JPH03216A - Multi-layered rotationally molded body - Google Patents
Multi-layered rotationally molded bodyInfo
- Publication number
- JPH03216A JPH03216A JP13556389A JP13556389A JPH03216A JP H03216 A JPH03216 A JP H03216A JP 13556389 A JP13556389 A JP 13556389A JP 13556389 A JP13556389 A JP 13556389A JP H03216 A JPH03216 A JP H03216A
- Authority
- JP
- Japan
- Prior art keywords
- layer
- mold
- resin
- layered
- molding
- 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
- 229920005989 resin Polymers 0.000 claims abstract description 39
- 239000011347 resin Substances 0.000 claims abstract description 39
- 239000000155 melt Substances 0.000 claims abstract description 10
- 238000000465 moulding Methods 0.000 abstract description 16
- 239000000843 powder Substances 0.000 abstract description 13
- 239000000463 material Substances 0.000 abstract description 12
- 238000001175 rotational moulding Methods 0.000 abstract description 11
- 238000010438 heat treatment Methods 0.000 abstract description 10
- 238000000034 method Methods 0.000 abstract description 9
- 238000002844 melting Methods 0.000 abstract description 6
- 230000008018 melting Effects 0.000 abstract description 6
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 abstract description 3
- 239000005038 ethylene vinyl acetate Substances 0.000 abstract description 3
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 abstract description 3
- 229920000098 polyolefin Polymers 0.000 abstract description 3
- 239000002184 metal Substances 0.000 abstract 1
- 239000010410 layer Substances 0.000 description 54
- 229920001903 high density polyethylene Polymers 0.000 description 7
- 239000004700 high-density polyethylene Substances 0.000 description 7
- -1 polyethylene Polymers 0.000 description 6
- 239000004698 Polyethylene Substances 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 5
- 229920000573 polyethylene Polymers 0.000 description 5
- 229920000092 linear low density polyethylene Polymers 0.000 description 4
- 239000004707 linear low-density polyethylene Substances 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000004952 Polyamide Substances 0.000 description 2
- 230000002950 deficient Effects 0.000 description 2
- 229920001684 low density polyethylene Polymers 0.000 description 2
- 239000004702 low-density polyethylene Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 229920002647 polyamide Polymers 0.000 description 2
- 229920000515 polycarbonate Polymers 0.000 description 2
- 239000004417 polycarbonate Substances 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 238000007493 shaping process Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229920007450 Kynar® 710 Polymers 0.000 description 1
- 239000002033 PVDF binder Substances 0.000 description 1
- 239000004676 acrylonitrile butadiene styrene Substances 0.000 description 1
- 239000012790 adhesive layer Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229920006351 engineering plastic Polymers 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000011229 interlayer Substances 0.000 description 1
- 229920001179 medium density polyethylene Polymers 0.000 description 1
- 239000004701 medium-density polyethylene Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000006082 mold release agent Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 229920002981 polyvinylidene fluoride Polymers 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 239000002356 single layer Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
- 229920005992 thermoplastic resin Polymers 0.000 description 1
Landscapes
- Laminated Bodies (AREA)
- Moulding By Coating Moulds (AREA)
Abstract
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。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a multilayer rotomolded body obtained by a new molding method, and more specifically, to an excellent multilayer rotomolded body with a uniform interlayer thickness structure. It is related to.
[従来の技術]
従来より1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。[Conventional technology] Conventionally, the single-turn molding method has lower mold manufacturing costs than other molding methods, so it is suitable for obtaining large molded products in high-mix, low-volume production. It is preferred for manufacturing large tanks made of stainless steel.
この回転成形法に用いられている樹脂とじては、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 resins used in this rotational molding method include high-density, medium-density, or low-density polyethylene, EVA, ABS,
They were polyamide, polycarbonate, etc.
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。In rotomolding, if different types of resins are combined to produce a multilayer rotomolded product, it is expected that by taking advantage of the characteristics of each resin, it will be possible to obtain superior properties not found in current single-layer rotomolded products. .
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。Attempts were made to do so, but due to the following technical difficulties,
At present, it has hardly been commercialized.
[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全型内溶融
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。[Problem to be solved by the invention] That is, the biggest technical difficulty is that the principle of shaping in the rotational molding method depends only on the natural flowability of the entire molten resin in the mold under gravity. Therefore, it is difficult to obtain a uniform thickness structure of each layer as in other multilayer molding methods, such as coextrusion molding.
本発明者等はその理由に関し種々検討した結果2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 inventors of the present invention have conducted various studies regarding the reason. 2. After the molding of the layers other than the innermost layer is completed, and while the molding of each layer is continued until the subsequent stage reaches the innermost layer, It has been found that the viscosity of the layer decreases due to the increase in temperature of the layer during additional heating, and that excessive fluidity is the main cause of disturbance in 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 Problem] As a result of intensive studies on this point, the inventors have discovered that by regulating the melt tension of the resin used for layers other than the innermost layer in rotational molding, the thickness structure of each layer can be made uniform. The present invention was completed by discovering that a multilayer rotomolded body of excellent quality could 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 are heated to 230°C.
This is a multilayer rotomolded body characterized by being made of 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, melt tension is an index for determining the degree of moldability difficulty due to elongation flow during melt molding processing of a thermoplastic resin, and is measured by the following method.
1敗張力
JIS K7210fMFR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。Using a heating furnace specified in 1 failure tension (JIS K7210fMFR test method), the melt tension is the tension shown when the melted discharged resin is withdrawn from an orifice of specified dimensions at a constant speed under the following conditions.
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
.955cn+)
オリフィス寸法:直径 0.2095cIT+長さ 0
.8cm
引取速度: 3.9 m7分
装置名称:メルトテンションテスター
(東洋精機製作新製)
最 層以 の層の 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℃ Load applied to molten resin: 2.16kg (cylinder diameter 0
.. 955cn+) Orifice dimensions: Diameter 0.2095cIT+Length 0
.. 8 cm Take-up speed: 3.9 m7 minutes Equipment name: Melt tension tester (newly manufactured by Toyo Seiki Seisakusho) Materials for layers below the innermost layer In the present invention, the material used for all layers except the innermost layer is 230
melt tension at °C greater than 0.5 g, preferably 1 g
It is necessary to choose a resin that is larger.
本発明で当該層に用いる230℃における溶融張力が0
.5gより大であるという条件を満たす材料を得るには
2例えばポリエチレンであれば1500kg/cm”以
上の圧力下で製造される高圧法ポリエチレンのうちM
F R(190℃、2.16kg)が10g710分よ
り低いもの、また、300kg/cm”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l。The melt tension at 230°C used for the layer in the present invention is 0.
.. To obtain a material that satisfies the condition that the weight is greater than 5g, 2. For example, in the case of polyethylene, M of high-pressure polyethylene manufactured under a pressure of 1500kg/cm or more
F R (190°C, 2.16 kg) is lower than 10 g 710 minutes, and among medium and low pressure polyethylene produced at a pressure of 300 kg/cm" or less, the MFR is 1.
g710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。It is possible to easily select from among those lower than g710 minutes. The material is not limited to polyethylene, but may be any material that satisfies the above conditions, and may include powdered blends of various resins,
Alternatively, it may be mixed as a powder.
膜力」B(社)佳赳
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1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(E
VA)、ABS樹脂の他、ポリアミ阻ポリカーボネート
、ポリフッ化ビニJ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〜lOg/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太き(なる傾向があり、またM
FR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。The innermost layer of the above-mentioned multilayer rotomolded body is molded at the last stage of multilayer molding.The raw materials for the innermost layer used in the present invention include polyolefin and ethylene-vinyl acetate copolymer. (E
VA), ABS resin, as well as engineering plastics such as polyamide polycarbonate and polyvinylene fluoride, any resin used for known rotational molding can be selected depending on the purpose, and there are no particular limitations. If we take polyethylene as an example,
MFR (190℃, 2.16kg) is 1-20g/10
It is preferable to use up to 10 minutes, especially in the range of 2 to 10 g/10 minutes. If the MFR is larger than 20, the resin sag on the inner surface tends to be thick and the MFR
When FR is less than 1, the smoothness of the inner surface tends to be insufficient. Note that, of course, materials for layers other than the above-mentioned innermost layer may be used as the material for the innermost layer.
旦翫成形
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。The multilayer rotomolded article referred to in the present invention can be produced using known rotomolding equipment, regardless of whether it is 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20〜5
0メツシユ以下、好ましくは30〜40メツシユのもの
が用いられ、通常、樹脂ベ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 5
A material having a mesh size of 0 mesh or less, preferably 30 to 40 meshes is used, and usually a mechanically pulverized resin pellet is used, but the resin powder obtained in the polymerization process 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当量の離形剤粉末を投入し、
公知の回転成形法と同様?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・けを与え、金型形状に賦形する。First, raw resin powder for the first layer (outermost layer) and an appropriate amount of mold release agent powder as needed are put into a rotary molding mold.
Is it similar to the known rotational molding method? The resin is heated and melted from the outside of the mold to a temperature above the melting point of the resin by heating the mold directly with a burner or indirectly in a furnace while simultaneously rotating or swinging the mold around two axes that are perpendicular to each other. The material is flowed and blown, and shaped into a mold shape.
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 shaping is almost completed, heating of the mold is stopped. Alternatively, the mold is taken out of the heating furnace, the injection port of the mold is opened, the resin raw material powder for the second layer is introduced, and the second layer resin is melted and shaped while being rotated and heated 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。In principle, any number of layers after the third layer can be formed using the same procedure if necessary depending on the design of the layer structure of the product.
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 that the interruption of heating for inputting raw materials for the second and subsequent layers be as short as possible from the viewpoint of uniformity of layer thickness, preferably within 3 minutes, and 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じては、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。Examples of products made by multilayer rotational molding include tanks with improved heat resistance or chemical resistance. In this case, it is conceivable to use an inexpensive polyolefin as a structural material for the outer layer, and to use a resin with excellent heat resistance or chemical resistance for the innermost layer that comes into contact with the contents. Furthermore, if necessary, an adhesive layer may be provided in the middle, and if the appearance of the product is important, 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
190℃、2.16kg荷重での測定値であり、溶融張
力は東洋精機製作所持メルトテンションテスターII型
を用い、温度230℃、押出速度0.716ctm3/
分、引取速度3−9 m7分の条件で測定した。[Example] In the following Examples and Comparative Examples, the MFR of the raw resin is a value measured at 190°C and a load of 2.16 kg, and the melt tension is measured at a temperature of 230°C using a melt tension tester type II owned by Toyo Seiki. , extrusion speed 0.716ctm3/
The measurement was carried out under conditions of 3-9 m and 7 minutes of take-up speed.
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■矢高
密度ポリエチレン[DPEI B Z 50Aを、また
内層用の樹脂としてペンウォルト社製ポリフッ化ビニリ
デン(PVDFJカイナー710を、それぞれ機械式粉
砕機により粉砕し、 30メツシユの金網を通過するが
40メツシユ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5R容量の回転成形用金型に投入し、2
40℃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, Mitsubishi Yuka High Density Polyethylene [DPEI B Z 50A] was used as the resin for the outer layer, and polyvinylidene fluoride (PVDFJ Kynar 710 manufactured by Penwald Co., Ltd.) was used as the resin for the inner layer. The powder was pulverized using a type 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 rotary molding mold with a capacity of 2
The mold was heated and melted in a furnace maintained at 40° C. while rotating the mold. When the melting was completed, the heating was temporarily interrupted, the mold opening was opened, and the raw material resin powder for the inner layer was introduced, and then the mold was rotated again in the 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l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
。After the melting was completed, the product was taken out of the furnace and cooled to give a rotomolded product having a two-layer structure as shown in FIG. 1. The layer structure was such that the outer layer 2 had a thickness of 4 mm and the inner layer 1 had a thickness of 1 mm, and as shown in FIG. 2, 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 The resin for the outer layer in Example 1 was changed from high-density polyethylene to the same high-density polyethylene and Mitsubishi Yuka's linear low-density polyethylene + LLDPE) Z90H at a weight ratio of 60:
Molding was carried out in the same manner as in Example 1 except that the mixture was changed to No. 40. 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。Example 3 Example 2 except that the blending ratio of high-density polyethylene and low-density polyethylene was changed to 30:70.
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。It was molded in the same manner as in Example 2. 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■製線状低密度ポリエチレン290F(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 Molding was carried out 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 290F (manufactured by Mitsubishi Yuka Corporation). The cross section of the molded product is shown in Figure 3. As shown in the figure, there was a variation in the thickness of the outer layer, indicating that the product was defective.
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■製線状低密度ポリエチレン890K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 carried out 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 890K manufactured by Mitsubishi Yuka. As shown in FIG. 4, the cross section of the molded product was found to be defective, with significant thickness variations in the outer layer.
以上の各実施例及び比較例の原料樹脂のVFR及び溶融
張力の測定値については第1表に示す。Measured values of VFR and melt tension of the raw resins of each of the above Examples and Comparative Examples are shown in Table 1.
[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 carrying out multilayer rotational molding, by regulating the melt tension of resins other than the innermost layer, it is possible to obtain a rotationally molded body with uniform thickness of each layer and excellent layer structure. I can do it.
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。
l:内層 2:外層FIG. 1 shows a vertical cross-sectional view of two-layer rotomolded bottles molded in Examples and Comparative Examples. 2 to 4 are enlarged views of section A in FIG. 1. l: Inner layer 2: Outer layer
Claims (1)
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 characterized in that all layers other than the innermost layer are made of a resin having a melt tension of more than 0.5 g at 230°C.
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 true JPH03216A (en) | 1991-01-07 |
JP2739654B2 JP2739654B2 (en) | 1998-04-15 |
Family
ID=15154738
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 (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1995001862A1 (en) * | 1993-07-03 | 1995-01-19 | Rover Group Limited | A method of rotational moulding and a moulding made thereby |
JP2010275462A (en) * | 2009-05-29 | 2010-12-09 | Mitsubishi Engineering Plastics Corp | Polycarbonate resin composition for rotational molding and pellet |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR102046895B1 (en) * | 2017-12-18 | 2019-12-04 | 김문호 | Hollow articles for container and manufacturing process thereof |
-
1989
- 1989-05-29 JP JP13556389A patent/JP2739654B2/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1995001862A1 (en) * | 1993-07-03 | 1995-01-19 | Rover Group Limited | A method of rotational moulding and a moulding made thereby |
JP2010275462A (en) * | 2009-05-29 | 2010-12-09 | Mitsubishi Engineering Plastics Corp | Polycarbonate resin composition for rotational molding and pellet |
Also Published As
Publication number | Publication date |
---|---|
JP2739654B2 (en) | 1998-04-15 |
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