JP3432788B2 - Hybrid powder consisting of collagen and resin components - Google Patents
Hybrid powder consisting of collagen and resin componentsInfo
- Publication number
- JP3432788B2 JP3432788B2 JP2000216233A JP2000216233A JP3432788B2 JP 3432788 B2 JP3432788 B2 JP 3432788B2 JP 2000216233 A JP2000216233 A JP 2000216233A JP 2000216233 A JP2000216233 A JP 2000216233A JP 3432788 B2 JP3432788 B2 JP 3432788B2
- Authority
- JP
- Japan
- Prior art keywords
- leather
- weight
- collagen
- parts
- powder
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000000843 powder Substances 0.000 title claims description 70
- 102000008186 Collagen Human genes 0.000 title claims description 60
- 108010035532 Collagen Proteins 0.000 title claims description 60
- 229920001436 collagen Polymers 0.000 title claims description 60
- 229920005989 resin Polymers 0.000 title claims description 26
- 239000011347 resin Substances 0.000 title claims description 26
- 239000000835 fiber Substances 0.000 claims description 32
- 239000002245 particle Substances 0.000 claims description 23
- 229920000642 polymer Polymers 0.000 claims description 3
- 239000010985 leather Substances 0.000 description 62
- 239000000047 product Substances 0.000 description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 33
- 230000000052 comparative effect Effects 0.000 description 21
- 238000000034 method Methods 0.000 description 19
- 238000010521 absorption reaction Methods 0.000 description 16
- 239000000839 emulsion Substances 0.000 description 16
- 239000011248 coating agent Substances 0.000 description 14
- 239000010408 film Substances 0.000 description 14
- 238000000576 coating method Methods 0.000 description 12
- 229920005992 thermoplastic resin Polymers 0.000 description 12
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 10
- 238000010298 pulverizing process Methods 0.000 description 9
- 239000011230 binding agent Substances 0.000 description 8
- 238000001035 drying Methods 0.000 description 8
- 239000000203 mixture Substances 0.000 description 8
- 210000003491 skin Anatomy 0.000 description 8
- 238000012360 testing method Methods 0.000 description 7
- 238000009826 distribution Methods 0.000 description 6
- 239000000463 material Substances 0.000 description 6
- 239000003973 paint Substances 0.000 description 6
- 210000004243 sweat Anatomy 0.000 description 6
- 229920000178 Acrylic resin Polymers 0.000 description 5
- 239000004925 Acrylic resin Substances 0.000 description 5
- 238000007334 copolymerization reaction Methods 0.000 description 5
- 238000003795 desorption Methods 0.000 description 5
- 229920000578 graft copolymer Polymers 0.000 description 5
- 229910052742 iron Inorganic materials 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000000465 moulding Methods 0.000 description 5
- 239000000049 pigment Substances 0.000 description 5
- 238000006116 polymerization reaction Methods 0.000 description 5
- 239000004800 polyvinyl chloride Substances 0.000 description 5
- 229920000915 polyvinyl chloride Polymers 0.000 description 5
- 239000003381 stabilizer Substances 0.000 description 5
- 208000005156 Dehydration Diseases 0.000 description 4
- MQIUGAXCHLFZKX-UHFFFAOYSA-N Di-n-octyl phthalate Natural products CCCCCCCCOC(=O)C1=CC=CC=C1C(=O)OCCCCCCCC MQIUGAXCHLFZKX-UHFFFAOYSA-N 0.000 description 4
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 4
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 4
- 239000000654 additive Substances 0.000 description 4
- BJQHLKABXJIVAM-UHFFFAOYSA-N bis(2-ethylhexyl) phthalate Chemical compound CCCCC(CC)COC(=O)C1=CC=CC=C1C(=O)OCC(CC)CCCC BJQHLKABXJIVAM-UHFFFAOYSA-N 0.000 description 4
- 238000006243 chemical reaction Methods 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- 230000018044 dehydration Effects 0.000 description 4
- 238000006297 dehydration reaction Methods 0.000 description 4
- 239000000178 monomer Substances 0.000 description 4
- 239000007921 spray Substances 0.000 description 4
- 210000001519 tissue Anatomy 0.000 description 4
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 3
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 3
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 229920006243 acrylic copolymer Polymers 0.000 description 3
- 230000000996 additive effect Effects 0.000 description 3
- 238000004040 coloring Methods 0.000 description 3
- 238000004925 denaturation Methods 0.000 description 3
- 230000036425 denaturation Effects 0.000 description 3
- 210000004207 dermis Anatomy 0.000 description 3
- 229910001873 dinitrogen Inorganic materials 0.000 description 3
- VOZRXNHHFUQHIL-UHFFFAOYSA-N glycidyl methacrylate Chemical compound CC(=C)C(=O)OCC1CO1 VOZRXNHHFUQHIL-UHFFFAOYSA-N 0.000 description 3
- 238000010409 ironing Methods 0.000 description 3
- 238000004898 kneading Methods 0.000 description 3
- 239000002352 surface water Substances 0.000 description 3
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 239000003431 cross linking reagent Substances 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000001804 emulsifying effect Effects 0.000 description 2
- 238000007731 hot pressing Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 235000013372 meat Nutrition 0.000 description 2
- 239000012452 mother liquor Substances 0.000 description 2
- 239000004417 polycarbonate Substances 0.000 description 2
- -1 polyethylene Polymers 0.000 description 2
- 229920005749 polyurethane resin Polymers 0.000 description 2
- 238000003825 pressing Methods 0.000 description 2
- 230000003068 static effect Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229920003002 synthetic resin Polymers 0.000 description 2
- 239000000057 synthetic resin Substances 0.000 description 2
- 229920002803 thermoplastic polyurethane Polymers 0.000 description 2
- 229920001187 thermosetting polymer Polymers 0.000 description 2
- 230000004584 weight gain Effects 0.000 description 2
- 235000019786 weight gain Nutrition 0.000 description 2
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 1
- 229910000975 Carbon steel Inorganic materials 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- 239000004640 Melamine resin Substances 0.000 description 1
- 229920000877 Melamine resin Polymers 0.000 description 1
- GYCMBHHDWRMZGG-UHFFFAOYSA-N Methylacrylonitrile Chemical compound CC(=C)C#N GYCMBHHDWRMZGG-UHFFFAOYSA-N 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000005062 Polybutadiene Substances 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 description 1
- 101710201629 Ribulose bisphosphate carboxylase/oxygenase activase 2, chloroplastic Proteins 0.000 description 1
- 229920001807 Urea-formaldehyde Polymers 0.000 description 1
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 125000005396 acrylic acid ester group Chemical group 0.000 description 1
- 229920005822 acrylic binder Polymers 0.000 description 1
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000003125 aqueous solvent Substances 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000010962 carbon steel Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004049 embossing Methods 0.000 description 1
- 210000002615 epidermis Anatomy 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000012213 gelatinous substance Substances 0.000 description 1
- 238000001879 gelation Methods 0.000 description 1
- 239000003349 gelling agent Substances 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 239000011256 inorganic filler Substances 0.000 description 1
- 229910003475 inorganic filler Inorganic materials 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 125000005641 methacryl group Chemical group 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000012778 molding material Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 206010033675 panniculitis Diseases 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 239000000088 plastic resin Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920002587 poly(1,3-butadiene) polymer Polymers 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920002857 polybutadiene Polymers 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000007592 spray painting technique Methods 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 210000000434 stratum corneum Anatomy 0.000 description 1
- 229920003048 styrene butadiene rubber Polymers 0.000 description 1
- 210000004304 subcutaneous tissue Anatomy 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 230000004580 weight loss Effects 0.000 description 1
Landscapes
- Synthetic Leather, Interior Materials Or Flexible Sheet Materials (AREA)
- Treatment And Processing Of Natural Fur Or Leather (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明はコラーゲンと樹脂成
分からなる皮革様成形品または皮革様塗膜用ハイブリッ
ド粉末に関し、特に、樹脂との親和性に優れたコラーゲ
ンと樹脂成分からなるハイブリッド粉末に関する。TECHNICAL FIELD The present invention relates to a hybrid powder for a leather-like molded article or a leather-like coating film, which comprises collagen and a resin component, and more particularly to a hybrid powder comprising collagen and a resin component, which have excellent affinity with a resin.
【0002】[0002]
【従来の技術】皮革は、生物種ごとに特有の優美な外観
を呈する皮革表層を活かして古くから日用品の素材とし
て利用されており、コラーゲン線維束の交絡による柔軟
性と強靱性を併せもち、且つ耐久性と吸湿性と耐熱性と
耐寒性に優れているという特性を有している。2. Description of the Related Art Leather has been used as a material for daily necessities for a long time by taking advantage of the leather surface layer, which has an elegant appearance peculiar to each species, and has both flexibility and toughness due to the entanglement of collagen fiber bundles. In addition, it has the characteristics of excellent durability, hygroscopicity, heat resistance and cold resistance.
【0003】しかし、天然皮革は、天然繊維製品や合成
樹脂製品に比べた場合、生物から採取される皮革の部位
が異なると物性値が異なるという欠点を有し、皮革表面
に損傷があると商品価値を低下させるので、生物から採
取した皮革のすべての部分を必ずしも利用できるとは限
らないという不都合な点がある。従って、天然皮革製品
は他の素材(天然繊維製品や合成樹脂製品)に比べて高
コストの材料になる。また、天然皮革は精肉生産の過程
で産出される副産物であり、供給量に限界がある。そこ
で、天然皮革を粉末化し、この皮革粉末を樹脂材料と混
合することによって天然皮革に似せた皮革様成形品を提
供しようとする試みがある。However, compared with natural fiber products and synthetic resin products, natural leather has the disadvantage that the physical properties of the leather are different when the parts of the leather taken from different organisms are different. It has the disadvantage that not all parts of leather taken from living organisms are necessarily available, as it reduces its value. Therefore, the natural leather product becomes a high cost material compared to other materials (natural fiber product and synthetic resin product). Further, natural leather is a by-product produced during the meat production process, and its supply is limited. Therefore, there is an attempt to pulverize natural leather and mix the leather powder with a resin material to provide a leather-like molded article that resembles natural leather.
【0004】例えば、特開昭62−240400号公報
には、「50メッシュ(296μm)乃至250メッシ
ュ(59μm)の粒径の乾燥皮革粉と熱可塑性樹脂と顔
料とが混練加熱成形されてなる皮革様成形品において、
前記混入顔料が熱可塑性樹脂と共に成形材構成皮革粉に
結着されている皮革様成形品」が開示されている(以下
「公知技術1」という)。また、特開昭63−1131
1号公報には、「50メッシュ乃至250メッシュの粒
径の乾燥皮革粉が重量比60%以内で熱可塑性樹脂コン
パウンドに混合され、成形金属に注入されて型成形され
てなる皮革様成形品」が開示されている(以下「公知技
術2」という)。さらに、特開昭63−22864号公
報には、「50メッシュ乃至250メッシュの粒径の乾
燥皮革粉が熱可塑性樹脂コンパウンドに重量比60%以
内で混合され、押出型成形されている皮革様成形品」が
開示されている(以下「公知技術3」という)。しか
し、これらの各公報に記載された皮革様成形品は、皮革
粉末として比較的粗い(粒径の大きな)粉末が用いられ
ているので、熱可塑性樹脂に配合した場合の流動性に乏
しく、熱可塑性樹脂中に皮革粉を均一に分散させること
ができない。その結果、成形品としての強度が劣った
り、皮革様成形品に皮革特有の特性を付与することがで
きず、平滑な表面を有する成形品を得ることができな
い。For example, Japanese Patent Laid-Open No. 62-240400 discloses a leather made by kneading and molding dry leather powder having a particle size of 50 mesh (296 μm) to 250 mesh (59 μm), a thermoplastic resin and a pigment. In molded products like
A "leather-like molded article in which the above-mentioned mixed pigment is bound to a leather powder forming a molding material together with a thermoplastic resin" is disclosed (hereinafter referred to as "known art 1"). Also, JP-A-63-1131
No. 1 discloses "a leather-like molded product obtained by mixing dry leather powder having a particle size of 50 mesh to 250 mesh with a thermoplastic resin compound within a weight ratio of 60%, and injecting it into a molding metal and molding." Is disclosed (hereinafter referred to as "known art 2"). Further, Japanese Patent Laid-Open No. 63-22864 discloses "Leather-like molding in which dry leather powder having a particle size of 50 mesh to 250 mesh is mixed with a thermoplastic resin compound within a weight ratio of 60% and extrusion molding is performed. "Product" is disclosed (hereinafter referred to as "known art 3"). However, since the leather-like molded articles described in each of these publications use a relatively coarse (large particle size) powder as a leather powder, they have poor fluidity when blended with a thermoplastic resin, Leather powder cannot be uniformly dispersed in the plastic resin. As a result, the strength of the molded product is inferior, the leather-specific molded product cannot be given the characteristics peculiar to leather, and a molded product having a smooth surface cannot be obtained.
【0005】また、特開平3−195800号公報に
は、微細な皮革粉と樹脂からなる皮革様成形品を提供す
るために、「床皮から酵素の作用によって分子状コラー
ゲンを含む精製コラーゲン組織を得、このコラーゲン組
織を湿式粉砕し、湿式粉砕後のコラーゲン組織に無機物
の架橋剤を加えて架橋処理することによってコラーゲン
線維凝集体を作り、このコラーゲン線維凝集体を脱水乾
燥後に粉砕してコラーゲン粉末を得、このコラーゲン粉
末を熱可塑性樹脂と混合したものを成形することによっ
て皮革様成形品を得る方法。」が記載されている(以下
「公知技術4」という)。しかし、分子状コラーゲンを
含むコラーゲン組織を無機物の架橋剤で架橋させてコラ
ーゲン線維凝集体を得ているため耐水性に劣り、このコ
ラーゲン粉末と熱可塑性樹脂とを混合するとき、水系溶
剤中においてコラーゲン粉末が膨潤を起こしやすいの
で、皮革様塗料として用いるのに適していないという欠
点がある。Further, Japanese Patent Application Laid-Open No. 3-195800 discloses, in order to provide a leather-like molded article composed of fine leather powder and a resin, "purified collagen tissue containing molecular collagen from the floor skin by the action of an enzyme. The collagen tissue is obtained by wet pulverization, and the collagen tissue after the wet pulverization is subjected to a crosslinking treatment by adding a crosslinking agent of an inorganic substance to produce a collagen fiber aggregate, and the collagen fiber aggregate is dehydrated and dried and then pulverized to obtain a collagen powder. And obtaining a leather-like molded article by molding a mixture of this collagen powder and a thermoplastic resin. "(Hereinafter referred to as" known art 4 "). However, since the collagen tissue containing molecular collagen is cross-linked with an inorganic cross-linking agent to obtain collagen fiber aggregates, the water resistance is poor, and when the collagen powder and the thermoplastic resin are mixed, the collagen powder is mixed in an aqueous solvent. Since the powder easily swells, it is not suitable for use as a leather-like paint.
【0006】また、なめし革を加熱水蒸気により加熱、
膨潤してコラーゲン線維を膠着させて固定し、脱水乾燥
後にそのなめし革を粉砕してコラーゲン粉末を得る方法
(以下「公知技術5」という)も提案されているが、皮
革を加熱水蒸気で処理するときにコラーゲン線維のかな
りの部分がゼラチン質に変性するので、この方法で得ら
れたコラーゲン粉末と熱可塑性樹脂から皮革様水系塗料
を得られたとしても、塗料の粘度が高くなってうまく塗
布できなかったり、塗装被膜がベタツキ、塗装被膜の耐
水性が劣るという欠点がある。[0006] Further, the tanned leather is heated with heated steam,
A method (hereinafter referred to as "known art 5") of swelling to fix collagen fibers by sticking them together, dehydration and drying, and then crushing the tanned leather to obtain collagen powder has also been proposed. Since a considerable part of the collagen fibers is modified into gelatinous substance, even if a leather-like water-based paint can be obtained from the collagen powder and thermoplastic resin obtained by this method, the viscosity of the paint increases and it cannot be applied well. In addition, the coating film is sticky and the coating film has poor water resistance.
【0007】[0007]
【発明が解決しようとする課題】一般的に皮革(なめし
加工されていないものを「皮」といい、なめし加工され
ているものを「革」という)を、微細な径のものに粉砕
することは困難であって、公知技術1〜3に記載されて
いるように、従来の皮革様成形品では、比較的粗い径の
皮革粉しか得ることができなかったので、熱可塑性樹脂
中にその皮革粉を均一に分散させることができず、成形
品の強度が劣ったり、平滑な表面を有する成形品を得る
ことができなかった。また、公知技術4、5に記載され
たコラーゲン粉末から得た皮革様塗膜は耐水性に劣ると
いう欠点がある。[Problems to be Solved by the Invention] Generally, crushing leather (non-tanned leather is called "leather" and tanned leather is called "leather") into fine particles. Since it is difficult to obtain a leather powder having a relatively coarse diameter in the conventional leather-like molded article as described in the known techniques 1 to 3, it is difficult to obtain the leather in the thermoplastic resin. The powder could not be dispersed uniformly, the strength of the molded product was poor, and a molded product having a smooth surface could not be obtained. Further, the leather-like coating film obtained from the collagen powder described in the known arts 4 and 5 has a drawback that it has poor water resistance.
【0008】本発明は従来の技術の有するこのような問
題点に鑑みてなされたものであって、その目的は、強靱
で平滑な表面を有する皮革様成形品および耐水性に優れ
た皮革様塗膜を得ることのできるコラーゲンと樹脂成分
からなる微細なハイブリッド粉末を提供することにあ
る。The present invention has been made in view of such problems of the prior art, and an object thereof is a leather-like molded article having a tough and smooth surface and a leather-like coating excellent in water resistance. It is an object of the present invention to provide a fine hybrid powder composed of collagen and a resin component capable of obtaining a film.
【0009】[0009]
【課題を解決するための手段】上記目的を達成するため
に本発明は、コラーゲン粗線維の側面を無触媒グラフト
共重合によって形成された樹脂成分で縫合するようにし
てコラーゲン線維束を形成し、このコラーゲン線維束を
乾燥後に粉砕することによってコラーゲンと樹脂成分か
らなる微細なハイブリッド粉末を得ることができる。[Means for Solving the Problems] In order to achieve the above object, the present invention forms a collagen fiber bundle by stitching the side surface of a collagen coarse fiber with a resin component formed by non-catalytic graft copolymerization, By pulverizing this collagen fiber bundle after drying, a fine hybrid powder composed of collagen and a resin component can be obtained.
【0010】[0010]
【発明の実施の形態】すなわち、本発明は、コラーゲン
線維成分と、重量比で該コラーゲン線維成分に対して5
0〜200重量%の樹脂成分とを有するものをグラフト
共重合することによって得た重合体を乾燥後に粉砕する
ことによって得ることのできるコラーゲンと樹脂成分か
らなるハイブリッド粉末を第一の発明とし、上記第一の
発明において、ハイブリッド粉末は、40μm以下の粒
径のものが90重量%以上であって、その平均粒径が5
〜20μmであるハイブリッド粉末を第二の発明とす
る。BEST MODE FOR CARRYING OUT THE INVENTION That is, according to the present invention, a collagen fiber component is used in a weight ratio of 5 to the collagen fiber component.
A hybrid powder comprising collagen and a resin component, which can be obtained by drying and pulverizing a polymer obtained by graft-copolymerizing a resin having 0 to 200% by weight of the resin component, is defined as the first invention, and In the first invention, the hybrid powder has a particle size of 40 μm or less in an amount of 90% by weight or more and has an average particle size of 5
The second invention is a hybrid powder having a particle size of 20 μm.
【0011】第一の発明によれば、コラーゲン線維をグ
ラフト共重合によって形成された樹脂成分で縫合するよ
うにしてコラーゲン線維束を形成することができるの
で、コラーゲン線維同士の絡みつきがなく、乾燥後に汎
用粉砕機で粉砕することによって、コラーゲンと樹脂成
分からなる微細なハイブリッド粉末を得ることができ
る。このハイブリッド粉末と熱可塑性樹脂および必要に
応じて添加する添加剤とを混練すると、微細なハイブリ
ッド粉末は混練物中に均一に分散し、この混練物を常法
により成形して強靱で平滑な表面を有する皮革様成形品
を得ることができる。また、上記ハイブリッド粉末と熱
可塑性樹脂または熱硬化性樹脂および必要に応じて添加
する添加剤とを混練したものを皮革上に塗布すると、耐
水性に優れた塗膜を形成することができる。According to the first aspect of the present invention, since collagen fiber bundles can be formed by stitching collagen fibers with a resin component formed by graft copolymerization, there is no entanglement between collagen fibers, and the collagen fibers are not entangled after drying. By pulverizing with a general-purpose pulverizer, a fine hybrid powder composed of collagen and a resin component can be obtained. When this hybrid powder is kneaded with a thermoplastic resin and an additive added as necessary, fine hybrid powder is uniformly dispersed in the kneaded product, and the kneaded product is molded by a conventional method to obtain a tough and smooth surface. It is possible to obtain a leather-like molded product having Further, when a mixture of the hybrid powder, a thermoplastic resin or a thermosetting resin, and an additive that is added as necessary is kneaded and applied onto leather, a coating film having excellent water resistance can be formed.
【0012】コラーゲン線維成分に対する樹脂成分の比
率がコラーゲン線維成分の50重量%未満であると、コ
ラーゲン粗線維表面はグラフト共重合されているが線維
内部はグラフト共重合されていない、いわば生コラーゲ
ン線維が存在し、この生コラーゲン線維は粉砕が困難で
あって、しかも分級困難な糸状のコラーゲンを発生させ
るという欠点がある。一方、コラーゲン線維成分に対す
る樹脂成分の比率がコラーゲン線維成分の200重量%
を超えると、すなわち、ハイブリッド粉末中のコラーゲ
ン成分の比率が低下すると、ハイブリッド粉末の重要な
特性である吸放湿能力の低下につながるという欠点があ
る。そこで、コラーゲン線維成分に対する樹脂成分の比
率は、コラーゲン線維成分の50〜200重量%とする
のが好ましい。係る樹脂成分としては、メタクリル酸メ
チルおよびメタクリル酸グリシジルモノマーとの共重合
によるグラフトポリマー、あるいはメタクリル酸メチル
およびメタクリル酸グリシジルモノマーとその他のモノ
マー、例えば、スチレン、酢酸ビニル、アクリロニトリ
ル、メタクリロニトリル、メタクリル酸ハイドロキシエ
ステル等メタクリル酸メチルと共重合しうるビニルモノ
マーとの共重合によるグラフトポリマーを使用すること
ができる。When the ratio of the resin component to the collagen fiber component is less than 50% by weight of the collagen fiber component, the surface of the collagen coarse fiber is graft-copolymerized but the interior of the fiber is not graft-copolymerized. However, this raw collagen fiber has a drawback that it is difficult to pulverize, and moreover, it produces thread-like collagen which is difficult to classify. On the other hand, the ratio of resin component to collagen fiber component is 200% by weight of collagen fiber component.
If it exceeds, that is, if the ratio of the collagen component in the hybrid powder decreases, there is a drawback that the moisture absorption / desorption ability, which is an important characteristic of the hybrid powder, decreases. Therefore, the ratio of the resin component to the collagen fiber component is preferably 50 to 200% by weight of the collagen fiber component. As such a resin component, a graft polymer obtained by copolymerization with a methyl methacrylate and a glycidyl methacrylate monomer, or a methyl methacrylate and a glycidyl methacrylate monomer and another monomer, for example, styrene, vinyl acetate, acrylonitrile, methacrylonitrile, methacryl A graft polymer obtained by copolymerization with a vinyl monomer copolymerizable with methyl methacrylate such as acid hydroxyester can be used.
【0013】熱可塑性樹脂としては、例えば、ポリエチ
レン、ポリプロピレン、ポリブタジエン、ポリスチレ
ン、ポリ塩化ビニル、ポリアミド、ポリカーボネート、
スチレン−ブタジエンブロックコポリマー等の公知のも
のを使用することができる。Examples of the thermoplastic resin include polyethylene, polypropylene, polybutadiene, polystyrene, polyvinyl chloride, polyamide, polycarbonate,
Known substances such as styrene-butadiene block copolymer can be used.
【0014】熱硬化性樹脂としては、例えば、ポリウレ
タン樹脂、メラミン樹脂、ユリア樹脂等の塗料用に適し
た公知のものを使用することができる。As the thermosetting resin, for example, known resins suitable for coating materials such as polyurethane resin, melamine resin and urea resin can be used.
【0015】添加剤としては、可塑剤、安定剤、充填
剤、着色剤、溶剤、分散剤など各種のものを使用するこ
とができる。As the additive, various kinds of additives such as a plasticizer, a stabilizer, a filler, a colorant, a solvent and a dispersant can be used.
【0016】また、ハイブリッド粉末は、40μm以下
の粒径のものが90重量%以上であれば、成形品の表面
をより平滑にしうるので好ましい。さらに、ハイブリッ
ド粉末の平均粒径が5μm未満の場合、粉砕コストが高
くなるばかりでなく、粉砕時間の増加とともにコラーゲ
ン成分の変性、着色が起こるという欠点があり、20μ
mを超えると、皮革様被膜形成において、被膜を薄膜化
することと被膜に光沢を付与することが困難になるとい
う欠点がある。そこで、ハイブリッド粉末の平均粒径
は、5〜20μmとするのが好ましい。The hybrid powder having a particle size of 40 μm or less is preferably 90% by weight or more because the surface of the molded product can be made smoother. Further, when the average particle size of the hybrid powder is less than 5 μm, not only the crushing cost becomes high, but also the denaturation and coloring of the collagen component occur with the increase of the crushing time.
If it exceeds m, there is a drawback that it becomes difficult to form a thin film and impart gloss to the film in forming a leather-like film. Therefore, the average particle size of the hybrid powder is preferably 5 to 20 μm.
【0017】[0017]
【実施例】以下、本発明の各実施例を工程順に説明す
る。
1.ハイブリッド粉末の製造
(a)コラーゲン粗繊維の製造
生体皮を通常の皮革製造における石灰漬、脱毛、脱脂、
脱灰等の工程を経て、裸皮から表皮および皮下組織を除
いた真皮部分(いわゆる床皮)を直径2mmのスクリーン
を付けたミートチョッパーで粗砕した皮を1.5〜2.
5重量%の水分含有率まで乾燥し、この粗砕乾燥皮を固
定刃および回転刃から構成されるウィリー型粉砕機に投
入し、直径1mmのスクリーンを通過したコラーゲン粗線
維を得た。このコラーゲン粗線維の粒度分布は以下のと
おりである。
150メッシュを通過したもの =0%
50メッシュ超〜150メッシュ未満を通過したもの=
23重量%
50メッシュを通過したもの =77重量%
(b)重合処理
そして、攪拌装置付き重合反応容器(図示せず、内容積
1600リットル)に、水1000重量部、酢酸17重
量部、上記コラーゲン粗繊維100重量部、プロピレン
オキシド5重量部およびメタクリル酸グリシジル0.4
重量部を添加して攪拌しながら35℃で24時間保持し
た。ついで、同反応容器にメタクリル酸メチル100重
量部を添加し、窒素ガスを同反応容器内に通入して重合
母液から酸素を除去した。そして、同反応容器内に窒素
ガスを通入しながら攪拌し、35〜40℃で48時間保
持した。そして、窒素ガスの通入を停止して重合を終了
させた後、硫酸アルミニウム15重量部と適量の水酸化
ナトリウム水溶液を同反応容器内に添加し、重合母液の
pHを7〜8に調整し、さらに24時間保持した。
(c)脱水処理
上記グラフト共重合処理で得られた重合体の水分含有率
を下げて後記する乾燥処理の時間を短縮するために、遠
心分離機を用いて水分含有率が75重量%になるまで脱
水した。この水分含有率は後記する乾燥時間を短縮する
ために80重量%以下とするのが好ましい。脱水のため
に使用する機器としては、遠心分離機以外に、フィルタ
ープレス、スクリュープレス等の公知の脱水機器を使用
することができる。
(d)乾燥処理
遠心分離機で水分含有率を下げてチップ状となったグラ
フト共重合体の水分含有率をさらに下げて後記する粉砕
処理を容易にするために、風通しのよい日陰の場所に脱
水されたグラフト共重合体を広げて水分含有率20重量
%程度まで風乾し、次いで、50℃の熱風乾燥機を用い
て、水分含有率3重量%まで乾燥させた。この水分含有
率は後記する粉砕処理を容易にするために10重量%以
下とするのが好ましい。
(e)粉砕処理
乾燥処理されたチップ状グラフト共重合体を振動ミルを
用いて粉砕し、以下の表1に示すような粒度分布を有す
るコラーゲンと樹脂からなるハイブリッド粉末を得た。
粉砕条件は、下記の通りである。
粉砕筒材質=ステンレス鋼
粉砕筒全容積=3.6リットル
粉砕方式=バッチ式
粉砕媒体=一般炭素鋼ロッド(直径19mm)
振動数=1200サイクル/min.
処理量=1.0kg/Hr
粉砕機としては、振動ミル以外に、ハンマーミル、ジェ
ットミル、ボールミル等の粉砕機を使用することができ
る。ハイブリッド粉末の平均粒径を5μm未満にしよう
とすると、著しく粉砕時間が長くなり、粉体の熱変性お
よび着色が誘起される。そのため、粉砕コストを抑制
し、粉体の熱変性および着色を誘起させないようにする
ために、ハイブリッド粉末の平均粒径を5μm以上にす
るのが好ましい。皮革様被膜を薄膜化しやすくなる点と
被膜に光沢を与えやすくするという理由により、ハイブ
リッド粉末の最大径は50μm以下にするのが好まし
く、20μm以下にするのがより好ましい。Embodiments of the present invention will be described below in the order of steps. 1. Manufacture of hybrid powder (a) Manufacture of collagen coarse fiber Living skin is limed, dehaired, and defatted in ordinary leather manufacturing.
After the steps such as decalcification, the dermis (so-called dermis) obtained by removing the epidermis and subcutaneous tissue from the naked dermis was coarsely crushed with a meat chopper equipped with a screen having a diameter of 2 mm.
After drying to a water content of 5% by weight, this coarsely crushed and dried skin was put into a wheelie type pulverizer composed of a fixed blade and a rotary blade to obtain a collagen coarse fiber which passed through a screen having a diameter of 1 mm. The particle size distribution of this collagen crude fiber is as follows. Those that passed 150 mesh = 0% Those that passed more than 50 mesh and less than 150 mesh =
23 wt% after passing through 50 mesh = 77 wt% (b) Polymerization treatment Then, in a polymerization reaction vessel equipped with a stirrer (not shown, internal volume: 1600 liters), 1000 parts by weight of water, 17 parts by weight of acetic acid, the above collagen 100 parts by weight of coarse fiber, 5 parts by weight of propylene oxide and 0.4 of glycidyl methacrylate
Parts by weight were added and the mixture was maintained at 35 ° C. for 24 hours while stirring. Then, 100 parts by weight of methyl methacrylate was added to the reaction vessel, and nitrogen gas was introduced into the reaction vessel to remove oxygen from the polymerization mother liquor. Then, the mixture was stirred while introducing nitrogen gas into the same reaction vessel, and kept at 35 to 40 ° C. for 48 hours. Then, after stopping the passage of nitrogen gas to terminate the polymerization, 15 parts by weight of aluminum sulfate and an appropriate amount of an aqueous solution of sodium hydroxide are added to the reaction vessel to adjust the pH of the polymerization mother liquor to 7 to 8. , And held for another 24 hours. (C) Dehydration treatment In order to reduce the water content of the polymer obtained by the above graft copolymerization treatment and shorten the time of the drying treatment described below, the water content becomes 75% by weight using a centrifuge. Dehydrated until. This water content is preferably 80% by weight or less in order to shorten the drying time described later. As a device used for dehydration, a known dehydration device such as a filter press or a screw press can be used in addition to the centrifugal separator. (D) Drying treatment To reduce the water content of the graft copolymer in the form of chips by further lowering the water content with a centrifuge, and to facilitate the pulverization process described later, place it in a well-ventilated and shaded place. The dehydrated graft copolymer was spread and air dried to a water content of about 20% by weight, and then dried using a hot air dryer at 50 ° C. to a water content of 3% by weight. This water content is preferably 10% by weight or less in order to facilitate the pulverization process described later. (E) Pulverizing treatment The dried chip-shaped graft copolymer was pulverized using a vibration mill to obtain a hybrid powder composed of collagen and resin having a particle size distribution as shown in Table 1 below.
The grinding conditions are as follows. Material of crushing cylinder = Stainless steel crushing cylinder Total volume = 3.6 liters Crushing method = Batch type crushing medium = General carbon steel rod (diameter 19 mm) Frequency = 1200 cycles / min. Amount of processing = 1.0 kg / Hr As a crusher Other than the vibration mill, a crusher such as a hammer mill, a jet mill or a ball mill can be used. If the average particle size of the hybrid powder is made to be less than 5 μm, the pulverization time becomes extremely long, and thermal denaturation and coloring of the powder are induced. Therefore, it is preferable that the average particle diameter of the hybrid powder is 5 μm or more in order to suppress the crushing cost and to prevent the thermal denaturation and coloring of the powder. The maximum diameter of the hybrid powder is preferably 50 μm or less, and more preferably 20 μm or less, for the reason that the leather-like film is likely to be thinned and the film is likely to be glossy.
【0018】[0018]
【表1】 [Table 1]
【0019】表1のものの平均粒径は、8μmであっ
た。
2.皮革様成形品の製造および皮革様塗膜の形成
(1)実施例1、2と比較例1、2
〔実施例1〕表1の粒径分布を有するハイブリッド粉末
50重量部とフタール酸ジオクチル30重量部と安定剤
3重量部とポリ塩化ビニル100重量部を混練機(図示
せず)を用いて160℃で混練し、その後、熱プレスし
て0.5mm厚のシートを得た。そのシートは、表面が平
滑で光沢のある天然の皮革の風合いを有するものであっ
た。
〔実施例2〕また、表1の粒径分布を有するハイブリッ
ド粉末30重量部とフタール酸ジオクチル30重量部と
安定剤3重量部とポリ塩化ビニル100重量部を同混練
機を用いて160℃で混練し、その後、熱プレスして
0.5mm厚のシートを得た。そのシートは、表面が平滑
で光沢のある天然の皮革の風合いを有するものであっ
た。The average particle size of those in Table 1 was 8 μm. 2. Production of leather-like molded article and formation of leather-like coating film (1) Examples 1 and 2 and Comparative Examples 1 and 2 [Example 1] 50 parts by weight of hybrid powder having a particle size distribution shown in Table 1 and dioctyl phthalate 30 By weight, 3 parts by weight of the stabilizer and 100 parts by weight of polyvinyl chloride were kneaded at 160 ° C. using a kneader (not shown), and then hot pressed to obtain a 0.5 mm thick sheet. The sheet had a natural leather texture with a smooth surface and gloss. [Example 2] Further, 30 parts by weight of a hybrid powder having a particle size distribution shown in Table 1, 30 parts by weight of dioctyl phthalate, 3 parts by weight of a stabilizer and 100 parts by weight of polyvinyl chloride were used at 160 ° C using the same kneader. After kneading and then hot pressing, a 0.5 mm thick sheet was obtained. The sheet had a natural leather texture with a smooth surface and gloss.
【0020】上記実施例1、2の成形シートの機械的特
性を表2に示し、吸放湿特性を表3に示す。The mechanical properties of the molded sheets of Examples 1 and 2 are shown in Table 2, and the moisture absorption / desorption properties are shown in Table 3.
【0021】[0021]
【表2】 [Table 2]
【0022】なお、摩擦係数の測定は、表面性試験機
「HEIDON−14R」を用いて、常法により静摩擦
係数と動摩擦係数を測定した。試験条件は、以下のとお
りである。The coefficient of friction was measured by a conventional method using a surface tester "HEIDON-14R" to measure the coefficient of static friction and the coefficient of dynamic friction. The test conditions are as follows.
【0023】圧子=3cm×3cm平面圧子 圧子移動速度=1000mm/分 荷重=100g(11g/cm2)Indenter = 3 cm × 3 cm Flat indenter Indenter moving speed = 1000 mm / min Load = 100 g (11 g / cm 2 ).
【0024】[0024]
【表3】 [Table 3]
【0025】なお、吸放湿特性に関する表3(および下
記の表5)に示す各特性値は、以下のようにして測定し
た。The characteristic values shown in Table 3 (and Table 5 below) relating to the moisture absorption and desorption characteristics were measured as follows.
【0026】表面が外気に曝されるように透湿カップに
セットした試料を、予め80℃で1晩乾燥させた後、3
5℃で相対湿度85%の環境下に移し、経時による重量
増加量を60分後(または10分後)に測定した(吸湿
性試験)。そして、その後直ちに35℃で相対湿度30
%の環境下に移して1時間後に重量減少量を測定した
(放湿性試験)。A sample set in a moisture permeable cup so that its surface is exposed to the outside air was dried in advance at 80 ° C. overnight and then 3
The sample was transferred to an environment of 5 ° C. and a relative humidity of 85%, and the amount of weight increase with time was measured after 60 minutes (or 10 minutes) (hygroscopicity test). Immediately thereafter, the relative humidity is 30 at 35 ° C.
%, The amount of weight loss was measured 1 hour later (moisture release test).
【0027】なお、表面吸湿量と表面放湿量は、次式に
より算出した。The surface moisture absorption amount and the surface moisture release amount were calculated by the following equations.
【0028】表面吸湿量=((60分後又は10分後の
試料重量)−(乾燥時の試料重量))/(試料面積)
表面放湿量=((放湿試験開始時の試料重量)−(1時
間後の試料重量))/(試料面積)
また、表面吸水度は、重量既知の試料の表面のみを水に
2分間浸らせた後、水滴状に試料に付着している水をぬ
ぐい去った後、その試料の重量増加量を測定し、その重
量増加量を試料面積で除したものを表面吸水度とした。Surface moisture absorption amount = ((Sample weight after 60 minutes or 10 minutes)-(Sample weight when dried)) / (Sample area) Surface moisture release amount = ((Sample weight at the start of moisture release test) -(Sample weight after 1 hour)) / (Sample area) As for the surface water absorption, after immersing only the surface of the sample of known weight in water for 2 minutes, the water adhering to the sample in the form of water droplets is measured. After wiping off, the weight gain of the sample was measured, and the weight gain was divided by the sample area to obtain the surface water absorption.
【0029】吸汗度は、皮表角層水分測定装置である、
商品名「Model Skicon−200」 のものを用いて、予め腕
の内側部分の皮膚表面水分量を測定した。次いで、その
腕の内側部分に試料を2分間押しつけ、再度、皮膚表面
水分量を測定し、次式を用いて吸汗度を算出した。表3
と表5に示す数値は、5回の測定値の平均である。吸汗
度は、数値が小さいほど吸汗性に優れていることを示
す。The degree of sweat absorption is measured by a skin surface stratum corneum moisture measuring device,
Using a model name “Model Skicon-200”, the water content on the skin surface of the inner part of the arm was measured in advance. Then, the sample was pressed against the inner part of the arm for 2 minutes, the water content on the skin surface was measured again, and the sweat absorption rate was calculated using the following formula. Table 3
The values shown in Table 5 and Table 5 are the averages of five measurements. The smaller the numerical value of the degree of sweat absorption, the better the sweat absorption.
【0030】吸汗度=(試料を押しつけた後の皮膚表面
水分量)×100/(押しつけ前の皮膚表面水分量)
〔比較例1〕また、比較例1として、粒径分布が100
〜0.3μmの範囲にわたり、平均粒径が40μmであ
る乾燥皮革粉30重量部とフタール酸ジオクチル30重
量部と安定剤3重量部とポリ塩化ビニル100重量部を
同混練機を用いて160℃で混練し、その後、熱プレス
して0.5mm厚のシートを得た。そのシートは、表面が
やや粗く、天然の皮革の風合いを有しているとは言えな
かった。
〔比較例2〕また、比較例2として、粒径分布が100
〜2μmの範囲にわたり、平均粒径が18μmである乾
燥皮革粉30重量部とフタール酸ジオクチル30重量部
と安定剤3重量部とポリ塩化ビニル100重量部を同混
練機を用いて160℃で混練し、その後、熱プレスして
0.5mm厚のシートを得た。そのシートは、表面がやや
粗く、天然の皮革の風合いを有しているとは言えなかっ
た。Sweat absorbency = (water amount on skin surface after pressing sample) × 100 / (water amount on skin surface before pressing) [Comparative Example 1] In Comparative Example 1, the particle size distribution was 100.
To 0.3 μm, 30 parts by weight of dry leather powder having an average particle size of 40 μm, 30 parts by weight of dioctyl phthalate, 3 parts by weight of stabilizer and 100 parts by weight of polyvinyl chloride were used at 160 ° C. using the same kneader. And then hot pressed to obtain a 0.5 mm thick sheet. The sheet had a rather rough surface and could not be said to have a natural leather texture. [Comparative Example 2] As Comparative Example 2, the particle size distribution was 100.
Kneading 30 parts by weight of dry leather powder having an average particle size of 18 μm, 30 parts by weight of dioctyl phthalate, 3 parts by weight of stabilizer and 100 parts by weight of polyvinyl chloride over a range of up to 2 μm at 160 ° C. using the same kneader. Then, hot pressing was performed to obtain a sheet having a thickness of 0.5 mm. The sheet had a rather rough surface and could not be said to have a natural leather texture.
【0031】比較例1、2の成形シートの機械的特性を
表4に示し、吸放湿特性を表5に示す。The mechanical properties of the molded sheets of Comparative Examples 1 and 2 are shown in Table 4, and the moisture absorption / desorption properties are shown in Table 5.
【0032】[0032]
【表4】 [Table 4]
【0033】[0033]
【表5】 [Table 5]
【0034】表2〜5より、以下の点が明らかである。
実施例1、2のシートは、比較例1、2のシートよ
り強度が高い。
実施例1、2のシートの表面は平滑であるから、静
摩擦係数および動摩擦係数ともに比較例1、2のシート
のものより低い。
実施例1、2のシートの表面吸湿量、表面放湿量お
よび表面吸水度の数値は、いずれも比較例1、2のシー
トの数値より十分に高く、一方、吸汗度の数値は、比較
例1、2のシートの数値より十分に低い。このように、
本発明のハイブリッド粉末を原料とする成形品の吸放湿
特性は極めて優れていることが分かる。
(2)実施例3
3本ペイントローラ上で一液型ポリウレタン樹脂溶液
(固形分33重量%)100重量部にN、Nジメチルホ
ルムアミド20重量部とメチルエチルケトン10重量部
と上記ハイブリッド粉末20重量部を添加し、同混練機
を用いて混練し、ペースト状物を得た。次いで、床革上
に上記ペーストをロールコーターによって一定の厚さに
塗布した。そして、この床革を水中に浸漬し、塗膜が十
分に硬化した後水中より取り出し、この床革をネット張
り乾燥機に張り付けて風乾し、静水圧プレスにて90℃
で皮革様の型押し加工を施すと、光沢のある天然の皮革
の風合いを有する皮革様成形品を得ることができた。
(3)実施例4、5と比較例3
〔実施例4〕アクリル酸エステル樹脂をエマルジョン化
した下塗り用バインダー200重量部と上記ハイブリッ
ド粉末25重量部と水200重量部と水性顔料100重
量部の混合物をホモジナイザー(図示せず)を用いてエ
マルジョン化した。次いで、床革上に上記エマルジョン
をロールコーターによって一定の厚さに塗装した。そし
て、この床革をネット張り乾燥機に張り付けて風乾し、
表面温度が90℃に設定されたアイロンによってアイロ
ン掛けを行うと、光沢のある天然の皮革の風合いを有す
る皮革様成形品を得ることができた。
〔実施例5〕ブタジエンポリマーをエマルジョン化した
下塗り用バインダー200重量部と上記ハイブリッド粉
末35重量部と水200重量部と水性顔料100重量部
の混合物を同ホモジナイザーを用いてエマルジョン化し
た。次いで、床革上に上記エマルジョンをロールコータ
ーによって一定の厚さに塗装した。そして、この床革を
ネット張り乾燥機に張り付けて風乾し、表面温度が90
℃に設定されたアイロンによってアイロン掛けを行う
と、光沢のある天然の皮革の風合いを有する皮革様成形
品を得ることができた。
〔比較例3〕比較例3として、実施例4、5において、
本発明のハイブリッド粉末に代えて公知技術4に記載さ
れた方法で得たコラーゲン粉末を用いた以外は実施例
4、5と同じ方法で皮革様成形品を得ようとしたが、上
記下塗りバインダーにそのコラーゲン粉末を配合すると
きにゲル化現象を起こし、目的とする皮革様塗膜形成用
エマルジョンを得ることはできなかった。
(4)実施例6、7と比較例4、5
〔実施例6〕アクリル樹脂系タイトコート剤A(ローム
&ハース社製の商品名「LT−87」)150重量部
と、アクリル樹脂系タイトコート剤B(ローム&ハース
社製の商品名「プライマル892」)120重量部と水
550重量部と浸透剤(ローム&ハース社製の商品名
「L−219」)120重量部と上記ハイブリッド粉末
60重量部を同ホモジナイザーを用いてエマルジョン化
し、吹き付け塗装機によって上記エマルジョンを床革上
に吹き付け塗装し、表面温度が90℃に設定されたアイ
ロンによってアイロン掛けを行うと、光沢のある天然の
皮革の風合いを有する皮革様成形品を得ることができ
た。
〔実施例7〕アクリル樹脂、ウレタン樹脂および無機充
填剤からなる塗料(TFL社製の商品名「ロダベースT
AM」)140重量部とウレタン樹脂バインダー(TF
L社製の商品名「デクタネWBO」)70重量部とアク
リル樹脂バインダー(TFL社製の商品名 「ロダクリ
ル155」)280重量部と顔料(ローム&ハース社製
の商品名「デアカラー」)130重量部と水300重量
部と浸透剤(ローム&ハース社製の商品名「L−21
9」)30重量部と上記ハイブリッド粉末50重量部を
同ホモジナイザーを用いてエマルジョン化し、表面温度
が90℃に設定されたアイロンによって床革にアイロン
掛けを行った後、吹き付け塗装機によって上記エマルジ
ョンをこの床革上に吹き付け塗装すると、光沢のある天
然の皮革の風合いを有する皮革様成形品を得ることがで
きた。
〔比較例4〕比較例4として、実施例6、7において、
本発明のハイブリッド粉末に代えて公知技術4に記載さ
れた方法で得たコラーゲン粉末を用いた以外は実施例
6、7と同じ方法で皮革様成形品を得ようとした。その
結果、前者(実施例6に対応するプロセス)の場合に
は、床革上にエマルジョンを吹き付け塗装することはで
きたが、後者(実施例7に対応するプロセス)の場合に
は、ホモジナイザー内の液にコラーゲン粉末が均一に分
散したエマルジョンを得ることはできず、ペースト化し
たので、床革にエマルジョンを吹き付け塗装することは
できなかった。
〔比較例5〕比較例5として、実施例6、7において、
本発明のハイブリッド粉末に代えて、通常のクロムなめ
しを施した皮革屑を裁断後、加熱水蒸気によりオートク
レーブ内で加熱、膨潤した後、乾燥・粉砕したコラーゲ
ン粉末(公知技術5に相当するもの)を用いた以外は実
施例6、7と同じ方法で皮革様成形品を得ようとした。
その結果、前者(実施例6に対応するプロセス)の場合
には、ホモジナイザー内の液に皮革粉が均一に分散した
エマルジョンを得ることはできず、ゲル化したので、床
革にエマルジョンを吹き付け塗装することはできなかっ
た。なお、後者(実施例7に対応するプロセス)の場合
には、床革上にエマルジョンを吹き付け塗装することは
できた。
(5)床革仕上げ剤への配合テスト
本発明のハイブリッド粉末10重量部を、以下に示す1
0品目の各床革仕上げ剤100重量部へ添加すると、い
ずれの床革仕上げ剤の場合でも、本発明のハイブリッド
粉末は良好に分散してエマルジョン化し、ゲル化するこ
とはなかった。The following points are clear from Tables 2-5. The sheets of Examples 1 and 2 have higher strength than the sheets of Comparative Examples 1 and 2. Since the surfaces of the sheets of Examples 1 and 2 are smooth, both the static friction coefficient and the dynamic friction coefficient are lower than those of the sheets of Comparative Examples 1 and 2. The numerical values of the surface moisture absorption amount, the surface moisture release amount and the surface water absorption of the sheets of Examples 1 and 2 are all sufficiently higher than the numerical values of the sheets of Comparative Examples 1 and 2, while the numerical value of the sweat absorption is the comparative example. It is much lower than the numbers on the 1st and 2nd sheets. in this way,
It can be seen that the molded product made from the hybrid powder of the present invention has extremely excellent moisture absorption and desorption properties. (2) Example 3 100 parts by weight of one-component polyurethane resin solution (solid content: 33% by weight), 20 parts by weight of N, N dimethylformamide, 10 parts by weight of methyl ethyl ketone, and 20 parts by weight of the above hybrid powder were used on three paint rollers. The mixture was added and kneaded using the same kneader to obtain a paste. Next, the above paste was applied on the floor leather by a roll coater to a constant thickness. Then, the floor leather is dipped in water, and after the coating film is sufficiently cured, it is taken out of the water, and the floor leather is attached to a net dryer and air-dried.
When a leather-like embossing process was performed with, a leather-like molded product having a glossy natural leather texture could be obtained. (3) Examples 4 and 5 and Comparative Example 3 [Example 4] 200 parts by weight of an undercoating binder obtained by emulsifying an acrylic acid ester resin, 25 parts by weight of the hybrid powder, 200 parts by weight of water, and 100 parts by weight of an aqueous pigment. The mixture was emulsified using a homogenizer (not shown). Then, the above emulsion was coated on the floor leather with a roll coater to a constant thickness. Then, stick this floor leather to a net dryer and air dry,
When ironing was performed with an iron having a surface temperature set to 90 ° C., a leather-like molded product having a glossy natural leather texture could be obtained. Example 5 A mixture of 200 parts by weight of a binder for an undercoat obtained by emulsifying a butadiene polymer, 35 parts by weight of the hybrid powder, 200 parts by weight of water and 100 parts by weight of an aqueous pigment was emulsified using the same homogenizer. Then, the above emulsion was coated on the floor leather with a roll coater to a constant thickness. Then, this floor leather is attached to a net dryer and air-dried, and the surface temperature is 90%.
Ironing with an iron set to ℃ made it possible to obtain a leather-like molded product having a glossy natural leather texture. Comparative Example 3 As Comparative Example 3, in Examples 4 and 5,
An attempt was made to obtain a leather-like molded article in the same manner as in Examples 4 and 5 except that the collagen powder obtained by the method described in the known art 4 was used in place of the hybrid powder of the present invention. When the collagen powder was blended, a gelation phenomenon occurred, and the intended emulsion for forming a leather-like coating film could not be obtained. (4) Examples 6 and 7 and Comparative Examples 4 and 5 [Example 6] 150 parts by weight of acrylic resin-based tight coating agent A (trade name "LT-87" manufactured by Rohm & Haas Co.) and acrylic resin-based tight 120 parts by weight of coating agent B (trade name "Primal 892" manufactured by Rohm & Haas), 550 parts by weight of water, 120 parts by weight of penetrant (trade name "L-219" manufactured by Rohm & Haas), and the above hybrid powder 60 parts by weight of the same homogenizer was emulsified, the above emulsion was spray-painted on the floor leather with a spray coating machine, and ironing was carried out with an iron whose surface temperature was set to 90 ° C. It was possible to obtain a leather-like molded product having the texture of. [Example 7] A coating composed of an acrylic resin, a urethane resin and an inorganic filler (trade name "Rodabase T" manufactured by TFL).
AM ") 140 parts by weight and urethane resin binder (TF
L company's trade name "Dectane WBO") 70 parts by weight, acrylic resin binder (TFL's trade name "Rodacryl 155") 280 parts by weight, and pigment (Rohm &Haas' trade name "Dear Color") 130 parts by weight Parts and 300 parts by weight of water and penetrant (trade name "L-21 manufactured by Rohm & Haas Co., Ltd.
9 ") 30 parts by weight and 50 parts by weight of the above hybrid powder are emulsified using the same homogenizer, iron the floor leather with an iron whose surface temperature is set to 90 ° C., and then spray the above emulsion with a spray coater. By spray-painting on this floor leather, a leather-like molded product having a glossy natural leather texture could be obtained. Comparative Example 4 As Comparative Example 4, in Examples 6 and 7,
A leather-like molded article was sought to be obtained in the same manner as in Examples 6 and 7, except that the collagen powder obtained by the method described in the known art 4 was used instead of the hybrid powder of the present invention. As a result, in the case of the former (process corresponding to Example 6), the emulsion could be spray-painted on the floor leather, but in the case of the latter (process corresponding to Example 7), inside the homogenizer. It was not possible to obtain an emulsion in which collagen powder was uniformly dispersed in the above liquid, and it was made into a paste, so it was not possible to spray paint the floor leather with the emulsion. Comparative Example 5 As Comparative Example 5, in Examples 6 and 7,
Instead of the hybrid powder of the present invention, after cutting leather scraps that have been subjected to normal chrome tanning, collagen powder (corresponding to known technique 5) that has been heated and swelled in an autoclave with steam and dried and crushed is used. An attempt was made to obtain a leather-like molded article by the same method as in Examples 6 and 7 except that the leather-like molded article was used.
As a result, in the case of the former (process corresponding to Example 6), it was not possible to obtain an emulsion in which leather powder was evenly dispersed in the liquid in the homogenizer, and gelling occurred, so the emulsion was spray-painted on the floor leather. I couldn't. In the latter case (process corresponding to Example 7), the emulsion could be spray-coated on the floor leather. (5) Compounding test into floor leather finishing agent 10 parts by weight of the hybrid powder of the present invention is shown below as 1
When added to 100 parts by weight of each of the floor leather finishes of item 0, the hybrid powder of the present invention was well dispersed, emulsified, and did not gel in any of the floor leather finishes.
【0035】しかし、公知技術4、5に記載された方法
で得たコラーゲン粉末の場合には、いずれも9品目の仕
上げ剤(以下のNo. 2〜No. 10のもの)において
ゲル化し、これらの仕上げ剤を用いた場合、皮革様塗料
として用いることはできないと判断された。
10品目の床革仕上げ剤(以下のNo.1〜No. 10
のもの)
No. 1=スタ−ルフィニシュ社製の商品名「1761
−A」(アクリル系水溶性樹脂)
No. 2=スタ−ルフィニシュ社製の商品名「RA−2
353」(アクリル系水溶性樹脂)
No. 3=ローム&ハース社製の商品名「LT−76」
(アクリル共重合エマルジョン)
No. 4=ローム&ハース社製の商品名「ハイドラック
PC」(アクリルトップコート)
No. 5=ローム&ハース社製の商品名「プライマルH
PB−980」(アクリルエマルジョンバインダー)
No. 6=ローム&ハース社製の商品名「プライマルE
863」(アクリルエマルジョンバインダー
No. 7=ローム&ハース社製の商品名「ST−84」
(熱可塑性アクリル共重合エマルジョンバインダー)
No. 8=ローム&ハース社製の商品名「SB150」
(アクリルバインダー)
No. 9=ローム&ハース社製の商品名「SB」(耐屈
曲性ベースバインダー)
No. 10=ローム&ハース社製の商品名「プライマル
S−1」(アクリル共重合エマルジョン)
(6)耐水試験
実施例6で得た皮革様成形品と、比較例4で得た皮革様
成形品(実施例6に対応するプロセスによるもの)と、
比較例5で得た皮革様成形品(実施例7に対応するプロ
セスによるもの)について、耐水試験を行った結果を以
下の表6に示す。However, in the case of the collagen powders obtained by the methods described in the publicly known techniques 4 and 5, all of the gelling agents were gelled in 9 kinds of finishing agents (the following Nos. 2 to 10), and It was judged that the above-mentioned finishing agent cannot be used as a leather-like paint. 10 floor leather finishing agents (No. 1 to No. 10 below)
No. 1 = Product name “1761” manufactured by Star Finish Co., Ltd.
-A "(acrylic water-soluble resin) No. 2 = product name" RA-2 "manufactured by Star Finnish
353 "(water-soluble acrylic resin) No. 3 = product name" LT-76 "manufactured by Rohm & Haas Co.
(Acrylic Copolymer Emulsion) No. 4 = Rohm & Haas brand name "Hydrac PC" (acrylic top coat) No. 5 = Rohm & Haas brand name "Primal H"
PB-980 "(acrylic emulsion binder) No. 6 = product name" Primal E "manufactured by Rohm & Haas
863 "(acrylic emulsion binder No. 7 = trade name" ST-84 "manufactured by Rohm & Haas)
(Thermoplastic acrylic copolymer emulsion binder) No. 8 = Product name "SB150" manufactured by Rohm & Haas Co.
(Acrylic binder) No. 9 = product name "SB" manufactured by Rohm & Haas (flexible base binder) No. 10 = product name "Primal S-1" manufactured by Rohm & Haas (acrylic copolymer emulsion) (6) Water resistance test Leather-like molded article obtained in Example 6 and leather-like molded article obtained in Comparative Example 4 (by the process corresponding to Example 6),
The leather-like molded article obtained in Comparative Example 5 (by the process corresponding to Example 7) was subjected to a water resistance test, and the results are shown in Table 6 below.
【0036】[0036]
【表6】 [Table 6]
【0037】表6に明らかなように、実施例6で得た皮
革様成形品は、比較例4および5による皮革様成形品に
比べて、極めて優れた耐水性を有することが分かる。As is clear from Table 6, the leather-like molded products obtained in Example 6 have extremely excellent water resistance as compared with the leather-like molded products of Comparative Examples 4 and 5.
【0038】[0038]
【発明の効果】本発明は上記のように構成されているの
で、以下の効果を有する。
(1)本発明のハイブリッド粉末を用いることにより、
強靱で平滑な表面を有する、天然の皮革の風合いを有す
る皮革様成形品を得ることができる。
(2)本発明のハイブリッド粉末を用いることにより、
耐水性に優れた皮革様塗膜を形成することができる。Since the present invention is constructed as described above, it has the following effects. (1) By using the hybrid powder of the present invention,
It is possible to obtain a leather-like molded product having a tough, smooth surface and a texture of natural leather. (2) By using the hybrid powder of the present invention,
A leather-like coating film having excellent water resistance can be formed.
───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) D06N 3/00 - 3/18 C14B 7/04 ─────────────────────────────────────────────────── ─── Continuation of front page (58) Fields investigated (Int.Cl. 7 , DB name) D06N 3/00-3/18 C14B 7/04
Claims (2)
ーゲン線維成分に対して50〜200重量%の樹脂成分
とを有するものをグラフト共重合することによって得た
重合体を乾燥後に粉砕することによって得ることのでき
るコラーゲンと樹脂成分からなるハイブリッド粉末。1. A polymer obtained by graft-copolymerizing a collagen fiber component and a resin component having a weight ratio of 50 to 200% by weight with respect to the collagen fiber component is dried and then pulverized. A hybrid powder composed of collagen and a resin component that can be obtained.
径のものが90重量%以上であって、その平均粒径が5
〜20μmである請求項1記載のハイブリッド粉末。2. The hybrid powder has a particle size of 40 μm or less in an amount of 90% by weight or more and has an average particle size of 5%.
The hybrid powder according to claim 1, which has a size of -20 μm.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000216233A JP3432788B2 (en) | 2000-07-17 | 2000-07-17 | Hybrid powder consisting of collagen and resin components |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2000216233A JP3432788B2 (en) | 2000-07-17 | 2000-07-17 | Hybrid powder consisting of collagen and resin components |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2002030300A JP2002030300A (en) | 2002-01-31 |
| JP3432788B2 true JP3432788B2 (en) | 2003-08-04 |
Family
ID=18711528
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2000216233A Expired - Fee Related JP3432788B2 (en) | 2000-07-17 | 2000-07-17 | Hybrid powder consisting of collagen and resin components |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP3432788B2 (en) |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2014231645A (en) * | 2011-09-16 | 2014-12-11 | メルクス株式会社 | Artificial leather paste, and artificial leather sheet and repair material including the same |
| CN103215392A (en) * | 2013-05-04 | 2013-07-24 | 西南大学 | Ultrasonic emulsifying degreasing method for animal skin |
| TWI661001B (en) * | 2017-11-13 | 2019-06-01 | 瀚醫生技股份有限公司 | Collagen-containing plastic masterbatch, method for producing the same, product made therefrom and use thereof |
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- 2000-07-17 JP JP2000216233A patent/JP3432788B2/en not_active Expired - Fee Related
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| Publication number | Publication date |
|---|---|
| JP2002030300A (en) | 2002-01-31 |
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