JPH0457812A - Modified polyolefin resin - Google Patents
Modified polyolefin resinInfo
- Publication number
- JPH0457812A JPH0457812A JP16837590A JP16837590A JPH0457812A JP H0457812 A JPH0457812 A JP H0457812A JP 16837590 A JP16837590 A JP 16837590A JP 16837590 A JP16837590 A JP 16837590A JP H0457812 A JPH0457812 A JP H0457812A
- Authority
- JP
- Japan
- Prior art keywords
- polyolefin resin
- modified polyolefin
- weight
- radical generator
- imide compound
- 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
- 229920005672 polyolefin resin Polymers 0.000 title claims abstract description 23
- -1 imide compound Chemical class 0.000 claims abstract description 29
- 239000000126 substance Substances 0.000 claims description 5
- 229910052751 metal Inorganic materials 0.000 abstract description 6
- 239000002184 metal Substances 0.000 abstract description 6
- 230000009965 odorless effect Effects 0.000 abstract description 3
- 239000011521 glass Substances 0.000 abstract description 2
- 150000001451 organic peroxides Chemical class 0.000 abstract description 2
- 229920000098 polyolefin Polymers 0.000 abstract description 2
- 238000000034 method Methods 0.000 description 11
- 230000000704 physical effect Effects 0.000 description 10
- 238000001125 extrusion Methods 0.000 description 9
- 239000003365 glass fiber Substances 0.000 description 9
- 229920000219 Ethylene vinyl alcohol Polymers 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 7
- UFRKOOWSQGXVKV-UHFFFAOYSA-N ethene;ethenol Chemical compound C=C.OC=C UFRKOOWSQGXVKV-UHFFFAOYSA-N 0.000 description 6
- 239000004715 ethylene vinyl alcohol Substances 0.000 description 6
- 229920005989 resin Polymers 0.000 description 6
- 239000011347 resin Substances 0.000 description 6
- IYMZEPRSPLASMS-UHFFFAOYSA-N 3-phenylpyrrole-2,5-dione Chemical compound O=C1NC(=O)C(C=2C=CC=CC=2)=C1 IYMZEPRSPLASMS-UHFFFAOYSA-N 0.000 description 5
- 239000004743 Polypropylene Substances 0.000 description 5
- 150000002739 metals Chemical class 0.000 description 5
- 229920001155 polypropylene Polymers 0.000 description 5
- 238000005453 pelletization Methods 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- VOZRXNHHFUQHIL-UHFFFAOYSA-N glycidyl methacrylate Chemical compound CC(=C)C(=O)OCC1CO1 VOZRXNHHFUQHIL-UHFFFAOYSA-N 0.000 description 3
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- 125000002572 propoxy group Chemical group [*]OC([H])([H])C(C([H])([H])[H])([H])[H] 0.000 description 3
- 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
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 229920001577 copolymer Polymers 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 238000004898 kneading Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000007342 radical addition reaction Methods 0.000 description 2
- KDGNCLDCOVTOCS-UHFFFAOYSA-N (2-methylpropan-2-yl)oxy propan-2-yl carbonate Chemical compound CC(C)OC(=O)OOC(C)(C)C KDGNCLDCOVTOCS-UHFFFAOYSA-N 0.000 description 1
- UICXTANXZJJIBC-UHFFFAOYSA-N 1-(1-hydroperoxycyclohexyl)peroxycyclohexan-1-ol Chemical compound C1CCCCC1(O)OOC1(OO)CCCCC1 UICXTANXZJJIBC-UHFFFAOYSA-N 0.000 description 1
- XMYJXSITMZVPFY-UHFFFAOYSA-N 2,5-bis(butylperoxy)-2,5-dimethylhexane Chemical compound CCCCOOC(C)(C)CCC(C)(C)OOCCCC XMYJXSITMZVPFY-UHFFFAOYSA-N 0.000 description 1
- DMWVYCCGCQPJEA-UHFFFAOYSA-N 2,5-bis(tert-butylperoxy)-2,5-dimethylhexane Chemical compound CC(C)(C)OOC(C)(C)CCC(C)(C)OOC(C)(C)C DMWVYCCGCQPJEA-UHFFFAOYSA-N 0.000 description 1
- WFUGQJXVXHBTEM-UHFFFAOYSA-N 2-hydroperoxy-2-(2-hydroperoxybutan-2-ylperoxy)butane Chemical compound CCC(C)(OO)OOC(C)(CC)OO WFUGQJXVXHBTEM-UHFFFAOYSA-N 0.000 description 1
- FRIBMENBGGCKPD-UHFFFAOYSA-N 3-(2,3-dimethoxyphenyl)prop-2-enal Chemical compound COC1=CC=CC(C=CC=O)=C1OC FRIBMENBGGCKPD-UHFFFAOYSA-N 0.000 description 1
- YQUQWHNMBPIWGK-UHFFFAOYSA-N 4-isopropylphenol Chemical compound CC(C)C1=CC=C(O)C=C1 YQUQWHNMBPIWGK-UHFFFAOYSA-N 0.000 description 1
- 239000004593 Epoxy Substances 0.000 description 1
- YIVJZNGAASQVEM-UHFFFAOYSA-N Lauroyl peroxide Chemical compound CCCCCCCCCCCC(=O)OOC(=O)CCCCCCCCCCC YIVJZNGAASQVEM-UHFFFAOYSA-N 0.000 description 1
- 239000004594 Masterbatch (MB) Substances 0.000 description 1
- 238000000944 Soxhlet extraction Methods 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000000862 absorption spectrum Methods 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 239000001273 butane Substances 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000004040 coloring Methods 0.000 description 1
- LSXWFXONGKSEMY-UHFFFAOYSA-N di-tert-butyl peroxide Chemical compound CC(C)(C)OOC(C)(C)C LSXWFXONGKSEMY-UHFFFAOYSA-N 0.000 description 1
- 239000012933 diacyl peroxide Substances 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229920001903 high density polyethylene Polymers 0.000 description 1
- 239000004700 high-density polyethylene Substances 0.000 description 1
- 150000002432 hydroperoxides Chemical class 0.000 description 1
- 150000003949 imides Chemical class 0.000 description 1
- 239000011256 inorganic filler Substances 0.000 description 1
- 229910003475 inorganic filler Inorganic materials 0.000 description 1
- 125000001449 isopropyl group Chemical group [H]C([H])([H])C([H])(*)C([H])([H])[H] 0.000 description 1
- 238000010030 laminating Methods 0.000 description 1
- 239000000314 lubricant 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
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 description 1
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 239000012766 organic filler Substances 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 229920000306 polymethylpentene Polymers 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- MWNQXXOSWHCCOZ-UHFFFAOYSA-L sodium;oxido carbonate Chemical compound [Na+].[O-]OC([O-])=O MWNQXXOSWHCCOZ-UHFFFAOYSA-L 0.000 description 1
- 230000002269 spontaneous effect Effects 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 125000000999 tert-butyl group Chemical group [H]C([H])([H])C(*)(C([H])([H])[H])C([H])([H])[H] 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Landscapes
- Graft Or Block Polymers (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、ガラス繊維、金属およびエチレンビニルアル
コール共重合体(以下EVOHと略す)等との接着性が
改善された変性ポリオレフィン樹脂に関するものである
。[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to a modified polyolefin resin with improved adhesion to glass fibers, metals, ethylene vinyl alcohol copolymer (hereinafter abbreviated as EVOH), etc. be.
一般にポリオレフィン樹脂はその優れた機械的特性や耐
薬品性等のために自動車部品等様々な産業分野に好適に
用いられているが、その反面、剛性、寸法安定性や耐熱
性等に欠点があり、用途が限定されている。In general, polyolefin resins are suitable for use in various industrial fields such as automobile parts due to their excellent mechanical properties and chemical resistance, but on the other hand, they have drawbacks such as rigidity, dimensional stability, and heat resistance. , its uses are limited.
かかる欠点を解決するために、他の樹脂との組成物を形
成する方法、有機や無機のフィラーあるいは金属を添加
する方法がおこなわれてきた。しかしながら元来無極性
分子であるが故に極性物質との接着性や相溶性が悪く、
これを改良する種々の改質が検討されている。例えば極
性物質をブレンドしたり、無水マレイン酸やグリシジル
メタクリレート(以下、GMAと略す)などの極性子ツ
マ−をグラフト反応させることが公知の技術として用い
られているが、未だ充分な実用物性を供しえておらず、
また押出の際に異臭を発するなど問題があった。In order to solve these drawbacks, methods have been used to form a composition with other resins, or to add organic or inorganic fillers or metals. However, since it is originally a non-polar molecule, it has poor adhesion and compatibility with polar substances.
Various modifications to improve this are being considered. For example, known techniques include blending polar substances or grafting polar molecules such as maleic anhydride or glycidyl methacrylate (hereinafter abbreviated as GMA), but these techniques still do not provide sufficient practical physical properties. I haven't
Additionally, there were problems such as a strange odor being emitted during extrusion.
[発明が解決しようとする課題]
本発明の目的は、かかる問題を解決し、金属、ガラス繊
維等との接着性が改善された無臭性の変性ポリオレフィ
ン樹脂を提供することにある。[Problems to be Solved by the Invention] An object of the present invention is to solve these problems and provide an odorless modified polyolefin resin with improved adhesion to metals, glass fibers, and the like.
〔課題を解決するための手段]
本発明者等は、上記の問題を解決すべく鋭意検討した結
果、ポリオレフィン樹脂に特定のイミド化合物およびラ
ジカル発生剤を反応させてなる変性ポリオレフィン樹脂
が上記目的を達成できることを見出し、本発明に到達し
たものである。[Means for Solving the Problems] As a result of intensive studies to solve the above problems, the present inventors have found that a modified polyolefin resin obtained by reacting a specific imide compound and a radical generator with a polyolefin resin achieves the above object. We have discovered what can be achieved and have arrived at the present invention.
すなわち、ポリオレフィン樹脂100重量部に対して、
式(1)または式(2)で示されるイミド化合物0.1
〜20重量部およびラジカル発生剤0.01〜10重量
部を反応させてなる変性ポリオレフィン樹脂を提供する
ものである。That is, for 100 parts by weight of polyolefin resin,
Imide compound represented by formula (1) or formula (2) 0.1
A modified polyolefin resin is provided by reacting ~20 parts by weight with 0.01 to 10 parts by weight of a radical generator.
本発明で用いられるポリオレフィン樹脂としては、例え
ば、ポリプロピレン、ポリエチレン、プロピレン−エチ
レン共重合体、エチレン−プロピレンジシクロペンタジ
ェン共重合体、 エチレンプロピレンエチリデンノルボ
ー2ン共重合体、ポリ(4−メチル−ペンテン−1)な
どが挙げられる。Examples of the polyolefin resin used in the present invention include polypropylene, polyethylene, propylene-ethylene copolymer, ethylene-propylene dicyclopentadiene copolymer, ethylene propylene ethylidene norbo-2 copolymer, poly(4-methyl -pentene-1) and the like.
本発明で用いられる特定のイミド化合物とは、式(1)
または式(2)
で示され、その製法は商業的に入手し得るN−(4ヒド
ロキシ)フェニルマレイミドや2−(4’−ヒドロキシ
フェニル)プロパンなどの既存の酸イミド化合物にエピ
クロルヒドリンをアルカリ条件下で中和反応させて得る
ことができる。The specific imide compound used in the present invention is represented by formula (1)
Alternatively, it is represented by formula (2), and its production method involves adding epichlorohydrin to existing acid imide compounds such as commercially available N-(4-hydroxy)phenylmaleimide and 2-(4'-hydroxyphenyl)propane under alkaline conditions. It can be obtained by a neutralization reaction.
ラジカル発生剤としては一般には、有機過酸化物が挙げ
られるほか、酸化力のあるものであれば何でもよく、有
機、無機を問わない。具体的には、ケトンパーオキサイ
ド系として、メチルエチルケトンパーオキサイド、シク
ロヘキサノンパーオキサイド、ジアシルパーオキサイド
系として、ラウロイルパーオキサイド、ヘンシイルバー
オキサイド、ハイドロパーオキサイド系として、クメン
ハイドロパーオキサイド、L−ブチルハイドロパーオキ
サイド、ジアルキルパーオキサイド系として、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、ジ−t−ブチルパーオキ
サイド、2.5−ジメチル−2,5−ジ(−1−ブチル
パーオキシ)ヘキシン、3,1.3−ビス−(t−ブチ
ルパーオキシ−イソプロピル)ベンゼン、パーオキシケ
タール系として、2,2−ジ(t−ブチルパーオキシ)
ブタン、アルキルパーエステル系として、t−プチルパ
ーオキシヘンゾエート、パーカーボネート系として、t
−ブチルパーオキシイソプロビルカーポネート等が挙げ
られる。In general, the radical generating agent includes organic peroxides, and any radical generator may be used as long as it has oxidizing power, regardless of whether it is organic or inorganic. Specifically, ketone peroxides include methyl ethyl ketone peroxide, cyclohexanone peroxide, diacyl peroxides include lauroyl peroxide and hensyl peroxide, and hydroperoxides include cumene hydroperoxide and L-butyl hydroper. Dicumyl peroxide, 2,5-dimethyl-2,5-di(t-
butylperoxy)hexane, di-t-butylperoxide, 2,5-dimethyl-2,5-di(-1-butylperoxy)hexane, 3,1,3-bis-(t-butylperoxy) isopropyl)benzene, 2,2-di(t-butylperoxy) as a peroxyketal
Butane, alkyl perester type, t-butyl peroxyhenzoate, percarbonate type, t
-butylperoxyisopropyl carbonate and the like.
上記各成分の好適な組成条件はポリオレフィン100重
量部に対してイミド化合物0.1〜20重量部好ましく
は0.1〜10重量部およびラジカル発生剤0.01〜
1帽1部好ましくは0.03〜1重量部である。イミド
化合物およびラジカル発生剤の添加量が上記範囲より少
ない場合には十分な変性効果が得られず、多い場合には
樹脂の着色、分子量の低下、臭気の発生が起こるので好
ましくない。Suitable composition conditions for each of the above components are 0.1 to 20 parts by weight of the imide compound, preferably 0.1 to 10 parts by weight, and 0.01 to 10 parts by weight of the radical generator per 100 parts by weight of the polyolefin.
The amount is preferably 0.03 to 1 part by weight per hat. If the amount of the imide compound and radical generator added is less than the above range, a sufficient modification effect cannot be obtained, and if it is more than the above range, coloring of the resin, reduction in molecular weight, and generation of odor occur, which is not preferable.
さらに、本発明の変性ポリオレフィン樹脂中に酸化防止
剤等の安定剤、滑剤、紫外線吸収剤、帯電防止剤等を添
加してもかまわない。Furthermore, stabilizers such as antioxidants, lubricants, ultraviolet absorbers, antistatic agents, etc. may be added to the modified polyolefin resin of the present invention.
本発明の変性ポリオレフィン樹脂の製造方法に関しては
特に制限はなく、通常公知の方法を採用することができ
る。ポリオレフィン樹脂、イミド化合物およびラジカル
発生剤を高速撹拌機などを用いて均一混合した後、十分
な混練能力のある一軸または多軸の押出機で溶融混練し
て製造される。押出機中の反応温度は150〜250°
C1反応時間は0.5〜30分が望ましい。There are no particular limitations on the method for producing the modified polyolefin resin of the present invention, and generally known methods can be employed. It is produced by uniformly mixing a polyolefin resin, an imide compound, and a radical generator using a high-speed stirrer or the like, and then melt-kneading the mixture using a single-screw or multi-screw extruder with sufficient kneading capacity. The reaction temperature in the extruder is 150-250°
The C1 reaction time is preferably 0.5 to 30 minutes.
本発明で得られた変性ポリオレフィン樹脂は、ガラス繊
維や金属、EVOH等への接着性が改善され、充分な実
用物性を提供することが可能であるが、さらにマスター
バッチとして各種ポリオレフィン樹脂に添加して、ポリ
オレフィン樹脂の接着性を改善することもできる。The modified polyolefin resin obtained in the present invention has improved adhesion to glass fibers, metals, EVOH, etc., and can provide sufficient practical properties, but it can also be added to various polyolefin resins as a masterbatch. It is also possible to improve the adhesion of polyolefin resins.
以下に実施例を挙げて、本発明をさらに詳しく説明する
。なお、実施例および比較例に記した物性評価は次の方
法に従って実施した。The present invention will be explained in more detail with reference to Examples below. Note that the physical property evaluations described in Examples and Comparative Examples were performed according to the following method.
(1)押出変性時の臭気 異臭:押出時に臭気が発生し好ましくない。(1) Odor during extrusion modification Off-odor: Undesirable odor occurs during extrusion.
無臭:押出時に臭気はほとんどない。Odorless: There is almost no odor during extrusion.
(2)アイゾツト衝撃強度 JIS−に7110に準拠した。(2) Izotsu impact strength Compliant with JIS-7110.
(3)引張強度および伸び J I S−に7113に準拠した。(3) Tensile strength and elongation In accordance with JIS-7113.
(4)剥離強度
AI板あるいはEVOH板に、変性ポリオレフィン樹脂
を熱溶着した幅10111の短冊状試験片を作成し、測
定温度23°C1剥離角度180度、引張速度50mm
/minで、引張試験機を用いて塗膜を一端から剥離し
、その時の眉間剥離強度(kg)を測定した。(4) Peel strength A strip-shaped test piece with a width of 10111 mm was prepared by thermally welding modified polyolefin resin to an AI plate or an EVOH plate, and the measurement temperature was 23°C, the peeling angle was 180°, and the tensile speed was 50mm.
/min, the coating film was peeled from one end using a tensile tester, and the glabella peel strength (kg) at that time was measured.
実施例I
N−(4−ヒドロキシ)フェニルマレイミドとエピクロ
ルヒドリンとを1対1のモル比でアルカリ条件下におい
て中和反応させ、N−[4−(2,3エポキシ)プロポ
キシ]フェニルマレイミドを得た。Example I N-(4-hydroxy)phenylmaleimide and epichlorohydrin were neutralized in a 1:1 molar ratio under alkaline conditions to obtain N-[4-(2,3epoxy)propoxy]phenylmaleimide. .
ポリプロピレン樹脂〔三井東圧化学(株)社製商品名三
井ノーブレン〕100重量部に対して、N−(4−(2
,3エポキシ)プロポキシ〕フェニルマレイミド10重
量部およびジクミルパーオキサイド0.1重量部をヘン
シェルミキサーで混合した後、スクリュー径3h+m、
L/D・30の2軸押出機にて溶融温度200℃、ス
クリュー回転数100rp−でベレット状に押出し、変
性ポリプロピレン樹脂を得た。押出時に臭気はほとんど
なかった。得られた樹脂をクロロボルムにて8時間ソッ
クスレー抽出した後、赤外吸収スペクトルを調べたとこ
ろ、イミドに由来するカルボニルの吸収ビーク(165
0cm−’ )を有しており、上記イミド化合物がポリ
プロピレン樹脂にラジカル付加していることが確認され
た。N-(4-(2
, 3 epoxy) propoxy] After mixing 10 parts by weight of phenylmaleimide and 0.1 part by weight of dicumyl peroxide in a Henschel mixer, a screw diameter of 3 h + m,
A modified polypropylene resin was obtained by extruding into a pellet shape using a L/D 30 twin-screw extruder at a melting temperature of 200° C. and a screw rotation speed of 100 rpm. There was almost no odor during extrusion. After Soxhlet extraction of the obtained resin with chloroborm for 8 hours, the infrared absorption spectrum was examined, and an absorption peak of carbonyl derived from imide (165
0 cm-'), and it was confirmed that the imide compound was radically added to the polypropylene resin.
得られた変性ポリプロピレン樹脂100重量部に対して
、長さsIl■のガラスチョツプドストランドを20重
量部添加し、タンブラ−で充分混合した後押出しペレッ
ト化した0本ペレットから75トンの射出成形機で射出
成形した試験片を用いて物性試験を行いその結果を表1
に示す。To 100 parts by weight of the obtained modified polypropylene resin, 20 parts by weight of chopped glass strands having a length of sIl were added, thoroughly mixed in a tumbler, and then extruded to form pellets. 75 tons of the resulting pellets were then injection molded. A physical property test was conducted using a test piece injection molded using a machine, and the results are shown in Table 1.
Shown below.
また、変性ポリオレフィン樹脂を脱脂した軟質アルミニ
ウム板(AI板と略す)あるいは EVOH板上に置き
、加熱溶融プレスして接着し剥離試験片を作成して、剥
離強度を測定しその結果も表1に併せて示す。In addition, a modified polyolefin resin was placed on a degreased soft aluminum plate (abbreviated as AI plate) or an EVOH plate, and the sample was bonded by heating and melt pressing to create a peel test piece, and the peel strength was measured. The results are also shown in Table 1. Also shown.
上記の結果は何れも良好で、充分な実用物性を有する。All of the above results are good and have sufficient practical physical properties.
実施例2
実施例1において、N−C4−C2,3エポキシ)プロ
ポキシ〕フェニルマレイミドのかわりに、2−(4ヒド
ロキシフエニル)−2−(4’ マレイミドフェニル)
プロパンに変えた以外は実施例1と同様とし、その結果
を表1に示す。何れも良好で、充分な実用物性を有する
。Example 2 In Example 1, 2-(4hydroxyphenyl)-2-(4'maleimidophenyl) was used instead of N-C4-C2,3epoxy)propoxy]phenylmaleimide.
The procedure was the same as in Example 1 except that propane was used, and the results are shown in Table 1. All of them are good and have sufficient practical physical properties.
実施例3
実施例2において、ポリプロピレンのかわりに高密度ポ
リエチレン〔三井石油化学(株)製 商品名ハイゼック
ス〕に変えた以外は実施例2と同様とし、その結果を表
1に示す。何れも良好で、充分な実用物性を存する。Example 3 The procedure was the same as in Example 2, except that polypropylene was replaced with high-density polyethylene (trade name: HIZEX, manufactured by Mitsui Petrochemicals Co., Ltd.), and the results are shown in Table 1. All of them are good and have sufficient practical physical properties.
実施例4〜7
実施例1において、イミド化合物およびラジカル発生剤
を表1に示す割合で用いた以外は実施例1と同様とし、
その結果を表1に示す。何れも良好で、充分な実用物性
を有する。Examples 4 to 7 Same as Example 1 except that the imide compound and radical generator were used in the proportions shown in Table 1,
The results are shown in Table 1. All of them are good and have sufficient practical physical properties.
比較例1
実施例1において、イミド化合物の配合量を変えた以外
は実施例1と同様とし、その結果を表1に示す、イミド
化合物のラジカル付加が確認できなかった。また、ガラ
ス繊維との接着性が悪く実用物性も劣り、かつ剥離強度
も低い。Comparative Example 1 Example 1 was carried out in the same manner as in Example 1 except that the amount of the imide compound was changed, and the results are shown in Table 1. No radical addition of the imide compound was confirmed. In addition, it has poor adhesion to glass fibers, poor practical physical properties, and low peel strength.
比較例2
実施例1において、イミド化合物の配合量を変えた以外
は実施例1と同様とし、その結果を表1に示す、押出ベ
レット化の際に悪臭が発生した。Comparative Example 2 The procedure was the same as in Example 1 except that the amount of the imide compound was changed, and the results are shown in Table 1. A foul odor was generated during extrusion pelletizing.
また、ガラス繊維との接着性が悪く実用物性も劣り、か
つAIおよびEVOHとの剥離強度も低い。In addition, it has poor adhesion to glass fibers and poor practical properties, and also has low peel strength with AI and EVOH.
比較例3
実施例1において、ラジカル発生剤を用いなかった以外
は実施例1七同様とし、その結果を表1に示す。イミド
化合物のラジカル付加が確認できなかった。また、ガラ
ス繊維との接着性が悪く実用物性も劣り、かつ剥離強度
も低い。Comparative Example 3 The same procedure as in Example 17 was carried out except that no radical generator was used in Example 1, and the results are shown in Table 1. No radical addition of the imide compound could be confirmed. In addition, it has poor adhesion to glass fibers, poor practical physical properties, and low peel strength.
比較例4
実施例1において、ラジカル発生剤を表1に示す割合で
用いた以外は実施例1と同様とし、その結果を表1に示
す、過剰のラジカル発生剤のため分子量の低下が起こり
、押出ペレット化が不能であり、かつ悪臭が発生した。Comparative Example 4 Example 1 was the same as Example 1 except that the radical generator was used in the proportions shown in Table 1, and the results are shown in Table 1. Extrusion pelletization was not possible and a bad odor was generated.
比較例5
実施例1において、イミド化合物を無水マレイン酸にか
えた以外は実施例1と同様とし、その結果を表1に示す
、無水マレイン酸がラジカル付加していることが確認さ
れたが、押出ペレット化の際に悪臭が発生した。また、
ガラス繊維との接着性が悪(実用物性も劣り、かつAl
およびEVOHとの剥離強度も低い。Comparative Example 5 The same procedure as Example 1 was carried out except that the imide compound in Example 1 was changed to maleic anhydride, and the results are shown in Table 1. It was confirmed that maleic anhydride was radically added. A foul odor was generated during extrusion pelletization. Also,
Poor adhesion with glass fiber (poor practical properties, and Al
And the peel strength with EVOH is also low.
比較例6
実施例1において、イミド化合物をグリシジルメタクリ
レ−ドロ三洋化成(株)製]にかえた以外は実施例1と
同様とし、その結果を表1に示す、グリシジルメタクリ
レートがラジカル付加していることが確認されたが、押
出ペレット化の際に悪臭が発生した。また、ガラス繊維
との接着性が悪く実用物性も劣り、かつAIおよびEV
○11との剥離強度も低い。Comparative Example 6 The procedure was the same as in Example 1 except that the imide compound in Example 1 was changed to glycidyl methacrylate (manufactured by Sanyo Chemical Co., Ltd.), and the results are shown in Table 1. However, a bad odor was generated during extrusion pelletization. In addition, it has poor adhesion with glass fibers, poor practical physical properties, and
The peel strength with ○11 is also low.
(発明の効果;
本発明の変性ポリオレフィン樹脂は、ガラス繊維、金属
、EV○Hとの接着性に優れるため、補強、積層の効果
が大きく、自動車分野、家電分野、工業部品などに使用
でき、その利用価値は大きい。(Effects of the invention: The modified polyolefin resin of the present invention has excellent adhesion to glass fibers, metals, and EV○H, so it has great reinforcing and laminating effects, and can be used in the automobile field, home appliance field, industrial parts, etc. Its utility value is great.
特許出願人 三井東圧化学株式会社 手続主甫正書 (自発) 平成3年5月λ日Patent applicant: Mitsui Toatsu Chemical Co., Ltd. Procedural master's letter (spontaneous) May 1991 λ day
Claims (1)
たは式(2)で示されるイミド化合物0.1〜20重量
▲数式、化学式、表等があります▼(1) ▲数式、化学式、表等があります▼(2) 部およびラジカル発生剤0.01〜10重量部を反応さ
せてなる変性ポリオレフィン樹脂。[Claims] 0.1 to 20 parts by weight of the imide compound represented by formula (1) or formula (2) per 100 parts by weight of the polyolefin resin ▲ There are mathematical formulas, chemical formulas, tables, etc. ▼ (1) ▲ Mathematical formula , chemical formula, table, etc. ▼ (2) A modified polyolefin resin obtained by reacting 0.01 to 10 parts by weight of a radical generator and 0.01 to 10 parts by weight of a radical generator.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16837590A JPH0457812A (en) | 1990-06-28 | 1990-06-28 | Modified polyolefin resin |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP16837590A JPH0457812A (en) | 1990-06-28 | 1990-06-28 | Modified polyolefin resin |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0457812A true JPH0457812A (en) | 1992-02-25 |
Family
ID=15866935
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP16837590A Pending JPH0457812A (en) | 1990-06-28 | 1990-06-28 | Modified polyolefin resin |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0457812A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006132442A1 (en) * | 2005-06-09 | 2006-12-14 | Chugai Seiyaku Kabushiki Kaisha | Vitamin d-like compound |
-
1990
- 1990-06-28 JP JP16837590A patent/JPH0457812A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006132442A1 (en) * | 2005-06-09 | 2006-12-14 | Chugai Seiyaku Kabushiki Kaisha | Vitamin d-like compound |
US7935688B2 (en) | 2005-06-09 | 2011-05-03 | Chugai Seiyaku Kabushiki Kaisha | Vitamin D-like compound |
JP5166872B2 (en) * | 2005-06-09 | 2013-03-21 | 中外製薬株式会社 | Vitamin D-like compound |
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