JPH0615218B2 - Composite with modified polyolefin - Google Patents
Composite with modified polyolefinInfo
- Publication number
- JPH0615218B2 JPH0615218B2 JP60157022A JP15702285A JPH0615218B2 JP H0615218 B2 JPH0615218 B2 JP H0615218B2 JP 60157022 A JP60157022 A JP 60157022A JP 15702285 A JP15702285 A JP 15702285A JP H0615218 B2 JPH0615218 B2 JP H0615218B2
- Authority
- JP
- Japan
- Prior art keywords
- ethylene
- olefin
- composite
- carbon atoms
- olefin copolymer
- 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 - Lifetime
Links
- 229920000098 polyolefin Polymers 0.000 title claims description 42
- 239000002131 composite material Substances 0.000 title claims description 19
- 239000004711 α-olefin Substances 0.000 claims description 31
- 229920000089 Cyclic olefin copolymer Polymers 0.000 claims description 21
- 239000000203 mixture Substances 0.000 claims description 18
- 239000007789 gas Substances 0.000 claims description 17
- 238000000034 method Methods 0.000 claims description 17
- 229910052751 metal Inorganic materials 0.000 claims description 16
- 239000002184 metal Substances 0.000 claims description 16
- 150000008065 acid anhydrides Chemical class 0.000 claims description 12
- -1 ethylene- Chemical class 0.000 claims description 11
- 229920003023 plastic Polymers 0.000 claims description 11
- 239000004033 plastic Substances 0.000 claims description 11
- 125000004432 carbon atom Chemical group C* 0.000 claims description 10
- 239000003054 catalyst Substances 0.000 claims description 9
- 229910052782 aluminium Inorganic materials 0.000 claims description 8
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 8
- 239000000460 chlorine Substances 0.000 claims description 8
- 229910010272 inorganic material Inorganic materials 0.000 claims description 8
- 239000011147 inorganic material Substances 0.000 claims description 8
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 7
- 239000005977 Ethylene Substances 0.000 claims description 7
- 238000002156 mixing Methods 0.000 claims description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 6
- 229910052794 bromium Inorganic materials 0.000 claims description 6
- 229910052801 chlorine Inorganic materials 0.000 claims description 6
- 150000001875 compounds Chemical class 0.000 claims description 6
- 239000004698 Polyethylene Substances 0.000 claims description 5
- 125000001931 aliphatic group Chemical group 0.000 claims description 5
- 239000002243 precursor Substances 0.000 claims description 5
- ZOXJGFHDIHLPTG-UHFFFAOYSA-N Boron Chemical compound [B] ZOXJGFHDIHLPTG-UHFFFAOYSA-N 0.000 claims description 4
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 claims description 4
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 claims description 4
- 125000000217 alkyl group Chemical group 0.000 claims description 4
- 125000002029 aromatic hydrocarbon group Chemical group 0.000 claims description 4
- 229910052796 boron Inorganic materials 0.000 claims description 4
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 claims description 4
- 229910052740 iodine Inorganic materials 0.000 claims description 4
- 229920000573 polyethylene Polymers 0.000 claims description 4
- 239000007795 chemical reaction product Substances 0.000 claims description 3
- 229920001971 elastomer Polymers 0.000 claims description 3
- 239000000806 elastomer Substances 0.000 claims description 3
- 239000000377 silicon dioxide Substances 0.000 claims description 3
- 239000010936 titanium Substances 0.000 claims description 3
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 claims description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 2
- 239000002879 Lewis base Substances 0.000 claims description 2
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 2
- 230000003213 activating effect Effects 0.000 claims description 2
- 150000001336 alkenes Chemical class 0.000 claims description 2
- 125000005907 alkyl ester group Chemical group 0.000 claims description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 2
- 125000001309 chloro group Chemical group Cl* 0.000 claims description 2
- 238000010924 continuous production Methods 0.000 claims description 2
- 150000004292 cyclic ethers Chemical class 0.000 claims description 2
- 239000003085 diluting agent Substances 0.000 claims description 2
- 229920001038 ethylene copolymer Polymers 0.000 claims description 2
- 229910052736 halogen Inorganic materials 0.000 claims description 2
- 150000002367 halogens Chemical class 0.000 claims description 2
- 150000002430 hydrocarbons Chemical group 0.000 claims description 2
- 239000001257 hydrogen Substances 0.000 claims description 2
- 229910052739 hydrogen Inorganic materials 0.000 claims description 2
- PNDPGZBMCMUPRI-UHFFFAOYSA-N iodine Chemical group II PNDPGZBMCMUPRI-UHFFFAOYSA-N 0.000 claims description 2
- 239000011630 iodine Substances 0.000 claims description 2
- 150000007527 lewis bases Chemical class 0.000 claims description 2
- 239000007788 liquid Substances 0.000 claims description 2
- 239000000178 monomer Substances 0.000 claims description 2
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims description 2
- 150000002902 organometallic compounds Chemical class 0.000 claims description 2
- 229910052763 palladium Inorganic materials 0.000 claims description 2
- 239000002245 particle Substances 0.000 claims description 2
- 230000000737 periodic effect Effects 0.000 claims description 2
- 230000000379 polymerizing effect Effects 0.000 claims description 2
- 229930195734 saturated hydrocarbon Natural products 0.000 claims description 2
- 239000007787 solid Substances 0.000 claims description 2
- 229910052719 titanium Inorganic materials 0.000 claims description 2
- 150000003623 transition metal compounds Chemical class 0.000 claims description 2
- 229910052720 vanadium Inorganic materials 0.000 claims description 2
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 claims description 2
- 150000003682 vanadium compounds Chemical class 0.000 claims description 2
- 150000001735 carboxylic acids Chemical class 0.000 claims 2
- 159000000032 aromatic acids Chemical class 0.000 claims 1
- 125000003118 aryl group Chemical group 0.000 claims 1
- 239000012876 carrier material Substances 0.000 claims 1
- 238000012360 testing method Methods 0.000 description 12
- 230000000052 comparative effect Effects 0.000 description 11
- 239000005038 ethylene vinyl acetate Substances 0.000 description 11
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 description 11
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 10
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 9
- 229920006242 ethylene acrylic acid copolymer Polymers 0.000 description 8
- 239000012071 phase Substances 0.000 description 8
- 229920001903 high density polyethylene Polymers 0.000 description 7
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 7
- 239000000853 adhesive Substances 0.000 description 6
- 230000001070 adhesive effect Effects 0.000 description 6
- 239000004700 high-density polyethylene Substances 0.000 description 6
- 229910000019 calcium carbonate Inorganic materials 0.000 description 5
- 239000006229 carbon black Substances 0.000 description 5
- 239000011888 foil Substances 0.000 description 5
- 150000001451 organic peroxides Chemical class 0.000 description 5
- SMZOUWXMTYCWNB-UHFFFAOYSA-N 2-(2-methoxy-5-methylphenyl)ethanamine Chemical compound COC1=CC=C(C)C=C1CCN SMZOUWXMTYCWNB-UHFFFAOYSA-N 0.000 description 4
- NIXOWILDQLNWCW-UHFFFAOYSA-N 2-Propenoic acid Natural products OC(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 description 4
- 238000000465 moulding Methods 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 229920001684 low density polyethylene Polymers 0.000 description 3
- 239000004702 low-density polyethylene Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 150000002739 metals Chemical class 0.000 description 3
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 3
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 2
- XMNIXWIUMCBBBL-UHFFFAOYSA-N 2-(2-phenylpropan-2-ylperoxy)propan-2-ylbenzene Chemical compound C=1C=CC=CC=1C(C)(C)OOC(C)(C)C1=CC=CC=C1 XMNIXWIUMCBBBL-UHFFFAOYSA-N 0.000 description 2
- 239000004342 Benzoyl peroxide Substances 0.000 description 2
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical group C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 description 2
- VZCYOOQTPOCHFL-OWOJBTEDSA-N Fumaric acid Chemical compound OC(=O)\C=C\C(O)=O VZCYOOQTPOCHFL-OWOJBTEDSA-N 0.000 description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- 239000004743 Polypropylene Substances 0.000 description 2
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 2
- 235000019400 benzoyl peroxide Nutrition 0.000 description 2
- LSXWFXONGKSEMY-UHFFFAOYSA-N di-tert-butyl peroxide Chemical compound CC(C)(C)OOC(C)(C)C LSXWFXONGKSEMY-UHFFFAOYSA-N 0.000 description 2
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 2
- 239000000347 magnesium hydroxide Substances 0.000 description 2
- 229910001862 magnesium hydroxide Inorganic materials 0.000 description 2
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 description 2
- 239000011976 maleic acid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- 229920001155 polypropylene Polymers 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 239000012808 vapor phase Substances 0.000 description 2
- NALFRYPTRXKZPN-UHFFFAOYSA-N 1,1-bis(tert-butylperoxy)-3,3,5-trimethylcyclohexane Chemical compound CC1CC(C)(C)CC(OOC(C)(C)C)(OOC(C)(C)C)C1 NALFRYPTRXKZPN-UHFFFAOYSA-N 0.000 description 1
- LIKMAJRDDDTEIG-UHFFFAOYSA-N 1-hexene Chemical compound CCCCC=C LIKMAJRDDDTEIG-UHFFFAOYSA-N 0.000 description 1
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 1
- JAHNSTQSQJOJLO-UHFFFAOYSA-N 2-(3-fluorophenyl)-1h-imidazole Chemical compound FC1=CC=CC(C=2NC=CN=2)=C1 JAHNSTQSQJOJLO-UHFFFAOYSA-N 0.000 description 1
- 241000208340 Araliaceae Species 0.000 description 1
- 229910001369 Brass Inorganic materials 0.000 description 1
- 235000005035 Panax pseudoginseng ssp. pseudoginseng Nutrition 0.000 description 1
- 235000003140 Panax quinquefolius Nutrition 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000004840 adhesive resin Substances 0.000 description 1
- 229920006223 adhesive resin Polymers 0.000 description 1
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000003078 antioxidant effect Effects 0.000 description 1
- WPYMKLBDIGXBTP-UHFFFAOYSA-N benzoic acid Chemical compound OC(=O)C1=CC=CC=C1 WPYMKLBDIGXBTP-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000010951 brass Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- HNEGQIOMVPPMNR-IHWYPQMZSA-N citraconic acid Chemical compound OC(=O)C(/C)=C\C(O)=O HNEGQIOMVPPMNR-IHWYPQMZSA-N 0.000 description 1
- 229940018557 citraconic acid Drugs 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000004132 cross linking Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000007865 diluting Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229920006244 ethylene-ethyl acrylate Polymers 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 239000001530 fumaric acid Substances 0.000 description 1
- 235000008434 ginseng Nutrition 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 239000011133 lead Substances 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- LVHBHZANLOWSRM-UHFFFAOYSA-N methylenebutanedioic acid Natural products OC(=O)CC(=C)C(O)=O LVHBHZANLOWSRM-UHFFFAOYSA-N 0.000 description 1
- 238000002715 modification method Methods 0.000 description 1
- 125000002524 organometallic group Chemical group 0.000 description 1
- 235000014366 other mixer Nutrition 0.000 description 1
- 239000012785 packaging film Substances 0.000 description 1
- 229920006280 packaging film Polymers 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- YWAKXRMUMFPDSH-UHFFFAOYSA-N pentene Chemical compound CCCC=C YWAKXRMUMFPDSH-UHFFFAOYSA-N 0.000 description 1
- 230000000704 physical effect Effects 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
Landscapes
- Laminated Bodies (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Description
【発明の詳細な説明】 技術分野 本発明は、通常気相・低圧法により、有機金属触媒を用
いて製造された直鎖状エチレン−α−オレフィン共重合
体を不飽和カルボン酸またはその酸無水物をグラフト化
して変性したポリオレフィンを用いて金属、無機物、プ
ラスチツクと接着または混合することによつて作られた
複合物に関する。TECHNICAL FIELD The present invention relates to a linear ethylene-α-olefin copolymer produced using an organometallic catalyst, usually by a vapor-phase / low-pressure method, to obtain an unsaturated carboxylic acid or an acid anhydride thereof. The present invention relates to a composite made by adhering or mixing a metal, an inorganic material, and a plastic with a polyolefin modified by grafting an object.
従来技術とその問題点 従来、ポリオレフィンを不飽和カルボン酸またはその酸
無水物をグラフト化することにより変性する場合、ポリ
オレフィンとして低圧法低密度ポリエチレン(L−LD
PE)、高密度ポリエチレン(HDPE)、ポリプロピ
レン(PP)、エチレンアクリル酸エチル共重合体(E
EA)及びエチレン酢酸ビニル共重合体(EVA)が使
用されている。しかるに、L−LDPE、HDPE、P
Pの場合、これらを用いた変性ポリオレフィンは、接着
性樹脂として金属と金属、金属とプラスチツクの間の接
着に用いた場合、積層物を剛直にしてしまう欠点があ
る。また、EEA、EVAの場合は軟化温度が低いため
積層物は低温度で変性を来たす欠点がある。Conventional technology and its problems Conventionally, when a polyolefin is modified by grafting an unsaturated carboxylic acid or an acid anhydride thereof, a low pressure low density polyethylene (L-LD) is used as the polyolefin.
PE), high density polyethylene (HDPE), polypropylene (PP), ethylene ethyl acrylate copolymer (E
EA) and ethylene vinyl acetate copolymer (EVA) have been used. However, L-LDPE, HDPE, P
In the case of P, the modified polyolefin using these has a defect that when used as an adhesive resin for adhesion between metal and metal or between metal and plastic, the laminate becomes rigid. Further, in the case of EEA and EVA, the softening temperature is low, so that the laminate has a drawback of being modified at a low temperature.
近年、高圧法に代えて、気相・低圧法で製造された直鎖
状の密度0.910g/ml以下のエチレン−α−オレフィ
ン共重合体がユニオンカーバイド社により開発されたの
で、これを用いて前記の変性ポリオレフィンを用いた複
参物の欠点を改善すべく本発明者等は鋭意研究の結果、
前記の気相・低圧法による直鎖状エチレン−α−オレフ
ィン共重合体をベースとした変性ポリオレフィンを金
属、無機物、または異種プラスチツクと接着または混合
することにより作られる複合物の耐熱性などの機械的性
質が大巾に改善されることを予期せずして見出した。In recent years, in place of the high pressure method, a linear ethylene-α-olefin copolymer having a density of 0.910 g / ml or less produced by the gas phase / low pressure method was developed by Union Carbide Co. As a result of intensive research by the present inventors, in order to improve the drawbacks of compound ginseng using the modified polyolefin,
Machine such as heat resistance of a composite made by adhering or mixing a modified polyolefin based on a linear ethylene-α-olefin copolymer by the gas phase / low pressure method with a metal, an inorganic material, or a heterogeneous plastic Unexpectedly found that the physical properties were greatly improved.
発明の目的 本発明は、良好な機械的性質を備えた、変性ポリオレフ
ィンによる複合物を提供することを目的とする。OBJECT OF THE INVENTION The present invention aims to provide composites with modified polyolefins with good mechanical properties.
発明の具体的説明 即ち、本発明は、気相・低圧法で製造された密度が0.9
10g/ml以下の直鎖状エチレン−α−オレフィン共重
合体を不飽和カルボン酸またはその酸無水物をグラフト
化して変性したポリオレフィンを金属、無機物または異
種プラスチツクと接着または混合することにより複合物
としたことを特徴とする変性ポリオレフィンによる複合
物に関するものである。Detailed Description of the Invention That is, according to the present invention, the density produced by the vapor phase / low pressure method is 0.9.
A linear ethylene-α-olefin copolymer of 10 g / ml or less is grafted with an unsaturated carboxylic acid or an acid anhydride thereof to modify a modified polyolefin, and the polyolefin is bonded or mixed with a metal, an inorganic substance or a different plastic to form a composite. The present invention relates to a composite made from a modified polyolefin characterized by the above.
なお、本発明は、上記の変性したポリオレフィンに必要
に応じて異種ポリマー、酸化防止剤、着色剤、有機過酸
化物、架橋促進剤等の各種添加剤を配合するものであ
る。In the present invention, various additives such as a different polymer, an antioxidant, a colorant, an organic peroxide and a crosslinking accelerator are blended with the above modified polyolefin as required.
本発明において、エチレン−α−オレフィン共重合体と
は、エチレンが50%以上、望ましくは70%以上を占
め、α−オレフィンが炭素数3〜12のものを言う。α
−オレフィンは、直鎖状または分岐状でよく、例えばプ
ロピレン、ブテン−1、ペンテン−1、ヘキセン−1、
ヘプテン−1、オクテン−1、4−メチルペンテン−
1、4−メチルヘキセン−1、4,4−ジメチルペンテン
−1等がある。In the present invention, the ethylene-α-olefin copolymer means ethylene having 50% or more, preferably 70% or more, and α-olefin having 3 to 12 carbon atoms. α
The olefin may be linear or branched, for example propylene, butene-1, pentene-1, hexene-1,
Heptene-1, octene-1,4-methylpentene-
1,4-methylhexene-1,4,4-dimethylpentene-1 and the like.
これらのエチレン−α−オレフィン共重合体は、周期律
表において、第IV〜VIII族の遷移金属化合物と、第I〜
III族の有機金属化合物の組合せにより生成する触媒、
所謂チーグラー触媒を用いて気相で製造され、製造条件
は従来の高圧法ポリエチレンに比較すると気相・低圧で
実施できる。These ethylene-α-olefin copolymers are represented by Group IV to VIII transition metal compounds and Group I to VIII in the periodic table.
A catalyst produced by a combination of Group III organometallic compounds,
It is manufactured in the gas phase using a so-called Ziegler catalyst, and the manufacturing conditions can be carried out in the gas phase / low pressure as compared with the conventional high-pressure polyethylene.
更に詳しくは、本発明の直鎖状エチレン−α−オレフィ
ン共重合体は、流動床反応帯域中で10゜〜80℃の温
度かつ7,000KPa以下の圧力にて、(a)0.35:1〜8.
0:1の高級αオレフィン対エチレンのモル比でエチレ
ン及び3〜8個の炭素原子を有する少なくとも1種の高
級α−オレフィンと、b)少なくとも25モル%の少なく
とも1種の希釈ガスとを含有する気体混合物を式: MgmTi(OR)nXp〔ED〕q 〔式中、Rは1〜14個の炭素原子を有する脂肪族若し
くは芳香族の炭化水素基又はCOR′であり、ここで
R′は1〜14個の炭素原子を有する脂肪族若しくは芳
香族の炭化水素基であり、 XはCl、Br、I及びその混合物よりなる群から選択
され、 EDは脂肪族若しくは芳香族酸のアルキルエステル、脂
肪族エーテル、環式エーテル及び脂肪族ケトンよりなる
群から選択される有機電子供与化合物であり、 mは0.5〜56であり、 nは0.1又は2であり、 pは2〜116であり、 qは2〜85である〕 を有する先駆体組成物からなる触媒系の粒子と連続的に
接触させ、前記先駆体組成物を不活性キヤリヤ材料で希
釈すると共に式: Al(R′)dX′eHf 〔式中、X′はCl又はOR″であり、 R′及びR″は1〜14個の炭素原子を有する飽和炭化
水素基であり、 eは0〜1.5であり、 fは0又は1であり、 d+e+f=3である〕 を有する有機アルミニウム化合物で完全に活性化させ、
前記活性化化合物を前記反応帯域中における全アルミニ
ウム対チタンのモル比が10:1〜400:1となるよ
うな量で使用することを特徴とするエチレン共重合体の
連続製造方法で製法されたものであり、特開昭59−2
30011号に詳細に説明されている。More specifically, the linear ethylene-α-olefin copolymer of the present invention is (a) 0.35 at a temperature of 10 ° to 80 ° C and a pressure of 7,000 KPa or less in a fluidized bed reaction zone. 1-8.
Containing ethylene and at least one higher alpha-olefin having 3 to 8 carbon atoms in a molar ratio of 0: 1 higher alpha-olefin to ethylene, and b) at least 25 mol% of at least one diluent gas. A gas mixture having the formula: Mg m Ti (OR) n X p [ED] q [wherein R is an aliphatic or aromatic hydrocarbon group having 1 to 14 carbon atoms or COR ′, Wherein R'is an aliphatic or aromatic hydrocarbon group having 1 to 14 carbon atoms, X is selected from the group consisting of Cl, Br, I and mixtures thereof, and ED is an aliphatic or aromatic acid Is an organic electron-donating compound selected from the group consisting of alkyl esters, aliphatic ethers, cyclic ethers, and aliphatic ketones, m is 0.5 to 56, n is 0.1 or 2, and p is Is 2 to 116, and q is 2 to 8 In a] continuously contacted with the catalyst system of particles consisting of precursor composition having the formula with diluting the precursor composition with an inert Kiyariya materials: Al (R ') d X ' e H f [ Wherein X ′ is Cl or OR ″, R ′ and R ″ are saturated hydrocarbon groups having 1 to 14 carbon atoms, e is 0 to 1.5, and f is 0 or 1 And d + e + f = 3],
It was prepared by a continuous process for producing an ethylene copolymer, characterized in that the activating compound was used in an amount such that the molar ratio of total aluminum to titanium in the reaction zone was 10: 1 to 400: 1. And is disclosed in JP-A-59-2.
It is described in detail in No. 30011.
更にまた、本発明の直鎖状エチレン−α−オレフィン共
重合体はエチレンを単独で又は少なくとも1種のC3〜
C10α−オレフィンとともに気相中で約10℃〜約11
5℃の温度において、 (A)(1)塩素、臭素又はよう素による三ハロゲン化パラジ
ウム(a)と該三ハロゲン化バナジウムが可溶である液状
の有機ルイス塩基である電子供与体(b)との反応生成物
であるバナジウム化合物と (2)次式 MXa (ここでMはほう素か又はAlR(3-a)のいずれかであり、
各Rはそれぞれアルキルであるが、ただしいずれのR基
においても脂肪族炭素原子の総数は14を越えず、 Xは塩素、臭素又はよう素であり、 aは0、1又は2であり、ただしMがほう素のときはa
は3である) を有する変性剤 とをシリカ又はアルミナから本質上なる固体不活性担体
上に担持させたものから本質上なる担持された先駆物質
と、 (B)次式 AlR3 (ここでRは先に定義した通りである) を有する助触媒と、 (C)次式 R′bCX′(4-b) (ここでR′は水素又は非置換の若しくはハロゲン置換
された低級アルキルであり、X′はハロゲンであり、 Bは0、1又は2である) を有する促進剤 を含む触媒組成物と接触させることによつて単量体を重
合させることからなるポリエチレンの製造法で製造され
たものであり、特開昭59-230006号に詳細に説明されて
いる。Furthermore, the linear ethylene-α-olefin copolymer of the present invention comprises ethylene alone or at least one C 3- .
About 10 ° C to about 11 in the gas phase together with C 10 α-olefin.
(A) (1) Palladium trihalide (a) with chlorine, bromine or iodine at a temperature of 5 ° C. and an electron donor (b) which is a liquid organic Lewis base in which the vanadium trihalide is soluble. A vanadium compound which is a reaction product of (2) with the following formula MX a (where M is either boron or AlR (3-a) ,
Each R is each alkyl, provided that the total number of aliphatic carbon atoms in any R group does not exceed 14, X is chlorine, bromine or iodine, and a is 0, 1 or 2, A when M is boron
And a supported agent consisting essentially of a silica or alumina supported on a solid inert carrier, and (B) the following formula AlR 3 (where R is Is as defined above) and (C) is of the formula R'b CX ' (4-b) where R'is hydrogen or unsubstituted or halogen-substituted lower alkyl. , X'is a halogen and B is 0, 1 or 2) and is prepared by a method for producing polyethylene comprising polymerizing a monomer by contacting it with a catalyst composition comprising a promoter having And is described in detail in JP-A-59-230006.
本発明で用いられる不飽和カルボン酸またはその酸無水
物としては、アクリル酸、マレイン酸、イタコン酸、フ
マール酸、ハイミツク酸、シトラコン酸またはこれらの
酸無水物等であるが、特にアクリル酸または無水マレイ
ン酸を用いることが好ましい。添加する不飽和カルボン
酸またはその酸無水物の量は、直鎖状エチレン−α−オ
レフィン共重合体100重量部に対し、0.01重量部未
満では接着強度が低く、3.0重量部を超えると、刺激臭
が強く好ましくない。従つて、0.01〜3.0重量部を使
用する。Examples of the unsaturated carboxylic acid or its acid anhydride used in the present invention include acrylic acid, maleic acid, itaconic acid, fumaric acid, hymic acid, citraconic acid, and acid anhydrides thereof. It is preferred to use maleic acid. When the amount of the unsaturated carboxylic acid or its acid anhydride to be added is less than 0.01 parts by weight with respect to 100 parts by weight of the linear ethylene-α-olefin copolymer, the adhesive strength is low and 3.0 parts by weight is added. If it exceeds, the pungent odor is strong and it is not preferable. Therefore, 0.01 to 3.0 parts by weight are used.
本発明において、直鎖状エチレン−α−オレフィン共重
合体に不飽和カルボン酸またはその酸無水物を添加させ
る際に用いられる有機過酸化物としては、ベンゾイルパ
ーオキサイド、ジ−t−ブチルパーオキサイド、ジクミ
ルパーオキサイド、2,5ジメチル−2,5−ジ−t−ブチ
ルパーオキシヘキサン、1,1−ビス(t−ブチルパーオ
キシ)−3,5,5−トリメチルシクロヘキサン等が挙げら
れる。有機過酸化物の量は、直鎖状エチレン−α−オレ
フィン共重合体100重量部に対し、0.5重量部を超え
ると得られる変性樹脂をフイルムとした場合、ゲルおよ
びフイツシユアイが発生するので好ましくない。一方、
0.01重量部以下では、付加率が不充分となつて接着力
が不足する。従つて、0.001〜0.5重量部の範囲にあ
ることが望ましい。In the present invention, the organic peroxide used when adding the unsaturated carboxylic acid or its acid anhydride to the linear ethylene-α-olefin copolymer is benzoyl peroxide or di-t-butyl peroxide. , Dicumyl peroxide, 2,5-dimethyl-2,5-di-t-butylperoxyhexane, 1,1-bis (t-butylperoxy) -3,5,5-trimethylcyclohexane and the like. When the amount of the organic peroxide exceeds 0.5 parts by weight with respect to 100 parts by weight of the linear ethylene-α-olefin copolymer, a gel and a fisheye are generated when the modified resin obtained is a film. Not preferable. on the other hand,
If it is less than 0.01 parts by weight, the addition rate will be insufficient and the adhesive strength will be insufficient. Therefore, it is desirable to be in the range of 0.001 to 0.5 parts by weight.
本発明の変性樹脂は、前記の直鎖状エチレン−α−オレ
フィン共重合体に不飽和カルボン酸またはその酸無水物
を添加して、公知の種々の変性方法を適用して製造する
ことが出来る。例えば上記の直鎖状エチレン−α−オレ
フィン共重合体に不飽和カルボン酸またはその酸無水物
とベンゾイルパーオキサイド、ジ−t−ブチルパーオキ
サイド、ジクミルパーオキサイドなどの有機過酸化物を
添加し、ヘンシエルミキサー、リボンブレンダー、タン
ブラーなどの混合機で混合し、この混合物をバンバリー
ミキサー、単軸または多軸の押出機で150〜300
℃、好ましくは180〜250℃で溶融・混練する。The modified resin of the present invention can be produced by adding an unsaturated carboxylic acid or an acid anhydride thereof to the above-mentioned linear ethylene-α-olefin copolymer and applying various known modification methods. . For example, an unsaturated carboxylic acid or its acid anhydride and an organic peroxide such as benzoyl peroxide, di-t-butyl peroxide, or dicumyl peroxide are added to the above linear ethylene-α-olefin copolymer. , A Hensiel mixer, a ribbon blender, a tumbler, and other mixers, and this mixture is mixed with a Banbury mixer, a single-screw or multi-screw extruder for 150 to 300.
Melt and knead at ℃, preferably 180 ~ 250 ℃.
このようにして得られた変性ポリオレフィンは、単独で
使用されるが、これに未変性のエラストマーまたはポリ
オレフィンを添加して使用することが出来る。例えば、
上記で得られた変性ポリオレフィンにエチレン−プロピ
レン共重合体(EPR)、のようなエラストマー、或い
は高圧法低密度ポリエチレン、エチレン−アクリル酸共
重合体(EEA)、エチレン−酢酸ビニル共重合体(E
VA)のようなポリオレフィンが使用可能である。The modified polyolefin thus obtained is used alone, but an unmodified elastomer or polyolefin may be added to it. For example,
An elastomer such as ethylene-propylene copolymer (EPR), or high-pressure low density polyethylene, ethylene-acrylic acid copolymer (EEA), ethylene-vinyl acetate copolymer (E) is added to the modified polyolefin obtained above.
Polyolefins such as VA) can be used.
本発明に用いられる金属は、アルミニウム、鉄、ステン
レス、黄銅、鉛などが挙げられる。また、無機物として
は、水酸化アルミニウム、水酸化マグネシウム、炭酸カ
ルシウム、ガラス繊維、シリカ、タルク、カーボンブラ
ツクなどが挙げられ、さらに、プラスチツクとしては、
ポリエチレン、ポリアミド、けん化EVAなどが挙げら
れる。Examples of the metal used in the present invention include aluminum, iron, stainless steel, brass and lead. Examples of the inorganic material include aluminum hydroxide, magnesium hydroxide, calcium carbonate, glass fiber, silica, talc, carbon black, and the like. Further, as the plastic,
Examples include polyethylene, polyamide, saponified EVA, and the like.
本発明における複合物は、前記の変性ポリオレフィン
と、上記の金属、無機物またはプラスチツクから選択さ
れるものとの溶融状態での接着または混合によつて得ら
れる。接着および混合の方法は、特に限定されるもので
はなく、例えば接着についてはそれぞれをフイルム、シ
ート状としておき、熱圧着する方法、ダイ外部でラミネ
ートする方法、ダイ内部でラミネートする方法、押出コ
ーテイングする方法などの公知の方法を利用することが
出来る。また、混合については、変性ポリオレフィンと
金属または無機物をバンバリーミキサー、単軸または多
軸の押出機で溶融・混練するなどの公知の方法を利用す
ることが出来る。The composite in the present invention is obtained by adhesion or mixing in a molten state with the above-mentioned modified polyolefin and one selected from the above-mentioned metals, inorganic materials or plastics. The method of adhering and mixing is not particularly limited. For example, regarding adhering, each of them is formed into a film or a sheet and thermocompression bonded, laminated outside the die, laminated inside the die, or extrusion coated. A known method such as a method can be used. For the mixing, known methods such as melting and kneading the modified polyolefin and the metal or inorganic substance with a Banbury mixer or a single-screw or multi-screw extruder can be used.
本発明の複合物は、接着については変性ポリオレフィン
と前記の金属、プラスチツクから選択されるものに積層
する2層構造、更に変性ポリオレフィンをサンドイツチ
した3層構造を基本とし、混合については、変性ポリオ
レフィンに前記の金属、無機物から選択されるものにも
のを分散させたものである。The composite of the present invention has a two-layer structure in which a modified polyolefin is laminated on a material selected from the above-mentioned metals and plastics for adhesion, and a three-layer structure in which modified polyolefin is further laminated. It is a dispersion of one selected from the above-mentioned metals and inorganic materials.
したがつて、本発明の複合物における変性ポリオレフィ
ンと金属、無機物または異種プラスチツクとの相対的割
合は最終製品の用途によつて広範に変えることができ
る。Therefore, the relative proportions of modified polyolefin and metal, inorganic or heterogeneous plastic in the composites of the present invention can vary widely depending on the end product application.
以上、本発明による変性ポリオレフィンは、前記の金
属、無機物または各種のプラスチツクと良好な接着性を
示し、接着強さの高い積層物を作ることが出来、このも
のは、ガス不過性、耐湿性、耐油性などの利用を生か
し、包装用のフイルム、シート、ボトル、容器などに使
用することが出来る。また、本発明による変性ポリオレ
フィンに前記の金属、無機物、カーボンブラツクなどを
大量に配合して混練し、機械的性質の良好な複合物を作
ることが出来、このものは、電磁波遮蔽、電力ケーブル
遮蔽層、導電性遮水テープ、難燃性材料などに使用する
ことが出来る。As described above, the modified polyolefin according to the present invention shows good adhesion with the above-mentioned metal, inorganic material or various kinds of plastics, and it is possible to form a laminate having high adhesive strength, which is gas impermeable, moisture resistant, It can be used for packaging films, sheets, bottles, containers, etc. by taking advantage of its oil resistance. Further, the modified polyolefin according to the present invention can be mixed with a large amount of the above-mentioned metal, inorganic material, carbon black, etc. and kneaded to make a composite having good mechanical properties. It can be used for layers, conductive water-blocking tapes, flame-retardant materials, etc.
以下、本発明を実施例により更に詳しく説明するが、本
発明はこれらの実例に制限されるものではない。Hereinafter, the present invention will be described in more detail by way of examples, but the present invention is not limited to these examples.
実施例1〜4、比較例1〜4 密度の異なる直鎖状エチレン−α−オレフィン共重合
体、高密度ポリエチレン、EVA及びEEA等のポリマ
ーと無水マレイン酸、アクリル酸及び有機過酸化物をそ
れぞれ表1に示す割合でヘンシエルミキサーにより常法
で混合し、混合物をベント付直径50mmの押出機に供給
して200℃で混練、押出すことにより変性し、円筒状
のベレツトを作製した。Examples 1 to 4 and Comparative Examples 1 to 4 Polymers such as linear ethylene-α-olefin copolymers having different densities, high density polyethylene, EVA and EEA, and maleic anhydride, acrylic acid and organic peroxides, respectively. The proportions shown in Table 1 were mixed by a conventional method with a Henschel mixer, and the mixture was supplied to an extruder with a vent and a diameter of 50 mm, kneaded and extruded at 200 ° C. to be modified to produce a cylindrical beret.
ここで得られた各変性ポリオレフィンのベレツトを、熱
プレス成形機により165℃で100kg/cm2、2分間の
条件で厚さ0.5mm、縦150mm、横180mmのシートを
成形した。この各シートと厚さ0.2mmのアルミニウム箔
をアルミニウム箔、変性ポリオレフィン、アルミニウム
箔の順に重ね合せ、温度180℃、圧力30kg/mm2で
2分間圧着して3層積層物を得た。Each modified polyolefin pellet obtained here was molded into a sheet having a thickness of 0.5 mm, a length of 150 mm, and a width of 180 mm by a hot press molding machine at 165 ° C. under 100 kg / cm 2 for 2 minutes. An aluminum foil, a modified polyolefin, and an aluminum foil were laminated in this order on each sheet and an aluminum foil having a thickness of 0.2 mm, and pressure-bonded at a temperature of 180 ° C. and a pressure of 30 kg / mm 2 for 2 minutes to obtain a three-layer laminate.
上記の3層積層物を、巾10mm、長さ150mmの試験片
に切断し、インストロン万能引張試験機にてJIS K
6854に従つて剥離試験を行い、変性ポリオレフィ
ンとアルミニウム箔との間の接着強さを測定した。但
し、引張速度は100mm/分のT形剥離であり、23
℃、50℃及び70℃と測定温度を変化させた。結果を
表2に示す。The above-mentioned three-layer laminate is cut into a test piece having a width of 10 mm and a length of 150 mm, and JIS K test is performed by an Instron universal tensile tester.
A peel test was performed according to 6854 to measure the adhesive strength between the modified polyolefin and the aluminum foil. However, the pulling speed is 100 mm / min for T-shaped peeling, and
The measurement temperature was changed to ℃, 50 ℃ and 70 ℃. The results are shown in Table 2.
また、前記の各変性ポリオレフィンを熱プレス成形機で
成形することにより得られた厚さ0.5mm、縦150mm、
横180mmのシートから、巾6mm、長さ100mmの試験
片を切出し、これらについてJIS P 8115で規
定される耐折強さを測定した。結果を同じく表2に示
す。In addition, each modified polyolefin described above is molded by a hot press molding machine to obtain a thickness of 0.5 mm, a length of 150 mm,
A test piece having a width of 6 mm and a length of 100 mm was cut out from a sheet having a width of 180 mm, and the folding endurance specified in JIS P 8115 was measured for each of the test pieces. The results are also shown in Table 2.
なお、前記の各変性ポリオレフィンを熱プレス成形機に
よつて厚さ1.0mm、縦150mm、横180mmのシートを
成形し、これからASTM D 638で規定されるダ
イCで打抜いた試験片を作製する。これらの試験片につ
いて同じくASTM D 638に従つてステイフネス
を測定し、その結果を表2に示す。A sheet of 1.0 mm in thickness, 150 mm in length and 180 mm in width was formed from each of the above modified polyolefins using a hot press molding machine, and a die C punched out from the sheet according to ASTM D 638 was used to make a test piece. To do. For these test pieces, the stiffness was also measured according to ASTM D638, and the results are shown in Table 2.
実施例1〜3において、密度が0.910g/ml以下の直
鎖状エチレン−α−オレフィンを無水マレイン酸または
アクリル酸で変性したポリオレフィンは、23〜70℃
の各温度でアルミニウム箔に対て良好な接着力を有し、
ステイフネスが小さいことから柔軟性が高い反面、耐折
強さが著しく大きく破損し難い特徴がある。この特徴
は、実施例4に示すように、直鎖状エチレン−α−オレ
フィンに他のポリオレフィン、例えばEEAを組合せた
ものを無水マレイン酸で変性したポリオレフィンについ
ても認められる。 Polyolefins obtained by modifying linear ethylene-α-olefins having a density of 0.910 g / ml or less with maleic anhydride or acrylic acid in Examples 1 to 23 have a temperature of 23 to 70 ° C.
Has good adhesion to aluminum foil at each temperature of
It has a high flexibility because it has a small staying strength, but it also has a feature that it has a large folding endurance and is hard to break. This characteristic is also observed in a polyolefin obtained by modifying a linear ethylene-α-olefin with another polyolefin, for example, EEA in combination with maleic anhydride, as shown in Example 4.
比較例1に示す直鎖状エチレン−α−オレフィンの密度
が0.910g/mlよりも大きい場合と、比較例2に示す
高密度ポリエチレンの場合は、耐折強さが小さく且つ柔
軟性が乏しい性能を示し、比較例3及び4のEVA、E
EAの場合は、柔軟性は良好であるが温度が上昇するに
伴い、接着強さが急激に低下することが認められる。In the case where the density of the linear ethylene-α-olefin shown in Comparative Example 1 is higher than 0.910 g / ml and the case of the high-density polyethylene shown in Comparative Example 2, the folding endurance is small and the flexibility is poor. Showing the performance, EVA and E of Comparative Examples 3 and 4
In the case of EA, although the flexibility is good, it is recognized that the adhesive strength sharply decreases as the temperature rises.
実施例5〜8、比較例5〜6 表1に示した実施例1及び3、比較例2及び3の変性ポ
リオレフィンと、酸化鉄、水酸化マグネシウム、炭酸カ
ルシウムを表3に示す比率で混合し、バンバリーミキサ
ーを用いて、165℃で15分間混練した。Examples 5 to 8 and Comparative Examples 5 to 6 The modified polyolefins of Examples 1 and 3 and Comparative Examples 2 and 3 shown in Table 1 were mixed with iron oxide, magnesium hydroxide and calcium carbonate in the ratio shown in Table 3. The mixture was kneaded at 165 ° C. for 15 minutes using a Banbury mixer.
それぞれの混練物を、熱プレス成形機を用いて、150
℃で100kg/cm2、2分間プレスして厚さ1.0mmと2.
0mmのシートを成形した。厚さ1.0mmのシートからJI
S K 6760で規定されるダンベル状試験片に打抜
き、引張速度100mm/分で引張強さ及び伸びを測定し
た。Each kneaded product was heated to 150 using a hot press molding machine.
Pressed at 100kg / cm 2 for 2 minutes, thickness 1.0mm and 2.
A 0 mm sheet was molded. From a sheet with a thickness of 1.0 mm to JI
A dumbbell-shaped test piece specified by SK 6760 was punched out, and the tensile strength and elongation were measured at a tensile speed of 100 mm / min.
また、厚さ2.0mmのシートから、JIS K 7216
で規定される幅6.0mm、長さ38.0mmの長方形の試験片
を打抜き、これ等についてぜい化温度を測定した。In addition, from a sheet with a thickness of 2.0 mm, JIS K 7216
A rectangular test piece having a width of 6.0 mm and a length of 38.0 mm specified in 1. was punched out, and the embrittlement temperature was measured.
上記の結果を表4に示すが、実施例5〜8から判るよう
に密度0.910g/mlの気相・低圧法で製造した直鎖状
エチレン−α−オレフィンを無水マレイン酸またはアク
リル酸で変性したポリオレフィンと、金属、無機物等を
混練したものは、充分大きな引張強さ、伸び及び低温ぜ
い性を有しているが、比較例5及び6に示す高密度ポリ
エチレン及びEVAを無水マレイン酸で変性したものは
いずれも引張強さが小さく、低温ぜい性が不充分であ
る。The above results are shown in Table 4. As can be seen from Examples 5 to 8, linear ethylene-α-olefins produced by the gas phase low pressure method with a density of 0.910 g / ml were treated with maleic anhydride or acrylic acid. The modified polyolefin, kneaded with a metal, an inorganic substance and the like have sufficiently large tensile strength, elongation and low temperature embrittlement, but the high density polyethylene and EVA shown in Comparative Examples 5 and 6 are mixed with maleic anhydride. All of those modified by (1) have low tensile strength and insufficient low temperature brittleness.
実施例9〜12、比較例7〜9 表1に示した実施例1及び比較例2の変性ポリオレフィ
ンとEVA、EEA及びカーボンブラツク、炭酸カルシウムを
表4に示す比率で混合し、バンバリーミキサーを用い
て、165℃で15分間混練した。 Examples 9 to 12 and Comparative Examples 7 to 9 The modified polyolefins of Example 1 and Comparative Example 2 shown in Table 1 were mixed with EVA, EEA, carbon black and calcium carbonate in the ratios shown in Table 4, and a Banbury mixer was used. And kneaded at 165 ° C. for 15 minutes.
得られた混合物を、実施例5〜8、比較例7〜8と同一
の操作を行なつて引張強さ及び伸び測定用ダンベル状試
験片とぜい化温度測定用長方形試験片を得た。The obtained mixture was subjected to the same operations as in Examples 5 to 8 and Comparative Examples 7 to 8 to obtain dumbbell-shaped test pieces for measuring tensile strength and elongation and rectangular test pieces for measuring embrittlement temperature.
上記の試験片について、引張強さ、伸び及びぜい化温度
を測定し、その結果を表5に示すが、実施例9〜12か
ら判るように、密度0.910g/mlの気相・低圧法で製
造した直鎖状エチレン−α−オレフィンを無水マレイン
酸で変性したポリオレフィンと、未変性のEVA或いは
EEAの混合物、又はこれ等に更にカーボンブラツク或
いは炭酸カルシウムを添加した混合物は、充分大きな引
張強さ、伸び及び低温ぜい性を有している。一方、比較
例7〜9に示す高密度ポリエチレンを無水マレイン酸で
変性したポリオレフィンと未変性のEVA或いはEEA
の混合物、又は、これ等にカーボンブラツク、或いは炭
酸カルシウムを添加した混合物は、いずれも引張強さと
伸びが小さく、低温ぜい性が不充分である。Tensile strength, elongation and embrittlement temperature were measured for the above test pieces, and the results are shown in Table 5. As can be seen from Examples 9 to 12, the gas phase density of 0.910 g / ml / low pressure was obtained. A linear ethylene-α-olefin produced by the method of the present invention and a mixture of a polyolefin modified with maleic anhydride and an unmodified EVA or EEA, or a mixture obtained by further adding carbon black or calcium carbonate to it has a sufficiently large tensile strength. It has strength, elongation and low temperature brittleness. On the other hand, the polyolefins obtained by modifying the high-density polyethylenes shown in Comparative Examples 7 to 9 with maleic anhydride and unmodified EVA or EEA
Or a mixture of carbon black and calcium carbonate added thereto has low tensile strength and elongation and insufficient low temperature brittleness.
以上説明したように、本発明は密度0.910g/ml以下
である気相・低圧法で製造された直鎖状エチレン−α−
オレフィン共重合体に不飽和カルボン酸またはその酸無
水物をグラフト化して変性したポリオレフィンを金属、
無機物または異種プラスチツクと接着または混合するこ
とにより複合物を作ることに関するものであり、従来の
変性ポリオレフィンでは得られない高温度における接着
強さ、良好な耐折強さ、充分な柔軟性、引張強さ、伸び
及び低温脆性が付与され、その工業的価値は極めて大な
るものがある。 As described above, the present invention has a density of 0.910 g / ml or less and is a linear ethylene-α-produced by the gas phase / low pressure method.
Metallic polyolefin modified by grafting an unsaturated carboxylic acid or its acid anhydride onto an olefin copolymer,
It relates to the formation of composites by adhering or mixing with inorganic substances or different types of plastics, and has adhesive strength at high temperatures, good folding endurance, sufficient flexibility, tensile strength that cannot be obtained with conventional modified polyolefins. Strain, elongation and low temperature brittleness are imparted, and their industrial value is extremely high.
Claims (6)
圧法で製造された直鎖状エチレン−α−オレフィン共重
合体に不飽和カルボン酸またはその酸無水物をグラフト
化して変性したポリオレフィンを金属、無機物または異
種プラスチツクと接着または混合することにより複合物
としたことを特徴とする変性ポリオレフィンによる複合
物。1. A straight-chain ethylene-α-olefin copolymer produced by a gas-phase / low-pressure method having a density of 0.910 g / ml or less is modified by grafting an unsaturated carboxylic acid or an acid anhydride thereof. A composite by a modified polyolefin, characterized in that a composite is prepared by adhering or mixing the above-mentioned polyolefin with a metal, an inorganic material or a different kind of plastic.
8の範囲にある気相・低圧法で製造された直鎖状エチレ
ン−α−オレフィン共重合体である特許請求の範囲第1
項記載の複合物。2. The number of carbon atoms constituting the α-olefin is 3 to.
A linear ethylene-α-olefin copolymer produced by a gas phase / low pressure method within the range of Claim 8.
The compound according to the item.
が周期律表において、第IV〜VIII族の遷移金属化合物と
第I〜III族の有機金属化合物の組合せにより生成する
触媒、所謂チーグラー触媒を用いて気相・低圧法で製造
された特許請求の範囲第1項記載の複合物。3. A catalyst, a so-called Ziegler, produced by combining a linear ethylene-α-olefin copolymer with a transition metal compound of groups IV to VIII and an organometallic compound of groups I to III in the periodic table. The composite according to claim 1, which is produced by a gas phase / low pressure method using a catalyst.
圧法で製造された直鎖状エチレン−α−オレフィン共重
合体に不飽和カルボン酸またはその酸無水物をグラフト
化して変性したポリオレフィンに未変性のエラストマー
またはポリオレフィンを添加した混合物より成る特許請
求の範囲第1項記載の複合物。4. A straight chain ethylene-α-olefin copolymer produced by a gas phase / low pressure method having a density of 0.910 g / ml or less, is modified by grafting an unsaturated carboxylic acid or an acid anhydride thereof. A composite according to claim 1 which comprises a mixture of an unmodified elastomer or a polyolefin added to said polyolefin.
が流動床反応帯域中で10゜〜80℃の温度かつ7,00
0KPa以下の圧力にて、(a)0.35:1〜8.0:1の
高級αオレフィン対エチレンのモル比でエチレン及び3
〜8個の炭素原子を有する少なくとも1種の高級α−オ
レフィンと、(b)少なくとも25モル%の少なくとも1
種の希釈ガスとを含有する気体混合物を式: MgmTi(OR)nXp〔ED〕q 〔式中、Rは1〜14個の炭素原子を有する脂肪族若し
くは芳香族の炭化水素基又はCOR′であり、ここで
R′は1〜14個の炭素原子を有する脂肪族若しくは芳
香族の炭化水素基であり、XはCl、Br、I及びその
混合物よりなる群から選択され、 EDは脂肪族若しくは芳香族酸のアルキルエステル、脂
肪族エーテル、環式エーテル及び脂肪族ケトンよりなる
群から選択される有機電子供与化合物であり、 mは0.5〜56であり、 nは0.1又は2であり、 pは2〜116であり、 qは2〜85である〕 を有する先駆体組成物からなる触媒系の粒子と連続的に
接触させ、前記先駆体組成物を不活性キヤリヤ材料で希
釈すると共に式: Al(R′)dX′eHf 〔式中、X′はCl又はOR″であり、 R′及びR″は1〜14個の炭素原子を有する飽和炭化
水素基であり、 eは0〜1.5であり、 fは0又は1であり、 d+e+f=3である〕 を有する有機アルミニウム化合物で完全に活性化させ、
前記活性化化合物を前記反応帯域中における全アルミニ
ウム対チタンのモル比が10:1〜400:1となるよ
うな量で使用することを特徴とするエチレン共重合体の
連続製造方法で製法されたものである特許請求の範囲第
1項記載の複合物。5. A linear ethylene-.alpha.-olefin copolymer having a temperature of 10.degree.-80.degree. C. and 7,000 in a fluidized bed reaction zone.
At pressures below 0 KPa, (a) ethylene and 3 at a molar ratio of higher α-olefin to ethylene of 0.35: 1 to 8.0: 1.
At least one higher alpha-olefin having from 8 to 8 carbon atoms, and (b) at least 25 mol% of at least 1
A gas mixture containing a diluent gas of the formula: MgmTi (OR) n X p [ED] q [wherein R is an aliphatic or aromatic hydrocarbon group having 1 to 14 carbon atoms or COR]. Is R ', where R'is an aliphatic or aromatic hydrocarbon group having 1 to 14 carbon atoms, X is selected from the group consisting of Cl, Br, I and mixtures thereof, and ED is a fatty group. An organic electron-donating compound selected from the group consisting of alkyl esters of aromatic or aromatic acids, aliphatic ethers, cyclic ethers and aliphatic ketones, m is 0.5 to 56, n is 0.1 or 2 and p is 2 to 116 and q is 2 to 85] are continuously contacted with particles of a catalyst system comprising a precursor composition, and the precursor composition is an inert carrier material. Dilute and formula: Al (R ′) d X ′ e H f [ Wherein X ′ is Cl or OR ″, R ′ and R ″ are saturated hydrocarbon groups having 1 to 14 carbon atoms, e is 0 to 1.5, and f is 0 or 1 And d + e + f = 3],
It was prepared by a continuous process for producing an ethylene copolymer, characterized in that the activating compound was used in an amount such that the molar ratio of total aluminum to titanium in the reaction zone was 10: 1 to 400: 1. The composite according to claim 1, which is a composite.
がエチレンを単独で又は少なくとも1種のC3〜C10α
−オレフィンとともに気相中で約10℃〜約115℃の
温度において、 (A) (1)塩素、臭素又はよう素による三ハロゲン化パラ
ジウム(a)と該三ハロゲン化バナジウムが可溶である液
状の有機ルイス塩基である電子供与体(b)との反応生成
物であるバナジウム化合物と (2)次式 MXa (ここでMはほう素か又はAlR(3−a)のいずれか
であり、各Rはそれぞれアルキルであるが、ただしいず
れのR基においても脂肪族炭素原子の総数は14を越え
ず、 Xは塩素、臭素又はよう素であり、 aは0、1又は2であり、ただしMがほう素のときはa
は3である) を有する変性剤 とをシリカ又はアルミナから本質上なる固体不活性担体
上に担持させたものから本質上なる担持された先駆物質
と、 (B) 次式 AlR3 (ここでRは先に定義した通りである) を有する助触媒と、 (C) 次式 R′bCX′(4−b) (ここでR′は水素又は非置換の若しくはハロゲン置換
された低級アルキルであり、X′はハロゲンであり、 bは0、1又は2である) を有する促進剤 を含む触媒組成物と接触させることによつて単量体を重
合させることからポリエチレンの製造法で製造されたも
のである特許請求の範囲第1項記載の複合物。6. The linear ethylene-α-olefin copolymer comprises ethylene alone or at least one C 3 -C 10 α.
(A) (1) Palladium trihalide (a) with chlorine, bromine or iodine and a liquid in which the vanadium trihalide is soluble at a temperature of about 10 ° C to about 115 ° C in the gas phase together with an olefin. And a vanadium compound which is a reaction product with an electron donor (b) which is an organic Lewis base of (2) the following formula MXa (where M is either boron or AlR (3-a), R is each alkyl, provided that the total number of aliphatic carbon atoms in any R group does not exceed 14, X is chlorine, bromine or iodine, a is 0, 1 or 2, and M is A is boron
Is a 3) and a supported precursor consisting essentially of a silica or alumina supported on a solid inert carrier consisting essentially of (B) the following formula AlR 3 (where R Is as defined above), and (C) is of the formula R'b CX '(4-b) where R'is hydrogen or unsubstituted or halogen-substituted lower alkyl. , X'is a halogen, and b is 0, 1 or 2) prepared by a process for producing polyethylene from polymerizing the monomer by contacting with a catalyst composition containing a promoter having The composite according to claim 1, which is a composite.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60157022A JPH0615218B2 (en) | 1985-07-18 | 1985-07-18 | Composite with modified polyolefin |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60157022A JPH0615218B2 (en) | 1985-07-18 | 1985-07-18 | Composite with modified polyolefin |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6218258A JPS6218258A (en) | 1987-01-27 |
| JPH0615218B2 true JPH0615218B2 (en) | 1994-03-02 |
Family
ID=15640470
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60157022A Expired - Lifetime JPH0615218B2 (en) | 1985-07-18 | 1985-07-18 | Composite with modified polyolefin |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0615218B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5007574A (en) * | 1989-09-14 | 1991-04-16 | Metcal, Inc. | Desoldering device |
| CN118832889B (en) * | 2024-07-01 | 2025-02-18 | 江苏中鑫家居新材料股份有限公司 | Preparation method of fire-resistant and stain-resistant SPC floor |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4338944A (en) * | 1980-06-16 | 1982-07-13 | The Kendall Company | Therapeutic device |
-
1985
- 1985-07-18 JP JP60157022A patent/JPH0615218B2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6218258A (en) | 1987-01-27 |
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