば、これらの処理のうちの一部を省略してもよい。さらに説明をすると、例えば仮乾燥処理および本乾燥処理のいずれかを省略する態様でもよい。また、乾燥処理においては、ハンギング法、ドライインウォーター法、冷凍真空乾燥、真空乾燥、熱風乾燥など周知の乾燥処理方法を用いてもよい。  Although it has been explained above that drying treatment, dipping treatment, temporary drying treatment, and main drying treatment are performed, the present invention is not limited thereto. For example, some of these processes may be omitted. To explain further, for example, an embodiment may be adopted in which either the temporary drying process or the main drying process is omitted. Moreover, in the drying process, a well-known drying process method such as a hanging method, dry-in-water method, freeze-vacuum drying, vacuum drying, or hot air drying may be used. 
以下では、図2および図3を参照しながらドライフラワー10の他の製造工程の例について説明をする。 まず、上記図2を参照しながら説明したドライフラワー10製造工程においては、図3(A)に示すように、植物本体20の乾燥処理(S301)、浸漬処理(S302)、仮乾燥処理(S303)、本乾燥処理(S304)を順に行う。  Below, an example of another manufacturing process for the dried flower 10 will be explained with reference to FIGS. 2 and 3. First, in the dried flower 10 manufacturing process explained with reference to FIG. 2 above, as shown in FIG. ) and the main drying process (S304) are performed in this order. 
一方、図3(B)に示す他の製造工程においては、以下の処理が施される。具体的には、まず植物本体20に乾燥処理が施される(S311)。この乾燥処理においては、乾燥剤4(図2(A)参照)が用いられる。そして、乾燥剤4によって乾燥された植物本体20は、冷凍装置(不図示)によって冷凍される(S312)。そして、冷凍された植物本体20は、真空乾燥装置(不図示)によって真空乾燥される(S313)。すなわち、本製造工程においては、乾燥剤4を用いた乾燥処理と冷凍真空乾燥処理との2段階で植物本体20を乾燥させる。  On the other hand, in the other manufacturing process shown in FIG. 3(B), the following processing is performed. Specifically, first, the plant body 20 is subjected to a drying process (S311). In this drying process, a desiccant 4 (see FIG. 2(A)) is used. The plant body 20 dried by the desiccant 4 is then frozen by a freezing device (not shown) (S312). Then, the frozen plant body 20 is vacuum dried by a vacuum drying device (not shown) (S313). That is, in this manufacturing process, the plant body 20 is dried in two stages: a drying process using the desiccant 4 and a freeze-vacuum drying process. 
次に、真空乾燥が施された植物本体20に浸漬処理が施される(S314)。この浸漬処理においては、樹脂液6(図2(C)参照)に植物本体20が浸漬される。そして、樹脂液6が付着した植物本体20に本乾燥処理が施される(S315)。この本乾燥処理においては、植物本体20が吊り下げられた状態(図2(D)参照)で保持される。  Next, the plant body 20 that has been vacuum dried is subjected to a dipping treatment (S314). In this immersion process, the plant body 20 is immersed in the resin liquid 6 (see FIG. 2(C)). Then, the main drying process is performed on the plant body 20 to which the resin liquid 6 has adhered (S315). In this main drying process, the plant body 20 is held in a suspended state (see FIG. 2(D)). 
ここで、冷凍処理(S312参照)においては、例えば冷凍装置の庫内を-80℃乃至-60℃の温度として、12時間乃至24時間保持する。このことにより、植物本体20が確実に凍結される。なお、冷凍装置の庫内温度(-80℃乃至-60℃)、および冷凍工程に要する期間である冷凍期間(3時間乃至24時間)は、真空乾燥工程を経た後の植物本体20の外観の良否を判定した検査結果より導かれたものである。  Here, in the freezing process (see S312), for example, the temperature inside the refrigerator is set to -80° C. to -60° C. and maintained for 12 hours to 24 hours. This ensures that the plant body 20 is frozen. Note that the internal temperature of the freezing device (-80°C to -60°C) and the freezing period (3 hours to 24 hours) required for the freezing process are based on the appearance of the plant body 20 after the vacuum drying process. This is derived from the test results that determine pass/fail. 
また、真空乾燥処理(S313参照)においては、例えば真空乾燥装置の庫内を室温として、12時間乃至3日保持することで実行される。さらに説明をすると、50Pa以下、好ましくは5Pa以下、さらに好ましくは1Pa以下において、40℃以下、好ましくは30℃以下、さらに好ましくは20℃以下の温度下で、12時間乃至3日程度保持することで実行される。このことにより、植物本体20が確実に乾燥される。植物本体20の水分率は、真空乾燥後に例えば5%以下になる。付言すると、真空乾燥工程において時間が経過するほど真空乾燥装置の庫内の気圧が減少していくが、庫内の気圧が5Pa以下となったときに、植物本体20が乾燥したものとしてもよい。なお、この真空乾燥工程に要する期間である加工期間(12時間乃至3日)は、加工された花植物本体20の外観の良否を判定した検査結果より導かれたものである。  Further, the vacuum drying process (see S313) is performed by, for example, keeping the interior of the vacuum drying device at room temperature for 12 hours to 3 days. To explain further, holding at a temperature of 40° C. or less, preferably 30° C. or less, more preferably 20° C. or less at a pressure of 50 Pa or less, preferably 5 Pa or less, more preferably 1 Pa or less for about 12 hours to 3 days. is executed. This ensures that the plant body 20 is dried. The moisture content of the plant body 20 becomes, for example, 5% or less after vacuum drying. In addition, the pressure inside the vacuum drying device decreases as time passes in the vacuum drying process, but the plant body 20 may be dried when the pressure inside the storage becomes 5 Pa or less. . The processing period (12 hours to 3 days), which is the period required for this vacuum drying process, was derived from the test results that determined the quality of the appearance of the processed flower plant body 20. 
ここで、例えば植物本体20は、花托17やがく19(図1参照)を備えることにより、花托17やがく19が花弁15を支持し、花弁15の変形が抑制される。一方で、花托17(図1参照)は、植物本体20において径が太い部分であり、他の部分と比較して、植物本体20内の水分を乾燥させることが困難な部分である。このような部分については、図3(B)に示すように、冷凍真空乾燥処理を施すことが好ましい。このことにより、植物本体20の乾燥がより確実に実行され得る。付言すると、乾燥がより確実になることで、ドライフラワー10にカビが発生することなどが抑制され得る。なお、図3(B)に示すように乾燥材4を用いた乾燥処理とともに冷凍真空乾燥処理を施してもよいし、図3(B)とは異なり乾燥材4を用いた乾燥処理を施さずに冷凍真空乾燥処理を施してもよい。  Here, for example, the plant body 20 includes the flower receptacles 17 and calyxes 19 (see FIG. 1), so that the flower receptacles 17 and calyxes 19 support the petals 15, and deformation of the petals 15 is suppressed. On the other hand, the flower receptacle 17 (see FIG. 1) is a portion with a large diameter in the plant body 20, and is a portion in which it is difficult to dry water in the plant body 20 compared to other portions. For such a portion, it is preferable to perform freeze-vacuum drying treatment as shown in FIG. 3(B). This allows the plant body 20 to be dried more reliably. Additionally, by making the drying more reliable, the occurrence of mold on the dried flowers 10 can be suppressed. Note that as shown in FIG. 3(B), freeze-vacuum drying treatment may be performed together with drying treatment using desiccant material 4, or unlike FIG. 3(B), drying treatment using desiccant material 4 is not performed. may be subjected to freeze-vacuum drying treatment. 
また、植物本体20は、冷凍真空乾燥処理にともない色や形状などの外観が変化することが抑制され、生花に近い外観および柔軟性を有している。また、この植物本体20に形成される樹脂膜30は膜厚が薄く、かつ変形可能である。このことにより、ドライフラワー10に生花同様の外観や手触りを付与することが可能となる。  Further, the plant body 20 is suppressed from changing its appearance such as color and shape due to the freeze-vacuum drying process, and has an appearance and flexibility similar to that of a fresh flower. Further, the resin film 30 formed on the plant body 20 is thin and deformable. This makes it possible to give the dried flower 10 the appearance and feel of a fresh flower. 
<樹脂膜30> 樹脂膜30は、例えば以下のような性質を持つ。樹脂膜30は、100%伸び引張応力1.0~1.1MPaの軟質である。また、樹脂膜30は、引張破断伸び1,000%以上で変位追従性に優れている。また、樹脂膜30は、引張破断強さ17.6~18.7MPaである。付言すると、樹脂膜30は、軟質コーティングあるいは塗装組成物である。  <Resin film 30> The resin film 30 has, for example, the following properties. The resin film 30 is soft and has a tensile stress of 1.0 to 1.1 MPa at 100% elongation. Furthermore, the resin film 30 has a tensile elongation at break of 1,000% or more and is excellent in displacement followability. Further, the resin film 30 has a tensile strength at break of 17.6 to 18.7 MPa. In addition, the resin film 30 is a soft coating or a coating composition. 
ここで、無黄変軟質塗料として、軟質性を付与するための特定のポリオール成分と特定のイソシアネート成分の2液を溶剤下で混合して、塗布する方法が知られている。この2液混合反応型の塗料は、塗布作業性が反応速度に依存することがあった。また、この2液混合反応型の塗料は、軟質性を付与させるために、塗膜の強靭性(引張伸びまたは引張強度)が低下することがあった。一方、本実施の形態の樹脂液6は、一液湿気硬化性の無黄変軟質塗料でありながらも、樹脂膜30は100%伸び引張応力が低い軟質であり、引張破断伸びに優れて即ち変位追従性に優れ、引張破断強さの強い強靭な塗膜を形成し得る。  Here, as a non-yellowing soft paint, a method is known in which two liquids, a specific polyol component and a specific isocyanate component for imparting flexibility, are mixed in a solvent and applied. The coating workability of this two-liquid mixed reaction type paint sometimes depends on the reaction rate. In addition, since this two-component mixed reaction type coating material imparts softness, the toughness (tensile elongation or tensile strength) of the coating film sometimes decreases. On the other hand, although the resin liquid 6 of this embodiment is a one-component moisture-curable non-yellowing soft paint, the resin film 30 is soft with low elongation and tensile stress at 100%, and has excellent tensile elongation at break. It can form a tough coating film with excellent displacement followability and high tensile strength at break. 
<樹脂液6> 上記図2(B)で説明した樹脂液6は、一液湿気硬化性の無黄変軟質塗料である。この樹脂液6は、理論量より少ない特定のポリオール成分と理論量の特定のポリイソシアネート化合物成分との反応から得られる末端に活性イソシアネート基を有するプレポリマーの溶剤溶液である。さらに説明をすると、樹脂液6は、ポリオール成分のヒドロキシル当量(OH)が、ポリイソシアネート化合物成分のイソシアネート当量(NCO)よりも小さい。この樹脂液6を塗料として被着体である植物本体20の表面に塗布して、溶剤の揮発と並行して空気中の水蒸気と反応してウレア結合を形成することで樹脂膜30が塗膜として形成される。  <Resin liquid 6> The resin liquid 6 described above in FIG. 2(B) is a one-component moisture-curable non-yellowing soft paint. This resin liquid 6 is a solvent solution of a prepolymer having active isocyanate groups at the terminals obtained from the reaction of a less than stoichiometric amount of a specific polyol component and a stoichiometric amount of a specific polyisocyanate compound component. To explain further, in the resin liquid 6, the hydroxyl equivalent (OH) of the polyol component is smaller than the isocyanate equivalent (NCO) of the polyisocyanate compound component. This resin liquid 6 is applied as a paint to the surface of the plant body 20 as an adherend, and in parallel with the volatilization of the solvent, it reacts with water vapor in the air to form urea bonds, thereby forming a resin film 30. is formed as. 
ここで、例えば樹脂液6は、(A)ポリオール成分が、官能基数2であって、数平均分子量2,000~3,000カーボネート系ポリオールであり、かつ末端に活性ヒドロキシ基を有し、(B)ポリイソシアネート成分が、官能基数2である脂環式ポリイソシアネートであり、かつ末端にイソシアネート基を有し、 上記(A)のポリオール成分のヒドロキシル当量(OH)は、上記(B)のポリイソシアネート成分のイソシアネート当量(NCO)よりも小さく、 上記(A)のポリオール成分と上記(B)のポリイソシアネート成分とを、(C)触媒の存在下で(D)溶剤中にて反応させた(E)ポリウレタン樹脂から構成された末端に活性イソシアネート基を有するプレポリマー溶液の塗料であり、(E)塗料を駆体に塗布して、約30秒で指触乾燥に至る溶剤の揮発と並行して空気中の水蒸気と反応してウレア結合を形成して約30秒で指触乾燥に至る速乾性塗料である。  Here, for example, in the resin liquid 6, the polyol component (A) is a carbonate polyol with a functional group number of 2 and a number average molecular weight of 2,000 to 3,000, and has an active hydroxyl group at the terminal, ( B) The polyisocyanate component is an alicyclic polyisocyanate having two functional groups and has an isocyanate group at the terminal, and the hydroxyl equivalent (OH) of the polyol component of (A) above is the same as the polyisocyanate component of (B) above. smaller than the isocyanate equivalent (NCO) of the isocyanate component, the polyol component of (A) above and the polyisocyanate component of (B) above are reacted in the presence of (C) a catalyst and (D) a solvent ( E) It is a prepolymer solution paint composed of a polyurethane resin and has active isocyanate groups at the end. It is a quick-drying paint that reacts with water vapor in the air to form urea bonds and is dry to the touch in about 30 seconds. 
(A)ポリオール成分は、官能基数2、分子量2,000~3,000の末端に活性ヒドロキシ基を有する液状カーボネート系ポリオールである。ここで、官能基数が2であることにより、直鎖状ポリマーを得やすくなる。官能基数が2未満の場合は、未硬化組成物になりやすい。また、官能基数が2より大きい場合は、網目状の架橋構造がポリマー構造中に作られるために塗膜の引張伸び率が低下するために好ましくない。また、官能基数が2未満の場合は、(E)プレポリマー溶液の液粘度が高くなることや、プレポリマー溶液がゲル化するため好ましくない。また、分子量が2,000未満の場合は、引張破断伸びが小さくなり変位追従性が劣るようになる。分子量が3,000より大きい場合は、液粘度が高くなり、(E)のプレポリマー溶液の液粘度が高くなるため好ましくない。  The polyol component (A) is a liquid carbonate polyol having two functional groups, a molecular weight of 2,000 to 3,000, and an active hydroxyl group at the end. Here, since the number of functional groups is 2, it becomes easier to obtain a linear polymer. When the number of functional groups is less than 2, the composition tends to be uncured. Moreover, when the number of functional groups is larger than 2, a network-like crosslinked structure is created in the polymer structure, which is not preferable because the tensile elongation rate of the coating film decreases. Moreover, when the number of functional groups is less than 2, it is not preferable because the liquid viscosity of the (E) prepolymer solution increases or the prepolymer solution gels. Furthermore, if the molecular weight is less than 2,000, the tensile elongation at break will be small and the displacement followability will be poor. If the molecular weight is greater than 3,000, the liquid viscosity becomes high, and the liquid viscosity of the prepolymer solution (E) becomes high, which is not preferable. 
(A)ポリオール成分の具体的な例示としては、塗膜の求める特性の達成と長期安定性、および液粘度、分子量と官能基数の調整等から、公知の室温で液状のカーボネート系ポリオールが好ましい。すなわち、液状のカーボネート系ポリオールは、メチル基等の枝を有するアルキルカーボネート結合によって繰り返す構造のために塗膜の樹脂を非結晶に、即ち透明塗膜に維持することができる。また、カーボネート結合の塗膜は耐候性に優れ、熱履歴やヒートショック耐久性に優れるため、当該塗膜のような直鎖構造の軟質でよく伸びる塗膜にとって好ましい。  As a specific example of the polyol component (A), known carbonate polyols that are liquid at room temperature are preferred from the viewpoint of achieving the desired properties of the coating film, long-term stability, and adjusting the liquid viscosity, molecular weight, and number of functional groups. That is, the liquid carbonate polyol can maintain the resin of the coating film in an amorphous state, that is, as a transparent coating film, because of its structure of repeating alkyl carbonate bonds having branches such as methyl groups. In addition, a carbonate-bonded coating film has excellent weather resistance, thermal history and heat shock resistance, and is therefore preferable for a coating film with a linear structure that is soft and stretches well, such as this coating film. 
液状カーボネート系ポリオールは、例えば、ジフェニルカーボネートと3-メチル-1,5-ペンタンージオールをエステル交換触媒の存在下で重縮合反応による公知の方法によって得られる。上記液状カーボネート系ポリオールとしては、例えば、クラポールC3090(クラレ社製)等を用いてもよい。また、液状カーボネ
ート系ポリオールとしては、公知のカーボネート系ポリオール、ε-カプロラクトン系ポリオール、ポリテトラメチレンポリオキシグリコール、β-メチル-δ-バレロラクトン系ポリオール等を用いてもよいし、これらの2種以上を併用してもよい。 
The liquid carbonate polyol can be obtained, for example, by a known method by polycondensation reaction of diphenyl carbonate and 3-methyl-1,5-pentanediol in the presence of a transesterification catalyst. As the liquid carbonate polyol, for example, Clapol C3090 (manufactured by Kuraray Co., Ltd.) may be used. Further, as the liquid carbonate polyol, known carbonate polyols, ε-caprolactone polyols, polytetramethylene polyoxyglycol, β-methyl-δ-valerolactone polyols, etc. may be used, or two of these polyols may be used. The above may be used in combination.
(B)ポリイソシアネート成分は、官能基数2の末端にイソシアネート基を有する脂環式ポリイソシアネートである。官能基数が2であることにより、直鎖状ポリマーの塗膜を得やすくなる。官能基数が2未満の場合は未硬化組成物になりやすい。官能基数が2より大きい場合は、網目状の架橋構造がポリマー構造中に作られるために塗膜の引張伸び率が低下するために好ましくない。また、(E)プレポリマー溶液の液粘度が高くなることや、プレポリマー溶液がゲル化するため好ましくない。  (B) The polyisocyanate component is an alicyclic polyisocyanate having two functional groups and an isocyanate group at the terminal. Since the number of functional groups is 2, it becomes easier to obtain a coating film of a linear polymer. When the number of functional groups is less than 2, the composition tends to be uncured. If the number of functional groups is greater than 2, it is not preferable because a network-like crosslinked structure is created in the polymer structure, resulting in a decrease in the tensile elongation rate of the coating film. Further, (E) is not preferable because the liquid viscosity of the prepolymer solution increases and the prepolymer solution gels. 
(B)ポリイソシアネート成分の例としては、一般的な脂環式の化合物を用いることができる。例えば、ポリイソシアネート成分して、メチレンビス(4,1-シクロヘキシレン)ジイソシアネート等を用いてもよいし、これらの2種以上を併用してもよい。また、ポリイソシアネート成分として、公知のヘキサメチレンジイソシアネート(HDI)またはその誘導体、キシリデンジイソシアネート、ノルボルネンジイソシアネート等を用いてもよいし、これらの2種以上を併用してもよい。  (B) As an example of the polyisocyanate component, a general alicyclic compound can be used. For example, methylene bis(4,1-cyclohexylene) diisocyanate or the like may be used as the polyisocyanate component, or two or more of these may be used in combination. Further, as the polyisocyanate component, known hexamethylene diisocyanate (HDI) or its derivatives, xylidene diisocyanate, norbornene diisocyanate, etc. may be used, or two or more of these may be used in combination. 
(C)触媒は、前記(B)イソシアネート成分と理論量より少ない(A)ポリオール成分との間のウレタン化反応を行わせてポリウレタン樹脂から構成された末端に活性イソシアネート基を有するプレポリマーを得るにあたって、所定のウレタン化触媒を用いることができる。このウレタン化触媒としては、第3級アミン化合物や有機金属化合物等の公知の触媒を用いることができる。また、ウレタン化触媒としては、例えば、トリエチレンジアミン、N,N-ジメチルヘキサメチレンジアミン、N,N-ジメチルブタンジアミン、ジアザビシクロ(5,4,0)-7-ウンデセン(DBU)及びDBU塩、ビスマストリス(2-エチルヘキサノエート)、ジイソプロポキシビス(エチルアセトアセテート)チタン、オクチル酸鉛、ラウリル酸ジブチル錫等が好ましい。  (C) The catalyst causes a urethanization reaction between the isocyanate component (B) and a less than stoichiometric amount of the polyol component (A) to obtain a prepolymer having an active isocyanate group at the end and is composed of a polyurethane resin. In this process, a predetermined urethanization catalyst can be used. As this urethanization catalyst, known catalysts such as tertiary amine compounds and organometallic compounds can be used. In addition, examples of urethanation catalysts include triethylenediamine, N,N-dimethylhexamethylenediamine, N,N-dimethylbutanediamine, diazabicyclo(5,4,0)-7-undecene (DBU) and DBU salt, bismuth Preferred are tris(2-ethylhexanoate), diisopropoxybis(ethyl acetoacetate)titanium, lead octylate, dibutyltin laurate, and the like. 
(D)溶剤は、エステル系溶剤、ケトン系溶剤、芳香族系炭化水素溶剤、ハロゲン化炭化水素系溶剤、多価アルコールの誘導体を挙げることができ、好ましくはエステル系溶剤、ケトン系溶剤、多価アルコールの誘導体が有害危険性の少ないことから好ましい。例えば、エステル系溶剤としては、酢酸エチル、酢酸ブチル等があり、ケトン系溶剤としてはアセトン、メチルエチルケトン等があり、多価アルコールの誘導体としては、プロピレングリコールモノメチルエーテルアセテート等が好ましい。  (D) Solvents include ester solvents, ketone solvents, aromatic hydrocarbon solvents, halogenated hydrocarbon solvents, and polyhydric alcohol derivatives, preferably ester solvents, ketone solvents, and polyhydric alcohol derivatives. Derivatives of alcohols are preferred because of their low toxicity. For example, ester solvents include ethyl acetate, butyl acetate, etc., ketone solvents include acetone, methyl ethyl ketone, etc., and polyhydric alcohol derivatives include propylene glycol monomethyl ether acetate. 
ここで、上記(E)ポリウレタン樹脂から構成された末端に活性イソシアネート基を有するプレポリマー溶液を得るに際し、(B)イソシアネート成分と理論量の1/2の(A)ポリオール成分との反応比率は、ポリオールの水酸基(OH)に対するプレポリマーのイソシアネート基(NCO)の当量比、即ちNCO/OH比が1.95~2.5、より好ましくは2.0~2.1である。この当量比が2.5を越える場合には、(E)塗料中に残存する未反応活性イソシアネートが多くなり、塗布後の指触乾燥性が遅くなるために好ましくない。また、この当量比が1.95未満の場合には(E)塗料の粘度が高くなり、(E)塗料の製造及び塗工作業の作業性が悪化し得る。また、この当量比が2.0~2.1の場合は、(B)イソシアネート成分は全て反応してプレポリマーとなり、塗料中に未反応の(B)イソシアネート成分は無くなるために(E)塗料の成分安全性が高くなる。  Here, when obtaining a prepolymer solution having an active isocyanate group at the terminal and composed of the polyurethane resin (E), the reaction ratio between the isocyanate component (B) and the polyol component (A), which is 1/2 of the theoretical amount, is The equivalent ratio of the isocyanate groups (NCO) of the prepolymer to the hydroxyl groups (OH) of the polyol, that is, the NCO/OH ratio, is 1.95 to 2.5, more preferably 2.0 to 2.1. If this equivalent ratio exceeds 2.5, a large amount of unreacted active isocyanate remains in the coating material (E), which is undesirable because dryness to the touch after coating becomes slow. Furthermore, if this equivalent ratio is less than 1.95, the viscosity of (E) the paint becomes high, and the workability of (E) the manufacturing and coating operations of the paint may deteriorate. In addition, when this equivalent ratio is 2.0 to 2.1, all of the (B) isocyanate components react and become a prepolymer, and there is no unreacted (B) isocyanate component in the paint, so the (E) paint Ingredient safety is increased. 
(E)ポリウレタン樹脂から構成された末端に活性イソシアネート基を有するプレポリマー溶液の塗料は単体として用いることもできるが、以下に示す成分を添加することができる。まず、顔料を添加することができる。この顔料は、主成分としての前記(B)イソシアネート成分および(A)ポリオール成分の合計量100重量部当たり5重量部未満、好ましくは1重量部未満が好ましい。この顔料を添加すると、その添加量が多くなるに応じて得られる塗膜の硬度は低下する。顔料の例としては、ウレタン樹脂用顔料であれば特に限定はないが、ポリオールをビヒクルにして顔料を練りこんだペーストが使用上好ましい。例えば、ペースト状着色剤FTR(大日精化社製)の各色等を挙げることができる。  (E) The prepolymer solution coating composed of polyurethane resin and having an active isocyanate group at the end can be used alone, but the following components can be added. First, pigments can be added. The amount of this pigment is preferably less than 5 parts by weight, preferably less than 1 part by weight, per 100 parts by weight of the total amount of the isocyanate component (B) and the polyol component (A) as main components. When this pigment is added, the hardness of the resulting coating film decreases as the amount added increases. As an example of the pigment, there is no particular limitation as long as it is a pigment for urethane resin, but a paste in which the pigment is kneaded using a polyol as a vehicle is preferred for use. For example, each color of the paste coloring agent FTR (manufactured by Dainichiseika Chemical Co., Ltd.) can be used. 
また、組成物の耐久性,安定性の向上を図るために、安定剤として、熱安定剤、酸化防止剤、紫外線吸収剤、紫外線安定剤、充填剤等を、支障のない限りにおいて、1種または2種以上混合して用いることもできる。さらに、前述したもの以外にも、顔料、染料、難燃剤、消泡剤、分散剤、表面改質剤、水分吸着剤等を適宜添加することも可能である。  In addition, in order to improve the durability and stability of the composition, one type of stabilizer, such as a heat stabilizer, antioxidant, ultraviolet absorber, ultraviolet stabilizer, filler, etc., may be added as long as there is no problem. Alternatively, two or more kinds can be mixed and used. Furthermore, in addition to those mentioned above, pigments, dyes, flame retardants, antifoaming agents, dispersants, surface modifiers, water adsorbents, etc. can also be added as appropriate. 
さて、混合装置のある反応槽中に溶剤を入れ、次いで原料として用いられる(A)ポリオール成分を投入して溶剤中に混合分散させ、(B)ポリイソシアネート成分を投入し混合分散させ、次いで(C)触媒を投入して混合分散させたのちチッソ雰囲気下で攪拌を続け、それぞれ常温、または加温した状態で所定時間のウレタン化反応を行い(E)ポリウレタン樹脂から構成された末端に活性イソシアネート基を有するプレポリマー溶液の塗料が得られる。添加剤を混合する場合には、予めポリオール成分に混合させておくか、または主成分の混合時に添加してもよい。  Now, a solvent is put into a reaction tank equipped with a mixing device, then (A) polyol component used as a raw material is added and mixed and dispersed in the solvent, (B) polyisocyanate component is added and mixed and dispersed, and then ( C) After adding the catalyst and mixing and dispersing it, stirring is continued under a nitrogen atmosphere, and the urethanization reaction is carried out for a predetermined time at room temperature or in a heated state, respectively. (E) Active isocyanate is added to the terminals composed of polyurethane resin A coating of prepolymer solution with groups is obtained. When mixing additives, they may be mixed with the polyol component in advance, or may be added at the time of mixing the main components. 
而して一液湿気硬化性の無黄変軟質塗料が得られる。得られた当該塗料を、塗膜が「艶あり」または「艶なし」に仕上げる用途に応じて溶剤等で希釈し塗料中の樹脂分濃度を調整することで達成することができる。  As a result, a one-component moisture-curable non-yellowing soft paint is obtained. This can be achieved by diluting the obtained paint with a solvent or the like and adjusting the resin concentration in the paint depending on the purpose of finishing the paint film to be "glossy" or "non-glossy." 
前述の得られた(E)塗料は、約30秒で指触乾燥できる速乾性である。ここで、(E)塗料を駆体に塗布し、塗膜の最終強度を得るため、常温~120℃で数十秒~2時間以上水蒸気との反応を起こさせるとよい。しかる後に塗料は軟質強靭な透明塗膜となる。また、ポリプロピレン板(PP板)に塗布し、水蒸気と反応後の塗膜をPP板から剥がして取り出すこともできる。 The above-obtained paint (E) is quick-drying and can be dry to the touch in about 30 seconds. Here, it is preferable to apply the paint (E) to the precursor and allow it to react with water vapor at room temperature to 120° C. for several tens of seconds to 2 hours or more in order to obtain the final strength of the coating film. After that, the paint becomes a soft, tough, transparent film. Alternatively, it can be applied to a polypropylene plate (PP plate), and after reacting with water vapor, the coating film can be peeled off from the PP plate and taken out.
以下に実施例を挙げて、本発明を更に具体的に説明するが、本発明はこの実施例に限定されるものではない。  EXAMPLES The present invention will be described in more detail with reference to Examples below, but the present invention is not limited to these Examples. 
<実施例1> 攪拌羽根、還流装置、温度計を設置した加熱装置付き四つ口セパラブルフラスコに窒素ガス雰囲気下、脱水処理をされた酢酸エチルを350g投入し、次いでメチレンビス(4,1-シクロヘキシレン)ジイソシアネートを17.86g(0.139当量)を投入し、次に攪拌しながら常温下でクラポールC-3090クラレ社製(液状カーボネート系ポリオール;分子量3,000)を100g(0.067当量)投入し、次いで反応触媒としてジブチル-錫-ラウレート0.1gを反応槽に仕込み、反応液の温度が40℃以下に維持したまま4時間反応させた。次いで80℃で4時間還流反応させた。反応終了後、反応液を室温に戻したところでジブチル-錫-ラウレート0.9gを追加した上で攪拌混合して、ポリウレタン樹脂から構成された末端に活性イソシアネート基を有するプレポリマー溶液の塗料を得た。得られた上記塗料は25℃で粘度0.3Pa・sの液体であった。これを「実例-1」の記号で示す。  <Example 1> 350 g of dehydrated ethyl acetate was added to a four-necked separable flask equipped with a stirring blade, a reflux device, and a heating device in a nitrogen gas atmosphere, and then methylene bis(4,1- 17.86 g (0.139 equivalents) of cyclohexylene diisocyanate were added, and then 100 g (0.067 g. Then, 0.1 g of dibutyl-tin-laurate as a reaction catalyst was charged into the reaction tank, and the reaction was carried out for 4 hours while the temperature of the reaction solution was maintained at 40° C. or lower. Then, the mixture was refluxed at 80° C. for 4 hours. After the reaction was completed, when the reaction solution was returned to room temperature, 0.9 g of dibutyl-tin-laurate was added and mixed with stirring to obtain a prepolymer solution coating composed of polyurethane resin and having active isocyanate groups at the terminals. Ta. The obtained coating material was a liquid having a viscosity of 0.3 Pa·s at 25°C. This is indicated by the symbol “Example-1”. 
得られた「実例-1」の(E)塗料をPP板に塗布し、溶剤は速やかに蒸発した塗膜は30秒後には指触乾燥する。さらに、常温で2時間放置することによって水蒸気との反応を起こせしめ、しかる後に塗料は軟質強靭な透明塗膜となる。常温下で3日間放置したこの塗膜をPP板から剥がして取り出し軟質で強靭な透明な膜を得た。塗膜の100%伸び引張応力は1.1MPaと柔らかく(例えば、天然ゴム0.5MPa)、引張強さは18.7MPa(例えば、天然ゴム5MPa)、引張伸び率1,300%(例えば、天然ゴム600%)と強靭である。この塗膜を100℃の恒温槽下で10日間ばく露した結果、塗膜の外観に変化は見られず優れた耐久性を示した(天然ゴムは、1日までに分解による溶融)。  The obtained paint (E) of "Example-1" was applied to a PP board, and the solvent quickly evaporated and the paint film was dry to the touch after 30 seconds. Furthermore, by leaving it at room temperature for 2 hours, a reaction with water vapor is caused, after which the paint becomes a soft, tough, transparent coating. This coating film was left at room temperature for 3 days and then peeled off from the PP board to obtain a soft, tough and transparent film. The coating film has a soft tensile stress of 1.1 MPa at 100% elongation (for example, natural rubber 0.5 MPa), a tensile strength of 18.7 MPa (for example, natural rubber 5 MPa), and a tensile elongation rate of 1,300% (for example, natural rubber 5 MPa). 600% rubber) and strong. When this coating film was exposed for 10 days in a constant temperature bath at 100° C., no change was observed in the appearance of the coating film and it exhibited excellent durability (natural rubber melted due to decomposition within one day). 
<実施例2> イソホロンジイソシアネートを15.26g(0.139当量)を投入すること以外は実施例1と同様にして、プレポリマー溶液の塗料を得た。得られた上記塗料は25℃で粘度0.2Pa・sの液体であった。塗膜の100%伸び引張応力は1.0MPaと柔らかく、引張強さは17.6MPa、引張伸び率1,200%と強靭である。この塗膜を100℃の恒温槽下で10日間ばく露した結果、塗膜の外観に変化は見られず優れた耐久性を示した。(天然ゴムは、1日までに分解による溶融)。  <Example 2> A coating material of a prepolymer solution was obtained in the same manner as in Example 1 except that 15.26 g (0.139 equivalents) of isophorone diisocyanate was added. The obtained coating material was a liquid having a viscosity of 0.2 Pa·s at 25°C. The coating film has a soft tensile stress of 1.0 MPa at 100% elongation, and is strong with a tensile strength of 17.6 MPa and a tensile elongation rate of 1,200%. When this coating film was exposed for 10 days in a constant temperature bath at 100° C., no change was observed in the appearance of the coating film, and it showed excellent durability. (Natural rubber melts due to decomposition within one day). 
<実施例3> 得られた「実例-1」の(E)塗料100g(樹脂分濃度(NVと言う)25%)、酢酸エチル溶剤150gを加えて混合し、希釈塗料(NV10%)を得た。ドライフラワーをこの希釈溶液にディッピング(浸漬)して、風乾30秒で指触乾燥し、艶ありのコーティングされたドライフラワーを得た。このドライフラワーは、柔軟性があることが確認された。また、このドライフラワーは、コーティング前と比較して、艶(光沢感)がある外観となった。また、このドライフラワーは、コーティングしない場合と比較して、カビの発生が抑制された。  <Example 3> 100 g of the obtained (E) paint of "Example-1" (resin concentration (NV) 25%) and 150 g of ethyl acetate solvent were added and mixed to obtain a diluted paint (NV 10%). Ta. Dried flowers were dipped in this diluted solution and air-dried for 30 seconds to dry to the touch to obtain shiny coated dried flowers. This dried flower was confirmed to be flexible. Moreover, this dried flower had a glossy (glossy) appearance compared to before coating. In addition, the growth of mold was suppressed in this dried flower compared to when it was not coated. 
<実施例4> 得られた「実例-1」の(E)塗料100g(樹脂分濃度25%)に、酢酸エチル溶剤300gを加えて混合し、希釈塗料(NV5%)を得た。ドライフラワーをこの希釈溶液にディッピングして、風乾30秒で指触乾燥し、艶なしのコーティングされたドライフラワーを得た。このドライフラワーは、柔軟性があることが確認された。また、このドライフラワーは、コーティング前と比較して光沢感が大きく変化しない外観となった。また、このドライフラワーは、コーティングしない場合と比較して、カビの発生が抑制された。  <Example 4> 300 g of ethyl acetate solvent was added to 100 g (resin concentration 25%) of the obtained paint (E) of "Example-1" and mixed to obtain a diluted paint (NV 5%). Dried flowers were dipped in this diluted solution and air-dried for 30 seconds to dry to the touch to obtain matte coated dried flowers. This dried flower was confirmed to be flexible. Additionally, this dried flower had an appearance with no significant change in gloss compared to before coating. In addition, the growth of mold was suppressed in this dried flower compared to when it was not coated. 
<実施例5> 得られた「実例-1」の(E)塗料100g(NV25%)に、顔料0.5g(FTRレッド;大日精化社製)と酢酸エチル溶剤300gを加えて混合し、赤着色希釈塗料(NV5%)を得た。バラのドライフラワーをこの希釈溶液にディッピングして、風乾30秒で指触乾燥し、赤く着色された艶なしのコーティングされたドライフラワーを得た。このドライフラワーは、柔軟性があることが確認された。また、このドライフラワーは、コーティング前と比較して光沢感が大きくかわらず、赤く着色された外観となった。また、このドライフラワーは、コーティングしない場合と比較して、カビの発生が抑制された。  <Example 5> 0.5 g of pigment (FTR Red; manufactured by Dainichiseika Kaisha, Ltd.) and 300 g of ethyl acetate solvent were added to 100 g (NV 25%) of the obtained (E) paint of "Example-1" and mixed. A red colored diluted paint (NV5%) was obtained. Dried rose flowers were dipped in this diluted solution and air-dried for 30 seconds to dry to the touch to obtain a matte coated dried flower colored red. This dried flower was confirmed to be flexible. Furthermore, compared to before coating, this dried flower had a reddish appearance with no significant change in glossiness. In addition, the growth of mold was suppressed in this dried flower compared to when it was not coated. 
<測定条件等> 上記「液粘度」は、BH型液粘度計を用いて測定した結果の数値であり、塗工限度を8/Pa・s以下として、それより高い粘度を塗工難とする。  <Measurement conditions, etc.> The above "liquid viscosity" is the numerical value measured using a BH type liquid viscometer, and the coating limit is set to 8/Pa・s or less, and a viscosity higher than that is considered difficult to coat. . 
また、「100%伸び引張応力」及び「引張強さ」、「引張伸び率」は、JIS K6301に準じてダンベル状3号型の試験片にて引張試験を行い、それぞれ100%伸び時の応力(単位:MPa)、破断時応力(単位:MPa)、破断時伸び率(単位:%)の数値で示した。  In addition, "100% elongation tensile stress", "tensile strength", and "tensile elongation rate" are determined by performing a tensile test using a dumbbell-shaped No. 3 test piece according to JIS K6301, and calculating the stress at 100% elongation. (unit: MPa), stress at break (unit: MPa), and elongation at break (unit: %). 
本発明の一液湿気硬化性の無黄変軟質塗料は、塗布後は指触乾燥が30秒と速乾性が高く作業性に優れ、水蒸気と反応して、軟質で変位追従性に優れ強靭な透明塗膜提供し得る。  The one-component, moisture-curable, non-yellowing soft paint of the present invention dries quickly to the touch in 30 seconds after application, and has excellent workability.It reacts with water vapor to create a soft, tough coating with excellent displacement followability. A transparent coating can be provided. 
例えば、荷重を受けた柔らかい組成物は変形し、応力集中によって破損しやすいが、柔らかく変位追従性に優れた強靭な塗膜に包まれていれば甚だ都合がよい。例えば、ドライフラワーにおいて、ドライフラワーを当該一液湿気硬化性の無黄変軟質塗料を塗布またはディッピングすることで花弁や葉身の落下や破損を抑えることができる。  For example, a soft composition deforms under load and easily breaks due to stress concentration, but it would be extremely advantageous if it were covered with a strong coating that is soft and has excellent displacement followability. For example, in the case of dried flowers, by coating or dipping the dried flowers with the one-component moisture-curable non-yellowing soft paint, it is possible to prevent petals and leaf blades from falling or breaking. 
<変形例> 上記の説明においては、植物本体20の表面全体に樹脂膜30を形成することを説明したが、これに限定されない。例えば、植物本体20の花弁部分のみなど、植物本体20の表面の一部に樹脂膜30を形成する態様であってもよい。  <Modification> In the above description, it has been explained that the resin film 30 is formed on the entire surface of the plant body 20, but the present invention is not limited to this. For example, the resin film 30 may be formed on a part of the surface of the plant body 20, such as only on the petal portion of the plant body 20. 
なお、上記では種々の実施形態および変形例を説明したが、これらの実施形態や変形例同士を組み合わせて構成してももちろんよ
い。 また、本開示は上記の実施形態に何ら限定されるものではなく、本開示の要旨を逸脱しない範囲で種々の形態で実施することができる。 
Although various embodiments and modifications have been described above, it is of course possible to combine these embodiments and modifications. Further, the present disclosure is not limited to the above-described embodiments, and can be implemented in various forms without departing from the gist of the present disclosure.
植物本体20は、植物の一例である。浸漬処理、仮乾燥処理および本乾燥処理は、膜形成工程の一例である。不織布7は、吸収体の一例である。 The plant body 20 is an example of a plant. The dipping treatment, the temporary drying treatment, and the main drying treatment are examples of film forming steps. The nonwoven fabric 7 is an example of an absorbent material.
4…乾燥剤、6…樹脂液、10…ドライフラワー、15…花弁、17…花托、20…植物本体、30…樹脂膜 4... Desiccant, 6... Resin liquid, 10... Dried flower, 15... Petal, 17... Flower receptacle, 20... Plant body, 30... Resin film

Claims (12)

  1. 植物を乾燥させる乾燥工程と、 前記乾燥させた植物の表面に樹脂組成物の膜を形成する膜形成工程と、を有し、 前記樹脂組成物は、(A)ポリオール成分が、官能基数2であって、数平均分子量2,000~3,000の液状カーボネート系ポリオールであり、かつ末端に活性ヒドロキシ基を有し、(B)ポリイソシアネート成分が、官能基数2である脂環式ポリイソシアネートであり、かつ末端にイソシアネート基を有し、 前記(A)のポリオール成分のヒドロキシル当量(OH)は、前記(B)のポリイソシアネート成分のイソシアネート当量(NCO)よりも小さく、 前記(A)のポリオール成分と前記(B)のポリイソシアネート成分とを、(C)触媒の存在下で(D)溶剤中にて反応させた(E)ポリウレタン樹脂から構成された末端に活性イソシアネート基を有するプレポリマー溶液の塗料であり、 前記膜形成工程においては、前記乾燥させた植物の表面に前記(E)の塗料の膜を形成し、空気中の水蒸気と反応させてウレア結合を形成する 観賞用植物の製造方法。 The resin composition comprises a drying step of drying the plant, and a film forming step of forming a film of the resin composition on the surface of the dried plant. It is a liquid carbonate polyol with a number average molecular weight of 2,000 to 3,000 and has an active hydroxy group at the terminal, and (B) the polyisocyanate component is an alicyclic polyisocyanate having a functional group number of 2. and has an isocyanate group at the terminal, the hydroxyl equivalent (OH) of the polyol component (A) is smaller than the isocyanate equivalent (NCO) of the polyisocyanate component (B), and the polyol (A) A prepolymer solution having an active isocyanate group at the end and composed of (E) a polyurethane resin in which the component and the polyisocyanate component of (B) are reacted in the presence of (C) a catalyst in (D) a solvent. In the film forming step, a film of the paint of (E) is formed on the surface of the dried plant, and the film is reacted with water vapor in the air to form a urea bond. Production of ornamental plants. Method.
  2. 前記(A)のポリオール成分のヒドロキシル当量(OH)と前記(B)のポリイソシアネート成分のイソシアネート当量(NCO)との当量比率(NCO/OH)は1.95~2.5である請求項1記載の観賞用植物の製造方法。 Claim 1: The equivalent ratio (NCO/OH) between the hydroxyl equivalent (OH) of the polyol component (A) and the isocyanate equivalent (NCO) of the polyisocyanate component (B) is 1.95 to 2.5. Method for producing the described ornamental plants.
  3. 前記脂環式ポリイソシアネートは、メチレンビス(4,1-シクロヘキシレン)ジイソシアネートまたはイソホロンジイソシアネートである 請求項1記載の観賞用植物の製造方法。 The method for producing an ornamental plant according to claim 1, wherein the alicyclic polyisocyanate is methylene bis(4,1-cyclohexylene) diisocyanate or isophorone diisocyanate.
  4. 前記樹脂組成物の膜は、100%伸び引張応力が1.0~1.1MPaであり、引張破断伸びが1,000%以上であり、引張破断強さが17.6~18.7MPaである 請求項1記載の観賞用植物の製造方法。 The film of the resin composition has a 100% elongation tensile stress of 1.0 to 1.1 MPa, a tensile elongation at break of 1,000% or more, and a tensile strength at break of 17.6 to 18.7 MPa. A method for producing an ornamental plant according to claim 1.
  5. 前記(E)の塗料は、前記乾燥させた植物に前記塗料の膜を形成してから30秒以内に指触乾燥を来す 請求項1記載の観賞用植物の製造方法。 2. The method for producing an ornamental plant according to claim 1, wherein the paint (E) is dry to the touch within 30 seconds after forming a film of the paint on the dried plant.
  6. 前記(D)の溶剤は、酢酸エチル溶剤であり、 前記指触乾燥の工程に用いる塗料の樹脂分濃度が5~10%である 請求項5記載の観賞用植物の製造方法。 The method for producing an ornamental plant according to claim 5, wherein the solvent (D) is an ethyl acetate solvent, and the resin concentration of the paint used in the touch drying step is 5 to 10%.
  7. 前記指触乾燥の工程は前記乾燥させた植物を前記(E)の塗料を吸収する吸収体に配置して行い、 前記指触乾燥の工程の後に前記乾燥させた植物を吊るし前記塗料の膜をさらに乾燥させる 請求項6記載の観賞用植物の製造方法。 The drying to the touch step is carried out by placing the dried plants on an absorbent body that absorbs the paint of (E), and after the drying to the touch step, the dried plants are hung to form a film of the paint. The method for producing an ornamental plant according to claim 6, further comprising drying.
  8. 前記植物は、花托を備え、 前記乾燥工程において、冷凍された前記植物を真空乾燥させる 請求項1記載の観賞用植物の製造方法。 2. The method for producing an ornamental plant according to claim 1, wherein the plant includes a flower receptacle, and in the drying step, the frozen plant is vacuum-dried.
  9. 前記植物は、収穫されてから平面状に押し付けられることなく、前記乾燥工程において乾燥される 請求項8記載の観賞用植物の製造方法。 9. The method for producing an ornamental plant according to claim 8, wherein the plant is dried in the drying step without being pressed into a flat shape after being harvested.
  10. 花托を備える植物を冷凍し真空乾燥させる乾燥工程と、 前記乾燥させた植物の表面に樹脂組成物の膜を形成する膜形成工程と、を有し、 前記樹脂組成物は、(A)ポリオール成分が、官能基数2、分子量2,000~3,000の末端に活性ヒドロキシ基を有する液状カーボネート系ポリオールであり、(B)ポリイソシアネート成分が、官能基数2の末端にイソシアネート基を有するメチレンビス(4,1-シクロヘキシレン)ジイソシアネートまたはイソホロンジイソシアネートであり、 前記(A)のポリオール成分のヒドロキシル当量(OH)と前記(B)のポリイソシアネート成分のイソシアネート当量(NCO)との当量比率(NCO/OH)は1.95~2.5であり、 前記(A)のポリオール成分と前記(B)のポリイソシアネート成分とを、(C)触媒の存在下で(D)酢酸エチル溶剤中にて反応させた(E)ポリウレタン樹脂から構成された末端に活性イソシアネート基を有するプレポリマー溶液の塗料であり、 前記膜形成工程においては、前記乾燥させた植物の表面に前記(E)の塗料の膜を形成し、空気中の水蒸気と反応させてウレア結合を形成し、 前記(E)の塗料は、前記乾燥させた植物に前記膜を形成してから30秒以内に指触乾燥を来し、 前記樹脂組成物の膜は、100%伸び引張応力が1.0~1.1MPaであり、引張破断伸びが1,000%以上であり、引張破断強さが17.6~18.7MPaである 観賞用植物の製造方法。 A drying step of freezing and vacuum drying a plant with flower receptacles, and a film forming step of forming a film of a resin composition on the surface of the dried plant, the resin composition comprising (A) a polyol component. is a liquid carbonate polyol having an active hydroxyl group at the end with a functional number of 2 and a molecular weight of 2,000 to 3,000, and (B) the polyisocyanate component is a methylene bis(4) having a functional number of 2 and an isocyanate group at the end. , 1-cyclohexylene) diisocyanate or isophorone diisocyanate, and the equivalent ratio (NCO/OH) between the hydroxyl equivalent (OH) of the polyol component (A) and the isocyanate equivalent (NCO) of the polyisocyanate component (B). is 1.95 to 2.5, and the polyol component of (A) and the polyisocyanate component of (B) are reacted in the presence of (C) a catalyst and (D) in an ethyl acetate solvent. (E) A prepolymer solution coating composed of polyurethane resin and having an active isocyanate group at the end, and in the film forming step, a film of the coating of (E) is formed on the surface of the dried plant. , reacts with water vapor in the air to form urea bonds, the paint of (E) becomes dry to the touch within 30 seconds after forming the film on the dried plant, and the resin composition The film of the product has a 100% elongation tensile stress of 1.0 to 1.1 MPa, a tensile elongation at break of 1,000% or more, and a tensile strength at break of 17.6 to 18.7 MPa. manufacturing method.
  11. 請求項1記載の製造方法によって形成されてなる観賞用植物。 An ornamental plant formed by the production method according to claim 1.
  12. 乾燥した植物と、 前記植物の表面に形成された樹脂組成物の膜とを有し、 前記樹脂組成物の膜は、100%伸び引張応力が1.0~1.1MPaであり、引張破断伸びが1,000%以上であり、引張破断強さが17.6~18.7MPaである 観賞用植物。 It has a dried plant and a film of a resin composition formed on the surface of the plant, and the film of the resin composition has a 100% elongation tensile stress of 1.0 to 1.1 MPa, and a tensile elongation at break of 1.0 to 1.1 MPa. is 1,000% or more and has a tensile breaking strength of 17.6 to 18.7 MPa.
PCT/JP2023/025178 2022-07-08 2023-07-06 Ornamental plant production method and ornamental plant WO2024010072A2 (en)

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