JPS63110226A - Production of water-absorptive resin material - Google Patents
Production of water-absorptive resin materialInfo
- Publication number
- JPS63110226A JPS63110226A JP25525086A JP25525086A JPS63110226A JP S63110226 A JPS63110226 A JP S63110226A JP 25525086 A JP25525086 A JP 25525086A JP 25525086 A JP25525086 A JP 25525086A JP S63110226 A JPS63110226 A JP S63110226A
- Authority
- JP
- Japan
- Prior art keywords
- water
- resin material
- absorbing resin
- weight
- carboxylate
- 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.)
- Pending
Links
- 229920005989 resin Polymers 0.000 title claims abstract description 73
- 239000011347 resin Substances 0.000 title claims abstract description 73
- 239000000463 material Substances 0.000 title claims abstract description 34
- 238000004519 manufacturing process Methods 0.000 title claims description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 49
- 239000000203 mixture Substances 0.000 claims abstract description 32
- 239000002131 composite material Substances 0.000 claims abstract description 22
- 125000003055 glycidyl group Chemical group C(C1CO1)* 0.000 claims abstract description 22
- 229920000098 polyolefin Polymers 0.000 claims abstract description 20
- 238000002844 melting Methods 0.000 claims abstract description 8
- 230000008018 melting Effects 0.000 claims abstract description 8
- 150000007942 carboxylates Chemical class 0.000 claims description 15
- 230000002745 absorbent Effects 0.000 claims description 11
- 239000002250 absorbent Substances 0.000 claims description 11
- 238000010521 absorption reaction Methods 0.000 abstract description 27
- 238000001125 extrusion Methods 0.000 abstract description 13
- 238000004898 kneading Methods 0.000 abstract description 11
- 229920001495 poly(sodium acrylate) polymer Polymers 0.000 abstract description 2
- NNMHYFLPFNGQFZ-UHFFFAOYSA-M sodium polyacrylate Chemical compound [Na+].[O-]C(=O)C=C NNMHYFLPFNGQFZ-UHFFFAOYSA-M 0.000 abstract description 2
- 229920001577 copolymer Polymers 0.000 description 15
- -1 polyethylene Polymers 0.000 description 12
- 238000000034 method Methods 0.000 description 9
- 238000005187 foaming Methods 0.000 description 8
- 230000014759 maintenance of location Effects 0.000 description 8
- 238000002156 mixing Methods 0.000 description 8
- 238000000465 moulding Methods 0.000 description 6
- 239000000835 fiber Substances 0.000 description 5
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 5
- 229910052783 alkali metal Inorganic materials 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 239000005038 ethylene vinyl acetate Substances 0.000 description 4
- 239000000155 melt Substances 0.000 description 4
- 239000008188 pellet Substances 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- 239000004156 Azodicarbonamide Substances 0.000 description 3
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 3
- 239000005977 Ethylene Substances 0.000 description 3
- 239000004698 Polyethylene Substances 0.000 description 3
- 239000004743 Polypropylene Substances 0.000 description 3
- XOZUGNYVDXMRKW-AATRIKPKSA-N azodicarbonamide Chemical compound NC(=O)\N=N\C(N)=O XOZUGNYVDXMRKW-AATRIKPKSA-N 0.000 description 3
- 235000019399 azodicarbonamide Nutrition 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000000178 monomer Substances 0.000 description 3
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 3
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 3
- 229920000573 polyethylene Polymers 0.000 description 3
- 229920001155 polypropylene Polymers 0.000 description 3
- 229920005992 thermoplastic resin Polymers 0.000 description 3
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 2
- IMROMDMJAWUWLK-UHFFFAOYSA-N Ethenol Chemical compound OC=C IMROMDMJAWUWLK-UHFFFAOYSA-N 0.000 description 2
- JIGUQPWFLRLWPJ-UHFFFAOYSA-N Ethyl acrylate Chemical compound CCOC(=O)C=C JIGUQPWFLRLWPJ-UHFFFAOYSA-N 0.000 description 2
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 description 2
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 2
- XTXRWKRVRITETP-UHFFFAOYSA-N Vinyl acetate Chemical compound CC(=O)OC=C XTXRWKRVRITETP-UHFFFAOYSA-N 0.000 description 2
- 150000001340 alkali metals Chemical class 0.000 description 2
- 150000001336 alkenes Chemical class 0.000 description 2
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 2
- 239000002666 chemical blowing agent Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 229920000578 graft copolymer Polymers 0.000 description 2
- 238000007654 immersion Methods 0.000 description 2
- RPQRDASANLAFCM-UHFFFAOYSA-N oxiran-2-ylmethyl prop-2-enoate Chemical compound C=CC(=O)OCC1CO1 RPQRDASANLAFCM-UHFFFAOYSA-N 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- PNJWIWWMYCMZRO-UHFFFAOYSA-N pent‐4‐en‐2‐one Natural products CC(=O)CC=C PNJWIWWMYCMZRO-UHFFFAOYSA-N 0.000 description 2
- 229920000058 polyacrylate Polymers 0.000 description 2
- 229920005672 polyolefin resin Polymers 0.000 description 2
- 239000011734 sodium Substances 0.000 description 2
- 238000001291 vacuum drying Methods 0.000 description 2
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 2
- CZGWDPMDAIPURF-UHFFFAOYSA-N (4,6-dihydrazinyl-1,3,5-triazin-2-yl)hydrazine Chemical compound NNC1=NC(NN)=NC(NN)=N1 CZGWDPMDAIPURF-UHFFFAOYSA-N 0.000 description 1
- 229920003067 (meth)acrylic acid ester copolymer Polymers 0.000 description 1
- QLZJUIZVJLSNDD-UHFFFAOYSA-N 2-(2-methylidenebutanoyloxy)ethyl 2-methylidenebutanoate Chemical compound CCC(=C)C(=O)OCCOC(=O)C(=C)CC QLZJUIZVJLSNDD-UHFFFAOYSA-N 0.000 description 1
- KUDUQBURMYMBIJ-UHFFFAOYSA-N 2-prop-2-enoyloxyethyl prop-2-enoate Chemical compound C=CC(=O)OCCOC(=O)C=C KUDUQBURMYMBIJ-UHFFFAOYSA-N 0.000 description 1
- 229920002126 Acrylic acid copolymer Polymers 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 229920000089 Cyclic olefin copolymer Polymers 0.000 description 1
- MWRWFPQBGSZWNV-UHFFFAOYSA-N Dinitrosopentamethylenetetramine Chemical compound C1N2CN(N=O)CN1CN(N=O)C2 MWRWFPQBGSZWNV-UHFFFAOYSA-N 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- 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 1
- WHXSMMKQMYFTQS-UHFFFAOYSA-N Lithium Chemical compound [Li] WHXSMMKQMYFTQS-UHFFFAOYSA-N 0.000 description 1
- CERQOIWHTDAKMF-UHFFFAOYSA-M Methacrylate Chemical compound CC(=C)C([O-])=O CERQOIWHTDAKMF-UHFFFAOYSA-M 0.000 description 1
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 229920002125 Sokalan® Polymers 0.000 description 1
- 229920002472 Starch Polymers 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- VRFNYSYURHAPFL-UHFFFAOYSA-N [(4-methylphenyl)sulfonylamino]urea Chemical compound CC1=CC=C(S(=O)(=O)NNC(N)=O)C=C1 VRFNYSYURHAPFL-UHFFFAOYSA-N 0.000 description 1
- 239000011358 absorbing material Substances 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- CQEYYJKEWSMYFG-UHFFFAOYSA-N butyl acrylate Chemical compound CCCCOC(=O)C=C CQEYYJKEWSMYFG-UHFFFAOYSA-N 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 238000005034 decoration Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- UIWXSTHGICQLQT-UHFFFAOYSA-N ethenyl propanoate Chemical compound CCC(=O)OC=C UIWXSTHGICQLQT-UHFFFAOYSA-N 0.000 description 1
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 1
- SUPCQIBBMFXVTL-UHFFFAOYSA-N ethyl 2-methylprop-2-enoate Chemical compound CCOC(=O)C(C)=C SUPCQIBBMFXVTL-UHFFFAOYSA-N 0.000 description 1
- 229920001038 ethylene copolymer Polymers 0.000 description 1
- 229920006244 ethylene-ethyl acrylate Polymers 0.000 description 1
- 239000005042 ethylene-ethyl acrylate Substances 0.000 description 1
- XUCNUKMRBVNAPB-UHFFFAOYSA-N fluoroethene Chemical compound FC=C XUCNUKMRBVNAPB-UHFFFAOYSA-N 0.000 description 1
- 239000004088 foaming agent Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 238000010413 gardening Methods 0.000 description 1
- VOZRXNHHFUQHIL-UHFFFAOYSA-N glycidyl methacrylate Chemical compound CC(=C)C(=O)OCC1CO1 VOZRXNHHFUQHIL-UHFFFAOYSA-N 0.000 description 1
- 239000008240 homogeneous mixture Substances 0.000 description 1
- 238000003898 horticulture Methods 0.000 description 1
- 239000012770 industrial material Substances 0.000 description 1
- 239000011256 inorganic filler Substances 0.000 description 1
- 229910003475 inorganic filler Inorganic materials 0.000 description 1
- 229920000554 ionomer Polymers 0.000 description 1
- 229910052744 lithium Inorganic materials 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 125000005395 methacrylic acid group Chemical group 0.000 description 1
- ZIUHHBKFKCYYJD-UHFFFAOYSA-N n,n'-methylenebisacrylamide Chemical compound C=CC(=O)NCNC(=O)C=C ZIUHHBKFKCYYJD-UHFFFAOYSA-N 0.000 description 1
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- 229940065472 octyl acrylate Drugs 0.000 description 1
- ANISOHQJBAQUQP-UHFFFAOYSA-N octyl prop-2-enoate Chemical compound CCCCCCCCOC(=O)C=C ANISOHQJBAQUQP-UHFFFAOYSA-N 0.000 description 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 1
- 238000004806 packaging method and process Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000009512 pharmaceutical packaging Methods 0.000 description 1
- 239000004584 polyacrylic acid Substances 0.000 description 1
- 229920001083 polybutene Polymers 0.000 description 1
- 229920000306 polymethylpentene Polymers 0.000 description 1
- 239000011116 polymethylpentene Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000011342 resin composition Substances 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 239000008107 starch Substances 0.000 description 1
- 235000019698 starch Nutrition 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000006097 ultraviolet radiation absorber Substances 0.000 description 1
- 239000000052 vinegar Substances 0.000 description 1
- 229920006163 vinyl copolymer Polymers 0.000 description 1
- 229920001567 vinyl ester resin Polymers 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 238000004078 waterproofing Methods 0.000 description 1
- 239000001993 wax Substances 0.000 description 1
Landscapes
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
Abstract
Description
【発明の詳細な説明】
0)産業上の利用分野
本発明は、吸水性樹脂材の製造方法に関し、さらに詳し
くは、吸水速度が大きく、かつ、吸水後の吸水性樹脂の
保持性に優れ高吸水性を有するフィルム状、シート状、
ul、雄状等の吸水性樹脂材の製造方法に関する。DETAILED DESCRIPTION OF THE INVENTION 0) Industrial Application Field The present invention relates to a method for producing a water-absorbing resin material, and more specifically, it relates to a method for producing a water-absorbing resin material, and more specifically, it relates to a method for producing a water-absorbing resin material, and more specifically, a water-absorbing resin material having a high water absorption rate and excellent retention of the water-absorbing resin after water absorption. Water-absorbing film, sheet,
The present invention relates to a method for producing water-absorbing resin materials such as UL and male-shaped water-absorbing resin materials.
←)従来の技術
現在、吸水性樹脂は、紙おむつ、生理用品等の衛生材料
用吸収剤、lk園芸用保水剤、その他工業資材等として
、架橋ポリアクリル酸アルカリ金属塩、アクリル酸アル
カリ金属塩グラフトデンプン架橋物、ビニルアルコール
・アクリル酸アルカリ金属塩コポリマー架橋物、ビニル
アルコール・無水マレイン酸コホリマー架a物等が用い
られている。これらは、いずれの樹脂においても、吸水
後の形態保持性を得るために架橋体となっており、粉末
状である。←) Conventional technology Currently, water-absorbing resins are used as absorbents for sanitary materials such as disposable diapers and sanitary products, water retention agents for LK gardening, and other industrial materials. A starch crosslinked product, a vinyl alcohol/acrylic acid alkali metal salt copolymer crosslinked product, a vinyl alcohol/maleic anhydride copolymer crosslinked product, etc. are used. All of these resins are crosslinked in order to maintain their shape after water absorption, and are in powder form.
さらに、近年、吸水性樹脂の使用用途は拡大の一途をた
どっており、使用形態も粉末状だけでなく、フィルム、
シート、繊維等の形態での吸水性樹脂の要望が大きい。Furthermore, in recent years, the applications of water-absorbing resins have been expanding steadily, and the forms of use are not only powder, but also films,
There is a strong demand for water absorbent resins in the form of sheets, fibers, etc.
しかし、現行の吸水性樹脂は、架橋体であるところから
熱可塑性がなく、フィルム、シート、繊維等への加工が
著しく困難である。However, since current water-absorbing resins are crosslinked, they lack thermoplasticity, making it extremely difficult to process them into films, sheets, fibers, and the like.
一方、現行の吸水性樹脂にフィルム、繊維等成形加工性
を賦与すべく、例えば、ポリエチレン、ポリプロピレン
等ポリオレフィンと吸水性樹脂との混合においては、両
者の相溶性不良のために均一な混合物が得られないのみ
ならず、吸水速度および吸水性の低下が著しく、また吸
水後における吸水性樹脂の脱離が著しいという問題があ
り、さらに、エチレン−アクリル酸共重合体、エチレン
−アクリル酸エステル共重合体等の極性基含有ポリオレ
フィンと吸水性樹脂との混合においても、不均一混合の
問題は解消されるものの、その余の問題を残したもので
しかない。On the other hand, when mixing polyolefins such as polyethylene and polypropylene with water-absorbing resins in order to impart moldability to films, fibers, etc. to current water-absorbing resins, it is difficult to obtain a homogeneous mixture due to poor compatibility between the two. In addition, there are problems in that the water absorption rate and water absorbency are significantly reduced, and the water-absorbing resin is significantly desorbed after water absorption. Although the problem of non-uniform mixing is solved when a polar group-containing polyolefin and a water-absorbing resin are mixed together, other problems remain.
一方、それら混合物を発泡させることにより吸水速度を
1暉的に向上させ得ることが、特公昭61−37095
号公報によ抄知られているが、これとて、前述のその余
の問題を解決し得てはいない。On the other hand, it was reported in Japanese Patent Publication No. 61-37095 that the water absorption rate could be improved instantly by foaming the mixture.
Although an excerpt is known from the publication No. 1, it has not been able to solve the remaining problems mentioned above.
(−)発明が解決しようとする問題点
本発明者等は、カルボキシレート含有の吸水性樹脂とグ
リシジル基含有ポリオレフィンとを後者の融点以上の温
度で溶融混練してなる複合組成物が、成形加工性を有す
るのみならず、高吸水性を有し、吸水後における吸水性
樹脂の脱離がなくその保持性に優れる材料として有用で
あることを見出し、本発明に到達したものでろ抄、従っ
て、本発明は、吸水速度が大きく、かつ、吸水後の吸水
性樹脂の保持性に優れ高吸水性を有するフィルム状、シ
ート状、繊維状等の吸水性樹脂材の製造方法を提供する
ことを目的とする。(-) Problems to be Solved by the Invention The present inventors have discovered that a composite composition obtained by melt-kneading a carboxylate-containing water-absorbing resin and a glycidyl group-containing polyolefin at a temperature higher than the melting point of the latter can be molded and processed. The present invention has been developed based on the discovery that it is useful as a material that not only has high water absorption properties but also has excellent retention properties without desorption of water-absorbing resin after water absorption. An object of the present invention is to provide a method for producing water-absorbing resin materials in the form of films, sheets, fibers, etc., which have a high water absorption rate, excellent retention of water-absorbing resin after water absorption, and high water absorption properties. shall be.
に)問題点を解決するための手段
本発明の吸水性樹脂材の製造方法は、カルボキシレート
含有の吸水性樹脂5〜95重量%とグリシジル基含有ポ
リオレフィン95〜5重量%とを後者の融点以上の温度
で溶融混練して複合組成物となし、該複合組成物を押出
成形し発泡させることを特徴とする。B) Means for Solving the Problems The method for producing a water-absorbing resin material of the present invention involves mixing 5 to 95% by weight of a carboxylate-containing water-absorbing resin and 95 to 5% by weight of a glycidyl group-containing polyolefin at a temperature higher than the melting point of the latter. It is characterized in that it is melt-kneaded at a temperature of 100 to form a composite composition, and the composite composition is extruded and foamed.
本発明におけるカルボキシレート含有の吸水性樹脂は、
次のように定義される。The carboxylate-containing water absorbent resin in the present invention is
It is defined as follows.
先ス、「カルボキシレート」はカルボキシル基の中和塩
であって、一般式−〇〇〇Mで示される。このMは、−
価のアルカリ金属(Na、に等)またはアンモニウム(
NH4)である。吸水性樹脂のカルボキシル基とアルカ
リ金属との反応率は、吸水能力見合いで変更が可能であ
って、−般には40〜100%である。First, "carboxylate" is a neutralized salt of a carboxyl group, and is represented by the general formula -〇〇〇M. This M is -
valent alkali metals (Na, etc.) or ammonium (
NH4). The reaction rate between the carboxyl group of the water-absorbing resin and the alkali metal can be changed depending on the water-absorbing ability, and is generally 40 to 100%.
考えられる種々の用途からいって、このカルボキシレー
ト含有の吸水性樹脂は、吸水率が30〜2000倍程度
のものが好ましい。Considering various possible uses, this carboxylate-containing water-absorbing resin preferably has a water absorption rate of about 30 to 2000 times.
本発明におけるカルボキシレート含有の吸水性樹脂を製
造する代表的な方法は、特開昭58−42602号、同
58−71907号、同59−62665号、同61−
157513号公報等に示されている。Typical methods for producing the carboxylate-containing water-absorbing resin in the present invention include JP-A-58-42602, JP-A-58-71907, JP-A-59-62665, and JP-A-JP-A-Sho 61-61.
It is shown in JP157513 and the like.
本発明で使用するのに適したカルボキシレート含有の吸
水性樹脂の具体例は、例えば、架橋ポリアクリル酸ナト
リウム、同カリウム、同リチウム等の架橋ポリアクリル
酸アルカリ金属塩である。これらは架橋しているのが望
ましい。Specific examples of carboxylate-containing water absorbent resins suitable for use in the present invention are alkali metal salts of crosslinked polyacrylates, such as, for example, sodium, potassium, and lithium crosslinked polyacrylates. It is desirable that these are crosslinked.
架橋構造は、ジビニルないレジアクリル化合物、特に水
溶性のもの、例えばN、N’−メチレンビス−アクリル
アミド、エチレングリコールビスアクリレート、その他
を共重合させることによって導入することができる。Crosslinked structures can be introduced by copolymerizing divinyl-resacrylic compounds, especially those that are water-soluble, such as N,N'-methylene bis-acrylamide, ethylene glycol bis-acrylate, and others.
また、本発明で使用するのに適した吸水性樹脂は、粒径
が40ミクロン以下のものであゆ、1〜lOミクロンが
特に好ましい。粒径が40ミクロンより大きいと、組成
物を特にフィルム状に押出成形するにおいて安定生産性
を欠くことになる。The water-absorbing resin suitable for use in the present invention has a particle size of 40 microns or less, particularly preferably 1 to 10 microns. If the particle size is larger than 40 microns, stable productivity will be lacking, especially when extruding the composition into a film.
本発明におけるグリシジル基含有ポリオレフィンは、次
のように定義される。The glycidyl group-containing polyolefin in the present invention is defined as follows.
先ず、これはグリンジル基を含有するポリオレフィン切
崩であれば、主鎖共重合体およびグラフト共重合体のい
ずれでもよい。First, this may be either a main chain copolymer or a graft copolymer as long as it is a polyolefin truncation containing Grindyl groups.
主鎖共重合体としては、オレフィン、例えばエチレンと
、グリシジル基含有モノマーとの共重合体がある。具体
的には、エチレン−グリシジルアクリレート共重合体、
エチレン−グリシジルメタクリレート共重合体、および
エチレン−グリシジルクロトネート共重合体等が例示て
れ、一般に、オレフィン、例えばエチレンと、ビニル基
含有エポキシ化合物との共重合体は全て含まれる。また
、これらのエチレン共重合体は、柔軟性等の性質を賦与
するために、その他のコモノマーを共重合させたもので
あってもよい。ここで、その他のコモノマーとして使用
できるものには、エチレンと共重合できるモノマー全て
が含まれる。例えば、酢酸ビニル、プロピオン酸ビニル
等のビニルエステル、アクリル酸メチル、アクリル酸エ
チル、アクリル酸ブチル、アクリル酸オクチル等のアク
リル酸エステル、メタクリル酸メチル、メタクリル酸エ
チル等のメタクリル酸エステル、塩化ビニル、フッ化ビ
ニル等のハロゲン化ビニル等がある。The main chain copolymer includes a copolymer of an olefin, such as ethylene, and a monomer containing a glycidyl group. Specifically, ethylene-glycidyl acrylate copolymer,
Examples include ethylene-glycidyl methacrylate copolymers and ethylene-glycidyl crotonate copolymers, and generally all copolymers of olefins, such as ethylene, and vinyl group-containing epoxy compounds are included. Further, these ethylene copolymers may be copolymerized with other comonomers in order to impart properties such as flexibility. Here, other comonomers that can be used include all monomers that can be copolymerized with ethylene. For example, vinyl esters such as vinyl acetate and vinyl propionate; acrylic esters such as methyl acrylate, ethyl acrylate, butyl acrylate, and octyl acrylate; methacrylic esters such as methyl methacrylate and ethyl methacrylate; vinyl chloride; Examples include vinyl halides such as vinyl fluoride.
グラフト共重合体としては、ポリエチレン、ポリプロピ
レン、ポリブテン、ポリメチルペンテン等へのグリシジ
ル基含有モノマーのグラフト物がある。グラフト用に用
いられる七ツマ−の具体例としては、グリシジルアクリ
レート、グリシジルアクリレート、グリシジルクロトネ
ート、ビニルグリシジル等がある。Examples of graft copolymers include grafts of glycidyl group-containing monomers onto polyethylene, polypropylene, polybutene, polymethylpentene, and the like. Specific examples of hexamers used for grafting include glycidyl acrylate, glycidyl acrylate, glycidyl crotonate, and vinylglycidyl.
このようなグリシジル基含有ポリオレフィンのグリシジ
ル基含有縫は、0.1〜20重敬%が適当である。グリ
シジル基含有量が0.1重i%未満であると、吸水性樹
脂材として吸水後の吸水性樹脂の保持性が不十分となる
傾向にあり、一方、グリシジル基含有量が20重量%を
越えると、ゲル化して成形性が失なわれる傾向にある。The glycidyl group-containing stitch of such a glycidyl group-containing polyolefin is suitably 0.1 to 20% by weight. If the glycidyl group content is less than 0.1% by weight, the water-absorbing resin material tends to have insufficient retention of the water-absorbing resin after water absorption.On the other hand, if the glycidyl group content is less than 20% by weight If it exceeds it, it tends to gel and lose moldability.
好適には0.5〜15重量%、さらに好適には1〜10
重量%である。Preferably 0.5 to 15% by weight, more preferably 1 to 10% by weight
Weight%.
また、本発明で使用するのに適したグリシジル基含有ポ
リオレフィンは、メルトフローレートが0.01 t/
10分以上のものであり、0.1〜zoor/lo分
が好ましく、1〜502/10分が特に好ましい。メル
トフローレートがo、oxr/lo分より小さいと、組
成物の流動性が劣し押出成形が困難となる。Further, the glycidyl group-containing polyolefin suitable for use in the present invention has a melt flow rate of 0.01 t/
The duration is preferably 10 minutes or more, preferably 0.1 to zoor/lo minutes, and particularly preferably 1 to 502/10 minutes. If the melt flow rate is less than o, oxr/lo, the composition will have poor fluidity and will be difficult to extrude.
また、グリシジル基含有ポリオレフィンの形状は、粉末
、ベレットのいずれでも良いが、分散性の点からは粉末
が望ましい。Further, the shape of the glycidyl group-containing polyolefin may be either powder or pellet, but powder is preferable from the viewpoint of dispersibility.
本発明において、カルボキシレート含有の吸水性樹脂と
グリシジル基含有ポリオレフィンの配合割合は、前者の
吸水性樹脂が5〜95重量%、好ましくは10〜70重
量%、後者のポリオレフィンが95〜5重量%、好まし
くは90〜30重量%である。前者の吸水性樹脂が5型
持%未満では吸水性能が低くて、この組成物を吸水性を
有する材料として用いる優位性がなくなるっ一方、95
重量%を越えると押出成形が困難となる。In the present invention, the blending ratio of the carboxylate-containing water-absorbing resin and the glycidyl group-containing polyolefin is 5 to 95% by weight, preferably 10 to 70% by weight of the former water-absorbing resin, and 95 to 5% by weight of the latter polyolefin. , preferably 90 to 30% by weight. If the former water-absorbing resin has a type content of less than 5%, the water-absorbing performance will be low, and the advantage of using this composition as a water-absorbing material will be lost.
If it exceeds % by weight, extrusion molding becomes difficult.
両者の配合割合は、この範囲内で使用用途に応じて適宜
設定できるが、一般に、吸水性能を重視する用途にはカ
ルボキシレート含有の吸水性樹脂を多く、一方、成形性
を重視する用途にはグリシジル基含有ポリオレフィンの
割合を多くすることが好ましい。The blending ratio of both can be set as appropriate within this range depending on the intended use, but generally, for applications where water absorption performance is important, a large amount of carboxylate-containing water absorbent resin is used, while for applications where moldability is important, a large amount of water absorbent resin is used. It is preferable to increase the proportion of the glycidyl group-containing polyolefin.
カルボキシレート含有の吸水性樹脂とグリシジル基含有
ポリオレフィンとは、グリシジル基含有ポリオレフィン
の融点以上の温度で溶融混練することにより複合組成物
と逼れる。The carboxylate-containing water-absorbing resin and the glycidyl group-containing polyolefin are mixed into a composite composition by melt-kneading them at a temperature higher than the melting point of the glycidyl group-containing polyolefin.
本発明における組成物は、この二成分の単純な混合物で
はなくて、溶融混線によりこの二成分が少なくとも部分
的に反応しているものと推定され、この場合の反応は、
カルボキシレート基とグリシジル基との間で生起してい
るものと推定される。本発明において複合組成物とは、
以上の意味でいうものである。The composition of the present invention is not a simple mixture of these two components, but it is presumed that these two components have at least partially reacted due to melt mixing, and in this case, the reaction is as follows:
It is presumed that this occurs between a carboxylate group and a glycidyl group. In the present invention, the composite composition is
This is in the above sense.
この溶融混線に使用される混練機は、熱可塑性樹脂の混
練に使用される慣用のものでよく、具体的には、例えば
、ブラベンダーブラストグラフ、CIM、FCM等の二
軸混練機、−軸押出機等がある。The kneading machine used for this melt mixing may be a conventional kneading machine used for kneading thermoplastic resins, and specifically, for example, a two-shaft kneading machine such as a Brabender blastograph, CIM, FCM, etc. There are extruders, etc.
複合組成物の具体的な製造方法としては、混練温度は一
般に120〜280℃であや、最高温度は使用されるグ
リシジル基含有ポリオレフィンあるいはカルボキシレー
ト含有の吸水性樹脂の種類によって異なるけれども、1
30〜250℃が好適である。混線温度が120℃未満
では、両成分の反応が良好に行なわれない。一方、樹脂
の一部が劣化を伴う。混練機内滞留時間は2秒以上であ
り、好ましくは3秒以上である。As a specific method for producing the composite composition, the kneading temperature is generally 120 to 280°C, and the maximum temperature varies depending on the type of glycidyl group-containing polyolefin or carboxylate-containing water-absorbing resin used.
A temperature of 30 to 250°C is suitable. If the crosstalk temperature is less than 120° C., the reaction between both components will not proceed well. On the other hand, a part of the resin is accompanied by deterioration. The residence time in the kneader is 2 seconds or more, preferably 3 seconds or more.
混練機内滞留時間が2秒未満では、満足すべき吸水性樹
脂組成物が得られない。If the residence time in the kneader is less than 2 seconds, a satisfactory water absorbent resin composition cannot be obtained.
なお、組成物の製造に当って、他のポリオレフィン樹脂
、例えばポリエチレン、ポリプロピレン、エチレン−α
−オレフィン共重合体、エチレン−酢酸ビニル共重合体
、エチレン−(メタ)アクリル酸共重合体およびその金
属イオン架橋体、エチレン−(メタ)アクリル酸エステ
ル共重合体等を95重量%以下、好ましくは50重量%
以下の割合でブレンドすることもできるし、石油樹脂、
ワックス、安定剤、帯電防止剤、紫外線吸収剤、滑剤、
無機充填剤等を配合することもできる。これらの補助資
材は、前記必須二成分を溶融混練して複合組成物を形成
させる過程で存在させることもできるし、複合組成物が
形成されたのちに添加することもできる。In addition, in producing the composition, other polyolefin resins such as polyethylene, polypropylene, ethylene-α
- 95% by weight or less of olefin copolymers, ethylene-vinyl acetate copolymers, ethylene-(meth)acrylic acid copolymers and their metal ion crosslinked products, ethylene-(meth)acrylic acid ester copolymers, etc., preferably is 50% by weight
It can also be blended in the following proportions, petroleum resin,
Wax, stabilizer, antistatic agent, ultraviolet absorber, lubricant,
Inorganic fillers and the like can also be blended. These auxiliary materials can be present during the process of melt-kneading the two essential components to form a composite composition, or can be added after the composite composition is formed.
本発明において、この複合組成物は、押出成形され発泡
される。In the present invention, this composite composition is extruded and foamed.
押出成形は、熱可塑性樹脂における慣用の方法でなされ
、例えば、Tダイ成形法、インフレーション成形法、カ
レンダー成形法、フィラメント成形法等により、組成物
はフィルム状、シート状等の膜状物、リボン状、積雄状
等の糸状物等とされる。Extrusion molding is carried out by a conventional method for thermoplastic resins, such as T-die molding, inflation molding, calendar molding, filament molding, etc., to form a composition into a membrane-like object such as a film or sheet, or a ribbon. It is considered to be a filamentous substance such as a cylindrical or cylindrical shape.
なお、前述した複合組成物の製造は、との押出成形に供
する前に予め複合組成物となしベレット化しておく場合
、および、押出成形時に成形機の溶融混線部で直接に複
合組成物とする場合のいずれでもよいが、押出成形前に
予め複合組成物としておく前者の方が好ましい。The above-mentioned composite composition can be manufactured by forming the composite composition into pellets in advance before extrusion molding, or by directly forming the composite composition in the melt mixing section of the molding machine during extrusion molding. Either case may be used, but it is preferable to form a composite composition in advance before extrusion molding.
また、発泡方法も、熱可塑性樹脂における慣用の方法が
用いられる。例えば、前述した複合組成物の製造の段階
で、アゾジカルボンアミド、トリヒドラジノトリアジン
、p−トルエンスルホニルセミカルバジド、ジニトロソ
ペンタメチレンテトラミン等の化学発泡剤を使用ポリオ
レフィンの全量100重量部に対して0.5〜30重量
部重量部節囲で予め添加しておくか、複合組成物の製造
後で押出成形に供する段階で、前述の化学発泡剤を添加
するか、等によ臥組成物を押出発泡させる方法、または
、押出成形後に発泡させる方法、或いは、押出成形の段
階で、ブタン、ペンタン、ヘキサン、ヘプタン等の物理
発泡剤を同上程度の割合で注入して押出発泡させる方法
等が用いられる。なか゛で、押出発泡させる方法が最も
好ましい。Further, as the foaming method, a conventional method for thermoplastic resins is used. For example, at the stage of manufacturing the above-mentioned composite composition, chemical blowing agents such as azodicarbonamide, trihydrazinotriazine, p-toluenesulfonyl semicarbazide, dinitrosopentamethylenetetramine, etc. are used. .5 to 30 parts by weight may be added in advance, or the above-mentioned chemical blowing agent may be added at the stage of extrusion molding after the production of the composite composition, or by extrusion of the composition. A method of foaming, a method of foaming after extrusion molding, or a method of injecting a physical foaming agent such as butane, pentane, hexane, heptane, etc. at the same ratio at the extrusion molding stage and extrusion foaming is used. . Among these, the most preferred method is extrusion foaming.
本発明において、押出成形し発泡させた吸水性樹脂材を
、さらに、縦横の少くとも一方向に2〜5倍程度の倍率
で延伸させることにより、吸水速度、吸水性の一層の向
上を計ることができる。In the present invention, the extrusion-molded and foamed water-absorbing resin material is further stretched in at least one direction (vertical and horizontal) at a magnification of about 2 to 5 times to further improve the water absorption rate and water absorption properties. Can be done.
本発明の製造方法によりmられる吸水性樹脂材は、単独
のフィルム、シートとして、好ましくはポリオレフィン
樹脂等の他材料との積層フィルム、シートとして、或は
織成する等して、食品包装用、薬品包装用、農園芸用、
結露防止、内装等の建材用、止水等の土木用、衛生用品
用、油水分離用、帯電防止用等の分野への応用が可能で
ある。The water-absorbing resin material produced by the production method of the present invention can be used as a single film or sheet, preferably as a laminated film or sheet with other materials such as polyolefin resin, or as a weave, for food packaging, For pharmaceutical packaging, agriculture and horticulture,
It can be applied to fields such as dew condensation prevention, building materials such as interior decoration, civil engineering applications such as waterproofing, sanitary products, oil/water separation, and antistatic applications.
(ロ)作用および効果
本発明の吸水性樹脂材の製造方法は、カルボキシレート
含有の吸水性樹脂とグリシジル基含有ポリオ〆フインと
を溶用混練した複合組成物を用い仝ので、吸水後におけ
る吸水性樹脂の脱離がなくその保持性に優れるばかゆで
なく、発泡させてなるので吸水速度が大きく、全体とし
て高吸水性を有するフィルム状、シート状、繊維状等の
吸水性樹脂材を製造することができるものである。(B) Function and Effect The method for producing a water-absorbing resin material of the present invention uses a composite composition obtained by dissolving and kneading a carboxylate-containing water-absorbing resin and a glycidyl group-containing polyolefin. To produce water-absorbing resin materials in the form of films, sheets, fibers, etc., which have a high water absorption rate as a whole and have a high water absorption rate because they are foamed instead of being made by foaming, and have high water absorption properties as a whole. It is something that can be done.
(へ)実施例
以下の実施例、比較例において、発泡倍率、吸水率、吸
水性樹脂保持率は次の測定法によった。(f) Examples In the following Examples and Comparative Examples, the expansion ratio, water absorption rate, and water absorbent resin retention rate were measured by the following measuring method.
発泡倍率
吸水率
1リツトルのビーカーに吸水性樹脂材約1?及び純水約
1リツトルをそれぞれ秤量して入れ、所定時間放置して
十分に膨潤させる。Foaming ratio: Water absorption: Approximately 1 liter of water-absorbing resin material in a 1-liter beaker? and about 1 liter of pure water were weighed and added to each, and left to swell for a predetermined period of time.
次いで、8メツシユ篩で水切りをし、樹脂材表面に付着
している水を戸紙で取や除いたのち、樹脂材を秤量する
。吸水率の算出は、下記式を用いて行なう。Next, the resin material is drained using an 8-mesh sieve, and the water adhering to the surface of the resin material is removed using a door paper, and then the resin material is weighed. The water absorption rate is calculated using the following formula.
吸水率測定に用いた樹脂材を5時間水中に浸漬して膨潤
させる。次いで水切りをし、70℃、24時間真空乾燥
処理を行い樹脂材より水を除去する。水浸漬前の樹脂材
重量と真空乾燥処理後の樹脂材重量の差を樹脂材の乾燥
51、量とすると吸水性樹脂保持率は次式で計算される
。The resin material used for water absorption measurement is immersed in water for 5 hours to swell. Next, water is drained and vacuum drying is performed at 70° C. for 24 hours to remove water from the resin material. When the difference between the weight of the resin material before immersion in water and the weight of the resin material after vacuum drying treatment is defined as the drying amount of the resin material, the water-absorbing resin retention rate is calculated by the following formula.
吸水性樹脂保持率後)=
水浸漬前の樹脂材中の吸水性樹脂材駆1)×100
実施例1
カルボキシレート含有の吸水性樹脂トシて、表面架橋処
理未実施のポリアクリル酸す) IJウム20重漬%と
、グリシジル基含有ポリオレフィンとして、エチレン−
エチルアクリレート−グリシジルメタクリレート共重合
体(エチルアクリレート含有Wk5重量シ、グリシジル
メタクリv−)含有i[o重量%、メルトフローレー)
10F/10分、融点96℃)SO重寸%と、この共重
合体100重量部に対して6重1部のアゾジカルボンア
ミドとを、バンバリーミキサ−にて160℃で6分間溶
融混練して複合組成物となしベレット化した。After water-absorbing resin retention rate) = Water-absorbing resin content in resin material before immersion in water 1) × 100 Example 1 Carboxylate-containing water-absorbing resin (polyacrylic acid without surface crosslinking treatment) IJ As a glycidyl group-containing polyolefin, ethylene-
Ethyl acrylate-glycidyl methacrylate copolymer (ethyl acrylate containing Wk5 weight, glycidyl methacrylate v-) containing i [o weight %, melt flow rate]
10F/10 minutes, melting point 96℃) SO weight % and 6 parts of azodicarbonamide per 100 parts by weight of this copolymer were melt-kneaded at 160℃ for 6 minutes in a Banbury mixer. The composite composition was made into a pellet.
得うれたベレットと、エチレン−酢酸ビニル共重合体(
酢酸ビニル含有量12重@%、メルトフローレー)9f
/10分)とを、各々、別の押出機を用いて、二層サー
キューラーダイで200℃で共押出すると共に複合組成
物を発泡させ、ブローアツプ比3.0、引取比2.0で
空冷インフレーション成形することにより、吸水性樹脂
材1が1.0fi、エチレン−酢酸ビニル共重合体1が
0.1 tmの厚みの積層シートを製造した。The obtained pellet and ethylene-vinyl acetate copolymer (
Vinyl acetate content 12w@%, melt flow rate) 9f
/10 minutes) were coextruded at 200°C with a two-layer circular die using separate extruders, and the composite composition was foamed at a blow-up ratio of 3.0 and a take-up ratio of 2.0. A laminated sheet having a thickness of 1.0 fi of the water-absorbing resin material 1 and 0.1 tm of the ethylene-vinyl acetate copolymer 1 was produced by air-cooled inflation molding.
得られた積層シートの吸水性樹脂材層の発泡倍率、吸水
率、および吸水後の吸水性樹脂保持率を表に示す。The expansion ratio, water absorption rate, and water absorbent resin retention rate after water absorption of the water absorbent resin material layer of the obtained laminated sheet are shown in the table.
実施例2
ポリアクリル酸ナトリウムを20重1%、エチレン−エ
テルアクリレート−グリシジルメタクリレート共重合体
を40重型筒、エチレン−酢酸ビニル共重合体を40重
型筒、アゾジカルボンアミドを両者共重合体の合計11
Qo重量部に対して6重層部として複合組成物とした外
は、実施例1と同様にして積層シートを製造した。Example 2 Sodium polyacrylate was 20 weight 1%, ethylene-ether acrylate-glycidyl methacrylate copolymer was 40 heavy cylinders, ethylene-vinyl acetate copolymer was 40 heavy cylinders, azodicarbonamide was the total of both copolymers. 11
A laminate sheet was produced in the same manner as in Example 1, except that the composite composition was prepared by adding 6 parts to the weight of Qo.
得られた積層シートの吸水性樹脂材層の性質を表に示す
。The properties of the water-absorbing resin material layer of the obtained laminated sheet are shown in the table.
比較例1
アゾジカルボンアミドを用いなかった外は、実施例1と
同様にして吸水性樹脂層0.1w+m、エチレン−酢2
ビニル共重合体層0.1 wtrの厚みの積層シートを
製造した。Comparative Example 1 A water-absorbing resin layer of 0.1 w+m, ethylene-vinegar 2
A laminate sheet with a vinyl copolymer layer thickness of 0.1 wtr was produced.
比較例2
エチレン−エチルアクリレ−) −りIJシジルメタク
リレート共重合体の代りにエチレン−酢酸ビニル共重合
体を用いた外は、実施例1と同様にして積層シートを製
造した。Comparative Example 2 A laminate sheet was produced in the same manner as in Example 1, except that an ethylene-vinyl acetate copolymer was used instead of the ethylene-ethyl acrylate (IJ cidyl methacrylate) copolymer.
比較例3
エチレン−エチルアクリレート−グリシジルメタクリレ
ート共重合体の代妙にアイオノマー樹脂(三井デュポン
■製、)・イミジン170’7)を用いた外は、実施例
1と同様にして積層シートを製造した。Comparative Example 3 A laminated sheet was produced in the same manner as in Example 1, except that an ionomer resin (Mitsui DuPont ■, Imidine 170'7) was used instead of the ethylene-ethyl acrylate-glycidyl methacrylate copolymer. .
(以下余白) 特許出願人 三菱油化株式会社 代理人 弁理士 長 谷 正 久 (ほか1名)(Margin below) Patent applicant: Mitsubishi Yuka Co., Ltd. Agent: Patent Attorney Masahisa Nagatani (1 other person)
Claims (1)
リシジル基含有ポリオレフィン95〜5重量%とを後者
の融点以上の温度で溶融混練して複合組成物となし、該
複合組成物を押出成形し発泡させることを特徴とする吸
水性樹脂材の製造方法。5 to 95% by weight of a carboxylate-containing water absorbent resin and 95 to 5% by weight of a glycidyl group-containing polyolefin are melt-kneaded at a temperature above the melting point of the latter to form a composite composition, and the composite composition is extruded and foamed. A method for producing a water-absorbing resin material.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25525086A JPS63110226A (en) | 1986-10-27 | 1986-10-27 | Production of water-absorptive resin material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP25525086A JPS63110226A (en) | 1986-10-27 | 1986-10-27 | Production of water-absorptive resin material |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63110226A true JPS63110226A (en) | 1988-05-14 |
Family
ID=17276127
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP25525086A Pending JPS63110226A (en) | 1986-10-27 | 1986-10-27 | Production of water-absorptive resin material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63110226A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2017033785A1 (en) * | 2015-08-24 | 2017-03-02 | 日東電工株式会社 | Foaming composition for filling, foaming member for filling, and foam for filling |
-
1986
- 1986-10-27 JP JP25525086A patent/JPS63110226A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2017033785A1 (en) * | 2015-08-24 | 2017-03-02 | 日東電工株式会社 | Foaming composition for filling, foaming member for filling, and foam for filling |
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