JPH01263139A - Polypropylene resin composition - Google Patents
Polypropylene resin compositionInfo
- Publication number
- JPH01263139A JPH01263139A JP9017288A JP9017288A JPH01263139A JP H01263139 A JPH01263139 A JP H01263139A JP 9017288 A JP9017288 A JP 9017288A JP 9017288 A JP9017288 A JP 9017288A JP H01263139 A JPH01263139 A JP H01263139A
- Authority
- JP
- Japan
- Prior art keywords
- resin composition
- polypropylene resin
- crystalline polypropylene
- polymer
- prepared
- 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.)
- Granted
Links
- -1 Polypropylene Polymers 0.000 title claims abstract description 22
- 229920001155 polypropylene Polymers 0.000 title claims abstract description 16
- 239000004743 Polypropylene Substances 0.000 title claims abstract description 15
- 239000011342 resin composition Substances 0.000 title claims abstract description 6
- 229920000642 polymer Polymers 0.000 claims abstract description 13
- OIWOHHBRDFKZNC-UHFFFAOYSA-N cyclohexyl 2-methylprop-2-enoate Chemical compound CC(=C)C(=O)OC1CCCCC1 OIWOHHBRDFKZNC-UHFFFAOYSA-N 0.000 claims abstract description 8
- 230000000379 polymerizing effect Effects 0.000 claims abstract description 5
- 239000003054 catalyst Substances 0.000 abstract description 19
- 150000001875 compounds Chemical class 0.000 abstract description 16
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 abstract description 8
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 abstract description 8
- XJDNKRIXUMDJCW-UHFFFAOYSA-J titanium tetrachloride Chemical compound Cl[Ti](Cl)(Cl)Cl XJDNKRIXUMDJCW-UHFFFAOYSA-J 0.000 abstract description 8
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 abstract description 6
- 230000000704 physical effect Effects 0.000 abstract description 6
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 abstract description 5
- 238000010539 anionic addition polymerization reaction Methods 0.000 abstract description 4
- 150000002148 esters Chemical class 0.000 abstract description 4
- 239000001257 hydrogen Substances 0.000 abstract description 4
- 229910052739 hydrogen Inorganic materials 0.000 abstract description 4
- YONPGGFAJWQGJC-UHFFFAOYSA-K titanium(iii) chloride Chemical compound Cl[Ti](Cl)Cl YONPGGFAJWQGJC-UHFFFAOYSA-K 0.000 abstract description 4
- 150000001336 alkenes Chemical class 0.000 abstract description 2
- 229920001400 block copolymer Polymers 0.000 abstract description 2
- 229920005604 random copolymer Polymers 0.000 abstract description 2
- 125000004435 hydrogen atom Chemical class [H]* 0.000 abstract 1
- 239000000126 substance Substances 0.000 abstract 1
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 17
- 238000000034 method Methods 0.000 description 11
- 238000006116 polymerization reaction Methods 0.000 description 9
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 6
- 229910052719 titanium Inorganic materials 0.000 description 6
- 239000010936 titanium Substances 0.000 description 6
- 229910052723 transition metal Inorganic materials 0.000 description 6
- 150000003624 transition metals Chemical class 0.000 description 6
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 description 5
- 239000002667 nucleating agent Substances 0.000 description 5
- 229920002776 polycyclohexyl methacrylate Polymers 0.000 description 5
- 239000000843 powder Substances 0.000 description 5
- 229910052782 aluminium Inorganic materials 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 239000002002 slurry Substances 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 238000000605 extraction Methods 0.000 description 3
- 229910001629 magnesium chloride Inorganic materials 0.000 description 3
- 150000002894 organic compounds Chemical class 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- CXWXQJXEFPUFDZ-UHFFFAOYSA-N tetralin Chemical compound C1=CC=C2CCCCC2=C1 CXWXQJXEFPUFDZ-UHFFFAOYSA-N 0.000 description 3
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 description 2
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 description 2
- 125000000217 alkyl group Chemical group 0.000 description 2
- 238000005452 bending Methods 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- YNLAOSYQHBDIKW-UHFFFAOYSA-M diethylaluminium chloride Chemical compound CC[Al](Cl)CC YNLAOSYQHBDIKW-UHFFFAOYSA-M 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000012299 nitrogen atmosphere Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- XEMRAKSQROQPBR-UHFFFAOYSA-N (trichloromethyl)benzene Chemical compound ClC(Cl)(Cl)C1=CC=CC=C1 XEMRAKSQROQPBR-UHFFFAOYSA-N 0.000 description 1
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 description 1
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- 239000007818 Grignard reagent Substances 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
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical compound CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 description 1
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 1
- 125000005234 alkyl aluminium group Chemical group 0.000 description 1
- 230000000740 bleeding effect Effects 0.000 description 1
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 1
- 229910052794 bromium Inorganic materials 0.000 description 1
- 238000012662 bulk polymerization Methods 0.000 description 1
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- CJZGTCYPCWQAJB-UHFFFAOYSA-L calcium stearate Chemical compound [Ca+2].CCCCCCCCCCCCCCCCCC([O-])=O.CCCCCCCCCCCCCCCCCC([O-])=O CJZGTCYPCWQAJB-UHFFFAOYSA-L 0.000 description 1
- 235000013539 calcium stearate Nutrition 0.000 description 1
- 239000008116 calcium stearate Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 150000002170 ethers Chemical class 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 description 1
- 238000012685 gas phase polymerization Methods 0.000 description 1
- 150000004795 grignard reagents Chemical class 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 150000004820 halides Chemical class 0.000 description 1
- 125000004051 hexyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- 229920001519 homopolymer Polymers 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000011630 iodine Substances 0.000 description 1
- 229910052740 iodine Inorganic materials 0.000 description 1
- 229920001580 isotactic polymer Polymers 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 229910052749 magnesium Inorganic materials 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- YCCXQARVHOPWFJ-UHFFFAOYSA-M magnesium;ethane;chloride Chemical compound [Mg+2].[Cl-].[CH2-]C YCCXQARVHOPWFJ-UHFFFAOYSA-M 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- QSSJZLPUHJDYKF-UHFFFAOYSA-N methyl 4-methylbenzoate Chemical compound COC(=O)C1=CC=C(C)C=C1 QSSJZLPUHJDYKF-UHFFFAOYSA-N 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 1
- 125000002370 organoaluminium group Chemical group 0.000 description 1
- 150000002905 orthoesters Chemical class 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 239000002685 polymerization catalyst Substances 0.000 description 1
- 125000001436 propyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])[H] 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000012552 review Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- VOITXYVAKOUIBA-UHFFFAOYSA-N triethylaluminium Chemical compound CC[Al](CC)CC VOITXYVAKOUIBA-UHFFFAOYSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Abstract
Description
【発明の詳細な説明】
〔卒業上の利用分野]
本発明は特定の化合物を含有してなる結晶性ポリプロピ
レン樹脂組成物に関する。DETAILED DESCRIPTION OF THE INVENTION [Graduation Field of Application] The present invention relates to a crystalline polypropylene resin composition containing a specific compound.
ポリプロピレンは剛性に優れた重合体であるが、比較的
成形物の結晶化度が低く本来期待される物性に比べ通常
の成形物の物性は劣るという問題がある。これに対して
は、通常種々の核剤を添加する方法が行われており、剛
性に優れた成形体、或いは透明性に優れた成形体が得ら
れている。Although polypropylene is a polymer with excellent rigidity, there is a problem in that the degree of crystallinity of molded products is relatively low, and the physical properties of ordinary molded products are inferior to the originally expected physical properties. To solve this problem, a method of adding various nucleating agents is usually used, and a molded product with excellent rigidity or transparency is obtained.
核剤を添加する方法は簡便でしかも効果的であるが、比
較的多量の核を添加する必要がありそのため、核剤の分
散不良による成形物の物性のばらつきとか、添加した核
剤がブリードする問題があった。これに対しては、特定
の高分子化合物を添加することが知られているが更に効
果的な化合物が望まれる。The method of adding a nucleating agent is simple and effective, but it requires the addition of a relatively large amount of nucleating agents, which may cause variations in the physical properties of the molded product due to poor dispersion of the nucleating agent, or bleeding of the added nucleating agent. There was a problem. For this purpose, it is known to add a specific polymer compound, but a more effective compound is desired.
本発明者らはより効果的な化合物について鋭意探索し本
発明に到達した。The present inventors have diligently searched for more effective compounds and have arrived at the present invention.
即ち、本発明は、シクロヘキシルメタクリレートをアニ
オン重合して得た重合体を含有してなる結晶性ポリプロ
ピレン樹脂組成物である。That is, the present invention is a crystalline polypropylene resin composition containing a polymer obtained by anionically polymerizing cyclohexyl methacrylate.
本発明において使用する、シクロヘキシルメタクリレー
トの重合体は種々のアニオン重合触媒で製造法可能であ
るが、通常グリニヤー試薬で比較的低温で重合して得た
重合体が好ましく利用でき、重合方法としては、メチル
メタクリレートのアイソタクチクボリマーを製造する方
法として公知の方法が好ましく採用される(例えば、P
olmer Journal、Vol、1797?−9
80(1985)、Polymer LettersV
ol、9129−13H1971)参照)。シクロへキ
シルメタクリレートの重合体の分子量としては特に制限
はないが、通常数平均分子量として1000以上100
0万以下のものを用いるのが一般的である。The cyclohexyl methacrylate polymer used in the present invention can be produced using various anionic polymerization catalysts, but a polymer obtained by polymerizing with a Grignard reagent at a relatively low temperature is preferably used, and the polymerization method is as follows: A known method is preferably adopted as a method for producing an isotactic polymer of methyl methacrylate (for example, P
Olmer Journal, Vol, 1797? -9
80 (1985), Polymer Letters V
ol, 9129-13H1971)). There is no particular restriction on the molecular weight of the cyclohexyl methacrylate polymer, but the number average molecular weight is usually 1000 or more and 100
It is common to use a value of 0,000 or less.
本発明において、使用する結晶性ポリプロピレンとして
は、プロピレンの単独重合体のみならず、エチレン等の
他のオレフィンとのランダム或いはブロック共重合体を
示し、通常、他のオレフィンの含四としては、50重量
%以下である。これらのプロピレンの重合体を製造する
方法については特に制限はなく通常遷移金属触媒と有機
アルミニウム化合物からなる触媒が利用できる。In the present invention, the crystalline polypropylene used includes not only a homopolymer of propylene but also a random or block copolymer with other olefins such as ethylene. % by weight or less. There are no particular restrictions on the method for producing these propylene polymers, and catalysts usually composed of a transition metal catalyst and an organoaluminum compound can be used.
遷移金属触媒と有機アルミニウム化合物からなる触媒に
ついては公知の種々の高立体規則性のポリプロピレンを
与える触媒系が例示でき、遷移金属触媒としてはハロゲ
ン化チタンが好ましく用いられ、例えば四塩化チタンを
金属アルミニウム、水素或いは有機アルミニウムで還元
して得た三塩化チタン又はそれらを電子供与性化合物で
変性処理したものと有機アルミニウム化合物さらに必要
に応じ含酸素有機化合物などの立体規則性同上剤からな
る触媒系、或いはハロゲン化マグネシウム等の担体或い
はそれらを電子供与性化合物で処理したものにハロゲン
化チタンを担持してえたM+i金属触媒と有機アルミニ
ウム化合物、必要に応じ含酸素有機化合物などの立体規
則性向上剤からなる触媒系が例示される。(例えば以下
の文献に種々の例が記載されている。 Ziegler
−Natta Catalysts and Poly
merization by John Boor J
r(Academic Press)+Journal
of Macromorecular Sience
−Reviews in Macromolecula
r Cbemistry and Physics C
24,(3)355−385<1984)、同C25(
1) 578−97 (198ここで立体規則性向上剤
、或いは電子供与性化合物としては通常エーテル、エス
テル、オルソエステル、アルコキシ硅素化合物などの含
酸素化合物が好ましく例示でき、電子供与性化合物とし
てはさらにアルコール、アルデヒド、水なども使用可能
である。Examples of catalysts consisting of a transition metal catalyst and an organoaluminum compound include various known catalyst systems that provide polypropylene with high stereoregularity.Titanium halides are preferably used as transition metal catalysts.For example, titanium tetrachloride is combined with metallic aluminum. , a catalyst system consisting of titanium trichloride obtained by reduction with hydrogen or organoaluminium, or a modified version thereof with an electron-donating compound, an organoaluminum compound, and, if necessary, a stereoregular agent such as an oxygen-containing organic compound; Alternatively, an M+i metal catalyst obtained by supporting titanium halide on a carrier such as magnesium halide or a carrier treated with an electron-donating compound, an organoaluminum compound, and if necessary a stereoregularity improver such as an oxygen-containing organic compound. The following catalyst system is exemplified. (For example, various examples are described in the following documents. Ziegler
-Natta Catalysts and Poly
Merization by John Boor J
r(Academic Press)+Journal
of Macrorecular Science
-Reviews in Macromolecules
r Cbemistry and Physics C
24, (3) 355-385 <1984), same C25 (
1) 578-97 (198 Here, as the stereoregularity improver or the electron-donating compound, oxygen-containing compounds such as ethers, esters, orthoesters, and alkoxy silicon compounds can be exemplified preferably, and as the electron-donating compounds, further Alcohol, aldehyde, water, etc. can also be used.
有機アルミニウム化合物としては、トリプルキルアルミ
ニウム、ジアルキルアルミニウムハライド、アルキルア
ルミニウムセスキハライド、アルキ/L/フルミニウム
ジハライドが使用でき、アルキル基としてはメチル基、
エチル基、プロピル基、ブチル基、ヘキシル基などが例
示され、ハライドとしては塩素、臭素、沃素が例示され
る。As the organoaluminum compound, triple kyl aluminum, dialkyl aluminum halide, alkyl aluminum sesquihalide, alkyl/L/fluminium dihalide can be used, and the alkyl group is a methyl group,
Examples include ethyl group, propyl group, butyl group, hexyl group, etc., and examples of halides include chlorine, bromine, and iodine.
好ましいハロゲン化チタンとしては、アルミニウム、或
いは有機アルミニウムで四塩化チタンをエーテル、或い
はエステルで変性処理して得たもの、或いは塩化マグネ
シウムと有機化合物の共粉砕したものを四塩化チタンで
処理したもの、或いは塩化マグネシウムとアルコールの
反応物を炭化水素溶媒中に溶解し、ついで四塩化チタン
などの沈澱剤で処理することで炭化水素溶媒に不溶化し
、必要に応じエステル、エーテルなどの電子供与性の化
合物で処理しついで四塩化チタンで処理する方法などに
よって得られる担持したチタンのノ10ゲン化物である
。Preferred titanium halides include those obtained by modifying titanium tetrachloride with aluminum or organic aluminum with ether or ester, or those obtained by co-pulverizing magnesium chloride and an organic compound with titanium tetrachloride. Alternatively, the reaction product of magnesium chloride and alcohol is dissolved in a hydrocarbon solvent, and then treated with a precipitant such as titanium tetrachloride to make it insoluble in the hydrocarbon solvent, and if necessary, an electron-donating compound such as an ester or ether is added. It is a supported titanium oxide obtained by a method of treating with titanium and titanium tetrachloride.
本発明においてプロピレンの重合はペンタン、ヘキサン
、ヘプタン、オクタン、ベンゼン、トルエン等の不活性
媒体中で行うことも、或いはプロピレン自身を液状媒体
とする塊状重合法、或いは実質的に液状媒体の存在しな
い気相重合法で行うこともでき、その方法については特
に制限はなく公知の種々の方法、条件が採用される。例
えば、重合温度としては常温〜100°C1重合圧力と
しては常圧〜50Kg/cmzゲージで行なうのが一般
的である。In the present invention, the polymerization of propylene can be carried out in an inert medium such as pentane, hexane, heptane, octane, benzene, toluene, etc., or by a bulk polymerization method using propylene itself as a liquid medium, or by a method in which there is substantially no liquid medium. It can also be carried out by a gas phase polymerization method, and there are no particular limitations on the method, and various known methods and conditions can be employed. For example, the polymerization temperature is generally from normal temperature to 100° C., and the polymerization pressure is generally from normal pressure to 50 kg/cmz gauge.
本発明においてシクロへキシルメタクリレートをアニオ
ン重合によって重合して得た重合体とポリプロピレンの
量比としては、シクロへキシルメタクリレートの重合体
がO,OLwtppm以上であり、好ましくは、0.1
wLppm〜1000w100O程度である。In the present invention, the quantitative ratio of the polymer obtained by polymerizing cyclohexyl methacrylate by anionic polymerization to polypropylene is such that the polymer of cyclohexyl methacrylate has an O,OLwtppm or more, and preferably 0.1
It is about wLppm to 1000w100O.
0、O1wtppm以下では物性改良の効果がなく、ま
た10、OOwtppm以上いれても格別効果的ではな
い。If the amount is less than 0.01 wtppm, there is no effect of improving the physical properties, and if it is more than 10.00 wtppm, it is not particularly effective.
以下に実施を挙げ本発明をさらに説明する。 The present invention will be further explained by referring to the following examples.
実施例1
直径121の鋼球9Kgの入った内容積41の粉砕用ポ
ットを4個装備した振動ミルを用意する。各ボットに窒
素雰囲気下で塩化マグネシウム300g、テトラエトキ
シシラン60m1、α、α、α−トリクロロトルエン4
5m1を加え40時間粉砕した。こうして得た共粉砕物
300gを51のフラスコに入れ四塩化チタン1.51
、トルエン1.51を加え100°Cで30分間撹拌処
理し次いで上澄液を除き同様に四塩化チタン1.51、
トルエン1.51を加え100°Cで30分間撹拌処理
し次いで上澄液を除去し固形分をn−ヘキサンで繰り返
し洗浄して遷移金属触媒スラリーを得た。一部をサンプ
リングしチタン分を分析したところ1.9讐tχであっ
た。Example 1 A vibratory mill equipped with four grinding pots each having an internal volume of 41 and containing 9 kg of steel balls each having a diameter of 121 was prepared. Add 300 g of magnesium chloride, 60 ml of tetraethoxysilane, 4 ml of α, α, α-trichlorotoluene to each bottle under nitrogen atmosphere.
5ml was added and pulverized for 40 hours. 300 g of the co-pulverized material obtained in this way was put into a 51 flask, and 1.51 g of titanium tetrachloride was added.
, 1.51% of toluene was added, stirred at 100°C for 30 minutes, the supernatant was removed, and 1.51% of titanium tetrachloride was added,
1.51 g of toluene was added and stirred at 100° C. for 30 minutes, then the supernatant was removed and the solid content was repeatedly washed with n-hexane to obtain a transition metal catalyst slurry. When we sampled a portion and analyzed the titanium content, it was found to be 1.9%.
内容積200m l フラスコに窒素雰囲気下トルエン
40m1、上記遷移金属触媒20mg、ジエチルアルミ
ニウムクロライド0.12hl 、、p−トルイル酸メ
チル0゜06m1、トリエチルアルミニウム0.12m
1加えて触媒スラリーとした。この触媒スラリーを内容
積51のオートクレーブに入れプロピレン1.8kg
、水素3゜3N+を加え75°Cで2時間重合反応をお
こなった。Inner volume 200 ml flask under nitrogen atmosphere 40 ml of toluene, 20 mg of the above transition metal catalyst, 0.12 hl of diethylaluminium chloride, 0.06 ml of methyl p-toluate, 0.12 m of triethyl aluminum
1 was added to prepare a catalyst slurry. This catalyst slurry was placed in an autoclave with an internal volume of 51 kg, and 1.8 kg of propylene was added.
, 3°3N+ of hydrogen was added, and a polymerization reaction was carried out at 75°C for 2 hours.
重合反応の後未反応のプロピレンをパージし取りだした
重合体は80°Cs 60mml(gで12時間乾燥し
た。After the polymerization reaction, unreacted propylene was purged and the polymer was taken out and dried at 80° C. at 60 mml (g) for 12 hours.
380gのパウダーが得られ135°Cのテトラリン溶
液で測定した極限粘度(以下ηと略記する。)及び沸騰
ローへブタンで6時間ソックスレー抽出器で抽出した時
の抽出残率(以下Uと略記、抽出後パウダー重量/抽出
前パウダー重量を100分率で表示)を測定した。380 g of powder was obtained, and the intrinsic viscosity (hereinafter abbreviated as η) measured with a tetralin solution at 135 ° C and the extraction residual rate (hereinafter abbreviated as U, Powder weight after extraction/powder weight before extraction (expressed as a 100% ratio) was measured.
触媒としてエチルマグネシウムクロリドを用い、トルエ
ン溶媒中、触媒濃度0.1mol/1 、モノマー濃度
2mo+/1で一78°Cで12時間重合してポリシク
ロへキシルメタクリレートを得た(変化率92χ、トル
エン溶媒中、30℃の極限粘度は0.18であった。ポ
リプロピレンパウダーに上記反応で得たポリシクロへキ
シルメタクリレート10/10000.フェノール系の
安定剤10/ 10000重量比、及びステアリン酸カ
ルシウムを15/10000重量比加え追立しメルトフ
ローインデックスを測定しさらに厚さ11mmのインジ
ェクションシートを作り、曲げ剛性度を測定した。Using ethylmagnesium chloride as a catalyst, polymerization was carried out at -78°C for 12 hours in a toluene solvent at a catalyst concentration of 0.1 mol/1 and a monomer concentration of 2 mo+/1 to obtain polycyclohexyl methacrylate (change rate 92χ, toluene solvent The intrinsic viscosity at 30°C was 0.18. Polypropylene powder was mixed with polycyclohexyl methacrylate obtained in the above reaction at a weight ratio of 10/10,000, a phenolic stabilizer at a weight ratio of 10/10,000, and calcium stearate at a weight ratio of 15/10,000. In addition, the melt flow index was measured, and an injection sheet with a thickness of 11 mm was prepared, and the bending rigidity was measured.
メルト7u−インデックス (Ml) AST
M 01238(230℃)曲げ剛性度 A
STM 0747−63(20°C)又示差熱分析装置
を用いlOo(/winで昇温或いは降温することで融
点及び結晶か温度を最大ピーク温度として測定した結果
は表に示す。Melt 7u-index (Ml) AST
M 01238 (230℃) Bending rigidity A
STM 0747-63 (20° C.) Using a differential thermal analyzer, the melting point and crystal temperature were measured as the maximum peak temperature by raising or lowering the temperature by lOo (/win). The results are shown in the table.
比較例1
シンジオタクチックポリシクロへキシルメタクリレート
を用いなっかった他は実施例1と同様にした結果は表に
示す。Comparative Example 1 Example 1 was repeated except that syndiotactic polycyclohexyl methacrylate was not used. The results are shown in the table.
実施例2
市販の高活性三塩化チタン(東邦チタニウム類TACS
−21)を遷移金属触媒として用いた。三塩化チタン触
媒100mg 、ジエチルアルミニウムクロライド1.
0mlをトルエン中で混合し、次いで該スラリーを内容
積51のオートクレーブに入れ、プロピレン1.8kg
、水素4.4NI 、を加え75°Cで4時間重合を
行いポリプロピレン920gを得た。このプロピレンを
プロピレンオキシドlhlの存在下100 ”Cで1時
間処理した後、ポリプロピレンパウダーを取り出した。Example 2 Commercially available highly active titanium trichloride (Toho Titanium TACS)
-21) was used as a transition metal catalyst. Titanium trichloride catalyst 100mg, diethylaluminum chloride 1.
0 ml in toluene, then the slurry was placed in an autoclave with an internal volume of 51, and 1.8 kg of propylene was added.
, 4.4 NI of hydrogen were added, and polymerization was carried out at 75°C for 4 hours to obtain 920 g of polypropylene. This propylene was treated at 100''C for 1 hour in the presence of propylene oxide lhl, and then the polypropylene powder was taken out.
このポリプロピレンを用い実施例1で得たポリシクロへ
キシルメタクリレートを30wtppm用いた他は実施
例1と同様に評価した。Evaluation was carried out in the same manner as in Example 1, except that this polypropylene was used and 30 wtppm of polycyclohexyl methacrylate obtained in Example 1 was used.
比較例2
ポリシクロへキシルメタクリレートを用(1な力・つた
他は実施例2と同様にした結果は表に示す。Comparative Example 2 Using polycyclohexyl methacrylate (1) The same procedure as in Example 2 was performed except for the strength and strength. The results are shown in the table.
本発明の組成物は極めて物性に優れており工業的に価値
がある。The composition of the present invention has extremely excellent physical properties and is of industrial value.
Claims (1)
て得た重合体を含有してなる結晶性ポリプロピレン樹脂
組成物。(1) A crystalline polypropylene resin composition containing a polymer obtained by anionically polymerizing cyclohexyl methacrylate.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9017288A JP2713577B2 (en) | 1988-04-14 | 1988-04-14 | Polypropylene resin composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP9017288A JP2713577B2 (en) | 1988-04-14 | 1988-04-14 | Polypropylene resin composition |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01263139A true JPH01263139A (en) | 1989-10-19 |
JP2713577B2 JP2713577B2 (en) | 1998-02-16 |
Family
ID=13991071
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP9017288A Expired - Lifetime JP2713577B2 (en) | 1988-04-14 | 1988-04-14 | Polypropylene resin composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2713577B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004196990A (en) * | 2002-12-19 | 2004-07-15 | Mitsubishi Rayon Co Ltd | Thermoplastic resin composition |
WO2011096596A3 (en) * | 2010-04-27 | 2011-10-20 | 三菱レイヨン株式会社 | Dispersant for additive for polyolefin resin, polyolefin resin composition, and molded article |
-
1988
- 1988-04-14 JP JP9017288A patent/JP2713577B2/en not_active Expired - Lifetime
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2004196990A (en) * | 2002-12-19 | 2004-07-15 | Mitsubishi Rayon Co Ltd | Thermoplastic resin composition |
WO2011096596A3 (en) * | 2010-04-27 | 2011-10-20 | 三菱レイヨン株式会社 | Dispersant for additive for polyolefin resin, polyolefin resin composition, and molded article |
JP5794146B2 (en) * | 2010-04-27 | 2015-10-14 | 三菱レイヨン株式会社 | Dispersant for polyolefin resin additive, polyolefin resin composition and molded article |
Also Published As
Publication number | Publication date |
---|---|
JP2713577B2 (en) | 1998-02-16 |
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