JPS5825576B2 - Manufacturing method of rotomolded products - Google Patents
Manufacturing method of rotomolded productsInfo
- Publication number
- JPS5825576B2 JPS5825576B2 JP1871280A JP1871280A JPS5825576B2 JP S5825576 B2 JPS5825576 B2 JP S5825576B2 JP 1871280 A JP1871280 A JP 1871280A JP 1871280 A JP1871280 A JP 1871280A JP S5825576 B2 JPS5825576 B2 JP S5825576B2
- Authority
- JP
- Japan
- Prior art keywords
- polyethylene
- crosslinking
- manufacturing
- rotomolded
- gel fraction
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 238000004519 manufacturing process Methods 0.000 title claims description 6
- 239000004698 Polyethylene Substances 0.000 claims description 26
- -1 polyethylene Polymers 0.000 claims description 26
- 229920000573 polyethylene Polymers 0.000 claims description 26
- 238000004132 cross linking Methods 0.000 claims description 12
- 238000001175 rotational moulding Methods 0.000 claims description 5
- 238000000034 method Methods 0.000 claims description 4
- 229920001903 high density polyethylene Polymers 0.000 claims description 3
- 239000004700 high-density polyethylene Substances 0.000 claims 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 4
- 238000005336 cracking Methods 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 3
- 230000006353 environmental stress Effects 0.000 description 3
- NKSJNEHGWDZZQF-UHFFFAOYSA-N ethenyl(trimethoxy)silane Chemical compound CO[Si](OC)(OC)C=C NKSJNEHGWDZZQF-UHFFFAOYSA-N 0.000 description 3
- 238000000465 moulding Methods 0.000 description 3
- 150000001451 organic peroxides Chemical class 0.000 description 3
- 239000004594 Masterbatch (MB) Substances 0.000 description 2
- 239000003431 cross linking reagent Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 241000156978 Erebia Species 0.000 description 1
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical compound [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 description 1
- BGYHLZZASRKEJE-UHFFFAOYSA-N [3-[3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoyloxy]-2,2-bis[3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoyloxymethyl]propyl] 3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoate Chemical compound CC(C)(C)C1=C(O)C(C(C)(C)C)=CC(CCC(=O)OCC(COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)(COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)=C1 BGYHLZZASRKEJE-UHFFFAOYSA-N 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- RWCCWEUUXYIKHB-UHFFFAOYSA-N benzophenone Chemical compound C=1C=CC=CC=1C(=O)C1=CC=CC=C1 RWCCWEUUXYIKHB-UHFFFAOYSA-N 0.000 description 1
- 239000012965 benzophenone Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000002596 correlated effect Effects 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- AYOHIQLKSOJJQH-UHFFFAOYSA-N dibutyltin Chemical compound CCCC[Sn]CCCC AYOHIQLKSOJJQH-UHFFFAOYSA-N 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- FWDBOZPQNFPOLF-UHFFFAOYSA-N ethenyl(triethoxy)silane Chemical compound CCO[Si](OCC)(OCC)C=C FWDBOZPQNFPOLF-UHFFFAOYSA-N 0.000 description 1
- 229920001112 grafted polyolefin Polymers 0.000 description 1
- 229920001684 low density polyethylene Polymers 0.000 description 1
- 239000004702 low-density polyethylene Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- QUAMTGJKVDWJEQ-UHFFFAOYSA-N octabenzone Chemical compound OC1=CC(OCCCCCCCC)=CC=C1C(=O)C1=CC=CC=C1 QUAMTGJKVDWJEQ-UHFFFAOYSA-N 0.000 description 1
- 239000011347 resin Substances 0.000 description 1
- 229920005989 resin Polymers 0.000 description 1
- 229910000077 silane Inorganic materials 0.000 description 1
- SCPYDCQAZCOKTP-UHFFFAOYSA-N silanol Chemical compound [SiH3]O SCPYDCQAZCOKTP-UHFFFAOYSA-N 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- KSBAEPSJVUENNK-UHFFFAOYSA-L tin(ii) 2-ethylhexanoate Chemical compound [Sn+2].CCCCC(CC)C([O-])=O.CCCCC(CC)C([O-])=O KSBAEPSJVUENNK-UHFFFAOYSA-L 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Moulding By Coating Moulds (AREA)
Description
【発明の詳細な説明】 本発明はタンク等の回転成形品の製造方法に関する。[Detailed description of the invention] The present invention relates to a method for manufacturing rotomolded products such as tanks.
従来より、回転成形は樹脂の流れがよくないと極めて成
形しに(い方法であるため、ポリエチレンの回転成形品
は、溶融性の良好なポリエチレンを用い、回転成形温度
を170〜270℃の高温にして製造していた。Conventionally, rotomolding is a method that is extremely difficult to mold unless the resin flows well, so polyethylene rotomolded products are made using polyethylene with good melting properties, and the rotomolding temperature is set to a high temperature of 170 to 270°C. It was manufactured by
このような方法は未架橋ポリエチレンを使用する場合は
可能であるが、その場合、耐熱性、耐環境応力亀裂特性
、耐溶剤性等が不充分であるため、このような特性を必
要とするものには使用できなかった。This method is possible when using uncrosslinked polyethylene, but in that case, heat resistance, environmental stress cracking resistance, solvent resistance, etc. are insufficient, so it is not possible to use uncrosslinked polyethylene. could not be used.
上記特性を改善するため通常、ポリエチレンを架橋する
ことが行なわれているが、ジクミルパーオキサイド等の
汎用の架橋剤を含有するポリエチレンを、上記のような
高温で成形しようとすると、架橋剤が一部分解して早期
架橋をおこし、スコーチを生じて加工性を損うという欠
点があった。In order to improve the above properties, polyethylene is usually cross-linked, but when polyethylene containing a general-purpose cross-linking agent such as dicumyl peroxide is molded at the above-mentioned high temperatures, the cross-linking agent is It has the disadvantage that it partially decomposes and causes early crosslinking, causing scorch and impairing processability.
又架橋度が成形条件の微妙な違いにより影響を受けやす
(て一定せず、肌荒れ、ボイド等の外観不良や特性上問
題を生じる事が多かった。In addition, the degree of crosslinking is easily affected by subtle differences in molding conditions (and is not consistent), often resulting in poor appearance such as rough skin and voids, and problems with properties.
又金型腐食が起こりやすいという欠点もあった。Another drawback was that mold corrosion was likely to occur.
本発明者らは上記欠点に監み、ポリエチレンとして加水
架橋性シリコーングラフト化ポリエチレンを使用すれば
、成形温度が高温でも上記欠点が生じず、しかも架橋す
ることができるので極めて有用であることを見い出した
。The inventors of the present invention have taken into consideration the above-mentioned drawbacks and have found that if hydrolytically crosslinkable silicone-grafted polyethylene is used as the polyethylene, the above-mentioned drawbacks will not occur even at high molding temperatures, and it can be crosslinked, making it extremely useful. Ta.
すなわち本発明は、ポリエチレンから成る回転成形品を
製造するにあたり、加水架橋性シリコーングラフト化ポ
リエチレンを170〜270℃で回転成形し、ゲル分率
を10〜60%となるよう架橋することを特徴とする回
転成形品の製造方法に関する。That is, the present invention is characterized in that, in producing a rotationally molded article made of polyethylene, hydrolytically crosslinkable silicone-grafted polyethylene is rotomolded at 170 to 270°C and crosslinked to a gel fraction of 10 to 60%. The present invention relates to a method of manufacturing a rotationally molded product.
本発明に使用される加水架橋性シリコーングラフト化ポ
リエチレンは、ポリエチレンにジクミルパーオキサイド
(DCP)等の有機過酸化物の存在下でビニルトリメト
キシシラン(VTMO8)、ビニルトリエトキシシラン
等の不飽和シランを反応させてグラフト化したシリコー
ングラフト化ポリオレフィンと、ポリエチレンにジブチ
ル錫ジラウレー)(DBTDL)、オクタン酸第−錫等
のシラノール縮合触媒を添加した触媒マスターバッチと
を、一定の割合で混練して得られるか、あるいはDCP
、VTMO8,DBTDLを一工程でポリエチレンと混
練して得られるものであり、架橋は水分の供給により進
行する。Hydrolytically crosslinkable silicone-grafted polyethylene used in the present invention is produced by adding unsaturated polyethylene such as vinyltrimethoxysilane (VTMO8) or vinyltriethoxysilane to polyethylene in the presence of an organic peroxide such as dicumyl peroxide (DCP). A silicone-grafted polyolefin, which is grafted by reacting silane, and a catalyst masterbatch, which is prepared by adding a silanol condensation catalyst such as dibutyltin dilauret (DBTDL) or tin-octoate to polyethylene, are kneaded at a certain ratio. obtained or DCP
, VTMO8, and DBTDL are kneaded with polyethylene in one step, and crosslinking progresses by supplying moisture.
逆に、水分がなければ架橋が進行しないで、未架橋ポリ
エチレンと同様に取扱うことができ、回転成形法が適用
できるものである。Conversely, in the absence of moisture, crosslinking will not proceed, and it can be handled in the same manner as uncrosslinked polyethylene, and rotational molding can be applied.
成形後は、常温下でも空気中の微量の水分により架橋す
るので、従来の有機過酸化物を分解させて架橋させる方
法に比べて特に架熱を必要とせず、従って架橋設備を要
しない。After molding, crosslinking occurs even at room temperature with a small amount of moisture in the air, so compared to conventional methods of crosslinking by decomposing organic peroxides, no special crosslinking is required, and therefore no crosslinking equipment is required.
もちろん架橋を速く進行させるため温水等は使用しても
よい。Of course, warm water or the like may be used to speed up crosslinking.
本発明においてポリエチレンは低密度ポリエチレン、高
密度ポリエチレン等があるが耐熱性の点から特に高密度
ポリエチレン(密度0.930〜0.970)が好まし
い。In the present invention, the polyethylene includes low density polyethylene, high density polyethylene, etc., but high density polyethylene (density 0.930 to 0.970) is particularly preferred from the viewpoint of heat resistance.
本発明において、加水架橋性シリコーングラフト化ポリ
エチレンは完全架橋後のゲル分率が10〜60%のもの
が適切で、ゲル分率がこれより小さいと耐熱性、耐環境
応力亀裂特性が非常に低下し、これより太きいと肌荒れ
、ボイドが生じる。In the present invention, it is appropriate for the hydrolytically crosslinkable silicone-grafted polyethylene to have a gel fraction of 10 to 60% after complete crosslinking; if the gel fraction is smaller than this, the heat resistance and environmental stress cracking resistance will be significantly reduced. However, if it is thicker than this, it will cause rough skin and voids.
ゲル分率はグラフト化率と相関があるので、ゲル分率を
10〜60%にするためには、例えば、ポリエチレン1
00重量部に対してVTMO31,4〜2.8重量部、
DCPo、02〜0.10重量部と選択してグラフト化
率を調整するか、あるいはゲル分率が60%以上となる
グラフト化率のシリコーングラフト化ポリエチレンと、
グラフト化していないポリエチレンをブレンドして、ゲ
ル分率〕を60%以下とすることもできる。Since the gel fraction is correlated with the grafting rate, for example, polyethylene 1
00 parts by weight to VTMO31.4 to 2.8 parts by weight,
DCPo, the grafting rate is adjusted by selecting 02 to 0.10 parts by weight, or silicone-grafted polyethylene with a grafting rate such that the gel fraction is 60% or more;
It is also possible to make the gel fraction 60% or less by blending non-grafted polyethylene.
本発明に使用する加水架橋性シリコーングラフト化ポリ
エチレンには、アンテージクリスタル(川口化学社製商
品名)やイルガノックス1010(日本チバガイギー社
製商品名)等の、ポリエチレンに通常使用される酸化防
止剤を添加することもできる。The hydro-crosslinkable silicone-grafted polyethylene used in the present invention contains antioxidants commonly used in polyethylene, such as Antique Crystal (trade name, manufactured by Kawaguchi Chemical Co., Ltd.) and Irganox 1010 (trade name, manufactured by Nippon Ciba Geigy Co., Ltd.). can also be added.
又耐候性を向上させる目的でMARK1413、MAR
K LA−72−A(アデカアーガス社製商品名)等
のベンゾフェノン系安定剤を添加することもできる。Also, for the purpose of improving weather resistance, MARK1413, MAR
A benzophenone stabilizer such as K LA-72-A (trade name, manufactured by Adeka Argus) may also be added.
次に実施例について説明する。Next, an example will be described.
実施例
第1表に示すシリコーングラフト化ポリエチレンと触媒
マスターバッチとを19:1の割合で混練し、200℃
で回転成形を行ない回転成形品を製造した。Example The silicone-grafted polyethylene shown in Table 1 and the catalyst masterbatch were kneaded at a ratio of 19:1, and the mixture was heated at 200°C.
Rotational molding was performed to produce a rotary molded product.
このもののゲル分率、耐環境応力亀裂特性は第2表の通
りであった。The gel fraction and environmental stress cracking resistance of this product were as shown in Table 2.
又比較として従来の有機過酸化物で架橋させたものの特
性を第3表に示す。For comparison, Table 3 shows the properties of a product crosslinked with a conventional organic peroxide.
以上の結果から明らかなように、本発明によれば安定し
た架橋度と優れた耐環境亀裂特性を有し、しかも表面状
態等が良好で加工性も改良され、ガソリンタンク、溶剤
タンク等の製造に極めて有効である。As is clear from the above results, the present invention has a stable degree of crosslinking and excellent environmental cracking resistance, has a good surface condition, and has improved processability, and can be used to manufacture gasoline tanks, solvent tanks, etc. It is extremely effective.
Claims (1)
り、加水架橋性シリコーングラフト化ポリエチレンを1
70〜270℃で回転成形し、ゲル分率を10〜60%
となるよう架橋することを特徴とする回転成形品の製造
方法。 2 ポリエチレンは高密度ポリエチレンである特許請求
の範囲第1項記載の回転成形品の製造方法。[Claims] 1. In producing a rotomolded product made of polyethylene, 1.
Rotational molding at 70-270℃, gel fraction 10-60%
A method for producing a rotationally molded product, characterized by crosslinking it so that it becomes . 2. The method for manufacturing a rotomolded product according to claim 1, wherein the polyethylene is high-density polyethylene.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1871280A JPS5825576B2 (en) | 1980-02-18 | 1980-02-18 | Manufacturing method of rotomolded products |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1871280A JPS5825576B2 (en) | 1980-02-18 | 1980-02-18 | Manufacturing method of rotomolded products |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56133119A JPS56133119A (en) | 1981-10-19 |
| JPS5825576B2 true JPS5825576B2 (en) | 1983-05-28 |
Family
ID=11979258
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1871280A Expired JPS5825576B2 (en) | 1980-02-18 | 1980-02-18 | Manufacturing method of rotomolded products |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5825576B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0658803U (en) * | 1993-01-28 | 1994-08-16 | 昭世 重永 | Ear cover for preventing stains during hair dyeing and perming work |
-
1980
- 1980-02-18 JP JP1871280A patent/JPS5825576B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56133119A (en) | 1981-10-19 |
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