Classifications

• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09D—COATING 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
  • C09D167/00—Coating compositions based on polyesters obtained by reactions forming a carboxylic ester link in the main chain; Coating compositions based on derivatives of such polymers
  • C09D167/04—Polyesters derived from hydroxycarboxylic acids, e.g. lactones
• • B—PERFORMING OPERATIONS; TRANSPORTING
  • B32—LAYERED PRODUCTS
  • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
  • B32B27/00—Layered products comprising a layer of synthetic resin
  • B32B27/36—Layered products comprising a layer of synthetic resin comprising polyesters
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J3/00—Processes of treating or compounding macromolecular substances
  • C08J3/02—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques
  • C08J3/03—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in aqueous media
  • C08J3/05—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in aqueous media from solid polymers
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J3/00—Processes of treating or compounding macromolecular substances
  • C08J3/12—Powdering or granulating
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
  • C08J7/00—Chemical treatment or coating of shaped articles made of macromolecular substances
  • C08J7/04—Coating
  • C08J7/046—Forming abrasion-resistant coatings; Forming surface-hardening coatings
• • C—CHEMISTRY; METALLURGY
  • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
  • C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
  • C08L29/00—Compositions of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an alcohol, ether, aldehydo, ketonic, acetal or ketal radical; Compositions of hydrolysed polymers of esters of unsaturated alcohols with saturated carboxylic acids; Compositions of derivatives of such polymers
  • C08L29/02—Homopolymers or copolymers of unsaturated alcohols
  • C08L29/04—Polyvinyl alcohol; Partially hydrolysed homopolymers or copolymers of esters of unsaturated alcohols with saturated carboxylic acids

Definitions

• the present invention relates to a poly(3-hydroxyalkanoate)-based powder and an aqueous suspension containing the powder.
• Poly(3-hydroxyalkanoate) resin (hereafter referred to as P3HA) has excellent seawater degradability and is a material that can solve the environmental problems caused by discarded plastics.
• P3HA Poly(3-hydroxyalkanoate) resin
• the mechanical properties of poly(3-hydroxybutyrate-co-3-hydroxyhexanoate), a type of P3HA can be flexibly controlled by changing the composition ratio of 3-hydroxyhexanoate.
• One possible mode of use of the P3HA powder is to redisperse the P3HA powder in an aqueous medium to form a slurry again, apply the slurry to a substrate, and heat-dry to form a P3HA resin film.
• the P3HA powder is to be redispersed in an aqueous medium, it is desired that the P3HA powder can be dispersed in the aqueous medium easily and with little effort.
• good dispersibility also increases the fluidity of the slurry, which can easily cause dripping when the slurry is applied to a substrate and then dried, which can hinder the formation of a uniform resin film. Therefore, it has been difficult to achieve both good dispersibility and suppression of dripping after application.
• the P3HA powder described in Patent Document 1 has room for improvement in this respect.
• one aspect of the present invention aims to provide a poly(3-hydroxyalkanoate)-based powder that has good dispersibility in an aqueous medium and is capable of suppressing dripping after application of an aqueous suspension obtained by dispersing the powder in an aqueous medium.
• Another aspect of the present invention aims to provide an aqueous suspension containing a poly(3-hydroxyalkanoate)-based powder, in which the poly(3-hydroxyalkanoate)-based powder has good dispersibility in an aqueous medium and dripping after application is suppressed.
• the present invention provides a poly(3-hydroxyalkanoate)-based powder containing a poly(3-hydroxyalkanoate)-based resin and polyvinyl alcohol,
• the polyvinyl alcohol has a saponification degree of 50 to 79 mol %,
• the viscosity of a 4% by weight aqueous solution of the polyvinyl alcohol at 20°C is 2 to 20 mPa s
• the present invention relates to a poly(3-hydroxyalkanoate)-based powder, in which the content of the polyvinyl alcohol is 2 to 10 parts by weight based on 100 parts by weight of the poly(3-hydroxyalkanoate)-based resin.
• the present invention also relates to a method for producing an aqueous suspension, which comprises a step of dispersing the poly(3-hydroxyalkanoate) powder in an aqueous medium.
• the present invention further provides an aqueous suspension comprising a poly(3-hydroxyalkanoate) powder and an aqueous medium, the poly(3-hydroxyalkanoate)-based powder contains a poly(3-hydroxyalkanoate)-based resin and polyvinyl alcohol;
• the polyvinyl alcohol has a saponification degree of 50 to 79 mol %,
• the viscosity of a 4% by weight aqueous solution of the polyvinyl alcohol at 20°C is 2 to 20 mPa s,
• the present invention also relates to an aqueous suspension in which the content of the polyvinyl alcohol is 2 to 10 parts by weight based on 100 parts by weight of the poly(3-hydroxyalkanoate) resin.
• the present invention also relates to a method for producing a laminate, comprising the steps of applying the aqueous suspension onto at least one surface of a substrate, and drying by heating to form a resin layer on the substrate.
• the present invention further provides a laminate including a base layer and a resin layer provided on at least one surface of the base layer, the resin layer contains a poly(3-hydroxyalkanoate)-based resin and polyvinyl alcohol;
• the polyvinyl alcohol has a saponification degree of 50 to 79 mol %,
• the viscosity of a 4% by weight aqueous solution of the polyvinyl alcohol at 20°C is 2 to 20 mPa s
• the present invention also relates to a laminate in which the content of the polyvinyl alcohol is 2 to 10 parts by weight based on 100 parts by weight of the poly(3-hydroxyalkanoate) resin.
• a poly(3-hydroxyalkanoate)-based powder that has good dispersibility in an aqueous medium and that can suppress dripping after application of the aqueous suspension obtained by dispersing the powder in an aqueous medium.
• an aqueous suspension containing a poly(3-hydroxyalkanoate)-based powder in which the poly(3-hydroxyalkanoate)-based powder has good dispersibility in an aqueous medium and dripping after application is suppressed.
• a laminate By applying the aqueous suspension to a substrate and drying by heating, a laminate can be suitably produced in which a poly(3-hydroxyalkanoate)-based resin layer is formed on the substrate.
• the aqueous suspension has high fluidity and is easy to apply uniformly to the substrate (i.e., has good coatability), and in addition, it thickens when dried by heating after application, making it less likely to drip. Therefore, a laminate having a highly uniform resin film can be produced with good productivity.
• Poly(3-hydroxyalkanoate)-based powder An embodiment according to one aspect of the present invention relates to a poly(3-hydroxyalkanoate)-based powder (hereinafter also referred to as P3HA powder) containing a poly(3-hydroxyalkanoate)-based resin and polyvinyl alcohol.
• Poly(3-hydroxyalkanoate) resin is a homopolymer or copolymer having at least one or more types of 3-hydroxyalkanoate units as a constituent monomer unit.
• the 3-hydroxyalkanoate unit is preferably represented by the following general formula (1). [-CHR-CH 2 -CO-O-] (1)
• R represents an alkyl group represented by C p H 2p+1 , and p represents an integer of 1 to 15.
• R include linear or branched alkyl groups such as methyl, ethyl, propyl, methylpropyl, butyl, isobutyl, t-butyl, pentyl, and hexyl.
• p is preferably 1 to 10, and more preferably 1 to 8.
• the P3HA is preferably P3HA produced from a microorganism.
• P3HA produced from a microorganism all of the 3-hydroxyalkanoate units are contained as (R)-3-hydroxyalkanoate units.
• P3HA preferably contains 3-hydroxyalkanoate units (particularly units represented by general formula (1)) in an amount of 50 mol% or more of all constituent monomer units, more preferably 60 mol% or more, and even more preferably 70 mol% or more.
• P3HA may contain only one or more types of 3-hydroxyalkanoate units as constituent monomer units of the polymer, or may contain other units (e.g., 4-hydroxyalkanoate units, etc.) in addition to one or more types of 3-hydroxyalkanoate units.
• P3HA is preferably a homopolymer of 3-hydroxybutyrate (hereinafter also referred to as 3HB) units or a copolymer containing 3HB units and other hydroxyalkanoate units, and more preferably contains at least the above-mentioned copolymer. It is preferable that the 3-hydroxybutyrate units are all (R)-3-hydroxybutyrate units.
• the other hydroxyalkanoate units may be 3-hydroxyalkanoate units other than 3HB units, or may be hydroxyalkanoate units other than 3-hydroxyalkanoate units (e.g., 4-hydroxyalkanoate units).
• the other hydroxyalkanoate units may include only one type, or may include two or more types.
• P3HA include poly(3-hydroxybutyrate) (abbreviation: P3HB), poly(3-hydroxybutyrate-co-3-hydroxypropionate), poly(3-hydroxybutyrate-co-3-hydroxyvalerate) (abbreviation: P3HB3HV), poly(3-hydroxybutyrate-co-3-hydroxyvalerate-3-hydroxyhexanoate), poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) (abbreviation: P3HB3HH), poly (3-hydroxybutyrate-co-3-hydroxyheptanoate), poly(3-hydroxybutyrate-co-3-hydroxyoctanoate), poly(3-hydroxybutyrate-co-3-hydroxynonanoate), poly(3-hydroxybutyrate-co-3-hydroxydecanoate), poly(3-hydroxybutyrate-co-3-hydroxyundecanoate), poly(3-hydroxybutyrate-co-4-hydroxybutyrate) (abbreviation: P3HB4HB), etc.
• poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) or poly(3-hydroxybutyrate-co-4-hydroxybutyrate) is preferred, and poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) is particularly preferred.
• the melting point and crystallinity of poly(3-hydroxybutyrate-co-3-hydroxyhexanoate) can be altered, which in turn changes physical properties such as Young's modulus and heat resistance, making it possible to impart physical properties between those of polypropylene and polyethylene.
• the P3HA may include at least two types of P3HA that differ from each other in crystallinity. Specifically, the P3HA may include at least two types of P3HA that differ from each other in the types of constituent monomers and/or the content ratios of the constituent monomers.
• the average content ratio of each monomer unit in all monomer units constituting the entire P3HA can be determined by a method known to those skilled in the art, for example, the method described in paragraph [0047] of WO 2013/147139.
• the average content ratio means the molar ratio of each monomer unit in all monomer units constituting the entire P3HA, and when P3HA is a mixture of two or more resins, it means the molar ratio of each monomer unit in all monomer units contained in the mixture.
• the weight average molecular weight (hereinafter also referred to as Mw) of P3HA is not particularly limited, but from the viewpoints of mechanical properties, processability, dispersibility, coatability, and suppression of dripping after coating, it is preferably 100,000 to 1,000,000, more preferably 150,000 to 900,000, and even more preferably 200,000 to 800,000. If the weight average molecular weight is 100,000 or more, sufficient mechanical properties can be obtained, and if it is 1,000,000 or less, a sufficient crystallization rate can be obtained and good processability can be achieved.
• the weight average molecular weight of P3HA can be determined by gel permeation chromatography (GPC) (Shodex GPC-101 manufactured by Showa Denko) using a polystyrene gel (Shodex K-804 manufactured by Showa Denko) in a column and chloroform as the mobile phase, and expressed as the molecular weight in terms of polystyrene.
• GPC gel permeation chromatography
• P3HA is produced, for example, from microorganisms capable of producing P3HA intracellularly.
• microorganisms isolated from nature and deposited in depositories of strains (e.g., IFO, ATCC, etc.), or mutants and transformants that can be prepared from them, can be used.
• the first bacterium to produce P3HB an example of P3HA, was Bacillus megaterium, discovered in 1925, and other natural microorganisms include Cupriavidus necator (formerly classified as Alcaligenes eutrophus and Ralstonia eutropha) and Alcaligenes latus. It is known that P3HA accumulates intracellularly in these microorganisms.
• examples of bacteria that produce copolymers of 3-hydroxybutyrate and other hydroxyalkanoates which are an example of P3HA
• examples of bacteria that produce copolymers of 3-hydroxybutyrate and other hydroxyalkanoates include Aeromonas caviae, which produces P3HB3HV and P3HB3HH, and Alcaligenes eutrophus, which produces P3HB4HB.
• Aeromonas caviae which produces P3HB3HV and P3HB3HH
• Alcaligenes eutrophus which produces P3HB4HB.
• Alcaligenes eutrophus AC32 strain (FERM BP-6038) (T. Fukui, Y. Doi, J. Bateriol., 179, pp. 4821-4830 (1997)) into which genes of the P3HA synthesis enzyme group have been introduced is more preferred.
• the bacterial cells may be genetically modified microorganisms into which various P3HA synthesis-related genes have been introduced according to the P3
• P3HA can also be produced by the method described in, for example, International Publication No. 2010/013483.
• Commercially available P3HA products include Kaneka Biodegradable Polymer PHBH (registered trademark) manufactured by Kaneka Corporation.
• the P3HA powder according to the present embodiment contains a specific amount of polyvinyl alcohol (hereinafter, also referred to as PVA) exhibiting a specific degree of saponification and aqueous solution viscosity, which improves the dispersibility of the P3HA powder when dispersed in an aqueous medium and the applicability of the aqueous suspension obtained by the dispersion to a substrate, and also suppresses dripping that may occur during heating and drying after the aqueous suspension is applied to a substrate.
• PVA polyvinyl alcohol
• PVA is usually a saponified vinyl ester polymer (a polymer that has at least a vinyl ester monomer as a constituent monomer). PVA usually contains vinyl alcohol units and vinyl ester monomer units.
• PVA with a degree of saponification of 50 mol% or more and 79 mol% or less is used.
• PVA with a degree of saponification of 50 mol% or more the dispersion stability when P3HA powder is dispersed in an aqueous medium is improved, and a uniform resin film can be formed.
• PVA with a degree of saponification of 79 mol% or less the viscosity of the aqueous suspension obtained by dispersing P3HA powder in an aqueous medium can increase when the suspension is heated. Therefore, dripping can be suppressed when the aqueous suspension is applied and then dried by heating.
• the upper limit of the saponification degree of the PVA is preferably 77 mol% or less, more preferably 75 mol% or less, and even more preferably 73 mol% or less, from the viewpoint of suppressing dripping after application.
• the lower limit of the saponification degree of the PVA is preferably 60 mol% or more, more preferably 65 mol% or more, even more preferably 68 mol% or more, and particularly preferably 70 mol% or more, from the viewpoint of dispersion stability.
• Commercially available products can be used as PVA having such a saponification degree.
• the saponification degree of PVA is measured by the method specified in JIS K6726.
• the PVA used in this embodiment has a viscosity of 2 mPa ⁇ s or more and 20 mPa ⁇ s or less, measured at 20°C as a 4 wt% aqueous solution of the PVA.
• a PVA with a viscosity of 2 mPa ⁇ s or more the dispersion stability when the P3HA powder is dispersed in an aqueous medium is improved, and a uniform resin film can be formed.
• the P3HA powder can be easily dispersed in an aqueous medium with little effort, the dispersibility of the P3HA powder is improved, and the aqueous suspension obtained by the dispersion can also be applied to a substrate with good properties. Furthermore, the viscosity of the aqueous suspension increases when it is heated, and therefore dripping can be suppressed when the aqueous suspension is applied and then dried by heating.
• the lower limit of the viscosity is preferably 3 mPa ⁇ s or more, more preferably 4 mPa ⁇ s or more, and even more preferably 5 mPa ⁇ s or more, from the viewpoint of dispersion stability.
• the upper limit of the viscosity is preferably 15 mPa ⁇ s or less, more preferably 10 mPa ⁇ s or less, and even more preferably 8 mPa ⁇ s or less, from the viewpoint of dispersibility, coatability, and suppression of dripping after application.
• the viscosity is an index showing the degree of polymerization of PVA, and is measured by a coaxial double cylindrical rheometer.
• the PVA may have units derived from monomers other than vinyl alcohol and vinyl ester monomers.
• the PVA may be PVA modified with other monomers.
• the content of PVA in the P3HA powder is set in the range of 2 parts by weight or more and 10 parts by weight or less per 100 parts by weight of P3HA contained in the P3HA powder.
• a PVA content of 2 parts by weight or more the viscosity of the aqueous suspension increases when heated, and therefore dripping during heating and drying after application of the aqueous suspension can be suppressed.
• a PVA content of 10 parts by weight or less the P3HA powder can be easily dispersed in an aqueous medium with little effort, resulting in good dispersibility of the P3HA powder, and also in good coatability of the aqueous suspension obtained by this dispersion onto a substrate.
• the lower limit of the PVA content is preferably 2.5 parts by weight or more, and more preferably 3 parts by weight or more, from the viewpoint of suppressing dripping after application.
• the upper limit of the PVA content is preferably 8 parts by weight or less, and more preferably 6 parts by weight or less, from the viewpoint of dispersibility of the P3HA powder and coatability of the aqueous suspension.
• poly(3-hydroxyalkanoate)-based powder As described above, the poly(3-hydroxyalkanoate) powder according to this embodiment contains P3HA and PVA.
• the P3HA powder may be substantially composed only of P3HA and PVA, but may also contain one or more of the following, provided that the effects of the invention are not impaired: dispersants or emulsifiers other than PVA, pH adjusters, inorganic fillers, colorants such as pigments and dyes, odor absorbers such as activated carbon and zeolite, fragrances such as vanillin and dextrin, plasticizers, antioxidants, weather resistance improvers, ultraviolet absorbers, crystal nucleating agents, lubricants, release agents, water repellents, antibacterial agents, sliding property improvers, and the like. Furthermore, the P3HA powder may contain various components resulting from the process of the manufacturing method described below, as long as the effects of the invention are not impaired.
• P3HA and PVA are the main components.
• the total proportion of P3HA and PVA in the entire P3HA powder may usually be 60-100% by weight, 80-100% by weight, 90-100% by weight, 95-100% by weight, or 99-100% by weight.
• the upper limit may be 99.9% by weight or less, or 99% by weight or less.
• the bulk density of the P3HA powder according to this embodiment is not particularly limited, but from the viewpoint of achieving good fluidity of the P3HA powder, it is preferably 0.3 to 0.6 kg/L, and more preferably 0.4 to 0.6 kg/L.
• the bulk density of the P3HA powder is measured according to the method described in JIS K-7365.
• the average particle size (D50) of the P3HA powder according to this embodiment is not particularly limited, but from the viewpoint of achieving good fluidity of the P3HA powder, it is preferably 10 to 200 ⁇ m, more preferably 50 to 180 ⁇ m, and even more preferably 60 to 100 ⁇ m.
• the method for measuring the average particle size (D50) of the P3HA powder is as follows. 0.2 g of the powder to be measured is added to 20 mL of ion-exchanged water and dispersed to obtain a dispersion liquid for measurement. The dispersion liquid for measurement is introduced into a laser diffraction/scattering type particle size distribution measuring device LA-950 (Horiba, Ltd.) and measurement is performed.
• the P3HA powder according to this embodiment preferably has a pH of 3 or more and 8 or less, measured when the powder is dispersed in water at a concentration of 50% by weight.
• the pH is within the above range, dripping after application of the aqueous suspension obtained by dispersing the P3HA powder in an aqueous medium can be further suppressed, and furthermore, discoloration and molecular weight reduction of P3HA due to heating can be suppressed.
• the upper limit is more preferably 7 or less, even more preferably 6 or less, particularly preferably 5 or less, and most preferably 4 or less.
• the lower limit is more preferably 4 or more, even more preferably 5 or more, and particularly preferably 6 or more.
• the P3HA powder according to this embodiment can be suitably used to prepare an aqueous suspension by dispersing it in an aqueous medium, as described below.
• the use is not limited to this, and the P3HA powder according to this embodiment can also be used to form various molded articles, such as films, sheets, tubes, plates, rods, containers (e.g., bottle containers, etc.), bags, parts, etc.
• the method for producing the P3HA powder according to the present embodiment is not particularly limited, but it can be suitably produced by sequentially carrying out the following steps (a) and (b).
• step (a) of this production method the specific PVA described above is added to a P3HA aqueous suspension.
• P3HA aqueous suspension P3HA is present in a dispersed state in an aqueous medium.
• an aqueous suspension containing P3HA may be abbreviated to "P3HA aqueous suspension”.
• the step (a) preferably includes the following steps (a1) and (a2).
• Step (a1) adding PVA to the P3HA aqueous suspension
• Step (a2) adjusting the pH of the P3HA aqueous suspension to 8 or less.
• the order in which steps (a1) and (a2) are performed is not particularly limited, but from the viewpoint of suppressing aggregation of P3HA in step (a2) and obtaining an aqueous suspension having better dispersion stability of P3HA, it is preferable to perform step (a2) after step (a1).
• the P3HA aqueous suspension used as the starting material is not particularly limited, but can be obtained, for example, by a method including a culture step in which a microorganism capable of producing P3HA within its cells is cultured, and, after the culture step, a purification step in which substances other than P3HA are decomposed and/or removed.
• the method for producing the P3HA powder according to this embodiment may include a step of obtaining an aqueous suspension of P3HA (e.g., a step including the above-mentioned culturing step and purification step) prior to step (a).
• the microorganism used in this step may be, for example, the microorganism described above.
• a purification step is usually carried out to decompose and/or remove impurities other than P3HA.
• This purification step is not particularly limited, and physical treatments, chemical treatments, biological treatments, etc. that a person skilled in the art can think of can be applied.
• the purification method described in WO 2010/067543 can be preferably applied.
• the amount of impurities remaining in the final product is largely determined by the purification process, so it is preferable to reduce these impurities as much as possible.
• impurities may be present as long as they do not impair the physical properties of the final product, but in cases where high purity P3HA is required, such as for medical applications, it is preferable to reduce the impurities as much as possible.
• An example of the degree of purification is the amount of protein in the aqueous suspension of P3HA.
• the amount of protein is preferably 30,000 ppm or less per weight of P3HA, more preferably 15,000 ppm or less, even more preferably 10,000 ppm or less, and most preferably 7,500 ppm or less.
• the purification means there are no particular limitations on the purification means, and for example, the above-mentioned known methods can be applied.
• the aqueous medium constituting the P3HA aqueous suspension may be water or a mixed solvent of water and a water-compatible organic solvent.
• the concentration of the water-compatible organic solvent is not particularly limited as long as it is equal to or lower than the solubility in water of the organic solvent used.
• the water-compatible organic solvent is not particularly limited, but the organic solvents described below can be used as appropriate.
• the aqueous medium constituting the P3HA aqueous suspension may contain other solvents, components derived from bacteria, compounds generated during purification, etc., as long as they do not impair the effects of the invention.
• the water content in the entire aqueous medium constituting the P3HA aqueous suspension is not particularly limited, but is preferably 5% by weight or more, more preferably 10% by weight or more, even more preferably 30% by weight or more, even more preferably 50% by weight or more, particularly preferably 70% by weight or more, and most preferably 90% by weight or more. There is no particular upper limit, and it may be 100% by weight or less.
• the P3HA aqueous suspension before being subjected to step (a) usually has a pH of more than 8 by undergoing the above purification step. Therefore, the P3HA aqueous suspension obtained in step (a1) may have a pH of more than 8. Therefore, it is preferable to adjust the pH of the P3HA aqueous suspension to 8 or less in step (a2).
• the adjustment method is not particularly limited, and examples thereof include a method of adding an acid.
• the acid is not particularly limited, and may be either an organic acid or an inorganic acid, whether or not it is volatile. More specifically, examples of the acid that can be used include sulfuric acid, hydrochloric acid, phosphoric acid, and acetic acid.
• the upper limit of the pH of the P3HA aqueous suspension adjusted in the adjustment step is preferably 8 or less.
• the pH of the P3HA aqueous suspension is more preferably 7 or less, even more preferably 6 or less, even more preferably 5 or less, and particularly preferably 4 or less.
• the lower limit of the pH is preferably 1 or more, more preferably 2 or more, and even more preferably 3 or more.
• the concentration of P3HA in the P3HA aqueous suspension obtained by step (a) is preferably 30% by weight or more, more preferably 40% by weight or more, and even more preferably 50% by weight or more, because this is economically advantageous in terms of drying utility and improves productivity.
• the upper limit of the P3HA concentration is preferably 65% by weight or less, more preferably 60% by weight or less, in order to avoid the possibility that P3HA reaches close packing and sufficient fluidity cannot be ensured.
• the method of adjusting the P3HA concentration is not particularly limited, and examples include methods of adding an aqueous medium and removing a part of the aqueous medium (for example, by removing the supernatant after centrifugation). The adjustment of the P3HA concentration may be performed at any stage of step (a) or may be performed before step (a).
• step (b) the aqueous suspension prepared in step (a) (i.e., the aqueous suspension containing P3HA and PVA) is spray-dried.
• the spray-drying method include a method in which the aqueous suspension is supplied in the form of fine droplets into a dryer and dried while contacting with hot air in the dryer.
• the method of supplying the aqueous suspension in the form of fine droplets into the dryer (atomizer) is not particularly limited, and includes known methods such as a method using a rotating disk and a method using a nozzle.
• the contact method between the droplets and hot air in the dryer is not particularly limited, and includes a parallel flow method, a counterflow method, and a method using both of these.
• the drying temperature during spray drying in step (b) may be any temperature that can remove most of the aqueous medium from the droplets of the aqueous suspension. It can be set appropriately under conditions that can dry to the desired moisture content and minimize deterioration in quality (reduction in molecular weight, loss of color, etc.) and melting.
• the temperature of the hot air blown into the spray dryer can be selected appropriately in the range of 100 to 300°C.
• the volume of hot air in the dryer can also be set appropriately depending on, for example, the size of the dryer.
• Aqueous suspension of P3HA powder Another embodiment of the present invention relates to an aqueous suspension (hereinafter also referred to as an aqueous suspension of P3HA powder) containing the above-mentioned P3HA powder (powder containing P3HA and PVA) and an aqueous medium.
• the P3HA powder exists in a dispersed state in the aqueous medium.
• the aqueous medium contained in the aqueous suspension of P3HA powder may be water or a mixed solvent of water and an organic solvent compatible with water.
• concentration of the water-compatible organic solvent in the mixed solvent is not particularly limited as long as it is equal to or lower than the solubility in water of the organic solvent used.
• the organic solvent compatible with water is not particularly limited, but examples thereof include alcohols such as methanol, ethanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, iso-butanol, pentanol, hexanol, and heptanol; ketones such as acetone and methyl ethyl ketone; ethers such as tetrahydrofuran and dioxane; nitriles such as acetonitrile and propionitrile; amides such as dimethylformamide and acetamide; dimethyl sulfoxide, pyridine, and piperidine.
• alcohols such as methanol, ethanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, iso-butanol, pentanol, hexanol, and heptanol
• ketones such as acetone and methyl ethyl ketone
• methanol, ethanol, 1-propanol, 2-propanol, 1-butanol, 2-butanol, iso-butanol, acetone, methyl ethyl ketone, tetrahydrofuran, dioxane, acetonitrile, propionitrile, etc. are preferred because they are easy to remove.
• methanol, ethanol, 1-propanol, 2-propanol, butanol, acetone, etc. are more preferred because they are easily available.
• methanol, ethanol, and acetone are particularly preferred.
• the water content in the entire aqueous medium constituting the aqueous suspension of P3HA powder is not particularly limited, but is preferably 5% by weight or more, more preferably 10% by weight or more, even more preferably 30% by weight or more, even more preferably 50% by weight or more, particularly preferably 70% by weight or more, and most preferably 90% by weight or more. There is no particular upper limit, and it may be 100% by weight or less.
• the content of P3HA powder in the aqueous suspension of P3HA powder is preferably 20% by weight or more, since dripping after application of the aqueous suspension can be further suppressed and drying properties after application can be improved.
• the concentration of the P3HA powder is more preferably 30% by weight or more, even more preferably 35% by weight or more, even more preferably 40% by weight or more, and particularly preferably 45% by weight or more.
• the upper limit of the concentration of the P3HA powder is preferably 65% by weight or less, more preferably 60% by weight or less, and even more preferably 55% by weight or less, in order to avoid the possibility that the P3HA powder reaches close packing and sufficient fluidity cannot be secured.
• the aqueous suspension of P3HA powder preferably has a pH of 3 or more and 8 or less.
• the pH is within the above range, dripping of the suspension after application can be further suppressed, and discoloration and molecular weight reduction of P3HA due to heating can be suppressed.
• the upper limit is more preferably 7 or less, even more preferably 6 or less, particularly preferably 5 or less, and most preferably 4 or less.
• the lower limit is more preferably 4 or more, even more preferably 5 or more, and particularly preferably 6 or more.
• the aqueous suspension of P3HA powder may contain one or more of the following, provided that the effects of the invention are not impaired: dispersants or emulsifiers, pH adjusters, inorganic fillers, colorants such as pigments and dyes, odor absorbers such as activated carbon and zeolite, fragrances such as vanillin and dextrin, plasticizers, antioxidants, weather resistance improvers, ultraviolet absorbers, crystal nucleating agents, lubricants, release agents, water repellents, antibacterial agents, sliding property improvers, and the like. Furthermore, the aqueous suspension of P3HA powder may contain various components resulting from the process of the production method described below, as long as the effects of the invention are not impaired.
• the main components are the P3HA powder and the aqueous medium described above.
• the proportion of P3HA powder in the total solid content of the aqueous suspension of P3HA powder may usually be 60-100% by weight, 80-100% by weight, 90-100% by weight, 95-100% by weight, or 99-100% by weight.
• the upper limit may be 99% by weight or less, or 95% by weight or less.
• volume median diameter of the P3HA powder in an aqueous suspension of P3HA powder is preferably 50 times or less than the volume median diameter of the primary particles of the P3HA powder (hereinafter also referred to as "primary particle diameter").
• volume median diameter of the P3HA powder in an aqueous suspension of P3HA powder is 50 times or less than the volume median diameter of the primary particle diameter, the aqueous suspension of P3HA powder exhibits better fluidity, and therefore tends to have better coatability to a substrate.
• the volume median diameter of the P3HA powder is more preferably 20 times or less than the volume median diameter of the primary particle diameter, and even more preferably 10 times or less.
• the volume median diameter of the P3HA powder in the aqueous suspension is preferably 0.5 to 5.0 ⁇ m, more preferably 1.0 to 4.5 ⁇ m, and even more preferably 1.0 to 4.0 ⁇ m, from the viewpoint of achieving excellent fluidity.
• the volume median diameter of the P3HA powder in the aqueous suspension is measured by the method described in the Examples using a HORIBA laser diffraction/scattering particle size distribution measuring device LA-950.
• the volume median diameter of the P3HA powder in the aqueous suspension can be used as an index of the dispersion state of P3HA in the aqueous suspension of P3HA powder.
• the method for adjusting the volume median diameter of the P3HA powder is not particularly limited, and known means (e.g., stirring) can be applied.
• an aqueous suspension of P3HA powder whose dispersion state has been destroyed by exposure to acidic conditions can be subjected to physical, chemical, biological, or other treatments that a person skilled in the art can consider, thereby restoring the P3HA powder in the aqueous suspension of P3HA powder to a dispersed state again (e.g., a state having the primary particle diameter of the P3HA powder described above).
• the aqueous suspension of P3HA powder according to this embodiment can be produced by dispersing the above-mentioned P3HA powder in an aqueous medium. Since P3HA powder with good dispersibility is used, the aqueous suspension according to this embodiment has good productivity and can suppress dripping during heating and drying after being applied to a substrate as a coating liquid.
• aqueous suspension of P3HA powder there are no particular limitations on the method for producing an aqueous suspension of P3HA powder, but it is preferable to disperse the P3HA powder in an aqueous medium, and then apply mechanical shear to separate the partially aggregated P3HA powder from each other. Applying mechanical shear is preferable in that it is possible to substantially eliminate aggregates and obtain an aqueous suspension containing P3HA powder with a uniform particle size.
• a shear crusher, agitator, homogenizer, ultrasonic waves, etc. can be used to apply mechanical shear.
• the pH of the resulting aqueous suspension may be adjusted.
• the pH of the aqueous medium may be adjusted before dispersing the P3HA powder in the aqueous medium.
• the method for adjusting the pH is not particularly limited, and examples thereof include a method of adding an acid.
• the acid is not particularly limited, and may be either an organic acid or an inorganic acid, whether or not it is volatile. More specifically, examples of acids that can be used include sulfuric acid, hydrochloric acid, phosphoric acid, and acetic acid.
• the aqueous suspension of P3HA powder according to this embodiment can be suitably used as an aqueous coating liquid for applying to a substrate and drying to form a resin film.
• the application is not limited to this, and the aqueous suspension of P3HA powder according to this embodiment can also be used as an impregnation processing raw material, a composite material raw material, a building material, a plastic modifier, and an adhesive.
• the aqueous suspension of P3HA powder according to this embodiment is applied to one or both sides of a substrate, followed by heating and drying to form a resin layer containing P3HA and PVA on the substrate, thereby producing a laminate.
• a method for producing a laminate and the resulting laminate also constitute aspects of the present invention.
• the substrate is not particularly limited, and substrates made of various materials can be used, but from the viewpoint of increasing the biodegradability of the entire laminate obtained, it is preferable that the substrate is biodegradable.
• the biodegradable substrate is not particularly limited, but examples thereof include paper (mainly composed of cellulose), cellophane, cellulose esters; polyvinyl alcohol, polyamino acids, polyglycolic acid, pullulan; wood, etc. Paper or cellophane is preferred, and paper is particularly preferred, because it has excellent heat resistance and is inexpensive.
• the type of paper is also not particularly limited, and examples thereof include cup base paper, kraft paper, fine paper, coated paper, tissue paper, glassine paper, and cardboard.
• the paper may contain additives such as water-resistant agents, water-repellents, and inorganic substances, as necessary.
• the substrate may be previously subjected to a surface treatment such as corona treatment, frame treatment, anchor coat treatment, etc. These surface treatments may be performed alone or in combination with a plurality of surface treatments.
• the method for applying the aqueous suspension of the P3HA powder to the substrate is not particularly limited, and any known method capable of forming a resin layer on the substrate can be used as appropriate. Specifically, the spraying method, scattering method, slit coater method, air knife coater method, roll coater method, bar coater method, comma coater method, blade coater method, screen printing method, gravure printing method, etc. can be used. Before applying the aqueous suspension, a step of performing a surface treatment such as corona treatment on the substrate may be carried out.
• the drying process after coating can be carried out using a known heating method. Examples include hot air heating, infrared heating, ultrasonic irradiation, microwave heating, roll heating, and hot plate heating. These can be used alone or in combination of two or more types. Conventionally, during such drying processes, dripping of the coating film was likely to occur, which could hinder the formation of a uniform resin film. However, by using the aqueous suspension of P3HA powder according to this embodiment, such dripping can be suppressed and a highly uniform resin film can be formed.
• the resin layer may be heated to a temperature at which the main resin component P3HA contained in the resin layer can melt, forming a film. This causes the P3HA in the resin layer to melt once and then cool and solidify, making the surface of the resin layer smooth and improving the adhesion between the base layer and the resin layer.
• the heating temperature in the drying process after application is preferably 130°C to 180°C.
• the heating time may be, for example, 10 seconds to 10 minutes.
• the above-mentioned coating and drying steps can be carried out in a batch manner, or can be carried out continuously while transporting the film-like substrate between multiple rolls.
• the weight per unit of P3HA in the resin layer (hereinafter also referred to as basis weight) is not particularly limited, but may be, for example, about 5 to 100 g/m 2.
• basis weight is within this range, defects such as pinholes can be prevented, the resin layer can have a strength sufficient for use, and functions such as water resistance can be efficiently exhibited.
• the thickness of the resin layer is not particularly limited, but may be about 5 to 100 ⁇ m from the viewpoint of preventing water absorption and ensuring flexibility.
• the laminate according to this embodiment includes at least a substrate layer and a P3HA- and PVA-containing resin layer provided on one or both sides of the substrate layer.
• the laminate may be composed of only these layers, or may include other layers in addition to these layers.
• Such other layers include a gas barrier layer, a printed layer, and other resin layers.
• the gas barrier layer may be a known layer, such as a metal foil, a metal vapor deposition film, a metal oxide vapor deposition film, a silicon oxide vapor deposition film, a polyvinyl alcohol film, and an ethylene-vinyl alcohol copolymer film.
• the gas barrier layer may be bonded to the substrate via an adhesive layer.
• the laminate according to this embodiment can be made into various molded articles by secondary processing.
• molded articles include tubes, plates, rods, packaging materials (e.g., bags), containers (e.g., bottle containers), and parts.
• packaging materials e.g., bags
• containers e.g., bottle containers
• the molded articles can be suitably used as various packaging container materials such as shopping bags, various bags, food and confectionery packaging materials, cups, trays, and cartons in various fields such as food, cosmetics, electronics, medicine, and pharmaceuticals.
• the molded articles can be suitably used as containers for holding liquids, particularly as containers for hot contents such as food and beverage cups for instant noodles, instant soup, coffee, etc., trays for prepared foods, bento boxes, and microwave foods, etc.
• the secondary processing can be carried out by any method known in the technical field, such as various bag making machines, filling and packaging machines, etc. Processing can also be carried out by using devices such as paper cup forming machines, punching machines, and box making machines. In these processing machines, known techniques can be used for bonding the laminate, such as heat sealing, impulse sealing, ultrasonic sealing, high frequency sealing, hot air sealing, and frame sealing. In particular, it is preferable that the molded body is one that has been secondary processed using a heat sealing method. The heat sealing may be carried out between the base layer and the resin layer, or between the resin layers.
• the molded article can also be composited with another molded article made of a material different from the molded article (e.g., fiber, thread, rope, woven fabric, knitted fabric, nonwoven fabric, paper, film, sheet, tube, plate, rod, container, bag, part, foam, etc.) in order to improve its physical properties.
• a material different from the molded article e.g., fiber, thread, rope, woven fabric, knitted fabric, nonwoven fabric, paper, film, sheet, tube, plate, rod, container, bag, part, foam, etc.
• These materials are also preferably biodegradable.
• a poly(3-hydroxyalkanoate)-based powder containing a poly(3-hydroxyalkanoate)-based resin and polyvinyl alcohol The polyvinyl alcohol has a saponification degree of 50 to 79 mol %, The viscosity of a 4% by weight aqueous solution of the polyvinyl alcohol at 20°C is 2 to 20 mPa s, The poly(3-hydroxyalkanoate) powder has a polyvinyl alcohol content of 2 to 10 parts by weight based on 100 parts by weight of the poly(3-hydroxyalkanoate) resin.
• the poly(3-hydroxyalkanoate)-based resin comprises a copolymer of 3-hydroxybutyrate units and other hydroxyalkanoate units.
• the poly(3-hydroxyalkanoate)-based resin comprises a copolymer of 3-hydroxybutyrate units and other hydroxyalkanoate units.
• a method for producing an aqueous suspension comprising a step of dispersing the poly(3-hydroxyalkanoate) powder according to any one of items 1 to 4 in an aqueous medium.
• An aqueous suspension comprising a poly(3-hydroxyalkanoate) powder and an aqueous medium, the poly(3-hydroxyalkanoate)-based powder contains a poly(3-hydroxyalkanoate)-based resin and polyvinyl alcohol;
• the polyvinyl alcohol has a saponification degree of 50 to 79 mol %,
• the viscosity of a 4% by weight aqueous solution of the polyvinyl alcohol at 20°C is 2 to 20 mPa s,
• the aqueous suspension has a polyvinyl alcohol content of 2 to 10 parts by weight based on 100 parts by weight of the poly(3-hydroxyalkanoate) resin.
• a method for producing a laminate comprising: applying the aqueous suspension according to any one of items 6 to 9 to at least one surface of a substrate, and drying the applied aqueous suspension by heating to form a resin layer on the substrate.
• a laminate including a base layer and a resin layer provided on at least one surface of the base layer, the resin layer contains a poly(3-hydroxyalkanoate)-based resin and polyvinyl alcohol;
• the polyvinyl alcohol has a saponification degree of 50 to 79 mol %,
• the viscosity of a 4% by weight aqueous solution of the polyvinyl alcohol at 20°C is 2 to 20 mPa s
• the laminate has a content of the polyvinyl alcohol of 2 to 10 parts by weight based on 100 parts by weight of the poly(3-hydroxyalkanoate) resin.
• the viscosity of the aqueous suspension was measured using a modular compact rheometer (Anton Paar) with a Peltier element temperature control system for a coaxial double cylinder at a shear rate range of 10 s -1 to 100 s -1 and at temperatures of 25°C, 40°C, and 50°C.
• An aqueous suspension with a Bingham yield value of zero means that the suspension can flow without the application of force, and is an indicator of good powder dispersibility in the aqueous suspension and good applicability of the aqueous suspension.
• an aqueous suspension with a positive Bingham yield value means that force must be applied to make the suspension flow, and is an indicator of how unlikely it is to drip after application.
• the spray-dried stock solution before spray drying was diluted with ion-exchanged water to a solid content concentration of 5 wt % to obtain a dispersion for measurement.
• the dispersion for measurement was introduced into a laser diffraction/scattering type particle size distribution measuring device LA-950 (Horiba, Ltd.) and measurement was performed.
• the obtained volume median diameter (particle size D50) was used as the measured value of the primary particle diameter of the P3HA powder.
• Method for measuring the average particle size of P3HA powder 0.2 g of the powder to be measured was added and dispersed in 20 mL of ion-exchanged water to obtain a dispersion for measurement.
• the dispersion for measurement was introduced into a laser diffraction/scattering type particle size distribution measuring device LA-950 (Horiba, Ltd.) and measurement was performed.
• the obtained volume median diameter (particle size D50) was taken as the measured value of the average particle size of the P3HA powder.
• the aqueous suspension of P3HA powder was diluted with ion-exchanged water to a solids concentration of 5 wt %, to obtain a dispersion for measurement.
• the dispersion for measurement was introduced into a laser diffraction/scattering type particle size distribution measuring device LA-950 (Horiba, Ltd.), and measurements were performed.
• the obtained volume median diameter (particle size D50) was used as the measured value of the volume median diameter of the P3HA powder in the aqueous suspension.
• Example 1 preparation of bacterial culture solution
• the cells were cultured in the same manner as in Comparative Example 3 of WO 2019/142717 to obtain a bacterial cell culture solution containing P3HA-containing bacterial cells.
• the composition ratio of the repeating units of P3HA was measured to be 89.9/10.1 (mol/mol).
• the sterilized culture solution (inactivated culture solution) obtained above was added with 30% sodium hydroxide to adjust the pH to 10.0 ⁇ 1.0, and the internal temperature was set to 70 ⁇ 2° C., and the molecular weight of P3HA in the cells was adjusted for 19 hours.
• the weight average molecular weight was 250,000.
• the enzyme-treated solution was centrifuged (4500 rpm, 10 minutes), and the supernatant was removed to concentrate it twice.
• an aqueous sodium hydroxide solution pH 11.0 in an amount equal to the amount of the removed supernatant was added, followed by centrifugation (4500 rpm, 10 minutes), and the supernatant was removed. This process was carried out again.
• the volume median diameter (particle size D50) of P3HA measured for the aqueous suspension obtained (spray-dried raw solution) was 3.3 ⁇ m.
• the volume median diameter corresponds to the primary particle diameter of the P3HA powder.
• the weight average molecular weight of P3HA was 220,000.
• the P3HA aqueous suspension thus obtained was sent to an atomizer using an OC-16 general-purpose spray dryer manufactured by Okawara Kakoki Co., Ltd., and spray-dried (hot air temperature: 110°C, exhaust air temperature: 63°C).
• a P3HA powder containing 100 parts by weight of P3HA and 3 parts by weight of PVA was obtained.
• the primary particle diameter of the P3HA powder was 3.3 ⁇ m, while the average particle diameter (D50) of the P3HA powder was 74.1 ⁇ m.
• the P3HA powder obtained above was mixed with distilled water in a weight ratio of 1:1. Then, using a high shear crusher (Primix Corporation homomixer model MARKII type), crushing was performed for 5 minutes at a shear rate of 22,000 s -1 to obtain an aqueous suspension of P3HA powder with a solid content concentration of 50% by weight.
• the volume median diameter (particle size D50) of the P3HA powder in the aqueous suspension obtained by this redispersion treatment was 3.2 ⁇ m.
• the pH of the aqueous suspension was 4.
• the viscosity of the obtained aqueous suspension was measured based on the above method, and the Bingham yield value was calculated. The results are shown in Table 1.
• Example 2 A P3HA powder was obtained in the same manner as in Example 1, except that a product name: Kuraray Poval L-9 (saponification degree: 71 mol %, viscosity of a 4 wt % aqueous solution at 20° C.: 5.8 mPa ⁇ s) was used as the PVA, and then an aqueous suspension of the P3HA powder was obtained and the Bingham yield value was calculated. The results are shown in Table 1.
• Example 3 A P3HA powder was obtained in the same manner as in Example 1, except that a PVA product named KURARAY POVAL L-11 (saponification degree: 72.5 mol %, viscosity of a 4 wt % aqueous solution at 20° C.: 6.5 mPa ⁇ s) was used, and then an aqueous suspension of the P3HA powder was obtained and the Bingham yield value was calculated. The results are shown in Table 1.
• Example 4 A P3HA powder was obtained in the same manner as in Example 1, except that a PVA product named Nippon Vinyl Acetate JR-05 (saponification degree: 72 mol %, viscosity of a 4 wt % aqueous solution at 20° C.: 5.5 mPa ⁇ s) was used, and then an aqueous suspension of the P3HA powder was obtained and the Bingham yield value was calculated. The results are shown in Table 1.
• Example 5 A P3HA powder was obtained in the same manner as in Example 1, except that a product name: Mitsubishi Chemical NK-05R (saponification degree: 73 mol %, viscosity of a 4 wt % aqueous solution at 20° C.: 5 mPa ⁇ s) was used as the PVA, and then an aqueous suspension of the P3HA powder was obtained and the Bingham yield value was calculated. The results are shown in Table 1.
• Example 1 A P3HA powder was obtained in the same manner as in Example 1, except that a product name: Kuraray Poval 5-88 (saponification degree: 87.8 mol%, viscosity of 4 wt% aqueous solution at 20°C: 5 mPa ⁇ s) was used as the PVA and the processing time of the high shear crusher was changed to 10 minutes, and then an aqueous suspension of the P3HA powder was obtained and the Bingham yield value was calculated.
• the primary particle size of the P3HA powder was 3.2 ⁇ m
• the average particle size (D50) of the P3HA powder was 84.1 ⁇ m
• the volume median diameter of the P3HA powder in the aqueous suspension after redispersion was 3.1 ⁇ m. The results are shown in Table 1.
• Example 2 A P3HA powder was obtained in the same manner as in Example 1, except that a PVA product named KURARAY POVAL 22-88 (saponification degree: 88 mol %, viscosity of 4 wt % aqueous solution at 20° C.: 22.5 mPa ⁇ s) was used and the processing time in the high shear crusher was changed to 10 minutes, and then an aqueous suspension of the P3HA powder was obtained and the Bingham yield value was calculated. The results are shown in Table 1.
• Comparative Example 3 A P3HA powder was obtained in the same manner as in Example 1, except that a product name: Kuraray Poval 5-82 (saponification degree: 81.5 mol %, viscosity of a 4 wt % aqueous solution at 20° C.: 4.85 mPa ⁇ s) was used as the PVA, and then an aqueous suspension of the P3HA powder was obtained and the Bingham yield value was calculated. The results are shown in Table 1.
• Comparative Example 4 A P3HA powder was obtained in the same manner as in Example 1, except that a product name: Kuraray Poval 3-80 (saponification degree: 80 mol %, viscosity of a 4 wt % aqueous solution at 20° C.: 3.05 mPa ⁇ s) was used as the PVA, and then an aqueous suspension of the P3HA powder was obtained and the Bingham yield value was calculated. The results are shown in Table 1.
• Example 5 A P3HA powder was obtained in the same manner as in Example 1, except that a PVA product named KURARAY POVAL 35-80 (saponification degree: 80 mol %, viscosity of 4 wt % aqueous solution at 20° C.: 32.4 mPa ⁇ s) was used and the processing time of the high shear crusher was changed to 10 minutes. Then, an aqueous suspension of the P3HA powder was obtained and the Bingham yield value was calculated. The results are shown in Table 1.
• Example 6 A P3HA powder was obtained in the same manner as in Example 1, except that a PVA product with a trade name of KURARAY POVAL 40-80E (saponification degree: 80 mol %, viscosity of a 4 wt % aqueous solution at 20° C.: 41 mPa ⁇ s) was used and the processing time in the high shear crusher was changed to 10 minutes, and then an aqueous suspension of the P3HA powder was obtained and the Bingham yield value was calculated. The results are shown in Table 1.
• Comparative Example 7 A P3HA powder was obtained in the same manner as in Example 1, except that a PVA product with a trade name of Nippon Vinyl Acetate JR-25E (saponification degree: 79.5 mol %, viscosity of a 4 wt % aqueous solution at 20° C.: 48 mPa ⁇ s) was used as the PVA and the processing time in the high shear crusher was changed to 10 minutes. Then, an aqueous suspension of the P3HA powder was obtained and the Bingham yield value was calculated. The results are shown in Table 1.
• Examples 1 to 5 use PVA with a degree of saponification of 50 to 79 mol % and a viscosity of a 4 wt % aqueous solution at 20°C in the range of 2 to 20 mPa ⁇ s.
• the Bingham yield value was 0.0 Pa at 25°C, while it showed a large positive value at 40°C or 50°C. From this, it can be understood that the dispersibility of the P3HA powder and the coatability of the aqueous suspension are good at 25°C, but the viscosity of the aqueous suspension increases upon heating, making it difficult for dripping to occur during heating and drying after application.
• Example 6 The preparation process of the bacterial culture solution was carried out in the same manner as in Comparative Example 1 of WO 2019/142845, and P3HB3HH (the composition ratio of 3HB unit / 3HH unit was 96.6 / 3.4 (mol / mol), the adjustment time in the molecular weight adjustment process was 16 hours, and the weight average molecular weight was 710,000) was used. Except for this, P3HA powder was obtained in the same manner as in Example 1, and then an aqueous suspension of P3HA powder was obtained to calculate the Bingham yield value.
• the primary particle size of the P3HA powder was 3.5 ⁇ m, the average particle size (D50) of the P3HA powder was 74.4 ⁇ m, and the volume median diameter of the P3HA powder in the aqueous suspension after redispersion was 3.2 ⁇ m.
• the results are shown in Table 2.
• Example 7 The preparation process of the bacterial culture solution was carried out in the same manner as in Example 20 of WO 2019/142717, and P3HB3HH (the composition ratio of 3HB unit / 3HH unit was 94.9 / 5.1 (mol / mol), the adjustment time in the molecular weight adjustment process was 11 hours, and the weight average molecular weight was 450,000) was used. Except for this, a P3HA powder was obtained in the same manner as in Example 1, and then an aqueous suspension of the P3HA powder was obtained to calculate the Bingham yield value.
• the primary particle size of the P3HA powder was 3.5 ⁇ m, the average particle size of the P3HA powder was 70.4 ⁇ m, and the volume median diameter of the P3HA powder in the aqueous suspension after redispersion was 3.6 ⁇ m.
• the results are shown in Table 2.
• Table 2 shows that in Examples 6 and 7, similar results to those in Example 1 were obtained, regardless of the difference in the 3HH unit ratio in P3HB3HH.
• Example 8 P3HB3HH (composition ratio of 3HB unit/3HH unit is 89.9/10.1 (mol/mol), weight average molecular weight is 560,000) obtained in the same manner as in Example 1 was used except that the adjustment time in the molecular weight adjustment step was 11 hours, and the processing time of the high shear crusher was changed to 10 minutes.
• P3HA powder was obtained in the same manner as in Example 1, and then an aqueous suspension of P3HA powder was obtained to calculate the Bingham yield value.
• the primary particle size of the P3HA powder was 2.7 ⁇ m, the average particle size of the P3HA powder was 73.4 ⁇ m, and the volume median diameter of the P3HA powder in the aqueous suspension after redispersion was 2.6 ⁇ m.
• Table 3 The results are shown in Table 3.
• Example 9 P3HB3HH (composition ratio of 3HB unit/3HH unit is 89.9/10.1 (mol/mol), weight average molecular weight is 760,000) obtained in the same manner as in Example 1 except that the adjustment time in the molecular weight adjustment step was 10 hours was used, and the processing time of the high shear crusher was changed to 10 minutes.
• P3HA powder was obtained in the same manner as in Example 1, and then an aqueous suspension of P3HA powder was obtained to calculate the Bingham yield value.
• the primary particle size of the P3HA powder was 2.7 ⁇ m, the average particle size of the P3HA powder was 68.9 ⁇ m, and the volume median diameter (particle size D50) of the P3HA powder in the aqueous suspension after redispersion was 2.9 ⁇ m.
• the results are shown in Table 3.
• Table 3 shows that in Examples 8 and 9, the same results as in Example 1 were obtained, regardless of the difference in the weight average molecular weight of P3HB3HH.
• Example 10 to 12 Comparative Examples 8 and 9
• a P3HA powder was obtained in the same manner as in Example 1, except that the amount of PVA was changed according to the description in Table 4, and then an aqueous suspension of the P3HA powder was obtained and the Bingham yield value was calculated.
• the primary particle size of the P3HA powder, the average particle size of the P3HA powder, and the volume median diameter of the P3HA powder in the aqueous suspension after redispersion were also measured. The results are shown in Table 4.
• Examples 13 to 15 P3HA powder was obtained in the same manner as in Example 1, except that the solids concentration in the aqueous suspension of P3HA powder (the proportion of P3HA powder in the aqueous suspension) was changed according to the description in Table 5 by changing the mixing ratio of P3HA powder and distilled water, and then an aqueous suspension of P3HA powder was obtained and the Bingham yield value was calculated. The results are shown in Table 5.
• Table 5 shows that in Examples 13 to 15, results similar to those of Example 1 were obtained, regardless of differences in the solids concentration in the aqueous suspension of P3HA powder.
• Example 16 to 19 A P3HA powder was obtained in the same manner as in Example 1, except that the amount of sulfuric acid added before spray drying was adjusted to change the pH of the P3HA aqueous suspension according to the description in Table 6. Then, an aqueous suspension of the P3HA powder was obtained and the Bingham yield value was calculated. The results are shown in Table 6. In this embodiment, the pH of the aqueous suspension of P3HA powder is substantially the same as the pH of the aqueous suspension of P3HA.

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