WO2009099201A1 - コアシェル型酸化亜鉛微粒子又はそれを含有する分散液、それらの製造方法及び用途 - Google Patents
コアシェル型酸化亜鉛微粒子又はそれを含有する分散液、それらの製造方法及び用途 Download PDFInfo
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- WO2009099201A1 WO2009099201A1 PCT/JP2009/052087 JP2009052087W WO2009099201A1 WO 2009099201 A1 WO2009099201 A1 WO 2009099201A1 JP 2009052087 W JP2009052087 W JP 2009052087W WO 2009099201 A1 WO2009099201 A1 WO 2009099201A1
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- Prior art keywords
- zinc oxide
- core
- oxide fine
- shell type
- fine particles
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- XLOMVQKBTHCTTD-UHFFFAOYSA-N Zinc monoxide Chemical compound [Zn]=O XLOMVQKBTHCTTD-UHFFFAOYSA-N 0.000 title claims abstract description 374
- 239000011787 zinc oxide Substances 0.000 title claims abstract description 187
- 239000011258 core-shell material Substances 0.000 title claims abstract description 100
- 239000006185 dispersion Substances 0.000 title claims abstract description 79
- 238000004519 manufacturing process Methods 0.000 title claims description 26
- 239000011859 microparticle Substances 0.000 title abstract 15
- 229920000642 polymer Polymers 0.000 claims abstract description 81
- 239000002245 particle Substances 0.000 claims abstract description 56
- 239000000843 powder Substances 0.000 claims abstract description 47
- 238000010992 reflux Methods 0.000 claims abstract description 30
- 239000011163 secondary particle Substances 0.000 claims abstract description 29
- 239000003960 organic solvent Substances 0.000 claims abstract description 19
- 238000010438 heat treatment Methods 0.000 claims abstract description 17
- 239000000203 mixture Substances 0.000 claims abstract description 16
- 150000003751 zinc Chemical class 0.000 claims abstract description 9
- ZOIORXHNWRGPMV-UHFFFAOYSA-N acetic acid;zinc Chemical group [Zn].CC(O)=O.CC(O)=O ZOIORXHNWRGPMV-UHFFFAOYSA-N 0.000 claims abstract description 8
- 239000004246 zinc acetate Substances 0.000 claims abstract description 8
- 230000000694 effects Effects 0.000 claims abstract description 7
- 239000002537 cosmetic Substances 0.000 claims abstract description 5
- 239000000835 fiber Substances 0.000 claims abstract description 4
- 238000002156 mixing Methods 0.000 claims abstract description 4
- 239000011347 resin Substances 0.000 claims abstract description 4
- 229920005989 resin Polymers 0.000 claims abstract description 4
- 239000010419 fine particle Substances 0.000 claims description 199
- 229920000036 polyvinylpyrrolidone Polymers 0.000 claims description 41
- 239000001267 polyvinylpyrrolidone Substances 0.000 claims description 41
- 235000013855 polyvinylpyrrolidone Nutrition 0.000 claims description 41
- 239000002612 dispersion medium Substances 0.000 claims description 38
- 239000011164 primary particle Substances 0.000 claims description 28
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 claims description 25
- 229920002153 Hydroxypropyl cellulose Polymers 0.000 claims description 20
- 239000001863 hydroxypropyl cellulose Substances 0.000 claims description 20
- 235000010977 hydroxypropyl cellulose Nutrition 0.000 claims description 20
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 18
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 239000002202 Polyethylene glycol Substances 0.000 claims description 12
- 229920001223 polyethylene glycol Polymers 0.000 claims description 12
- 238000009835 boiling Methods 0.000 claims description 9
- 239000002270 dispersing agent Substances 0.000 claims description 6
- WUOACPNHFRMFPN-UHFFFAOYSA-N alpha-terpineol Chemical compound CC1=CCC(C(C)(C)O)CC1 WUOACPNHFRMFPN-UHFFFAOYSA-N 0.000 claims description 3
- SQIFACVGCPWBQZ-UHFFFAOYSA-N delta-terpineol Natural products CC(C)(O)C1CCC(=C)CC1 SQIFACVGCPWBQZ-UHFFFAOYSA-N 0.000 claims description 3
- 239000011259 mixed solution Substances 0.000 claims description 3
- 229940116411 terpineol Drugs 0.000 claims description 3
- 238000004132 cross linking Methods 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 19
- 230000008569 process Effects 0.000 abstract description 4
- 238000001556 precipitation Methods 0.000 abstract 1
- 230000000052 comparative effect Effects 0.000 description 27
- 230000002776 aggregation Effects 0.000 description 14
- 239000007788 liquid Substances 0.000 description 14
- 238000002474 experimental method Methods 0.000 description 12
- 239000002105 nanoparticle Substances 0.000 description 12
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- 238000004220 aggregation Methods 0.000 description 9
- 239000003795 chemical substances by application Substances 0.000 description 8
- 238000002296 dynamic light scattering Methods 0.000 description 8
- 238000002329 infrared spectrum Methods 0.000 description 7
- 229910044991 metal oxide Inorganic materials 0.000 description 7
- 150000004706 metal oxides Chemical class 0.000 description 7
- 238000010521 absorption reaction Methods 0.000 description 6
- YZYKBQUWMPUVEN-UHFFFAOYSA-N zafuleptine Chemical compound OC(=O)CCCCCC(C(C)C)NCC1=CC=C(F)C=C1 YZYKBQUWMPUVEN-UHFFFAOYSA-N 0.000 description 6
- 238000005033 Fourier transform infrared spectroscopy Methods 0.000 description 5
- 238000005054 agglomeration Methods 0.000 description 5
- 230000015572 biosynthetic process Effects 0.000 description 5
- 239000003054 catalyst Substances 0.000 description 5
- 238000009826 distribution Methods 0.000 description 5
- 229920005862 polyol Polymers 0.000 description 5
- 150000003077 polyols Chemical class 0.000 description 5
- 238000001878 scanning electron micrograph Methods 0.000 description 5
- 239000002904 solvent Substances 0.000 description 5
- 239000011701 zinc Substances 0.000 description 5
- 239000000047 product Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000002131 composite material Substances 0.000 description 3
- 238000000151 deposition Methods 0.000 description 3
- 238000010304 firing Methods 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 229910021645 metal ion Inorganic materials 0.000 description 3
- 239000002244 precipitate Substances 0.000 description 3
- 229910052708 sodium Inorganic materials 0.000 description 3
- 239000011734 sodium Substances 0.000 description 3
- 239000012798 spherical particle Substances 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 2
- 239000003513 alkali Substances 0.000 description 2
- 238000004458 analytical method Methods 0.000 description 2
- 239000011324 bead Substances 0.000 description 2
- 239000002981 blocking agent Substances 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 230000008859 change Effects 0.000 description 2
- 239000011246 composite particle Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 238000012216 screening Methods 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 229910052725 zinc Inorganic materials 0.000 description 2
- 229910052688 Gadolinium Inorganic materials 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- PTFCDOFLOPIGGS-UHFFFAOYSA-N Zinc dication Chemical compound [Zn+2] PTFCDOFLOPIGGS-UHFFFAOYSA-N 0.000 description 1
- 150000001242 acetic acid derivatives Chemical class 0.000 description 1
- 150000004703 alkoxides Chemical class 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- -1 for example Polymers 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 229910052735 hafnium Inorganic materials 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 239000003999 initiator Substances 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 239000007791 liquid phase Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 229910052758 niobium Inorganic materials 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000008279 sol Substances 0.000 description 1
- 238000003980 solgel method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000007858 starting material Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000001629 suppression Effects 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 238000002411 thermogravimetry Methods 0.000 description 1
- 239000011882 ultra-fine particle Substances 0.000 description 1
- 229910052727 yttrium Inorganic materials 0.000 description 1
- 229910052984 zinc sulfide Inorganic materials 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Images
Classifications
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/19—Cosmetics or similar toiletry preparations characterised by the composition containing inorganic ingredients
- A61K8/27—Zinc; Compounds thereof
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/02—Cosmetics or similar toiletry preparations characterised by special physical form
- A61K8/0241—Containing particulates characterized by their shape and/or structure
- A61K8/0275—Containing agglomerated particulates
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/72—Cosmetics or similar toiletry preparations characterised by the composition containing organic macromolecular compounds
- A61K8/73—Polysaccharides
- A61K8/731—Cellulose; Quaternized cellulose derivatives
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
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- A61K8/00—Cosmetics or similar toiletry preparations
- A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
- A61K8/72—Cosmetics or similar toiletry preparations characterised by the composition containing organic macromolecular compounds
- A61K8/81—Cosmetics or similar toiletry preparations characterised by the composition containing organic macromolecular compounds obtained by reactions involving only carbon-to-carbon unsaturated bonds
- A61K8/817—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 a single or double bond to nitrogen or by a heterocyclic ring containing nitrogen; Compositions or derivatives of such polymers, e.g. vinylimidazol, vinylcaprolactame, allylamines (Polyquaternium 6)
- A61K8/8176—Homopolymers of N-vinyl-pyrrolidones. Compositions of derivatives of such polymers
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61Q—SPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
- A61Q17/00—Barrier preparations; Preparations brought into direct contact with the skin for affording protection against external influences, e.g. sunlight, X-rays or other harmful rays, corrosive materials, bacteria or insect stings
- A61Q17/04—Topical preparations for affording protection against sunlight or other radiation; Topical sun tanning preparations
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B82—NANOTECHNOLOGY
- B82Y—SPECIFIC USES OR APPLICATIONS OF NANOSTRUCTURES; MEASUREMENT OR ANALYSIS OF NANOSTRUCTURES; MANUFACTURE OR TREATMENT OF NANOSTRUCTURES
- B82Y30/00—Nanotechnology for materials or surface science, e.g. nanocomposites
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G9/00—Compounds of zinc
- C01G9/02—Oxides; Hydroxides
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C1/00—Treatment of specific inorganic materials other than fibrous fillers; Preparation of carbon black
- C09C1/04—Compounds of zinc
- C09C1/043—Zinc oxide
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- A61K2800/00—Properties of cosmetic compositions or active ingredients thereof or formulation aids used therein and process related aspects
- A61K2800/40—Chemical, physico-chemical or functional or structural properties of particular ingredients
- A61K2800/41—Particular ingredients further characterized by their size
- A61K2800/412—Microsized, i.e. having sizes between 0.1 and 100 microns
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- A61K2800/40—Chemical, physico-chemical or functional or structural properties of particular ingredients
- A61K2800/60—Particulates further characterized by their structure or composition
- A61K2800/61—Surface treated
- A61K2800/62—Coated
- A61K2800/624—Coated by macromolecular compounds
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2002/00—Crystal-structural characteristics
- C01P2002/70—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data
- C01P2002/72—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data by d-values or two theta-values, e.g. as X-ray diagram
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2002/00—Crystal-structural characteristics
- C01P2002/80—Crystal-structural characteristics defined by measured data other than those specified in group C01P2002/70
- C01P2002/82—Crystal-structural characteristics defined by measured data other than those specified in group C01P2002/70 by IR- or Raman-data
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2002/00—Crystal-structural characteristics
- C01P2002/80—Crystal-structural characteristics defined by measured data other than those specified in group C01P2002/70
- C01P2002/88—Crystal-structural characteristics defined by measured data other than those specified in group C01P2002/70 by thermal analysis data, e.g. TGA, DTA, DSC
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/01—Particle morphology depicted by an image
- C01P2004/03—Particle morphology depicted by an image obtained by SEM
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/01—Particle morphology depicted by an image
- C01P2004/04—Particle morphology depicted by an image obtained by TEM, STEM, STM or AFM
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- C—CHEMISTRY; METALLURGY
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- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
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- C01P2004/60—Particles characterised by their size
- C01P2004/62—Submicrometer sized, i.e. from 0.1-1 micrometer
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
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- C01P2004/64—Nanometer sized, i.e. from 1-100 nanometer
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- C—CHEMISTRY; METALLURGY
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- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/80—Particles consisting of a mixture of two or more inorganic phases
- C01P2004/82—Particles consisting of a mixture of two or more inorganic phases two phases having the same anion, e.g. both oxidic phases
- C01P2004/84—Particles consisting of a mixture of two or more inorganic phases two phases having the same anion, e.g. both oxidic phases one phase coated with the other
Definitions
- the present invention relates to a core-shell type zinc oxide fine particle or a dispersion containing the same, a method for producing the same, and a use thereof. More specifically, the present invention relates to a core-shell type zinc oxide applicable to a catalyst, an antireflection film, an ultraviolet shielding agent, and the like. The present invention relates to fine particles and a dispersion containing the fine particles, the zinc oxide fine particles for producing the fine particles, a method for producing the dispersion containing the fine particles, and a product thereof.
- Zinc oxide is a well-known material as an ultraviolet shielding agent.
- the prior literature discloses the use of an ultraviolet shielding agent using zinc oxide (see Patent Documents 1 and 2).
- UV screening agents are used in cosmetics and touch human skin. Therefore, it is desirable that the component be chemically inert.
- a stable dispersion cannot be obtained simply by dispersing dried zinc oxide fine particles in a dispersion medium by a usual method. This is because in order to obtain a stable dispersion, it is necessary to break up the aggregation of the zinc oxide fine particles once aggregated.
- the nanoparticle synthesis method is either a gas phase process or a liquid phase process, it generally aggregates strongly unless the nanoparticles are suppressed after the nanoparticles are generated. Once the nanoparticles are strongly agglomerated, it is generally difficult to remove the agglomeration even if a treatment for releasing the agglomeration is performed.
- Patent Document 6 discloses a technique for mechanically deaggregating using ceramic beads (see Patent Document 6), but in this case, contamination of impurities is considered as a problem.
- a dispersant it is necessary to add a dispersant to the solvent. From the above, it is necessary to synthesize zinc oxide fine particles that are easy to disperse (not easily agglomerated) without the addition of a dispersing agent as a method for solving the agglomeration.
- the nanoparticles are aggregated, it is difficult to separate them, so that if the nanoparticles are treated before aggregation, that is, at the same time as the formation of the nanoparticles, the dispersion of zinc oxide should be easy to disperse. is there.
- Non-Patent Documents 1 to 4 and Patent Document 7 examples in which such a concept is applied to a sol-gel method or a hydrolysis method have been reported (see Non-Patent Documents 1 to 4 and Patent Document 7). However, there has been no case where such a concept has been applied to the reflux method for depositing zinc oxide fine particles.
- each of the prior literatures discloses metal oxide ultrafine particles, a method for producing the same, and metal oxide fine particles (see Patent Documents 8 and 9).
- Spherical secondary particles in which primary particles of metal oxides of about 10 to 20 nm are aggregated with a small particle size distribution (standard deviation of particle size) of metal oxides of about 50 to 1000 nm, and dispersibility in liquid
- the core-shell type zinc oxide fine particles or the core-shell type zinc oxide fine particle dispersion liquids that are good.
- the present inventors in view of the above-mentioned prior art, suppress the aggregation of nanoparticles, and a method for producing nano-sized zinc oxide fine particles that retain long-term stability and a dispersion thereof
- a method for producing nano-sized zinc oxide fine particles that retain long-term stability and a dispersion thereof
- there are many advantages such as being able to use an organic solvent and sometimes not requiring a reaction initiator by using the reflux method.
- We have found new findings such as the ability to use inexpensive acetates instead of expensive alkoxides, and the ability to prepare core-shell type zinc oxide fine particles and dispersions thereof that suppress the aggregation of nanoparticles.
- the present invention has been completed.
- the present invention is a core-shell type zinc oxide fine particle having a particle size of about 50 to 1000 nm, a small particle size distribution (standard deviation of particle size), a spherical shape, Provided the core-shell type zinc oxide fine particles and the zinc oxide fine particle dispersion liquid in which the secondary particles are spherical and uniform in size and have good dispersibility in the liquid, and the reflux method is applied to the above concept It is an object of the present invention to provide a method for producing the core-shell type zinc oxide fine particles, the zinc oxide fine particle dispersion, and uses thereof.
- the present invention for solving the above-described problems comprises the following technical means.
- (1) Core-shell type zinc oxide fine particles 1) the core part is a secondary particle in which primary particles of zinc oxide are assembled in a spherical shape, 2) the shape of the secondary particles is uniform, and 3) the A core-shell type zinc oxide fine particle characterized in that a polymer layer serving as a shell portion is present on the surface of the secondary particle, and 4) the average particle diameter of the fine particle is from 50 nm to 1000 nm.
- the polymer layer is composed of a polymer of polyvinyl pyrrolidone (PVP), hydroxypropyl cellulose (HPC), or polyethylene glycol (PEG), or a polymer in which the polymer and diethylene glycol (DEG) are crosslinked.
- PVP polyvinyl pyrrolidone
- HPC hydroxypropyl cellulose
- PEG polyethylene glycol
- DEG diethylene glycol
- the core-shell type zinc oxide according to (1) wherein the layer is not separated from the secondary particles in the core portion even when the layer is washed, and the layer is present in a ratio of 5 wt% to 10 wt%. Fine particles.
- the core-shell type zinc oxide fine particles according to (1) wherein the primary particle diameter is 10 to 20 nm and the coefficient of variation of the secondary particle diameter is 0.1 or less.
- Core-shell type zinc oxide fine particle powder characterized by having.
- Core-shell type zinc oxide fine particle dispersion characterized in that the core-shell type zinc oxide fine particle or core-shell type zinc oxide fine particle powder according to any one of (1) to (4) is dispersed in a dispersion medium. liquid.
- a cosmetic having an ultraviolet shielding effect comprising the fine particles, fine particle powder, or fine particle dispersion according to any one of (1) to (6).
- a resin or fiber having an ultraviolet shielding effect wherein the fine particles, fine particle powder or fine particle dispersion according to any one of (1) to (6) is dispersed.
- a method for producing core-shell type zinc oxide fine particles, zinc oxide fine particle powder or zinc oxide fine particle dispersion (10)
- the zinc salt is zinc acetate
- the polymer is polyvinyl pyrrolidone (PVP), hydroxypropyl cellulose (HPC) or polyethylene glycol (PEG), and the high-boiling organic solvent is diethylene glycol (DEG).
- (11) The zinc oxide fine particles according to (9) or (10), wherein the concentration of the polymer (the weight of polymer added per unit organic solvent volume) is 100 kg / m 3 to 140 kg / m 3 . Production method.
- (12) The method for producing zinc oxide fine particles according to (9) or (10), wherein the polymer has an average molecular weight in terms of polyethylene glycol of from 4000 to 5000.
- the core-shell type zinc oxide fine particles referred to in the present invention are defined to mean fine particles having a polymer layer on the surface of secondary particles in which primary particles of zinc oxide are assembled in a spherical shape (see FIG. 1).
- the core-shell type zinc oxide fine particles are different from those in which a polymer exists on the surface of primary particles or secondary particles in which primary particles are irregularly aggregated.
- Prior literature discloses composite particles in which the surface of primary particles or aggregates is coated with a polymer compound, but the primary particles or aggregates are not spherical but have a non-uniform shape. This is because the metal oxide fine particles synthesized in advance are dispersed and pulverized using a disperser such as a bead mill in the manufacturing method disclosed in the above-mentioned document.
- the primary particles or the aggregated particles of the primary particles are crushed, but the aggregated particles of the primary particles after the pulverization are spherical and large like the core-shell type zinc oxide fine particles of the present invention. It ’s impossible to get it all together.
- the ratio of the polymer to be coated is 25 wt% or more, in the present invention, as will be described later, the ratio of the polymer is 5 to 10 wt%. Less than 25 wt%. This is because the polymer that is easily released is removed by washing. This is also a very different point from the composite particles of the above-mentioned document.
- the present invention is a core-shell type zinc oxide fine particle having an average particle diameter of the core-shell type zinc oxide fine particle of 50 nm to 1000 nm, and the shape of the secondary particle as the core part is spherical, The shape is spherical, the size is uniform, and the polymer that is the shell portion is attached to the surface of the zinc oxide secondary particle.
- the present invention is a core-shell type zinc oxide fine particle dispersion, wherein the core-shell type zinc oxide fine particles are dispersed in a dispersion medium.
- the present invention is the above core-shell type zinc oxide fine particle powder, which is characterized by having a property of being well dispersed in a dispersion medium to which no dispersant is added. Furthermore, the present invention is a method for producing core-shell type zinc oxide fine particles, comprising a step of obtaining a mixture by mixing a zinc salt and a polymer in a high boiling point organic solvent, and heating the mixture at a temperature of 160 ° C. or higher. And a step of depositing zinc oxide fine particles by refluxing.
- the zinc salt is preferably zinc acetate.
- the core-shell type zinc oxide fine particle dispersion is a dispersion of core-shell type zinc oxide fine particles, which is a dispersoid, in a dispersion medium, and can also be called a suspension, sol, or suspension instead of the dispersion. It is. Also, when the viscosity is high, it is also called a paste.
- the starting materials are zinc acetate, a high boiling point organic solvent, and a polymer.
- zinc acetate may be commercially available and is generally a hydrate.
- the high-boiling organic solvent is diethylene glycol (DEG), glycerin or the like, and more preferably DEG.
- the polymer is preferably one that dissolves in an organic solvent, such as polyvinylpyrrolidone (PVP), hydroxypropylcellulose (HPC), polyethylene glycol (PEG), and more preferably PVP or HPC.
- the concentration of zinc acetate is preferably 0.04 to 0.2 kmol / m 3 or more.
- the concentration of the polymer is preferably 100 kg / m 3 to 140 kg / m 3 .
- the concentration of the polymer is defined as the weight of the polymer added per unit solvent volume.
- the concentration of polymer ranges from 100 kg / m 3 of 140 kg / m 3, the above which is too small, because the dispersibility is deteriorated. Further, when the concentration of the polymer is more than the above range, spherical zinc oxide fine particles cannot be obtained.
- the mixture is heated and refluxed at a temperature of 160 to 200 ° C.
- This is a step of depositing zinc oxide by heating and refluxing at a predetermined temperature.
- an alkali such as sodium hydroxide or ammonia is added, but the present invention is characterized by not requiring it.
- sodium hydroxide or the like sodium or the like may be mixed into the finally obtained nanoparticles.
- alkali or the like is not required, so that such impurities cannot be mixed.
- the heating / refluxing time is about 10 to 120 minutes. If the heating / refluxing time is short, a large amount of unreacted zinc ions may remain, and if it is too long, an organic compound of zinc may be generated. Therefore, the heating / refluxing time of about 10 to 120 minutes is preferable, and more preferably 30 to 120 minutes.
- Primary particles of zinc oxide are nucleated in a high-boiling organic solvent (polyol) in which the polymer is uniformly dissolved.
- Polyol organic solvent
- zinc oxide acts as a catalyst on the surface of the secondary particles, and the polymer and / or organic solvent undergoes a crosslinking reaction to form a strong polymer layer. 5). When a strong polymer layer is sufficiently developed, it cannot aggregate and becomes core-shell type zinc oxide fine particles.
- the core-shell type zinc oxide fine particles are secondary particles in which primary particles of zinc oxide are gathered in a spherical shape at the core portion, and the shape of the secondary particles is uniform, and the shell portion is formed on the surface of the secondary particles. Is defined as having an average particle size of 50 nm to 1000 nm.
- the polymer layer of the shell part is composed of polyvinyl pyrrolidone (PVP), hydroxypropyl cellulose (HPC) or a related polymer thereof.
- PVP polyvinyl pyrrolidone
- HPC hydroxypropyl cellulose
- HPC polymers cross-linked with PVP or HPC and polyol
- polymers cross-linked with polyol and the like.
- the dispersion medium is the organic solvent used for the heating / refluxing. That is, if heating and refluxing are performed with diethylene glycol (DEG), the dispersion medium is DEG.
- DEG diethylene glycol
- the dispersion medium can be replaced by separating the dispersion medium and the dispersoid by centrifugation, removing the dispersion medium, and adding a desired dispersion medium. At this time, the polymer in the shell portion is not separated by washing, but is inseparable from the core.
- the polymer used in the above heating / refluxing may remain in the dispersion medium, and unreacted Zn ions may remain. For this reason, excess polymer can be removed by centrifuging and repeating solvent substitution.
- the core-shell type zinc oxide fine particles which are the dispersoid of the dispersion obtained by the above method, are spherical.
- the particle diameter is the particle diameter of the core-shell type zinc oxide fine particles, and is a particle diameter determined by observation with a scanning electron microscope (SEM).
- the secondary particles in the core part are aggregates of primary particles and may be referred to as primary aggregates.
- the primary particle size is 10 to 20 nm.
- Each particle of the spherical zinc oxide fine particles in the core portion is a secondary particle, not a primary particle.
- the zinc oxide fine particles may be those to which monovalent to pentavalent metal ions are added.
- metal ions such as Na, Ca, Y, Gd, Zr, Hf, and Nb are added.
- the shape and particle size of the zinc oxide fine particles can be confirmed by the following method.
- the particle diameter can be determined by a dynamic light scattering (DLS) method.
- This particle size is the particle size of particles that exist independently in the dispersion medium. This particle size is generally different from the particle size of fine particles observed by SEM or the like. The reason is that the fine particles are often further aggregated in the dispersion medium, and in this case, the size of the particles in which the fine particles are aggregated appears as a result.
- ⁇ Agglomerates of secondary particles may be referred to as secondary aggregates.
- the dynamic light scattering (DLS) method requires the refractive index of the dispersion medium and the viscosity of the dispersion medium, but literature values can be used for the refractive index of the dispersion medium.
- the viscosity of the dispersion medium is the same as that of the dispersion liquid, and the viscosity of the dispersion liquid is measured and used.
- the dispersion obtained by the above method is centrifuged and re-dispersed in water or ethanol about 3 times, and dried at 80 ° C., for example, to obtain a dry powder. About this, it observes by SEM and calculates
- the average particle diameter of the core-shell type zinc oxide fine particles is 50 nm to 1000 nm. Furthermore, core-shell type zinc oxide fine particles having a uniform particle size, that is, having a small coefficient of variation in particle size, are obtained at a rate of once every several synthesis experiments. In this case, the coefficient of variation is 0.25 or less, and may be 0.10 or less. This can be confirmed by SEM observation of the dry powder.
- the particle size in the dispersion medium is not more than twice that of the core-shell type zinc oxide fine particles. In the dispersion medium, it is shown that the core-shell type zinc oxide fine particles exist with almost no aggregation.
- the core-shell type zinc oxide fine particles there is naturally a polymer layer in the shell portion. This can be confirmed by investigating the dry powder by Fourier transform infrared spectrophotometer (FTIR) analysis and thermogravimetric (TG) analysis. Since the dry powder is subjected to centrifugation and redispersion in water or ethanol about three times, excess polymer unrelated to the core-shell type zinc oxide fine particles is removed. Further, since the drying is performed, the dispersion medium is sufficiently removed.
- the proportion of the polymer layer is preferably 5 to 10 wt%.
- FTIR Fourier transform infrared spectrophotometer
- the polymer for example, PVP, HPC, a polymer crosslinked with PVP, a polymer crosslinked with HPC, a polymer crosslinked with PVP or HPC and polyol, a polymer crosslinked with polyol, or What reacted with zinc oxide is preferable.
- the zinc oxide fine particles obtained in the present invention are chemically inactive because the polymer is attached to the zinc oxide surface.
- a UV screening agent for cosmetics it is desired that the fine particles are chemically inert because they directly touch human skin.
- the zinc oxide fine particles obtained in the present invention are considered to be excellent as an ultraviolet shielding agent.
- PVP is known to be safe and harmless to the human body
- a zinc oxide fine particle dispersion with PVP coated on the surface is promising as an ultraviolet shielding agent.
- An ultraviolet shielding effect is also expected when zinc oxide fine particles having an ultraviolet shielding effect are dispersed in a resin or the like and arbitrarily shaped such as a fiber or a bulk.
- the dry powder of the present invention can be easily dispersed by using, for example, an ultrasonic homogenizer without requiring a dispersant.
- the dispersion medium at this time is arbitrary, and is preferably any one of water, ethanol, terpineol, ethylene glycol, or a mixed solution in which a plurality of these are mixed. Even if the core-shell type zinc oxide fine particles are re-dispersed in these dispersion media, the particle size in the dispersion medium is not more than twice the particle size obtained by SEM observation, and the core-shell type zinc oxide fine particles are aggregated. Exist without.
- Such redispersibility is considered to be due to the presence of a polymer in the shell portion of the core-shell type zinc oxide fine particles. Furthermore, when baked at a temperature higher than 500 ° C., the polymer corresponding to the shell portion is completely removed. In this case, spherical zinc oxide fine particles are obtained.
- the zinc oxide fine particles are secondary particles in which primary particles are collected in a spherical shape.
- the core-shell type zinc oxide fine particles and the zinc oxide polymer composite composition are essentially completely different in structure.
- oxide fine particles In applying oxide fine particles to various products, it is rarely handled as a powder, and is generally dispersed in an arbitrary liquid and handled as a dispersion. However, oxide fine particles have a problem that the smaller the particle size, the easier the aggregation.
- zinc oxide fine particles or zinc oxide fine particle dispersions having a spherical particle size of about 50 to 1000 nm and good dispersibility in an arbitrary liquid such as water or an organic solvent.
- fine particles are generated by adding a basic substance such as sodium hydroxide or potassium hydroxide at the time of production, and it is considered that impurities such as sodium and potassium are mixed in the oxide.
- the present invention is a core-shell type zinc oxide fine particle
- the core part is a secondary particle in which primary particles of zinc oxide are assembled in a spherical shape, and the shape of the secondary particle is uniform.
- the manufacturing method of this is provided.
- the core-shell type zinc oxide fine particles of the present invention can be suitably applied to catalysts, antireflection films, ultraviolet shielding agents and the like.
- the present invention has the following effects. (1) It is possible to provide a core-shell type zinc oxide fine particle having a particle size of about 50 nm to 1000 nm, spherical, and having good dispersibility in the liquid, and a dispersion thereof. (2) A dry powder of core-shell type zinc oxide fine particles that can be easily redispersed can be provided. (3) A core-shell type zinc oxide fine particle dispersion liquid dispersed in an arbitrary dispersion medium can be provided. (4) A high-viscosity core-shell type zinc oxide fine particle dispersion, that is, a core-shell type zinc oxide fine particle paste can be provided. (5) A simple method for producing core-shell type zinc oxide fine particles and a dispersion of the zinc oxide fine particles can be provided.
- a high concentration zinc oxide fine particle dispersion can be obtained.
- Spherical zinc oxide fine particles are obtained by baking and removing the polymer by oxidation.
- (8) According to the present invention it is possible to provide a method for producing zinc oxide fine particles and a dispersion containing the same, and a product thereof, which can be applied to, for example, a catalyst, an antireflection film, and an ultraviolet blocking agent.
- DEG diethylene glycol
- PVP polyvinylpyrrolidone
- Zn (CH 3 COO) 2 ⁇ 2H 2 O zinc acetate dihydrate
- the concentration of the added polymer was 120 kg / m 3 .
- the average molecular weight of PVP is 10,000 as a catalog value.
- the mixture was heated and refluxed at 180 ° C. for 20 min. Thereafter, the mixture was cooled to obtain a core-shell type zinc oxide fine particle dispersion.
- the dispersion was centrifuged at 18000 rpm, and washed with water and ethanol. After washing, it was dried at 80 ° C. to obtain a powder.
- the particle size distribution of the dispersed particles was examined by a dynamic light scattering (DLS) method. The dried powder was observed with an SEM, and the particle size distribution was examined from the photograph.
- DLS dynamic light scattering
- the average particle diameter determined by the DLS method was 282 nm.
- An SEM image of the dry powder is shown in FIG. Spherical fine particles were observed.
- the particle size determined from the SEM image was 336 nm, which was almost the same as the average particle size of the fine particles in the dispersion immediately after reflux. This indicates that spherical fine particles observed by SEM are dispersed in the dispersion without agglomeration.
- the experiment was performed 6 times, and the coefficient of variation of the particle size of the obtained dry powder was 0.1 or less once. That is, it was confirmed that the particle diameters were uniform and monodispersed.
- Fig. 3 shows the XRD pattern of the dry powder.
- the diffraction pattern of the wurtzite structure was confirmed to be zinc oxide. This confirmed that zinc oxide contained in the fine particles and dry powder present in the dispersion immediately after reflux. When the crystallite was calculated from the diffraction peak width, it was confirmed to be 14 nm.
- FIG. 4 shows the IR spectrum of the dry powder. Moreover, IR spectrum of the dry powder of Comparative Example 5 shown later is shown. Comparative Example 5 was synthesized based on the synthesis conditions of Example 1 without adding PVP. Furthermore, the IR spectrum of PVP is also shown. In the IR spectrum of the dry powder of Example 1, an absorption peak was observed at 1600 cm ⁇ 1 .
- Example 1 TG analysis results are shown in FIG. When the temperature was raised to 900 ° C., the weight decreased by about 6%.
- the SEM image of the powder after firing at 500 ° C. was also spherical. Considering this and the results of FTIR and TG comprehensively, the fine particles of Example 1 have PVP or a polymer related to PVP on the surface. Thus, it was confirmed that the fine particles obtained in Example 1 were core-shell type zinc oxide fine particles in which the core was zinc oxide and the shell was a polymer.
- the dispersion stability of the dispersion obtained by redispersing the dry powder of Example 1 in water and the dispersion obtained by redispersing the dry powder of Comparative Example 5 in water were examined. 0.02 g of the dry powder of Example 1 or Comparative Example 5 was dispersed in 2 ml of water, and the state in which the dispersion was precipitated was observed.
- Example 1 had only a slight transparent layer, but Comparative Example 5 was divided into a slight transparent layer, a thin cloudy layer, and a dark cloudy layer.
- Example 1 the comparative example 5 was precipitated faster. Both samples were completely precipitated when stored for 2 days. However, in Example 1, the precipitate was soft and easily redispersed. In Comparative Example 5, the precipitate is hard and much remains on the bottom even if the container is shaken. From this, it was found that Example 1 has good redispersibility.
- Examples 2 to 8 As Examples 2 to 8, experiments were performed in which the concentration of zinc acetate dihydrate, the reflux time, the reflux temperature, and the like were changed based on the experimental conditions in Example 1. Table 1 shows the experimental conditions. In any of the examples, the core of the obtained fine particles was zinc oxide, and the shape of the fine particles was spherical.
- the particle size was in the range of 300 to 700 nm.
- Table 2 shows the details of the experimental results. Under the experimental conditions in Example 2, the experiment was performed 6 times, and the coefficient of variation of the particle diameter obtained from the SEM image of the obtained fine particles was 0.3 or less twice. Furthermore, one of them was obtained with a coefficient of variation of 0.15 or less and a uniform particle size.
- Example 9 and 10 As Examples 9 and 10, the experiment was performed based on Example 3 and changing the average molecular weight of PVP. Table 1 shows the experimental conditions. In any of the examples, the core of the obtained fine particles was zinc oxide, and the shape of the fine particles was spherical. The particle size ranged from 500 to 800 nm. Table 2 shows the details of the experimental results.
- Example 11 As an example 11, an experiment was performed by changing the added polymer from PVP to hydroxypropylcellulose (HPC) based on the example 3.
- Table 1 shows the experimental conditions.
- the core of the obtained fine particles was zinc oxide, and the shape of the fine particles was spherical.
- the particle size was in the range of about 400 nm.
- Table 2 shows the details of the experimental results.
- Comparative Examples 1 and 2 As Comparative Examples 1 and 2, based on Example 1, experiments were conducted by adding not only PVP and zinc acetate dihydrate but also 1 mL of water to DEG. Table 1 shows the experimental conditions. The core of the obtained fine particles was zinc oxide, but the shape of the fine particles was not spherical. Table 2 shows the details of the experimental results. From this, it was found that it is difficult to obtain only spherical particles when water is added even in a small amount to DEG added with PVP and zinc acetate dihydrate.
- Comparative Examples 3 and 4 As Comparative Examples 3 and 4, the experiment was performed using Example 1 as a basis and using ethylene glycol (EG) as a solvent instead of DEG. Other experimental conditions were also changed, and Table 1 shows the experimental conditions.
- EG ethylene glycol
- Table 1 shows the experimental conditions.
- the core of the obtained fine particles was zinc oxide, but the shape of the fine particles was not spherical.
- Comparative Example 4 the core of the obtained fine particles contained not only zinc oxide but a little other than oxide. Further, the shape of the fine particles was not spherical. Table 2 shows the details of the experimental results. From this, it was found that it is difficult to obtain only spherical particles when EG is used instead of DEG.
- Comparative Example 5 As Comparative Example 5, the experiment was conducted based on Example 1 without adding PVP. Table 1 shows the experimental conditions. The obtained fine particles were zinc oxide, and the shape of the fine particles was spherical. As described in detail in Example 1, the redispersibility was poor. From this, it was found that it is difficult to obtain fine particles having good redispersibility unless PVP is added.
- Comparative Example 6 As Comparative Example 6, the experiment was conducted based on Example 2, with the reflux temperature changed to 140 ° C. Table 1 shows the experimental conditions. The generated fine particles were few, and the shape of the obtained fine particles was not spherical. From this, it was found that it is difficult to obtain fine particles when the reflux temperature is low.
- Comparative Example 7 As Comparative Example 7, the experiment was conducted based on Example 2 without adding PVP. Table 1 shows the experimental conditions. The obtained fine particles were zinc oxide, and the shape of the fine particles was sometimes spherical, but fine particles that were not partially spherical were sometimes obtained. From this, it was found that it is sometimes difficult to obtain spherical fine particles when PVP is not added.
- Comparative Examples 8 to 10 As Comparative Examples 8 to 10, the experiment was conducted on the basis of Example 9 and changing the concentration of PVP, the concentration of zinc acetate dihydrate, and the reflux time. Table 1 shows the experimental conditions. In Comparative Examples 8 to 10, the core of the obtained fine particles was zinc oxide, but the shape of the fine particles was not spherical in all or part. In Comparative Example 8, the concentration of zinc acetate dihydrate was too high, in Comparative Example 9, the concentration of PVP was too high, and in Comparative Example 10, the reflux time was too short.
- the present invention relates to core-shell type zinc oxide fine particles or a dispersion containing the same, their production method and application, and according to the present invention, the particle size is about 50 nm to 1000 nm and is spherical.
- the core-shell type zinc oxide fine particles having good dispersibility in the liquid and the dispersion liquid thereof can be provided.
- a dry powder of core-shell type zinc oxide fine particles easily redispersed, a core-shell type zinc oxide fine particle dispersion dispersed in an arbitrary dispersion medium, a core-shell type zinc oxide fine particle dispersion having a high viscosity, A core-shell type zinc oxide fine particle paste can be provided.
- a simple method for producing core-shell type zinc oxide fine particles and a dispersion of the zinc oxide fine particles can be provided.
- spherical zinc oxide fine particles can be obtained by firing the zinc oxide fine particles and oxidizing and removing the polymer.
- INDUSTRIAL APPLICABILITY The present invention is useful, for example, as providing a method for producing zinc oxide fine particles and a dispersion containing the same, and a product thereof that can be applied to a catalyst, an antireflection film, an ultraviolet blocking agent, and the like.
- the schematic diagram of a core-shell structure is shown.
- the SEM image of the dry powder of Example 1 is shown.
- the XRD pattern of the dry powder of Example 1 is shown.
- the IR spectrum of the dry powder of Example 1 is shown.
- the TG curve of the dry powder of Example 1 is shown.
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Abstract
Description
(1)コアシェル型酸化亜鉛微粒子であって、1)そのコア部分は酸化亜鉛の一次粒子が球状に集合した二次粒子であり、2)その二次粒子の形状は揃っており、3)その二次粒子表面にシェル部分となる高分子の層が存在し、4)該微粒子の粒径の平均が50nmから1000nmである、ことを特徴とするコアシェル型酸化亜鉛微粒子。
(2)前記高分子の層が、ポリビニルピロリドン(PVP)、ヒドロキシプロピルセルロース(HPC)、又はポリエチレングリコール(PEG)の高分子、あるいは該高分子及びジエチレングリコール(DEG)が架橋した高分子で構成され、その層が洗浄してもコア部分の二次粒子から分離することがなく、かつ、その層が5wt%から10wt%の割合で存在している、前記(1)に記載のコアシェル型酸化亜鉛微粒子。
(3)一次粒子径が10から20nmであり、かつ、二次粒子径の変動係数が0.1以下である、前記(1)に記載のコアシェル型酸化亜鉛微粒子。
(4)前記(1)から(3)のいずれか1項に記載のコアシェル型酸化亜鉛微粒子を含有する乾燥粉体であって、分散剤を添加していない分散媒に良好に分散する性質を有することを特徴とするコアシェル型酸化亜鉛微粒子粉体。
(5)前記(1)から(4)のいずれか1項に記載のコアシェル型酸化亜鉛微粒子又はコアシェル型酸化亜鉛微粒子粉体が分散媒中に分散したことを特徴とするコアシェル型酸化亜鉛微粒子分散液。
(6)前記分散媒が、水、エタノール、テルピネオール、エチレングリコールのいずれか一つ、あるいは、これらが複数混合している混合溶液である、前記(5)に記載のコアシェル型酸化亜鉛微粒子分散液又は酸化亜鉛微粒子分散液。
(7)前記(1)から(6)のいずれか1項に記載の微粒子、微粒子粉体又は微粒子分散液を含有することを特徴とする紫外線遮蔽作用を有する化粧品。
(8)前記(1)から(6)のいずれか1項に記載の微粒子、微粒子粉体又は微粒子分散液を分散させたことを特徴とする紫外線遮蔽作用を有する樹脂又は繊維。
(9)前記(1)から(8)のいずれか1項に記載のコアシェル型酸化亜鉛微粒子、酸化亜鉛微粒子粉体又は酸化亜鉛微粒子分散液を製造する方法であって、亜鉛の塩と高分子を高沸点有機溶媒に混合して混合物を得る工程と、その混合物を160℃以上の温度で加熱・還流して酸化亜鉛微粒子を析出させ、コアシェル構造とする工程とを有することを特徴とする、コアシェル型酸化亜鉛微粒子、酸化亜鉛微粒子粉体又は酸化亜鉛微粒子分散液の製造方法。
(10)前記亜鉛の塩が、酢酸亜鉛であり、前記高分子がポリビニルピロリドン(PVP)、ヒドロキシプロピルセルロース(HPC)又はポリエチレングリコール(PEG)であり、前記高沸点有機溶媒が、ジエチレングリコール(DEG)である、前記(9)に記載の酸化亜鉛微粒子の製造方法。
(11)前記高分子の濃度(単位有機溶媒体積当たりに添加した高分子重量)が、100kg/m3から140kg/m3である、前記(9)又は(10)に記載の酸化亜鉛微粒子の製造方法。
(12)前記高分子のポリエチレングリコール換算での平均分子量が、4000から5000である、前記(9)又は(10)に記載の酸化亜鉛微粒子の製造方法。
本発明で言うコアシェル型酸化亜鉛微粒子とは、酸化亜鉛の一次粒子が球状に集合した二次粒子表面に高分子層が存在する微粒子を意味するものとして定義されるものであり(図1参照)、該コアシェル型酸化亜鉛微粒子は、一次粒子又は一次粒子が不規則に凝集した二次粒子の表面に高分子が存在するものとは異なる。
2.一次粒子が球状に凝集する。このときも、絶えず一次粒子が核生成する。
3.凝集粒子(二次粒子)の表面に核生成した一次粒子が球状に集まってくる。
4.このとき、二次粒子の表面で酸化亜鉛が触媒として働き高分子及び/又は有機溶媒が、架橋反応を生じて強固な高分子層が形成される。
5.強固な高分子層が十分発達すると、凝集ができなくなり、コアシェル型酸化亜鉛微粒子となる。
(1)粒径が50nmから1000nm程度で、球状で、液中での分散性が良好であるコアシェル型酸化亜鉛微粒子及びその分散液を提供することができる。
(2)容易に再分散するコアシェル型酸化亜鉛微粒子の乾燥粉体を提供できる。
(3)任意の分散媒に分散したコアシェル型酸化亜鉛微粒子分散液を提供できる。
(4)高粘度であるコアシェル型酸化亜鉛微粒子分散液、すなわち、コアシェル型酸化亜鉛微粒子ペーストを提供できる。
(5)コアシェル型酸化亜鉛微粒子及び当該酸化亜鉛微粒子の分散液の簡便な製造方法を提供できる。
(6)高濃度の酸化亜鉛微粒子分散液が得られる。
(7)焼成して、高分子を酸化除去することにより、球状の酸化亜鉛微粒子が得られる。
(8)本発明により、例えば、触媒、反射防止膜、紫外線遮断剤などに応用可能な、酸化亜鉛微粒子及びそれを含む分散液の製造方法及びその製品を提供することができる。
実施例2から8として、実施例1における実験条件を基本とし、酢酸亜鉛二水和物の濃度、還流時間、還流温度などを変更した実験を行った。表1に、実験条件を示す。いずれの実施例でも、得られた微粒子のコアは酸化亜鉛であり、微粒子の形状は球状であった。
実施例9及び10として、実施例3を基本とし、PVPの平均分子量を変更して実験を行った。表1に、実験条件を示す。いずれの実施例でも、得られた微粒子のコアは酸化亜鉛であり、微粒子の形状は球状であった。粒径は500から800nmの範囲であった。表2に、実験結果の詳細を示す。
実施例11として、実施例3を基本とし、添加した高分子をPVPからヒドロキシプロピルセルロース(HPC)に変更して実験を行った。表1に、実験条件を示す。得られた微粒子のコアは酸化亜鉛であり、微粒子の形状は球状であった。粒径は約400nmの範囲であった。表2に、実験結果の詳細を示す。
比較例1、2として、実施例1を基本とし、DEGにPVP、酢酸亜鉛二水和物だけでなく、水1mLを加え実験を行った。表1に、実験条件を示す。得られた微粒子のコアは酸化亜鉛であったが、微粒子の形状は球状でないものも含まれていた。表2に、実験結果の詳細を示す。このことから、PVP及び酢酸亜鉛二水和物を加えたDEGに少量でも水を加えると、球状粒子のみを得ることは困難であることが分かった。
比較例3、4として、実施例1を基本とし、DEGの代わりにエチレングリコール(EG)を溶媒とし、実験を行った。その他の実験条件も変更しており、表1に、実験条件を示す。比較例3では、得られた微粒子のコアは酸化亜鉛であったが、微粒子の形状は球状でなかった。
比較例5として、実施例1を基本とし、PVPを添加しないで実験を行った。表1に、実験条件を示す。得られた微粒子は酸化亜鉛であり、微粒子の形状は球状であった。実施例1で詳細に述べたとおり、再分散性が悪かった。このことから、PVPを添加しないと、再分散性が良好な微粒子を得ることは困難であることが分かった。
比較例6として、実施例2を基本とし、還流温度を140℃に変更し実験を行った。表1に、実験条件を示す。生成した微粒子はわずかであり、得られた微粒子の形状は球状でなかった。このことから、還流温度が低いと微粒子を得ることは困難であることが分かった。
比較例7として、実施例2を基本とし、PVPを添加しないで実験を行った。表1に、実験条件を示す。得られた微粒子は酸化亜鉛であり、微粒子の形状は球状である場合もあったが、一部球状でない微粒子が得られた場合もあった。このことから、PVPを添加しない場合、球状の微粒子を得ることは困難な場合があることが分かった。
比較例8から10として、実施例9を基本とし、PVPの濃度、酢酸亜鉛二水和物の濃度、還流時間を変更して実験を行った。表1に、実験条件を示す。比較例8から10では、得られた微粒子のコアは酸化亜鉛であったが、微粒子の形状は全て又は一部について球状でなかった。比較例8では、酢酸亜鉛二水和物の濃度が多すぎ、比較例9では、PVPの濃度が多すぎ、比較例10では、還流時間が短すぎた。
Claims (12)
- コアシェル型酸化亜鉛微粒子であって、1)そのコア部分は酸化亜鉛の一次粒子が球状に集合した二次粒子であり、2)その二次粒子の形状は揃っており、3)その二次粒子表面にシェル部分となる高分子の層が存在し、4)該微粒子の粒径の平均が50nmから1000nmである、ことを特徴とするコアシェル型酸化亜鉛微粒子。
- 前記高分子の層が、ポリビニルピロリドン(PVP)、ヒドロキシプロピルセルロース(HPC)、又はポリエチレングリコール(PEG)の高分子、あるいは該高分子及びジエチレングリコール(DEG)が架橋した高分子で構成され、その層が洗浄してもコア部分の二次粒子から分離することがなく、かつ、その層が5wt%から10wt%の割合で存在している、請求項1に記載のコアシェル型酸化亜鉛微粒子。
- 一次粒子径が10から20nmであり、かつ、二次粒子径の変動係数が0.1以下である、請求項1に記載のコアシェル型酸化亜鉛微粒子。
- 請求項1から3のいずれか1項に記載のコアシェル型酸化亜鉛微粒子を含有する乾燥粉体であって、分散剤を添加していない分散媒に良好に分散する性質を有することを特徴とするコアシェル型酸化亜鉛微粒子粉体。
- 請求項1から4のいずれか1項に記載のコアシェル型酸化亜鉛微粒子又はコアシェル型酸化亜鉛微粒子粉体が分散媒中に分散したことを特徴とするコアシェル型酸化亜鉛微粒子分散液。
- 前記分散媒が、水、エタノール、テルピネオール、エチレングリコールのいずれか一つ、あるいは、これらが複数混合している混合溶液である、請求項5に記載のコアシェル型酸化亜鉛微粒子分散液又は酸化亜鉛微粒子分散液。
- 請求項1から6のいずれか1項に記載の微粒子、微粒子粉体又は微粒子分散液を含有することを特徴とする紫外線遮蔽作用を有する化粧品。
- 請求項1から6のいずれか1項に記載の微粒子、微粒子粉体又は微粒子分散液を分散させたことを特徴とする紫外線遮蔽作用を有する樹脂又は繊維。
- 請求項1から8のいずれか1項に記載のコアシェル型酸化亜鉛微粒子、酸化亜鉛微粒子粉体又は酸化亜鉛微粒子分散液を製造する方法であって、亜鉛の塩と高分子を高沸点有機溶媒に混合して混合物を得る工程と、その混合物を160℃以上の温度で加熱・還流して酸化亜鉛微粒子を析出させ、コアシェル構造とする工程とを有することを特徴とする、コアシェル型酸化亜鉛微粒子、酸化亜鉛微粒子粉体又は酸化亜鉛微粒子分散液の製造方法。
- 前記亜鉛の塩が、酢酸亜鉛であり、前記高分子がポリビニルピロリドン(PVP)、ヒドロキシプロピルセルロース(HPC)又はポリエチレングリコール(PEG)であり、前記高沸点有機溶媒が、ジエチレングリコール(DEG)である、請求項9に記載の酸化亜鉛微粒子の製造方法。
- 前記高分子の濃度(単位有機溶媒体積当たりに添加した高分子重量)が、100kg/m3から140kg/m3である、請求項9又は10に記載の酸化亜鉛微粒子の製造方法。
- 前記高分子のポリエチレングリコール換算での平均分子量が、4000から5000である、請求項9又は10に記載の酸化亜鉛微粒子の製造方法。
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