JPS6211748A - Resin composition - Google Patents
Resin compositionInfo
- Publication number
- JPS6211748A JPS6211748A JP15008985A JP15008985A JPS6211748A JP S6211748 A JPS6211748 A JP S6211748A JP 15008985 A JP15008985 A JP 15008985A JP 15008985 A JP15008985 A JP 15008985A JP S6211748 A JPS6211748 A JP S6211748A
- Authority
- JP
- Japan
- Prior art keywords
- ethylene
- vinyl alcohol
- alcohol copolymer
- resin
- 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.)
- Pending
Links
- 239000011342 resin composition Substances 0.000 title claims abstract description 20
- 229920000219 Ethylene vinyl alcohol Polymers 0.000 claims abstract description 63
- 229920005989 resin Polymers 0.000 claims abstract description 44
- 239000011347 resin Substances 0.000 claims abstract description 44
- 239000000203 mixture Substances 0.000 claims abstract description 37
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims abstract description 23
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims abstract description 23
- 229910000000 metal hydroxide Inorganic materials 0.000 claims abstract description 14
- 150000004692 metal hydroxides Chemical class 0.000 claims description 13
- 239000002131 composite material Substances 0.000 claims description 12
- 229920001577 copolymer Polymers 0.000 abstract description 15
- 238000000465 moulding Methods 0.000 abstract description 11
- -1 compound metal hydroxide Chemical class 0.000 abstract description 8
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 abstract description 5
- 239000005977 Ethylene Substances 0.000 abstract description 5
- 238000007127 saponification reaction Methods 0.000 abstract description 4
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 abstract description 3
- 239000000470 constituent Substances 0.000 abstract description 2
- 230000000694 effects Effects 0.000 abstract description 2
- 239000005038 ethylene vinyl acetate Substances 0.000 abstract description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 abstract description 2
- 238000013329 compounding Methods 0.000 abstract 2
- 230000015556 catabolic process Effects 0.000 abstract 1
- 238000006731 degradation reaction Methods 0.000 abstract 1
- 230000008021 deposition Effects 0.000 abstract 1
- 239000004715 ethylene vinyl alcohol Substances 0.000 description 24
- 239000010410 layer Substances 0.000 description 16
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 13
- 230000006866 deterioration Effects 0.000 description 12
- 239000000047 product Substances 0.000 description 11
- 239000004743 Polypropylene Substances 0.000 description 10
- 239000004840 adhesive resin Substances 0.000 description 9
- 229920006223 adhesive resin Polymers 0.000 description 9
- 238000001125 extrusion Methods 0.000 description 9
- 238000010521 absorption reaction Methods 0.000 description 5
- 239000003054 catalyst Substances 0.000 description 5
- GDVKFRBCXAPAQJ-UHFFFAOYSA-A dialuminum;hexamagnesium;carbonate;hexadecahydroxide Chemical compound [OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[OH-].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Mg+2].[Al+3].[Al+3].[O-]C([O-])=O GDVKFRBCXAPAQJ-UHFFFAOYSA-A 0.000 description 5
- 229910001701 hydrotalcite Inorganic materials 0.000 description 5
- 229960001545 hydrotalcite Drugs 0.000 description 5
- 238000002156 mixing Methods 0.000 description 5
- 229920005992 thermoplastic resin Polymers 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 238000004806 packaging method and process Methods 0.000 description 4
- 229910010067 TiC2 Inorganic materials 0.000 description 3
- 239000006227 byproduct Substances 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 238000004132 cross linking Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 230000000873 masking effect Effects 0.000 description 3
- 239000008188 pellet Substances 0.000 description 3
- 230000035699 permeability Effects 0.000 description 3
- 229920001155 polypropylene Polymers 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 230000004888 barrier function Effects 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 238000000071 blow moulding Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 239000000796 flavoring agent Substances 0.000 description 2
- 235000019634 flavors Nutrition 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229910021645 metal ion Inorganic materials 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 238000005453 pelletization Methods 0.000 description 2
- 230000007017 scission Effects 0.000 description 2
- 239000002356 single layer Substances 0.000 description 2
- 239000002344 surface layer Substances 0.000 description 2
- GLXYOFXNKBTMQL-YKCHQESGSA-N (2S)-2-[[(2S)-2-[[(2S)-2-[[(2S)-1-[(2S)-6-amino-2-[[(2S)-4-amino-2-[[(2S)-2-[[(2S)-2-[[2-[[(2S)-1-[(2S)-6-amino-2-[[(2S,3S)-2-[[(2S)-2-[[(2S)-2-[[(2S)-2-amino-4-methylsulfanylbutanoyl]amino]-3-methylbutanoyl]amino]-5-(diaminomethylideneamino)pentanoyl]amino]-3-methylpentanoyl]amino]hexanoyl]pyrrolidine-2-carbonyl]amino]acetyl]amino]-3-hydroxypropanoyl]amino]propanoyl]amino]-4-oxobutanoyl]amino]hexanoyl]pyrrolidine-2-carbonyl]amino]-3-hydroxypropanoyl]amino]-3-carboxypropanoyl]amino]butanedioic acid Chemical compound CSCC[C@H](N)C(=O)N[C@@H](C(C)C)C(=O)N[C@@H](CCCNC(N)=N)C(=O)N[C@@H]([C@@H](C)CC)C(=O)N[C@@H](CCCCN)C(=O)N1CCC[C@H]1C(=O)NCC(=O)N[C@@H](CO)C(=O)N[C@@H](C)C(=O)N[C@@H](CC(N)=O)C(=O)N[C@@H](CCCCN)C(=O)N1[C@H](C(=O)N[C@@H](CO)C(=O)N[C@@H](CC(O)=O)C(=O)N[C@@H](CC(O)=O)C(O)=O)CCC1 GLXYOFXNKBTMQL-YKCHQESGSA-N 0.000 description 1
- 241000251468 Actinopterygii Species 0.000 description 1
- 229920000089 Cyclic olefin copolymer Polymers 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 244000089486 Phragmites australis subsp australis Species 0.000 description 1
- 235000014676 Phragmites communis Nutrition 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 241000270708 Testudinidae Species 0.000 description 1
- 229910010061 TiC13 Inorganic materials 0.000 description 1
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 150000008065 acid anhydrides Chemical class 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 125000005234 alkyl aluminium group Chemical group 0.000 description 1
- 229910002065 alloy metal Inorganic materials 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 230000008901 benefit Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 238000010504 bond cleavage reaction Methods 0.000 description 1
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 1
- 150000007942 carboxylates Chemical class 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 238000003776 cleavage reaction Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 239000000039 congener Substances 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000007334 copolymerization reaction Methods 0.000 description 1
- 238000005520 cutting process Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000002845 discoloration Methods 0.000 description 1
- 150000002148 esters Chemical class 0.000 description 1
- 229920006242 ethylene acrylic acid copolymer Polymers 0.000 description 1
- 229920001112 grafted polyolefin Polymers 0.000 description 1
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 description 1
- 229920001903 high density polyethylene Polymers 0.000 description 1
- 239000004700 high-density polyethylene Substances 0.000 description 1
- 230000001771 impaired effect Effects 0.000 description 1
- 229920000554 ionomer Polymers 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 229920000092 linear low density polyethylene Polymers 0.000 description 1
- 239000004707 linear low-density polyethylene Substances 0.000 description 1
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 1
- 229920001912 maleic anhydride grafted polyethylene Polymers 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
- 239000012046 mixed solvent Substances 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000002685 polymerization catalyst Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000004080 punching Methods 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 238000005201 scrubbing Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 238000010186 staining Methods 0.000 description 1
- 229920003002 synthetic resin Polymers 0.000 description 1
- 239000000057 synthetic resin Substances 0.000 description 1
- 239000010936 titanium Substances 0.000 description 1
- OGIDPMRJRNCKJF-UHFFFAOYSA-N titanium oxide Inorganic materials [Ti]=O OGIDPMRJRNCKJF-UHFFFAOYSA-N 0.000 description 1
- YONPGGFAJWQGJC-UHFFFAOYSA-K titanium(iii) chloride Chemical compound Cl[Ti](Cl)Cl YONPGGFAJWQGJC-UHFFFAOYSA-K 0.000 description 1
- 238000007666 vacuum forming Methods 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 230000000007 visual effect Effects 0.000 description 1
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
発明の利用分野
本発明は、プロピレン系樹脂及びエチレン−ビニルアル
コール共重合体を含有する樹脂組成物に関し、よシ詳細
には成形に際しエチレン−ビニ化アルコール共重合体の
劣化が有効に抑制された上記樹脂組成物に関する。DETAILED DESCRIPTION OF THE INVENTION Field of Application of the Invention The present invention relates to a resin composition containing a propylene resin and an ethylene-vinyl alcohol copolymer. The present invention relates to the above resin composition whose deterioration is effectively suppressed.
従来技術
エチレン−ビニルアルコール共重合体ハ、種々の樹脂の
内でも、酸素等の気体に対する耐透過性に最も優れた樹
脂の一つであシ、この特性を利用して、カトル、カップ
等の包装容器やフィルム等の分野に広く使用されている
。PRIOR ART Ethylene-vinyl alcohol copolymer is one of the resins that has the best permeability to gases such as oxygen among various resins.Using this property, it can be used to make cuttle, cup, etc. Widely used in fields such as packaging containers and films.
とのエチレン−ビニルアルコール共重合体は、湿度に対
して敏感であり、例えば100 S RHのような高湿
度Φ件下には、酸素の透過係数が約−桁大きい値となる
欠点を有する。この欠点を改善する目的で、エチレン−
ビニルアルコール共重合体を、Iリエチレン、ポリプロ
ピレン等の水蒸気や水に対する耐透過性に優れた低吸水
性樹脂とブレンドされて使用するか、或いは該共重合体
を含有するガスバリヤ一層を前記吸水性樹脂の内外表面
層でサンドイッチさせた積層構造とし、エチレン−ビニ
ルアルコール共重合体への湿度の影響を小さくする手法
が広く採用されている。The ethylene-vinyl alcohol copolymer is sensitive to humidity, and has the disadvantage that the oxygen permeability coefficient becomes about an order of magnitude larger under high humidity conditions such as 100 S RH. In order to improve this drawback, ethylene-
The vinyl alcohol copolymer is used in a blend with a low water absorbency resin that has excellent permeability to water vapor and water, such as polyethylene or polypropylene, or a gas barrier layer containing the copolymer is used with the water absorbent resin. A widely used method is to create a laminated structure sandwiched between inner and outer surface layers of ethylene-vinyl alcohol copolymer to reduce the influence of humidity on the ethylene-vinyl alcohol copolymer.
而してかような組成物乃至は積層構造物から包装容器を
製造する場合、特に前述した低吸水性樹脂の内でもプロ
ピレン系樹脂を用いた時にはエチレン−ビニルアルコー
ル共重合体が劣化する傾向にあシ、押出機内部における
黒色状付着物(焦げ)等発生式いは押出に際してダイリ
ップなどに付着するでル状物質(メヤニ)等が生じ、ま
たこれによシ成形品の外観特性や機械的特性が著しく損
われるという問題を生ずる。Therefore, when manufacturing packaging containers from such compositions or laminated structures, the ethylene-vinyl alcohol copolymer tends to deteriorate, especially when propylene resins are used among the low water absorbency resins mentioned above. Reeds, black-like deposits (scorch), etc. occur inside the extruder, or stick to the die lip during extrusion, resulting in the formation of stick-like substances (stick), which may also affect the appearance characteristics and mechanical properties of the molded product. A problem arises in that the characteristics are significantly impaired.
また前述した組成物乃至は積層構造物から包装容器を製
造する際、?トル等のプロー成形ではピンチオフによる
パリ、またカツグ成形の場合には打抜きクズ等のリグラ
インドが必然的に発生し、その再利用が省資源の見地か
ら必要となる。このリグラインド等のスクラップ組成物
はプロピレン系樹脂等の低吸水性樹脂とエチレン−ビニ
ルアルコール共重合体等を含有するブレンド物から成っ
ている。Also, when manufacturing a packaging container from the above-mentioned composition or laminated structure? In the case of blow molding such as a tortoise molding, cracks due to pinch-off inevitably occur, and in the case of cut molding, regrinding of punching scraps, etc. inevitably occurs, and their reuse is necessary from the standpoint of resource conservation. This scrap composition such as regrind is made of a blend containing a low water absorption resin such as a propylene resin and an ethylene-vinyl alcohol copolymer.
このスクラップ組成物中にプロピレン系樹脂が含まれて
いる場合、該組成物を容器の成形等に再利用すると、上
述したエチレン−ビニルアルコール共重合体の劣化傾向
は一層顕著なものとなシ、かくしてこれらスクラップ組
成物の再利用が阻まれている。If this scrap composition contains a propylene resin, the above-mentioned tendency of deterioration of the ethylene-vinyl alcohol copolymer will become even more pronounced if the composition is reused for molding containers, etc. The reuse of these scrap compositions is thus hampered.
発明の目的
従って本発明の目的は、上述した従来の欠点が解消され
たプロピレン系樹脂及びエチレン−ビニルアルコール共
重合体を含有する樹脂組成物を提供するにある。OBJECTS OF THE INVENTION Accordingly, an object of the present invention is to provide a resin composition containing a propylene resin and an ethylene-vinyl alcohol copolymer, which eliminates the above-mentioned conventional drawbacks.
本発明の他の目的は、成形に際して副生ずるプロピレン
系樹脂及びエチレン−ビニルアルコール共重合体のブレ
ンド物のりグラインド等のスクラ、グ組成物を有効に再
利用することが可能な樹脂組成物を提供することにある
。Another object of the present invention is to provide a resin composition capable of effectively reusing a scrubbing composition of a blend of a propylene resin and an ethylene-vinyl alcohol copolymer produced as a by-product during molding. It's about doing.
発明の構成
本発明によれば、プロピレン系樹脂、エチレン−ビニル
アルコール共重合体及びハイドロタルサイト型複合金属
水酸化物を含有して成ることを特徴とする樹脂組成物が
提供される。According to the present invention, there is provided a resin composition characterized by containing a propylene resin, an ethylene-vinyl alcohol copolymer, and a hydrotalcite type composite metal hydroxide.
発明の好適態様
本発明において重要な特徴は、プロピレン系樹脂及びエ
チレン−ビニルアルコール共重合体を含有するブレンド
物中に、ハイドロタルサイト型機、合金属水酸化物を配
合することにある。Preferred Embodiments of the Invention An important feature of the present invention is that a hydrotalcite type compound and an alloy metal hydroxide are blended into a blend containing a propylene resin and an ethylene-vinyl alcohol copolymer.
前述した様に、プロピレン系樹脂とエチレン−ビニルア
ルコール共重合体を含有するブレンド物を容器等の成形
に賦すると、エチレン−ビニルアルコール共重合体が劣
化し、混線溶融押出に際してスクリューなどへの黒色状
付着物(焦げ)、rル状物質(メヤニ)等の不都合を生
じるとともに、これによシ着色等による成形品の外観特
性の低下、樹脂分解物の匂い等によるフレーバー低下、
耐衝撃性等の機械的特性の低下等がもたらされるのであ
る。As mentioned above, when a blend containing a propylene resin and an ethylene-vinyl alcohol copolymer is applied to mold a container, etc., the ethylene-vinyl alcohol copolymer deteriorates, causing black color to the screw etc. during cross-wire melt extrusion. In addition to causing inconveniences such as scorched matter (scorch) and sludge, this also reduces the appearance characteristics of the molded product due to discoloration, etc., and reduces flavor due to the smell of resin decomposition products.
This results in a decrease in mechanical properties such as impact resistance.
本発明者等の研究によれば、この様なエチレン−ビニル
アルコール共重合体の劣化は、プロピレン系樹脂中に触
媒残渣として含まれている三塩化チタン(TiCts)
やその反応残留物等による架橋反応或いは分子切断など
が主原因であろうと推測される。According to research by the present inventors, such deterioration of ethylene-vinyl alcohol copolymer is caused by titanium trichloride (TiCts), which is contained as a catalyst residue in propylene resin.
It is assumed that the main cause is cross-linking reaction or molecular cleavage due to the reaction residues and the like.
即ちプロピレンの重合触媒としては一般にチーグラー・
ナツタ触媒(Tict3. At(CH3)、などのア
ルキルアルミニウム)が使用されているがプロピレン系
樹脂中には、このT I CL、或いはその反応物が触
媒残渣として微量ながら含まれておシ、押出等に際して
溶融温度に付されているエチレン−ビニルアルコール共
重合体と共存するために、該共重合体の架橋反応や分子
切断などが促進され、所謂劣化が進行するものと考えら
れる。In other words, as a propylene polymerization catalyst, Ziegler-
Natsuta catalyst (Alkylaluminum such as Tict3. At(CH3), etc.) is used, but the propylene resin contains a small amount of T I CL or its reactant as a catalyst residue. It is thought that because it coexists with the ethylene-vinyl alcohol copolymer that has been exposed to the melting temperature during this process, crosslinking reactions and molecular scission of the copolymer are promoted, resulting in so-called deterioration.
側光ば、エチレン−ビニルアルコール共重合体に、Ti
ct、 (1100pp )t ’rio□(l fb
) 。Side light, ethylene-vinyl alcohol copolymer, Ti
ct, (1100pp)t'rio□(l fb
).
At20. (1% )をそれぞれ添加して260℃に
加熱した時のメルト70−レート(260℃。At20. (1%) respectively and heated to 260°C. Melt 70-rate (260°C.
2160g)の経時変化を第1図に示す。この線図によ
れば、TiO□(曲線B)及びAt20. (曲線C)
を添加したものは、エチレン−ビニルアルコール共重合
体単独(曲線D)のものと、その経時変化が殆んど変ら
ないのに対し、TiC2,(曲線A)を添加したものは
、その添加量がTiC2等に比して著しく少ないにもか
かわらず、メルトインデックスの低下が顕著であること
が理解されよう。2160g) is shown in Fig. 1. According to this diagram, TiO□ (curve B) and At20. (Curve C)
The change over time of the one to which TiC2, (curve A) was added was almost the same as that of the ethylene-vinyl alcohol copolymer alone (curve D), whereas the amount added to TiC2, (curve A) It will be understood that the decrease in melt index is remarkable even though the amount is significantly lower than that of TiC2 and the like.
またリグラインド等のスクラップ組成物は、既に溶融押
出等の苛酷な作業に付されたものであるタメ、該組成物
中のエチレン−ビニルアルコール共重合体は既に劣化が
進行している。従ってこのスクラップ組成物を容器の成
形等に再利用した時には、上記触媒残渣である’r t
ct3等の作用によって、エチレン−ビニルアルコー
ル共重合体の劣化が急速に進行するものと思われる。In addition, scrap compositions such as regrind have already been subjected to severe operations such as melt extrusion, and the ethylene-vinyl alcohol copolymer in the composition has already deteriorated. Therefore, when this scrap composition is reused for molding containers, etc., the catalyst residue 'r t
It is thought that the deterioration of the ethylene-vinyl alcohol copolymer progresses rapidly due to the action of ct3 and the like.
本発明においては、この様なエチレン−ビニルアルコー
ル共重合体の熱劣化をハイドロタルサイト型複合金属水
酸化物を配合することによって防止するものである。In the present invention, such thermal deterioration of the ethylene-vinyl alcohol copolymer is prevented by blending a hydrotalcite type composite metal hydroxide.
このハイドロタルサイト型複合金属水酸化物は、一般式
、
y12 +、y1″F(OH)2X+33F−2Z(A
2つ、・aH20−・・・・−(1)式中、M2+はM
g等の2価金属イオン、M3+はAt等の3価金属イオ
ン、
を満足する正数であシ、
である。This hydrotalcite type composite metal hydroxide has the general formula, y12 +, y1″F(OH)2X+33F-2Z(A
2,・aH20−・・・・−(1) In the formula, M2+ is M
A divalent metal ion such as g, M3+ is a trivalent metal ion such as At, and a positive number satisfying the following.
によって示される。Indicated by
これらの複合金属水酸化物の内、式
%式%(2)
で表わされる化合物は、ハイドロタルサイトどして知ら
れる天然鉱物であり、この鉱物及び同族類は、協和化学
工業株式会社の出願に係る特公昭47−32198号、
48−29477号及び48−2947紛公報記載の方
法等によシ合成されるものである。Among these composite metal hydroxides, the compound represented by the formula % (2) is a natural mineral known as hydrotalcite, and this mineral and its congeners are disclosed in the application filed by Kyowa Chemical Industry Co., Ltd. Special Publication No. 47-32198,
It is synthesized by the method described in No. 48-29477 and No. 48-2947.
本発明では、これらのハイドロタルサイト型複合金属水
酸化物の内でも、特に式
%式%(3)
で表わされる水酸化物が好適である。In the present invention, among these hydrotalcite-type composite metal hydroxides, the hydroxide represented by the formula % (3) is particularly suitable.
上述したハイドロタルサイト型複合金属水酸化物は、塩
素イオンの捕捉機能に優れておシ、本発明ではこれを利
用してプロピレン系樹脂中に含まれるT i C13の
マスキングを行ない、エチレン−ビニルアルコール共重
合体の架橋等による劣化を防止するものである。The above-mentioned hydrotalcite-type composite metal hydroxide has an excellent ability to capture chlorine ions, and in the present invention, it is used to mask T i C13 contained in propylene resin, and to mask TiC13 contained in propylene resin. This prevents deterioration due to crosslinking of the alcohol copolymer.
このハイドロタルサイト型複合金属水酸化物によるマス
キングの機能は、(3)式で表わされる化合物を例にと
れば、例えば次式で示される。Taking the compound represented by formula (3) as an example, the masking function of this hydrotalcite-type composite metal hydroxide is shown by the following formula, for example.
Mg 4.s At2(OH) 1.Co、・3.5H
20+2HC2→Mg4.5AL2(OH)13C2z
+4.5HzO+CO2−−(’)本発明においてかか
るハイドロタルサイト型複合金属水酸化物は、プロピレ
ン系樹脂とエチレン−ビニルアルコール共重合体との合
計量当たシ10−5乃至5重量%、特に10 乃至1
重量−の量で含有される。Mg4. s At2(OH) 1. Co, 3.5H
20+2HC2→Mg4.5AL2(OH)13C2z
+4.5HzO+CO2--(') In the present invention, the hydrotalcite-type composite metal hydroxide contains 10-5 to 5% by weight, especially 10 to 1
It is contained in an amount of - by weight.
上記範囲よシも少量の場合には所望のマスキング効果が
達成されないためエチレン−ビニル7/l/コール共重
合体の劣化が防止し得す、また多量に使用した場合には
、押出特性や成形品の機械的特性或いは成形品のフレー
バなどに悪影響を及ばず。If the amount exceeds the above range, the desired masking effect will not be achieved and deterioration of the ethylene-vinyl 7/l/coal copolymer may be prevented. It does not adversely affect the mechanical properties of the product or the flavor of the molded product.
本発明ニオイて、エチレン−ビニルアルコール共重合体
としては、エチレン含有量が20乃至60モルチ、特に
25乃至50そルチであるエチレン−酢酸ビニル共重合
体を、ケン化度が96モルチ以上、特に99モルチ以上
となるようにケン化して得られる共重合体ケン化物が使
用される。このエチレンビニルアルコール共重合体ケン
化物は、フィルムを形成し得るに足る分子量を有するべ
きである。In the present invention, as the ethylene-vinyl alcohol copolymer, an ethylene-vinyl acetate copolymer having an ethylene content of 20 to 60 moles, especially 25 to 50 moles, and a saponification degree of 96 moles or more, especially A saponified copolymer obtained by saponifying the copolymer to a content of 99 mol or more is used. This saponified ethylene vinyl alcohol copolymer should have a molecular weight sufficient to form a film.
また一般に、フェノール:水の重量比で85:15の混
合溶媒中30℃で測定して、0.01dt/9以上、特
に0.05 di/E以上の粘度を有することが望まし
い。In general, it is desirable to have a viscosity of 0.01 dt/9 or more, particularly 0.05 di/E or more, as measured at 30° C. in a mixed solvent with a weight ratio of phenol:water of 85:15.
プロピレン系樹脂としては、重合乃至共重合に際してチ
ーグラー・ナツタ触媒が使用されるものであって、特に
ASTMD570で測定した吸水率が0.5チ以下、好
ましくは0.1%以下のプロピレン系樹脂が使用され、
代表的なもの止してアイソタクチック/ リプロピレン
、エチレンープロピレン共重合体、グロピレンープテン
ー1共重合体、エチレン−プロピレン−ブテン−1共重
合体等の結晶性重合体を挙げることができる。As the propylene resin, a Ziegler-Natsuta catalyst is used during polymerization or copolymerization, and in particular, a propylene resin with a water absorption rate of 0.5 inches or less, preferably 0.1% or less as measured by ASTM D570 is used. used,
Representative examples include crystalline polymers such as isotactic/lipropylene, ethylene-propylene copolymer, glopylene-butene-1 copolymer, and ethylene-propylene-butene-1 copolymer. I can do it.
本発明の樹脂組成物において、エチレン−ビニルアルコ
ール共重合体(EVOH)とプロピレン系樹脂(pp)
とは任意の比率で存在し得るが、一般的に言って
EVOH:PP=1 : 10 乃至1000:1、特
に1.10 乃至100 : 1
の重量比で存在するのがよい。In the resin composition of the present invention, ethylene-vinyl alcohol copolymer (EVOH) and propylene resin (pp)
Although EVOH:PP may be present in any ratio by weight, it is generally preferred that EVOH:PP be present in a weight ratio of 1:10 to 1000:1, particularly 1.10 to 100:1.
成形時に副生ずるリグラインド中においては、EVOH
:PP=1 : 2000乃至1:3の様に、EVOH
に対してプロピレン系樹脂の量がかなり過剰となってい
る。During regrind, which occurs as a by-product during molding, EVOH
:PP=1:2000 to 1:3, EVOH
The amount of propylene resin is considerably excessive.
本発明の樹脂組成物においては、上記のリグライト等の
スクラップ組成物を構成成分として使用することができ
る点で非常に有効である。The resin composition of the present invention is very effective in that scrap compositions such as the above-mentioned regrite can be used as constituent components.
本発明の樹脂組成物には、上述したエチレン−ビニルア
ルコール共重合体及びプロピレン系樹脂以外の他の熱可
塑性樹脂を配合することが可能である。The resin composition of the present invention may contain thermoplastic resins other than the above-mentioned ethylene-vinyl alcohol copolymer and propylene resin.
即チ、エチレン−ビニルアルコール共重合体は、湿度の
影響を少なくするためにポリプロピレン等の低吸水性樹
脂の内外表面層でサンドイッチさせた積層構造体などと
して通常使用されるが、エチレン−ビニルアルコール共
重合体と低吸水性樹脂とは一般に接着性がないので、こ
れら両樹脂層の一方或いは両方に接着剤樹脂を配合する
か、或いは両樹脂層の間に、接着剤樹脂層を設ける。こ
れらの接着剤樹脂は、当然リグラインドのブレンド物中
にも混入してくることになる。また、前述したブレンド
物を、別の低吸水性樹脂及び/又はエチレンビニルアル
コール共重合体と共押出する場合には、ブレンド物中に
接着剤樹脂を混入する場合もある。Ethylene-vinyl alcohol copolymer is usually used as a laminate structure sandwiched between inner and outer surface layers of low water absorbency resin such as polypropylene to reduce the influence of humidity, but ethylene-vinyl alcohol copolymer Since the copolymer and the low water absorption resin generally do not have adhesive properties, an adhesive resin is blended into one or both of these resin layers, or an adhesive resin layer is provided between the two resin layers. Naturally, these adhesive resins will also be mixed into the regrind blend. Further, when the above-mentioned blend is coextruded with another low water absorbency resin and/or an ethylene vinyl alcohol copolymer, an adhesive resin may be mixed into the blend.
このような接着剤樹脂としては、カルゲン酸。Such adhesive resins include calgenic acid.
カルがン酸無水物、カルボン酸塩、カルデン酸アミド、
カルデン酸エステル等に基づくカルボニル(−C−)
基を主鎖又は側鎖に、1乃至700ミリイクイパレン
ト(m−eq)/1oog樹脂、特に10乃至500
meq/100g樹脂の濃度で含有する熱可塑性樹脂が
挙げられる。接着剤樹脂の適当な例は、エチレン−アク
リル酸共重合体、イオン架橋オレフィン共重合体、無水
マレイン酸グラフトポリエチレン、無水マレイン酸グラ
フトポリプロピレン−アクリル酸グラフトポリオレフィ
ン、エチレン−酢酸ビニル共重合体、共重合ポリエステ
ル、共重合ポリアミド等である。Carganic acid anhydride, carboxylate, cardenic acid amide,
Carbonyl (-C-) based on caldic acid ester, etc.
groups in the main chain or side chains, 1 to 700 m-eq/10og resin, especially 10 to 500 m-eq.
Examples include thermoplastic resins containing at a concentration of meq/100g resin. Suitable examples of adhesive resins include ethylene-acrylic acid copolymers, ionically crosslinked olefin copolymers, maleic anhydride grafted polyethylene, maleic anhydride grafted polypropylene-acrylic acid grafted polyolefins, ethylene-vinyl acetate copolymers, These include polymerized polyester, copolymerized polyamide, etc.
これらの含カルがニル熱可塑性樹脂は一般にEVOHと
ppとの合計量100重量部当シ、200乃至0.01
重量部、特に100乃至0.1重量部の量で存在する。These cal-containing thermoplastic resins generally have a content of 200 to 0.01 parts by weight per 100 parts by weight of EVOH and pp.
It is present in an amount of parts by weight, especially from 100 to 0.1 parts by weight.
また上記接着剤用の樹脂以外に、例えば4σ重量%以下
の範囲において、高密度ポリエチレン。In addition to the above-mentioned adhesive resin, high-density polyethylene may be used, for example, in a range of 4σ weight % or less.
直鎖低密度ポリエチレン、アイオノマー等の他の熱可塑
性樹脂が配合されていてもよい。Other thermoplastic resins such as linear low density polyethylene and ionomers may also be blended.
本発明の樹脂組成物においては、上記の様な他の熱可塑
性樹脂が配合されている場合にも、ハイドロタルサイト
型複合金属水酸化物のマスキング効果は失われず、かく
してリグラインド等を有効に再使用することが可能とな
るものである。In the resin composition of the present invention, even when other thermoplastic resins such as those mentioned above are blended, the masking effect of the hydrotalcite-type composite metal hydroxide is not lost, thus making regrind etc. effective. It is possible to reuse it.
本発明の樹脂組成物は、溶融押出して、容器、フィルム
乃至シート等の形に成形する。この際、成形品を該組成
物単層から形成してもよく、また他の樹脂乃至は樹脂組
成物と共押出して積層構造の成形品とすることもできる
。The resin composition of the present invention is melt-extruded and molded into a container, film, sheet, or the like. At this time, the molded article may be formed from a single layer of the composition, or it may be coextruded with other resins or resin compositions to form a molded article with a laminated structure.
本発明の樹脂組成物との共押出に使用される他の樹脂と
しては、低吸水性樹脂、エチレンビニルアルコール共重
合体、接着剤樹脂或いはこれらの2種以上のブレンド物
を挙げることができる。その層構造の適当な数例は、本
発明の樹脂組成物をBL、低吸水性樹脂をLMR,エチ
レン−ビニルアルコール共重合体をEVOH,接着剤樹
脂をADで表わして、次の通シであるが、勿論本発明は
これに限定されない。Other resins used for coextrusion with the resin composition of the present invention include low water absorption resins, ethylene vinyl alcohol copolymers, adhesive resins, and blends of two or more of these. Suitable examples of the layer structure are as follows: the resin composition of the present invention is represented by BL, the low water absorption resin is represented by LMR, the ethylene-vinyl alcohol copolymer is represented by EVOH, and the adhesive resin is represented by AD. However, the present invention is of course not limited to this.
単層構造 BL 二層構造 BL/LMR,BL/EVOH 三層構造 BL/EVOH/BL、BL/EVOH+AD/BL。Single layer structure BL double layer structure BL/LMR, BL/EVOH three layer structure BL/EVOH/BL, BL/EVOH+AD/BL.
BL/EVOH+AD+LMR/BL、EVOH/AD
/BL、BVOH/BL/LMR
四層構造
LMR/BL/EVOH/LMR+AD%LMR/BL
/EVOH+AD/LMR
五層構造
BL/AD/EVOH/AD/BL%LMR/AD/E
VOH/AD/BL、BL/EVOH/BL/EVOH
/BL
六層構造
LMR/AD/EVOH/AD/BL/LMR七層構造
LMR/BL/AD/EVOH/AD/BL/LMR八
層構造
LMR/BL/LMR/AD/EVOH/へD/BL/
LMR
光層構造
LMR/BL/LMR/AD/EVOH/AD/LMR
/BL/LMR。BL/EVOH+AD+LMR/BL, EVOH/AD
/BL, BVOH/BL/LMR Four-layer structure LMR/BL/EVOH/LMR+AD%LMR/BL
/EVOH+AD/LMR Five-layer structure BL/AD/EVOH/AD/BL%LMR/AD/E
VOH/AD/BL, BL/EVOH/BL/EVOH
/BL Six-layer structure LMR/AD/EVOH/AD/BL/LMR Seven-layer structure LMR/BL/AD/EVOH/AD/BL/LMR Eight-layer structure LMR/BL/LMR/AD/EVOH/D/BL/
LMR Optical layer structure LMR/BL/LMR/AD/EVOH/AD/LMR
/BL/LMR.
本発明の樹脂組成物は、例えば押出機で溶融混練した後
、T−グイ、サーキュラ−ダイ等のダイスを通して所定
の形状に押出す。The resin composition of the present invention is melt-kneaded, for example, in an extruder, and then extruded into a predetermined shape through a die such as a T-Guy or a circular die.
多層同時押出の場合には、各樹脂層に対応する押出機で
溶融混練した後、多層多重ダイスを通して押出す。In the case of multilayer coextrusion, each resin layer is melt-kneaded in an extruder corresponding to the resin layer, and then extruded through a multilayer die.
成形物は、フィルム、シート、dζトル乃至チューブで
形成用パリソン乃至はパイプ、ボトル乃至チューブ成形
用ノリフオーム等の形をと9得る。The molded product can take the form of a film, a sheet, a dζtor or a tube, a parison or pipe for forming, a shape for forming a bottle or a tube, etc.9.
パリソン、パイプ或いはプリフォームからのがトルの形
成は、押出物を一対の割型でビ/チオフし、その内部に
流体を吹込むことにより8易に行われる。またパイプ乃
至はノリフオームを冷却した後、延伸温度に加熱し、軸
方向に延伸するとともに、流体圧によって周方向にブロ
ー延伸することにより、延伸プローyt”トル等が得ら
れる。Formation of a mold from a parison, pipe or preform is easily accomplished by cutting the extrudate through a pair of split molds and blowing fluid into the mold. Further, after cooling the pipe or the Noriform, it is heated to a stretching temperature, stretched in the axial direction, and blow-stretched in the circumferential direction using fluid pressure, thereby obtaining a stretched blower or the like.
更に、フィルム乃至シートを、真空成形、圧空成形、張
出成形、プラグアシスト成形等の手段に付することによ
り、カッグ状、トレイ状等の包装容器が得られる。Furthermore, by subjecting the film or sheet to vacuum forming, pressure forming, stretch forming, plug assist forming, or the like, a bag-shaped, tray-shaped, or other packaging container can be obtained.
発明の作用効果
かかる本発明の樹脂組成物においては、成形等に際して
組成物中のエチレン−ビニルアルコール共重合体成分の
熱劣化が有効に抑制されるため、−容器等の成形に供し
た場合、外観特性や耐衝撃性等の機械的特性を損うこと
なく、ガスバリヤ−性が湿度の影響によって低下するこ
とのない容器が得られる。Effects of the Invention In the resin composition of the present invention, thermal deterioration of the ethylene-vinyl alcohol copolymer component in the composition is effectively suppressed during molding, etc.; It is possible to obtain a container whose gas barrier properties do not deteriorate due to the influence of humidity without impairing its external appearance or mechanical properties such as impact resistance.
マタエチレンービニルアルコール共重合体成分の熱劣化
が防止されることによりて、押出特性も良好であシ、所
謂焦げ等の発生もなく、サージング、フィッシュアイ、
メヤニ等の欠陥のない押出物が得られる。By preventing heat deterioration of the mataethylene-vinyl alcohol copolymer component, extrusion properties are also good, and there is no occurrence of so-called scorching, surging, fish eyes, etc.
Extrudates free of defects such as dirt are obtained.
更に本発明によれば、容器の成形等によシ副生ずるリグ
ラインド等のスクラップ組成物を、容器等の成形に再利
用できるという顕著な利点が達成され、かかる本発明は
省資源の見地から極めて有用である。しかも本発明の樹
脂組成物を容器等の成形に供した場合、リグラインド等
のスクラップ組成物を、該組成物中にハイドロタルサイ
ト型複合金属水酸化物が前述した様な範囲内に含有され
ている限シにおいて、そのまま再利用することが可能と
なる。Furthermore, according to the present invention, a remarkable advantage has been achieved in that scrap compositions such as regrind produced as by-products in the molding of containers, etc. can be reused for molding containers, etc., and the present invention is advantageous from the viewpoint of resource saving. Extremely useful. Moreover, when the resin composition of the present invention is used to mold containers, etc., the composition contains a scrap composition such as regrind, and the hydrotalcite-type composite metal hydroxide is contained within the above-mentioned range. It is possible to reuse it as is, as long as it lasts.
本発明と次の例で説明する。The invention is illustrated in the following example.
実施例1゜
密度が0.91g滓、 (ASTMD−1505)、メ
ルト・インデックスが5.99 / 10 min、
(ASTMD−1238)のアイツタクチイック・ポリ
プロピレン(PIF−1)と、エチレン含有量が48モ
ルチ、ケン化度が96.1%、メルト・イアfyり、(
(MI 、ASTM D−1238)が20 fi/
10 min、のエチレン−ビニルアルコール共重合体
(EVOH−1)との混合比(重量比)が90:10の
混合物に0.05 PHR,のDHT−4A(協和化学
工業(株)製ハイドロタルサイト類化合物)を添加し、
ドライ・ブレンドした後に、このドライ・ブレンド物を
西独ブラベンダー社製のプラベンダー・プラストグラフ
会用いて、チェンバ一温度が230℃、ローター回転数
が65rpm。Example 1゜Density: 0.91g slag, (ASTMD-1505), Melt index: 5.99/10 min,
(ASTMD-1238) tactical polypropylene (PIF-1) with an ethylene content of 48 mole, a saponification degree of 96.1%, and a melt-fired (
(MI, ASTM D-1238) is 20 fi/
For 10 min, 0.05 PHR of DHT-4A (Kyowa Kagaku Kogyo Co., Ltd.'s Hydrotal) was mixed with ethylene-vinyl alcohol copolymer (EVOH-1) at a mixing ratio (weight ratio) of 90:10. Cytotype compounds) are added,
After dry blending, this dry blend was used in a Prabender Plastograph manufactured by Brabender, West Germany, at a chamber temperature of 230°C and a rotor rotation speed of 65 rpm.
の条件下で30分間の混練を行なった。Kneading was carried out for 30 minutes under these conditions.
以下、との混練物をAと記す。また、比較のために前記
DHT −4Aを添加しない混線物(PP−1とEVO
H−1との混合比は同じ)も上記と同じ条件で得た(以
下、この混練物をBと記す。)。Hereinafter, the kneaded product with is referred to as A. In addition, for comparison, we also prepared crosstalk products (PP-1 and EVO) to which DHT-4A was not added.
The mixture ratio with H-1 was the same) was also obtained under the same conditions as above (hereinafter, this kneaded product will be referred to as B).
これらA、Bの2s類の混練物!&250℃の高圧プレ
スによって厚さが約300μmのシートを作製した。そ
してそれらA、B各シートの単位面積(1m)を万能投
影機で100倍に拡大し、焦げ(黒色劣化物)を観察し
た。Aシートから観察された焦けの数は1個/1α2で
あったのに対し、Bシートから観測された焦げの数は7
2個/1crn2であった。A kneaded product of these 2s A and B! A sheet with a thickness of about 300 μm was produced by high-pressure pressing at &250°C. Then, the unit area (1 m) of each of the sheets A and B was magnified 100 times using a universal projector, and burnt (black deteriorated material) was observed. The number of burnt spots observed from sheet A was 1/1α2, while the number of burnt spots observed from sheet B was 7.
It was 2 pieces/1 crn2.
実施例2゜
密度が0.90 g、ん、 (ASTMD−1505)
、メルト・インデックスが1.1.9/10m1n、
(ASTMD−1238)のエチレン・プロピレン共重
合体(5wt%のエチレンを含有、以下PPと記す。)
100重址部に対し、1重量部のDHT−4A (実施
例1に記載)を添加し、直径が65■、有効長と直径の
比(L/I))が22のスクリューを内蔵した押出様に
よって前記PP+DHT系混合物を作製した。このとき
のベレタイジングの条件は押出機の設定温度がスクリュ
ーのフィード部分から順に200℃、200℃、230
℃、230℃、スクリューの回転数は45rpmであシ
、吐出量は50kg/hr であった。以下この混合物
を5−ppと記す。Example 2゜Density is 0.90 g (ASTMD-1505)
, melt index is 1.1.9/10m1n,
(ASTMD-1238) ethylene-propylene copolymer (contains 5 wt% ethylene, hereinafter referred to as PP)
1 part by weight of DHT-4A (described in Example 1) was added to 100 parts by weight, and extrusion was carried out using a built-in screw with a diameter of 65 cm and an effective length to diameter ratio (L/I) of 22. The PP+DHT mixture was prepared according to the method described above. The conditions for beletizing at this time are that the set temperature of the extruder is 200℃, 200℃, and 230℃ from the feed section of the screw.
The temperature was 230°C, the screw rotation speed was 45 rpm, and the discharge rate was 50 kg/hr. Hereinafter, this mixture will be referred to as 5-pp.
一方、エチレン含有量が27モルチ、ケン化度が99.
5モルチ、メルト・インデックス(ASTMD−123
8、但し、測定温度は210℃)のエチレン−ビニルア
ルコール共重合体(EVOH) 100重量部前記DH
T−4Aを0.5重量部添加し、上記と同じ押出機及び
ベレタイジング条件で前記EVOH+DHT系混合物(
ペレット)を得た。以下、このペレットをS −EVO
Hと記す。On the other hand, the ethylene content is 27 mole and the saponification degree is 99.
5 molti, melt index (ASTMD-123
8. However, the measurement temperature is 210°C) 100 parts by weight of ethylene-vinyl alcohol copolymer (EVOH) above DH
Adding 0.5 parts by weight of T-4A and using the same extruder and pelletizing conditions as above, the EVOH + DHT mixture (
pellets) were obtained. Below, this pellet is S-EVO
Write it as H.
これらの各ペレットを表1に示す混合比(同表中の単位
はそれぞれ′kg)でドライ・ブレンドした後に、それ
らの各混合物を上記の押出機及び内容積が450CCで
円筒状の&)層成型用金型を用いて、上記の各混合物か
らなるボトル(平均肉厚は約500μm )を成形し
た。押出及び成形条件は、ブロー成形条件が5.0 k
l? / cm2であった他は全て上記のペレタイノン
グ条件と同一であった。また、各ボトルは、押出開始か
ら約1時間経過後からサンプリングを始めた。ボトルを
一種類につき約200本採取した。以下、これらの&)
ルを表1中に記載のマークに従って、それぞれC,D、
E。After dry blending each of these pellets at the mixing ratio shown in Table 1 (each unit is 'kg' in the table), each mixture was transferred to the above-mentioned extruder and a cylindrical &) layer with an internal volume of 450 cc. Bottles (average wall thickness: approximately 500 μm) consisting of each of the above mixtures were molded using a mold. The extrusion and molding conditions are blow molding conditions of 5.0 k.
l? / cm2, all other conditions were the same as the pelletizing conditions described above. Sampling of each bottle began about 1 hour after the start of extrusion. Approximately 200 bottles of each type were collected. Below are these &)
C, D, and C, respectively, according to the marks listed in Table 1.
E.
F、G、H,I、Jと記す。They are written as F, G, H, I, and J.
得られた8種類の各ボトルに就いて、実施例1に記載し
た方法と同様に高圧プレスによってC〜Jシートを作製
し、実施例1記載の万能投影機で同じ条件に拡大し、焦
げ(黒色劣化物)を観察した。結果を表2に示す。表2
に於ける各数値は、一種類当り各100本のyjrトル
の胴中央部からプレスされた各シートのうち、焦げが認
められたボトルの本数を意味する。従って、値の小さい
ほうが“ボトル中の焦げ”が少ないと認められる。For each of the eight types of bottles obtained, sheets C to J were produced using a high-pressure press in the same manner as described in Example 1, enlarged under the same conditions using the universal projector described in Example 1, and charred ( (black degraded product) was observed. The results are shown in Table 2. Table 2
Each numerical value in , means the number of bottles in which scorch was observed among each sheet pressed from the center of the body of 100 YJR bottles per type. Therefore, it is recognized that the smaller the value, the less "burntness in the bottle."
次に、このテストに於て押出機のスタート直後から何分
後に押出機のダイリップに1メヤニ″(rル状物質)が
発生するかを、これら8種類の組成物に就いて、3名の
作業員により視覚で判定させた。結果を表2に併せて示
す。表2に於て、各位は上記3名の回答の平均値を5分
単位に纏めたものである。従って、表2に於て値の小さ
いもののほうが“メヤニ”の発生が遅い、即ち組成1勿
は耐劣化性に対して良好であると言える。Next, in this test, 3 people tested these 8 types of compositions to determine how many minutes after starting the extruder, 1" (rubber-like substance) would occur at the die lip of the extruder. The workers judged visually.The results are also shown in Table 2.In Table 2, each person summarizes the average value of the answers of the above three people in 5 minute units. It can be said that the smaller the value, the slower the occurrence of "stain", that is, the composition 1 is better in terms of resistance to deterioration.
さらに、約2時間の押出成形を終了した後、押出機から
スクリューを抜き出し、同スクリューのコンプレッショ
ン部分からメタリング部分にかけての”焦げ″の付着状
態を上記3名の作業員に視覚判定させた。結果を表2に
併せて示す。同表に於て、各位は、上記3名の作業員の
視覚判定により(1)スクリューに焦げが付着していな
い場合を1、(ii)焦げが若干付着している場合を2
、(]ii)焦げがかなシ付着している場合を3.4ψ
焦げのスクリューへの堆積が著しい場合を4というよう
に、それぞれ評点付けを行わせ、各回答の平均値を示し
ている。従って、数値の小さいもののほうが、スクリ□
ューへの焦げの程度が少ないと判定できる。Furthermore, after extrusion molding for about 2 hours was completed, the screw was removed from the extruder, and the three workers visually judged the state of "scorch" adhesion from the compression part to the metering part of the screw. The results are also shown in Table 2. In the same table, each person is given a 1 if there is no scorch on the screw, and a 2 if there is some scorch on the screw, based on the visual judgment of the three workers mentioned above.
, (]ii) 3.4ψ if there is some burnt material
A score of 4 was given for cases where there was significant accumulation of scorch on the screw, and the average value of each answer is shown. Therefore, the smaller the number, the more
It can be determined that the degree of scorching on the burner is small.
表1及び表2の結果から、PPまたはEVOHのうちの
、少なくともいずれか一方の合成樹脂にハイドロタルサ
イト類化合物を添加すると、PP/EVAL系混合物の
溶融押出に際して、゛焦げ″や”メヤニ”など、樹脂の
劣化を顕著に防止゛することが可能となる。From the results in Tables 1 and 2, it can be seen that when a hydrotalcite compound is added to at least one of PP or EVOH synthetic resins, "scorching" and "staining" occur during melt extrusion of PP/EVAL mixtures. etc., it becomes possible to significantly prevent the deterioration of the resin.
表 1 表2Table 1 Table 2
g l 図ハ、エチレン−ビニルアルコール共重合体に
、Tict、 、 TiO2及びAt20.を夫々添
加したものについて、経時とメルトフローレートとの関
係を示す線図である。
第1図g l Figure C, ethylene-vinyl alcohol copolymer has Tict, , TiO2 and At20. FIG. 3 is a diagram showing the relationship between time and melt flow rate for the respective additives. Figure 1
Claims (2)
共重合体及びハイドロタルサイト型複合金属水酸化物を
含有して成ることを特徴とする樹脂組成物。(1) A resin composition comprising a propylene resin, an ethylene-vinyl alcohol copolymer, and a hydrotalcite-type composite metal hydroxide.
共重合体とを10^7:1乃至1:1000の重量比で
含有し且つこれら両樹脂の合計量当りハイドロタルサイ
ト型複合金属水酸化物を10^−^5乃至5重量%の量
で含有する特許請求の範囲第1項記載の組成物。(2) Contains propylene resin and ethylene-vinyl alcohol copolymer in a weight ratio of 10^7:1 to 1:1000, and contains 10% of hydrotalcite-type composite metal hydroxide per total amount of both resins. A composition according to claim 1 containing from 5 to 5% by weight.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15008985A JPS6211748A (en) | 1985-07-10 | 1985-07-10 | Resin composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15008985A JPS6211748A (en) | 1985-07-10 | 1985-07-10 | Resin composition |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6211748A true JPS6211748A (en) | 1987-01-20 |
Family
ID=15489271
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15008985A Pending JPS6211748A (en) | 1985-07-10 | 1985-07-10 | Resin composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6211748A (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62179530A (en) * | 1986-02-03 | 1987-08-06 | Nippon Synthetic Chem Ind Co Ltd:The | Production of molding |
JPH01308440A (en) * | 1988-01-26 | 1989-12-13 | Nippon Synthetic Chem Ind Co Ltd:The | Resin composition |
JPH01308439A (en) * | 1988-01-26 | 1989-12-13 | Nippon Synthetic Chem Ind Co Ltd:The | Production of molding |
EP0440558A2 (en) * | 1990-02-01 | 1991-08-07 | Elf Atochem S.A. | Saponified ethylene-vinyl-acetate composition containing hydrotalcite and use thereof |
EP0483695A2 (en) * | 1990-10-29 | 1992-05-06 | Nippon Gohsei Kagaku Kogyo Kabushiki Kaisha | Resin composition and use thereof |
US6214426B1 (en) | 1997-04-23 | 2001-04-10 | Mitsui Chemicals, Inc. | Multilayered article, vessel and resin composition based on polyethylene |
US6777491B1 (en) | 1997-04-23 | 2004-08-17 | Mitsui Chemicals, Inc. | Multilayered article, vessel and resin composition based on polyethylene |
WO2007129369A1 (en) | 2006-04-25 | 2007-11-15 | The Nippon Synthetic Chemical Industry Co., Ltd. | Resin composition and multilayer structure making use of the same |
US7332025B2 (en) | 2004-08-24 | 2008-02-19 | The Nippon Synthetic Chemical Industry Co., Ltd. | Resin composition and process for preparing multi-layer structure using the same |
-
1985
- 1985-07-10 JP JP15008985A patent/JPS6211748A/en active Pending
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62179530A (en) * | 1986-02-03 | 1987-08-06 | Nippon Synthetic Chem Ind Co Ltd:The | Production of molding |
JPH0476376B2 (en) * | 1986-02-03 | 1992-12-03 | Nippon Synthetic Chem Ind | |
JPH01308440A (en) * | 1988-01-26 | 1989-12-13 | Nippon Synthetic Chem Ind Co Ltd:The | Resin composition |
JPH01308439A (en) * | 1988-01-26 | 1989-12-13 | Nippon Synthetic Chem Ind Co Ltd:The | Production of molding |
EP0440558A2 (en) * | 1990-02-01 | 1991-08-07 | Elf Atochem S.A. | Saponified ethylene-vinyl-acetate composition containing hydrotalcite and use thereof |
EP0483695A2 (en) * | 1990-10-29 | 1992-05-06 | Nippon Gohsei Kagaku Kogyo Kabushiki Kaisha | Resin composition and use thereof |
US6214426B1 (en) | 1997-04-23 | 2001-04-10 | Mitsui Chemicals, Inc. | Multilayered article, vessel and resin composition based on polyethylene |
US6777491B1 (en) | 1997-04-23 | 2004-08-17 | Mitsui Chemicals, Inc. | Multilayered article, vessel and resin composition based on polyethylene |
US7332025B2 (en) | 2004-08-24 | 2008-02-19 | The Nippon Synthetic Chemical Industry Co., Ltd. | Resin composition and process for preparing multi-layer structure using the same |
WO2007129369A1 (en) | 2006-04-25 | 2007-11-15 | The Nippon Synthetic Chemical Industry Co., Ltd. | Resin composition and multilayer structure making use of the same |
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