JP2739654B2 - Multi-layer rotary molding - Google Patents

Multi-layer rotary molding

Info

Publication number
JP2739654B2
JP2739654B2 JP13556389A JP13556389A JP2739654B2 JP 2739654 B2 JP2739654 B2 JP 2739654B2 JP 13556389 A JP13556389 A JP 13556389A JP 13556389 A JP13556389 A JP 13556389A JP 2739654 B2 JP2739654 B2 JP 2739654B2
Authority
JP
Japan
Prior art keywords
layer
resin
molding
rotational
melt tension
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 - Fee Related
Application number
JP13556389A
Other languages
Japanese (ja)
Other versions
JPH03216A (en
Inventor
誠巳 仲谷
桂三 阿部
孝弘 小津
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Chemical Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Mitsubishi Chemical Corp filed Critical Mitsubishi Chemical Corp
Priority to JP13556389A priority Critical patent/JP2739654B2/en
Publication of JPH03216A publication Critical patent/JPH03216A/en
Application granted granted Critical
Publication of JP2739654B2 publication Critical patent/JP2739654B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は多層回転成形体という新規な成形法より得ら
れる成形体に関し、より詳しくは層間厚み構成の均一に
整った優れた多層回転成形体に関するものである。
Description: TECHNICAL FIELD The present invention relates to a molded article obtained by a novel molding method called a multilayer rotational molded article, and more particularly, to an excellent multilayer rotational molded article having a uniform interlayer thickness structure. It is about.

[従来の技術] 従来より、回転成形法は他の成形法に比し、金型製作
費が安価なことから、多品種少量生産の大型成形物を得
るのに適しており、単層のプラスチックス製大型タンク
等を製作するのに好んで用いられている。
[Prior art] Conventionally, the rotational molding method is suitable for obtaining large-sized molded products of small-scale production of many kinds because the mold manufacturing cost is lower than other molding methods. It is used to manufacture large tanks made of steel.

この回転成形法に用いられている樹脂としては、高密
度、中密度又は低密度のポリエチレンやEVA、ABS、ポリ
アミド、ポリカーボネート等であった。
The resin used in this rotational molding method was high density, medium density or low density polyethylene, EVA, ABS, polyamide, polycarbonate and the like.

この回転成形において、異種の樹脂を組み合わせて多
層の回転成形体を製造すれば、それぞれの樹脂の特徴を
生かし、現在の単層の回転成形製品にない優れた特性の
ものが得られると期待され、その試みがなされたが、次
のような技術的困難のため、殆ど商品化されていないの
が現状である。
In this rotational molding, if a multi-layer rotational molded article is manufactured by combining different kinds of resins, it is expected that the characteristics of each resin will be utilized and excellent characteristics not present in the present single-layer rotational molded product will be obtained. Attempts have been made, but at present it has hardly been commercialized due to the following technical difficulties.

[発明が解決しようとする課題] すなわち、その技術的困難のうち、最大のものは、回
転成形法における賦形の原理を重力下における金型内溶
融樹脂の自然の流動性のみに依存させているため、他の
多層成形法、例えば共押出成形法、におけるような各層
の均一な厚み構成が得難いということである。
[Problems to be Solved by the Invention] That is, of the technical difficulties, the biggest one is that the principle of shaping in the rotational molding method depends only on the natural fluidity of the molten resin in the mold under gravity. Therefore, it is difficult to obtain a uniform thickness configuration of each layer as in other multilayer molding methods, for example, a coextrusion molding method.

本発明者等はその理由に関し種々検討した結果、最内
層以外の層は、それ自身の成形が終了した後、さらに後
続段が最内層に至るまで各層の成形が継続される間、当
該層にとって追加的にさらに加熱状態におかれ、この間
に当該層の温度上昇により粘度が低下し、過剰な流動性
を持つことが当該層の厚みを乱す最大の原因であること
を見出した。
The present inventors have conducted various studies on the reason, and as a result, the layers other than the innermost layer, after the molding of the layer itself is completed, while the molding of each layer is continued until the subsequent stage reaches the innermost layer, In addition, it was further heated, during which the viscosity of the layer was reduced by the increase in temperature, and it was found that excessive fluidity was the largest cause of disturbing the thickness of the layer.

[課題を解決するための手段] 発明者らはこの点に関し鋭意検討を重ねた結果、回転
成形において最内層以外の層に用いる樹脂の溶融張力を
規制することにより、各層の厚み構成が均一な、優れた
品質の多層回転成形体が得られることを見い出して本発
明を完成したものである。
[Means for Solving the Problems] As a result of intensive studies on this point, the inventors have found that by regulating the melt tension of the resin used for the layers other than the innermost layer in rotational molding, the thickness configuration of each layer is uniform. The present invention has been accomplished by finding that a multilayer rotational molded article of excellent quality can be obtained.

すなわち本発明は、最内層以外の全ての層が、230℃
における溶融張力が0.5gより大である樹脂からなること
を特徴とする多層回転成形体である。
That is, in the present invention, all layers except the innermost layer
Is a resin having a melt tension of more than 0.5 g.

ここで溶融張力とは、熱可塑性樹脂の溶融成形加工時
の伸長流動に起因する成形性難易度の判断指標であり、
以下の方法により測定される。
Here, the melt tension is a judgment index of the moldability difficulty due to the elongational flow during melt molding of the thermoplastic resin,
It is measured by the following method.

溶融張力 JIS K7210(MFR試験法)に規定されている加熱炉を用
い、下記の条件で規定寸法のオリフィスからの溶融吐出
樹脂を一定速度で引き取ったときに示される張力を溶融
張力とする。
Melt tension Using a heating furnace specified in JIS K7210 (MFR test method), the tension indicated when the molten resin discharged from the orifice of the specified dimensions is taken out at a constant speed under the following conditions is defined as the melt tension.

測定条件 溶融温度:230℃ 溶融樹脂に加える荷重:2.16kg (シリンダ径0.955cm) オリフィス寸法:直径 0.2095cm 長さ 0.8cm 引取速度:3.9m/分 装置名称:メルトテンションテスター (東洋精機製作所製) 最内層以外の層の材料 本発明で最内層以外の全ての層に使用する材料は230
℃における溶融張力が0.5gより大、好ましくは1gより大
である樹脂より選ぶことが必要である。
Measurement conditions Melting temperature: 230 ° C Load applied to the molten resin: 2.16 kg (cylinder diameter 0.955 cm) Orifice dimensions: diameter 0.2095 cm length 0.8 cm Take-off speed: 3.9 m / min Equipment name: Melt tension tester (Toyo Seiki Seisakusho) Materials of layers other than the innermost layer In the present invention, the material used for all the layers other than the innermost layer is 230
It is necessary to choose from resins whose melt tension at 0 ° C. is greater than 0.5 g, preferably greater than 1 g.

本発明で当該層に用いる230℃における溶融張力が0.5
gより大であるという条件を満たす材料を得るには、例
えばポリエチレンであれば1500kg/cm2以上の圧力下で製
造される高圧法ポリエチレンのうちMFR(190℃、2.16k
g)が10g/10分より低いもの、また、300kg/cm2以下の圧
力で製造される中低圧ポリエチレンのうち前記MFRが10g
/10分より低いものの中から容易に選ぶことが可能であ
る。また該材料としてはポリエチレンに限定されること
はなく、上記の条件を満たすものであればよく、また、
各種の樹脂をブレンドしたものを粉末化したもの、或は
粉末で混合したものでもよい。
The melt tension at 230 ° C. used for the layer in the present invention is 0.5
To obtain a material satisfying the conditions that it is larger than g, such MFR (190 ° C. Among the high-pressure polyethylene manufactured under 1500 kg / cm 2 or more pressure if polyethylene, 2.16K
g) is lower than 10 g / 10 minutes, and the above-mentioned MFR is 10 g among medium- and low-pressure polyethylene produced at a pressure of 300 kg / cm 2 or less.
It is easy to choose from those lower than / 10 minutes. In addition, the material is not limited to polyethylene, as long as it satisfies the above conditions,
Powdered materials obtained by blending various resins, or powdered materials may be used.

最内層の材料 上記多層回転成形体の最内層は多層成形の最後の段階
で成形されるが、本発明で用いられる最内層の原料とし
てはポリオレフィン、エチレン−酢酸ビニル共重合体
(EVA)、ABS樹脂の他、ポリアミド、ポリカーボネー
ト、ポリフッ化ビニリデン等のエンジニアリングプラス
チックス類をも含め、公知の回転成形に用いられる樹脂
なら何でも、その目的に応じて選ぶことができ、特に限
定されるものでなないが、ポリエチレンを例にとれば、
MFR(190℃、2.16kg)が1〜20g/10分までのものが好ま
しく、特に2〜10g/10分の範囲のものがよい。MFRが20
より大きい場合には内表面における樹脂のタレが大きく
なる傾向があり、またMFRが1より小さい場合には内表
面の平滑性が不充分となる傾向がある。なお、勿論上記
の最内層以外の層の材料を最内層の材料に用いても差し
支えない。
Material of innermost layer The innermost layer of the above-mentioned multilayer rotomolded article is formed at the last stage of the multilayer forming, and the raw material of the innermost layer used in the present invention includes polyolefin, ethylene-vinyl acetate copolymer (EVA), ABS In addition to resins, polyamide, polycarbonate, including engineering plastics such as polyvinylidene fluoride, any resin used for known rotary molding can be selected according to the purpose, and is not particularly limited. However, taking polyethylene as an example,
Preferably, the MFR (190 ° C., 2.16 kg) is up to 1 to 20 g / 10 minutes, and particularly preferably in the range of 2 to 10 g / 10 minutes. MFR is 20
If it is larger, the sagging of the resin on the inner surface tends to increase, and if MFR is smaller than 1, the smoothness of the inner surface tends to be insufficient. Of course, a material of a layer other than the above innermost layer may be used as a material of the innermost layer.

回転成形 本発明でいう多層回転成形体は、直接加熱法、間接加
熱法のいずれを問わず、公知の回転成形設備を用いて製
造可能である。
Rotational Molding The multilayer rotationally molded article referred to in the present invention can be produced using a known rotational molding equipment regardless of a direct heating method or an indirect heating method.

回転成形に用いられる樹脂粉末は、その粒径が20〜50
メッシュ以下、好ましくは30〜40メッシュのものが用い
られ、通常、樹脂ペレットを機械粉砕したものが用いら
れるが、重合工程で得られる樹脂粉末をそのまま用いて
もよい。
The resin powder used for rotational molding has a particle size of 20 to 50.
Mesh or less, preferably 30 to 40 mesh, is used. Usually, resin pellets obtained by mechanical pulverization are used, but resin powder obtained in the polymerization step may be used as it is.

最初、回転成形用金型内に第一層(最外層)用の原料
樹脂粉末及び必要に応じて適用量の離形剤粉末を投入
し、公知の回転成形法と同様に、金型を直角方向をなす
二軸を中心として同時に回転あるいは揺動させながら、
直接バーナーで加熱、あるいは間接的に炉内で加熱する
ことにより樹脂を金型の外部から樹脂の融点以上に加熱
溶融して流動性を与え、金型形状に賦形する。
First, the raw material resin powder for the first layer (outermost layer) and, if necessary, an applied amount of the release agent powder are charged into the mold for rotation molding, and the mold is set at a right angle in the same manner as in the known rotation molding method. While simultaneously rotating or swinging around the two axes forming the direction,
The resin is heated and melted from the outside of the mold to a temperature higher than the melting point of the resin by heating directly with a burner or indirectly in a furnace to give fluidity and shape the mold.

賦形がほぼ完了した時点で金型の加熱を中断する。あ
るいは金型を加熱炉内より取り出し、金型の投入口を開
放して、第二層の樹脂原料粉末を投入し、再度回転加熱
しながら第二層樹脂の溶融賦形を行なう。
When the shaping is almost completed, the heating of the mold is stopped. Alternatively, the mold is taken out of the heating furnace, the inlet of the mold is opened, the resin raw material powder of the second layer is charged, and the second layer resin is melt-shaped while rotating and heating again.

製品の層構成の設計に応じて必要ならば第三層以降の
成形を、原理的には何層でも、同じ手順で行なうことが
出来る。
If necessary according to the design of the layer structure of the product, the third and subsequent layers can be formed in the same procedure in principle for any number of layers.

この場合第二層以降の原料投入のための加熱の中断は
極力短時間とすることが層の厚さの均一性の点で好まし
く、望ましくは3分以内、さらに望ましくは1分以内が
よい。
In this case, it is preferable to interrupt the heating for charging the raw material after the second layer as short as possible from the viewpoint of uniformity of the thickness of the layer, preferably within 3 minutes, more preferably within 1 minute.

多層回転成形体 多層回転成形によりつくられる製品の例としては、耐
熱性あるいは耐薬品性を改良したタンク類等があげられ
る。この場合外層には構造材料として、安価なポリオレ
フィン類を使用し、内容物に触れる最内層には耐熱性あ
るいは耐薬品性の優れた樹脂を使用することが考えられ
る。また必要に応じ、中間に接着層を設けることや、製
品の外観を重んじる場合には、最外層を塗装したりシボ
加工することも可能である。
Multi-layer rotational molded article Examples of products produced by multilayer rotational molding include tanks having improved heat resistance or chemical resistance. In this case, it is conceivable that an inexpensive polyolefin is used as a structural material for the outer layer, and a resin having excellent heat resistance or chemical resistance is used for the innermost layer that contacts the contents. If necessary, an adhesive layer may be provided in the middle, and if the appearance of the product is valued, the outermost layer may be painted or textured.

[実施例] 以下の実施例及び比較例において、原料樹脂のMFRは1
90℃、2.16kg荷重での測定値であり、溶融張力は東洋精
機製作所製メルトテンションテスターII型を用い、温度
230℃、押出速度0.716cm3/分、引取速度3.9m/分の条件
で測定した。
[Examples] In the following Examples and Comparative Examples, the MFR of the raw material resin was 1
Measured at 90 ° C under a load of 2.16 kg.The melt tension was measured using a Toyo Seiki Seisakusho's melt tension tester type II.
The measurement was performed at 230 ° C., an extrusion speed of 0.716 cm 3 / min, and a take-up speed of 3.9 m / min.

実施例1 第1表に示すように外層用の樹脂として三菱油化
(株)製高密度ポリエチレン(HDPE)BZ50Aを、また内
層用の樹脂としてペンウオルト社製ポリフッ化ビニリデ
ン(PVDF)カイナー710を、それぞれ機械式粉砕機によ
り粉砕し、30メッシュの金網を通過するが40メッシュの
金網を通過しない粉体を得た。まず外層用の樹脂粉末を
5容量の回転成形用金型に投入し、240℃に維持した
炉内で、金型に回転を与えながら加熱溶融した。溶融が
完了した時点で加熱を一時中断し、金型開口部を開き内
層用の原料樹脂粉末を投入した後、再度240℃の炉内で
金型に回転を与えて樹脂を溶融賦形した。
Example 1 As shown in Table 1, high-density polyethylene (HDPE) BZ50A manufactured by Mitsubishi Yuka Co., Ltd. was used as the resin for the outer layer, and polyvinylidene fluoride (PVDF) Kiner 710 manufactured by Penwort was used as the resin for the inner layer. Each was pulverized by a mechanical pulverizer to obtain a powder that passed through a 30-mesh wire mesh but did not pass through a 40-mesh wire mesh. First, the resin powder for the outer layer was put into a 5-volume rotary molding die, and heated and melted in a furnace maintained at 240 ° C. while rotating the die. When the melting was completed, the heating was temporarily stopped, the opening of the mold was opened, and the raw material resin powder for the inner layer was charged. Then, the mold was again rotated in a furnace at 240 ° C. to melt and shape the resin.

溶融終了後炉内より取り出し、冷却することにより、
第1図のような二層構成の回転成形物を取り出した。層
の構成は外層2が4mm、内層1が1mmの厚みであり、第2
図に示すように厚みが均一で良好なものであった。
By taking out from the furnace after the completion of melting and cooling,
A rotary molded product having a two-layer structure as shown in FIG. 1 was taken out. The outer layer 2 has a thickness of 4 mm and the inner layer 1 has a thickness of 1 mm.
As shown in the figure, the thickness was uniform and good.

実施例2 実施例1における外層用樹脂を高密度ポリエチレンか
ら、同じ高密度ポリエチレンと三菱油化製線状低密度ポ
リエチレン(LLDPE)Z90Hとの重量比で60:40の配合物に
変更した外は実施例1と同様にして成形した。成形物の
断面は第2図に示すように良好であった。
Example 2 Except for changing the resin for the outer layer in Example 1 from a high-density polyethylene to a 60:40 weight ratio of the same high-density polyethylene and Mitsubishi Yuka Linear Low Density Polyethylene (LLDPE) Z90H The molding was performed in the same manner as in Example 1. The cross section of the molded product was good as shown in FIG.

実施例3 実施例2における高密度ポリエチレンと低密度ポリエ
チレンの配合比を30:70に変えた以外は、実施例2と同
様にして成形した。成形物の断面は第2図に示すように
良好であった。
Example 3 Molding was carried out in the same manner as in Example 2 except that the mixing ratio of high-density polyethylene and low-density polyethylene in Example 2 was changed to 30:70. The cross section of the molded product was good as shown in FIG.

比較例1 実施例1における外層用樹脂を高密度ポリエチレンか
ら、三菱油化(株)製線状低密度ポリエチレンZ90Hに変
更した以外は実施例1と同様に成形した。成形物の断面
は第3図にしめすように外層の厚み変動があり、不良で
あった。
Comparative Example 1 A molding was performed in the same manner as in Example 1 except that the resin for the outer layer in Example 1 was changed from high-density polyethylene to linear low-density polyethylene Z90H manufactured by Mitsubishi Yuka Corporation. As shown in FIG. 3, the cross section of the molded product was defective because the thickness of the outer layer varied.

比較例2 実施例1における外層用樹脂を高密度ポリエチレンか
ら、三菱油化(株)製線状低密度ポリエチレンR90Kに変
更した以外は実施例1と同様に成形した。成形物の断面
は第4図に示すように外層に著しい厚み変動があり、不
良であった。
Comparative Example 2 Molding was performed in the same manner as in Example 1 except that the resin for the outer layer in Example 1 was changed from high-density polyethylene to linear low-density polyethylene R90K manufactured by Mitsubishi Yuka Corporation. As shown in FIG. 4, the cross section of the molded product was defective because the outer layer had a remarkable thickness variation.

以上の各実施例及び比較例の原料樹脂のMFR及び溶融
張力の測定値については第1表に示す。
Table 1 shows the measured values of the MFR and the melt tension of the raw material resins of the above Examples and Comparative Examples.

[発明の効果] 本発明によれば多層回転成形を行なう場合に、最内層
以外の樹脂の溶融張力を規制することにより、各層の厚
みの均一な、層構成の優れた回転成形体を得ることがで
きる。
[Effects of the Invention] According to the present invention, when performing multi-layer rotational molding, by controlling the melt tension of the resin other than the innermost layer, it is possible to obtain a rotational molded body having a uniform thickness of each layer and an excellent layer configuration. Can be.

【図面の簡単な説明】[Brief description of the drawings]

第1図は実施例及び比較例で成形された二層の回転成形
ボトルの垂直断面図を示す。第2〜4図は第1図のA部
拡大図である。 1:内層、2:外層
FIG. 1 is a vertical cross-sectional view of a two-layer rotomolded bottle formed in Examples and Comparative Examples. 2 to 4 are enlarged views of a portion A in FIG. 1: Inner layer, 2: Outer layer

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】最内層以外の全ての層が、230℃における
溶融張力が0.5gより大である樹脂からなることを特徴と
する多層回転成形体。
1. A multilayer rotomolded article wherein all layers except the innermost layer are made of a resin having a melt tension at 230 ° C. of more than 0.5 g.
JP13556389A 1989-05-29 1989-05-29 Multi-layer rotary molding Expired - Fee Related JP2739654B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP13556389A JP2739654B2 (en) 1989-05-29 1989-05-29 Multi-layer rotary molding

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP13556389A JP2739654B2 (en) 1989-05-29 1989-05-29 Multi-layer rotary molding

Publications (2)

Publication Number Publication Date
JPH03216A JPH03216A (en) 1991-01-07
JP2739654B2 true JP2739654B2 (en) 1998-04-15

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP13556389A Expired - Fee Related JP2739654B2 (en) 1989-05-29 1989-05-29 Multi-layer rotary molding

Country Status (1)

Country Link
JP (1) JP2739654B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
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KR20190073043A (en) * 2017-12-18 2019-06-26 김문호 Hollow articles for container and manufacturing process thereof

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB9313800D0 (en) * 1993-07-03 1993-08-18 Rover Group A method of rotational moulding and a moulding made thereby
JP5428047B2 (en) * 2009-05-29 2014-02-26 三菱エンジニアリングプラスチックス株式会社 Polycarbonate resin composition pellets for rotational molding

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20190073043A (en) * 2017-12-18 2019-06-26 김문호 Hollow articles for container and manufacturing process thereof
KR102046895B1 (en) * 2017-12-18 2019-12-04 김문호 Hollow articles for container and manufacturing process thereof

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