JPH0325450B2 - - Google Patents
Info
- Publication number
- JPH0325450B2 JPH0325450B2 JP60026187A JP2618785A JPH0325450B2 JP H0325450 B2 JPH0325450 B2 JP H0325450B2 JP 60026187 A JP60026187 A JP 60026187A JP 2618785 A JP2618785 A JP 2618785A JP H0325450 B2 JPH0325450 B2 JP H0325450B2
- Authority
- JP
- Japan
- Prior art keywords
- nylon
- molded article
- foam
- glass fibers
- injection 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.)
- Expired - Lifetime
Links
- 239000003365 glass fiber Substances 0.000 claims description 18
- 239000006260 foam Substances 0.000 claims description 16
- 238000001746 injection moulding Methods 0.000 claims description 9
- 229920006122 polyamide resin Polymers 0.000 claims description 9
- 239000000835 fiber Substances 0.000 claims description 7
- 229920003189 Nylon 4,6 Polymers 0.000 claims description 5
- 229920002302 Nylon 6,6 Polymers 0.000 claims description 4
- 238000002485 combustion reaction Methods 0.000 claims description 2
- 239000008188 pellet Substances 0.000 description 9
- 230000000052 comparative effect Effects 0.000 description 7
- 229910052500 inorganic mineral Inorganic materials 0.000 description 6
- 238000000034 method Methods 0.000 description 6
- 239000011707 mineral Substances 0.000 description 6
- KIDHWZJUCRJVML-UHFFFAOYSA-N putrescine Chemical compound NCCCCN KIDHWZJUCRJVML-UHFFFAOYSA-N 0.000 description 6
- 239000011347 resin Substances 0.000 description 6
- 229920005989 resin Polymers 0.000 description 6
- 238000001125 extrusion Methods 0.000 description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 description 4
- 238000005187 foaming Methods 0.000 description 4
- 239000005700 Putrescine Substances 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 238000005453 pelletization Methods 0.000 description 3
- 238000006116 polymerization reaction Methods 0.000 description 3
- 229920002292 Nylon 6 Polymers 0.000 description 2
- 235000011037 adipic acid Nutrition 0.000 description 2
- 239000001361 adipic acid Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000000945 filler Substances 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229920000642 polymer Polymers 0.000 description 2
- GVNWZKBFMFUVNX-UHFFFAOYSA-N Adipamide Chemical compound NC(=O)CCCCC(N)=O GVNWZKBFMFUVNX-UHFFFAOYSA-N 0.000 description 1
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- JHWNWJKBPDFINM-UHFFFAOYSA-N Laurolactam Chemical compound O=C1CCCCCCCCCCCN1 JHWNWJKBPDFINM-UHFFFAOYSA-N 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Malonic acid Chemical compound OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- 229920000571 Nylon 11 Polymers 0.000 description 1
- 229920000299 Nylon 12 Polymers 0.000 description 1
- 229920000572 Nylon 6/12 Polymers 0.000 description 1
- -1 Polytetramethylene Polymers 0.000 description 1
- 239000003963 antioxidant agent Substances 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 229910052918 calcium silicate Inorganic materials 0.000 description 1
- 239000000378 calcium silicate Substances 0.000 description 1
- OYACROKNLOSFPA-UHFFFAOYSA-N calcium;dioxido(oxo)silane Chemical compound [Ca+2].[O-][Si]([O-])=O OYACROKNLOSFPA-UHFFFAOYSA-N 0.000 description 1
- 239000002666 chemical blowing agent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 150000004985 diamines Chemical class 0.000 description 1
- 229910001873 dinitrogen Inorganic materials 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 239000004088 foaming agent Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 238000011835 investigation Methods 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 150000003951 lactams Chemical class 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 238000012643 polycondensation polymerization Methods 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000007790 solid phase Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
- F05C—INDEXING SCHEME RELATING TO MATERIALS, MATERIAL PROPERTIES OR MATERIAL CHARACTERISTICS FOR MACHINES, ENGINES OR PUMPS OTHER THAN NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES
- F05C2225/00—Synthetic polymers, e.g. plastics; Rubber
- F05C2225/08—Thermoplastics
Landscapes
- Cylinder Crankcases Of Internal Combustion Engines (AREA)
- Manufacture Of Porous Articles, And Recovery And Treatment Of Waste Products (AREA)
- Injection Moulding Of Plastics Or The Like (AREA)
Description
【発明の詳細な説明】
(目的)
本発明は反りの改良されたポリアミド樹脂発泡
成形体に関する。
(従来技術)
ポリアミド樹脂はその優れた耐熱性および耐油
性から自動車部品を中心とする内燃機関部品に広
く使用されており、エンジンルーム内で使用され
る部品、たとえばシリンダーヘツドカバー、トラ
ンスミツシヨンカバー、インテークマニホールド
といつたシール性を要求される大型部品への展開
が積極的に試みられている。
これらの製品は大型部品であり、1個当りの単
量が大きく、また使用環境も厳しいことからガラ
ス繊維で補強された発泡体が最適と考えられる。
しかしながら、通常のチヨツプトストランドあ
るいはロービングタイプのガラス繊維(以後、通
常のガラス繊維と呼称する)を充填したポリアミ
ド樹脂ペレツトからこのような大型品を射出成形
すると、ガラス繊維の配向のため一般に反りが発
生し易く、これが欠点とされていた。反りに関し
ては発泡体でも事情は同じであり、成形品デザイ
ンによつては反りが解消されないケースが多くこ
れの改良が求められている。
ところで、各種充填材で補強されたポリアミド
樹脂射出成形品の反りを材料面から改良する手段
としては、発泡させない成形品の場合、粒状ある
いはL/Dの小さいミネラルを充填したり、通常
のガラス繊維とこれらミネラルを併用して用いる
ことが一般に行なわれている。しかしながら本発
明者が検討したところ、発泡体においてはこれら
の手法は適用できないことがわかつた。即ち、粒
状あるいはL/Dの小さいミネラルを用いた糸
は、確かに反りは改良するものの均一な発泡状態
を得ることができないこと、また通常のガラス繊
維と粒状あるいはL/Dの小さいミネラルを併用
した糸は、反りという面からも均一な発泡状態と
いう面からも不充分であることがわかつた。
このような実状に鑑み、本発明者は均一な発泡
状態を有し、しかも反りのない自動車のエンジン
ルーム内の大型部品に使用可能な発泡成形体を得
ることを目的に鋭意検討を行ない本発明に到達し
た。
(発明の構成、効果)
即ち、本発明者はL/Dが4以上15以下と特定
の範囲内にあるガラス繊維を、重量で13%以上50
%以下含有するポリアミド樹脂を発泡射出成形す
ることで、反り小さく、均一な発泡状態の成形体
を得ることができ、さらにポリアミド樹脂として
ナイロン46あるいはナイロン66を使用することで
自動車のエンジンルーム内で高温部と接触して使
用可能な耐熱性を得ることができることを見出
し、本発明に到達した。
以下に本発明を詳細に説明する。
本発明でいうL/Dが4以上15以下のガラス繊
維とは、ガラス繊維業会においてミルドフアイバ
ーと通称されているものであり、ガラス長繊維を
特定の長さになるように粉砕したものをさす。
L/Dの値は押出機で混練ペレタイズ化された状
態における値で、L/Dが4以上15以上の意味
は、この範囲に存在する繊維の比率が重量分率で
80%以上存在することをさす。L/Dがこの範囲
から上にはずれると成形時の収縮の異方性が顕著
になり反りが発生し易くなるため好ましくなく、
L/Dがこの範囲から下にずれると均一な発泡状
態が得られなくなるため好ましくない。
本発明でいうポリアミド樹脂は、反りの小さい
均一な発泡状態の発泡体を得る目的からは特に限
定されるものではなく、ジアミンとジカルボン酸
の縮重合で得られるナイロン46、ナイロン66、ナ
イロン612等、ラクタムの重合で得られるナイロ
ン6、ナイロン11、ナイロン12等、あるいはこれ
らのコポリマー、ブレンド物等を使用することが
できる。耐熱性の要求される用途には融点の高い
ナイロン46またはナイロン66が最も好ましい。
また、これらポリアミド樹脂はその組成中に酸
化防止剤、染顔料、耐侯剤、滑剤、可塑剤等を含
有していてもよい。
本発明でいう発泡体は、通常シヨートシヨツト
法と射出成形業会で呼称される化学発泡剤を含有
する樹脂ペレツトを射出成形機内で可塑化溶融
し、これを金型内に完全に充満しないように高速
充填し、発泡ガスの圧力を利用してキヤビテイー
内に充満させ発泡体を得る方法で最も簡便に得ら
れるが、特にこれに限定されるものではなく公知
の任意の発泡射出成形法で得ることができる。ま
た、発泡の程度は使用目的に応じて決定するため
特に限定されるものではないが、通常15%ないし
40%の気泡率(発泡体内の空間部の体積比率)に
おいて良好なセルの発泡体を得ることができる。
(実施例)
以下に本発明を実施例を用いて説明する。
〔実施例1〕
1.4−ジアミノブタンとアジピン酸から相対粘
度ηrel=3.0(25℃、95.5%硫酸中1重量%溶液)
のナイロン46(ポリテトラメチレンアジプアミド)
を重合した。重合はまず1.4−ジアミノブタンを
6mol%過剰に含ませた形で1.4−ジアミノブタン
とアジピン酸とを200℃〜220℃の温度下で3時間
反応させもろい固体状態のプレポリマーを得、次
いでこのプレポリマーを常圧、窒素ガスブロー下
で温度260℃3時間固相重合し最終ポリマー化し
た。得られたナイロン46にミルドフアイバー(径
13μm)33重量%を添加し、溶融樹脂温度が310℃
の条件下で押出機を通しペレツト化した。得られ
たペレツトを硫酸で溶解後ガラス繊維長を測定し
たところ、数平均繊維長は70μmでL/Dが4以
上15以下のものの重量比率は95%であつた。この
ペレツト表面に発泡剤として5フエニルテトラゾ
ルを0.3%ドライブレンドし、シヨートシヨツト
法で平均肉厚4mm、長さ330mm、幅110mm、高さ60
mmの箱状成形品を底部両端部から2点ピンゲート
方式で、平均気泡率が25%になるように、溶融樹
脂温度310℃の条件下で発泡射出成形した。
得られた箱状成形品を底面を上にして定盤上に
置き、側壁フランジ部の定盤面からの浮き上がり
の最大値をダイヤルゲージで測定した。次いで成
形品のセル状態を観察するために、500wの写真
撮影用ライトを用い成形品の裏面から光を当て、
肉眼で目視できる気泡の存在を、また成形品断面
のセル状態を走査型電子顕微鏡で観察した。さら
に成形品を200℃のギヤオーブン中に10時間放置
し、形態変化を中心に耐熱性を目視判定した。
〔実施例2〕
実施例1において、ナイロン46のかわりに相対
粘度ηrel=2.8のナイロン66を使用し、押出ペレ
タイズおよび射出成形条件を溶融樹脂温度290℃
とする以外は実施例1と同様に実施した。押出で
得られたペレツト内のガラス繊維長は、数平均長
で80μm、L/Dが4以上15以下のものの重量比
率は95%であつた。
〔比較例1〕
実施例2において、使用するミルドフアイバー
の添加量を10重量%とする以外は実施例2と同様
に実施した。
〔比較例2〕
実施例2において、ガラス繊維を径13μm3mm長
のチヨツプトストランド33重量%添加とする以外
は実施例2と同様に実施した。押出で得られたペ
レツト内のガラス繊維長は、数平均長で約
250μm、L/Dが15以上のものの重量比率は80%
であつた。
〔比較例3〕
実施例2において、添加するフイラーをケイ酸
カルシウム粉末33重量%とする外は実施例2と同
様に実施した。
〔比較例4〕
比較例2において、使用するポリマーをナイロ
ン6(ηrel=2.8)とし、押出ペレタイズおよび射
出成形時の溶融樹脂温度を260℃とする以外は、
比較例2と同様に実施した。押出で得られたペレ
ツト内のガラス繊維長は、数平均長で300μm、
L/Dが15以上のものの重量比率は90%であつ
た。
以上の各実施例、比較例の結果を第1表に示
す。
この表に示されたように特定のL/Dを有する
ガラス繊維で補強された糸は極めて満足できる効
果を示した。
【表】DETAILED DESCRIPTION OF THE INVENTION (Objective) The present invention relates to a polyamide resin foam molded article with improved warpage. (Prior art) Polyamide resin is widely used in internal combustion engine parts, mainly automobile parts, due to its excellent heat resistance and oil resistance, and is used in parts used in the engine room, such as cylinder head covers and transmission covers. Active efforts are being made to apply this technology to large parts that require good sealing, such as intake manifolds. Since these products are large parts, the amount per piece is large, and the environment in which they are used is harsh, a foam reinforced with glass fiber is considered optimal. However, when injection molding such large items from polyamide resin pellets filled with conventional chopped strand or roving type glass fibers (hereinafter referred to as conventional glass fibers), warpage generally occurs due to the orientation of the glass fibers. This was considered to be a drawback. Regarding warpage, the situation is the same with foams, and depending on the molded product design, there are many cases in which warpage cannot be eliminated, and improvements in this problem are required. By the way, as a means to improve the warpage of polyamide resin injection molded products reinforced with various fillers from a material standpoint, in the case of non-foamed molded products, it is possible to fill them with granular or minerals with a small L/D, or to fill them with ordinary glass fiber. It is common practice to use these minerals in combination. However, upon investigation by the present inventor, it was found that these methods cannot be applied to foams. In other words, threads using granular minerals or minerals with a small L/D do improve warpage, but cannot obtain a uniform foamed state, and threads that use granular minerals or minerals with a small L/D in combination with ordinary glass fibers The resulting yarn was found to be insufficient in terms of both warping and uniform foaming. In view of these circumstances, the present inventor has conducted extensive studies with the aim of obtaining a foam molded product that has a uniform foaming state and is free from warping and can be used for large parts in the engine room of an automobile, and has developed the present invention. reached. (Structure and Effect of the Invention) That is, the present inventor uses glass fibers whose L/D is within a specific range of 4 or more and 15 or less, by weight of 13% or more and 50% or more.
By foam injection molding polyamide resin containing less than The present invention was achieved by discovering that it is possible to obtain usable heat resistance by contacting a high-temperature part. The present invention will be explained in detail below. The glass fiber with an L/D of 4 or more and 15 or less as used in the present invention is commonly referred to as milled fiber in the glass fiber industry association, and is made by pulverizing long glass fibers to a specific length. As expected.
The value of L/D is the value in the state of kneading and pelletizing with an extruder, and the meaning of L/D of 4 or more and 15 or more is that the ratio of fibers existing in this range is the weight fraction.
Refers to the presence of 80% or more. If L/D deviates above this range, the anisotropy of shrinkage during molding becomes noticeable and warping is likely to occur, which is undesirable.
If L/D deviates below this range, it is not preferable because a uniform foamed state cannot be obtained. The polyamide resin referred to in the present invention is not particularly limited for the purpose of obtaining a uniformly foamed foam with little warpage, and includes nylon 46, nylon 66, nylon 612, etc. obtained by condensation polymerization of diamine and dicarboxylic acid. , nylon 6, nylon 11, nylon 12, etc. obtained by polymerization of lactam, or copolymers, blends, etc. of these can be used. For applications requiring heat resistance, nylon 46 or nylon 66, which have a high melting point, are most preferred. Further, these polyamide resins may contain antioxidants, dyes and pigments, weatherproofing agents, lubricants, plasticizers, etc. in their compositions. The foam referred to in the present invention is produced by plasticizing and melting resin pellets containing a chemical blowing agent in an injection molding machine, which is usually referred to as the shot shot method by the injection molding industry, and is made by plasticizing and melting the resin pellets in a mold so as not to completely fill the mold. The foam can be obtained most simply by filling the cavity at high speed and using the pressure of foaming gas to obtain a foam, but is not limited to this method, and can be obtained by any known foam injection molding method. I can do it. In addition, the degree of foaming is determined depending on the purpose of use and is not particularly limited, but it is usually 15% or more.
A foam with good cells can be obtained at a cell ratio of 40% (volume ratio of spaces within the foam). (Example) The present invention will be described below using examples. [Example 1] Relative viscosity ηrel = 3.0 from 1,4-diaminobutane and adipic acid (25°C, 1% by weight solution in 95.5% sulfuric acid)
Nylon 46 (Polytetramethylene adipamide)
was polymerized. Polymerization begins with 1,4-diaminobutane.
1,4-diaminobutane and adipic acid were reacted in excess of 6 mol% at a temperature of 200°C to 220°C for 3 hours to obtain a brittle solid prepolymer, and then this prepolymer was subjected to nitrogen gas blowing at normal pressure. Solid phase polymerization was carried out at 260°C for 3 hours to form the final polymer. Milled fiber (diameter
13μm) 33% by weight was added, and the melt resin temperature was 310℃.
It was pelletized through an extruder under the following conditions. After dissolving the obtained pellets in sulfuric acid, the glass fiber length was measured, and the number average fiber length was 70 μm, and the weight ratio of pellets with L/D of 4 to 15 was 95%. 0.3% 5-phenyltetrasol was dry-blended on the surface of the pellet as a foaming agent, and the average thickness was 4 mm, length was 330 mm, width was 110 mm, and height was 60 mm.
A box-shaped molded product having a diameter of 1.5 mm was foam injection molded from both ends of the bottom using a two-point pin gate method at a molten resin temperature of 310° C. so that the average bubble ratio was 25%. The obtained box-shaped molded product was placed on a surface plate with the bottom facing up, and the maximum value of the rise of the side wall flange portion from the surface of the surface plate was measured using a dial gauge. Next, in order to observe the cell state of the molded product, a 500W photography light was used to shine light from the back of the molded product.
The presence of bubbles visible to the naked eye and the state of cells in the cross section of the molded product were observed using a scanning electron microscope. Furthermore, the molded product was left in a gear oven at 200°C for 10 hours, and the heat resistance was visually evaluated, focusing on changes in shape. [Example 2] In Example 1, nylon 66 with a relative viscosity ηrel = 2.8 was used instead of nylon 46, and the extrusion pelletizing and injection molding conditions were set to a molten resin temperature of 290°C.
It was carried out in the same manner as in Example 1 except that. The number average length of glass fibers in the pellets obtained by extrusion was 80 μm, and the weight ratio of glass fibers with L/D of 4 to 15 was 95%. [Comparative Example 1] The same procedure as in Example 2 was carried out except that the amount of milled fiber used was 10% by weight. [Comparative Example 2] Example 2 was carried out in the same manner as in Example 2, except that glass fibers were added in an amount of 33% by weight of chopped strands with a diameter of 13 μm and a length of 3 mm. The number average length of glass fibers in the pellets obtained by extrusion is approximately
Weight ratio of 250μm and L/D of 15 or more is 80%
It was hot. [Comparative Example 3] The same procedure as in Example 2 was carried out except that the filler added was 33% by weight of calcium silicate powder. [Comparative Example 4] In Comparative Example 2, the polymer used was nylon 6 (ηrel=2.8), and the molten resin temperature during extrusion pelletizing and injection molding was 260°C.
It was carried out in the same manner as Comparative Example 2. The number average length of glass fibers in the pellets obtained by extrusion is 300 μm.
The weight ratio of those with L/D of 15 or more was 90%. Table 1 shows the results of the above examples and comparative examples. As shown in this table, glass fiber reinforced yarns with specific L/D showed very satisfactory effects. 【table】
Claims (1)
以下のガラス繊維を13重量%以上50重量%以下充
填したポリアミド樹脂を用いて発泡射出成形され
た成形体。 2 ポリアミド樹脂がナイロン46あるいはナイロ
ン66であるところの発泡射出成形された特許請求
の範囲第1項記載の成形体。 3 成形体が内燃機関用のシリンダーヘツドカバ
ーあるいはインテークマニホールドである特許請
求の範囲第1項又は第2項記載の成形体。[Claims] 1. The ratio L/D of fiber length (L) to fiber diameter (D) is 4 or more15
A molded article made by foam injection molding using a polyamide resin filled with the following glass fibers in an amount of 13% to 50% by weight. 2. The molded article according to claim 1, which is formed by foam injection molding, and the polyamide resin is nylon 46 or nylon 66. 3. The molded article according to claim 1 or 2, wherein the molded article is a cylinder head cover or intake manifold for an internal combustion engine.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60026187A JPS61188433A (en) | 1985-02-15 | 1985-02-15 | Polyamide resin foam improved in warpage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP60026187A JPS61188433A (en) | 1985-02-15 | 1985-02-15 | Polyamide resin foam improved in warpage |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61188433A JPS61188433A (en) | 1986-08-22 |
| JPH0325450B2 true JPH0325450B2 (en) | 1991-04-08 |
Family
ID=12186499
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP60026187A Granted JPS61188433A (en) | 1985-02-15 | 1985-02-15 | Polyamide resin foam improved in warpage |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61188433A (en) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6439457U (en) * | 1987-09-02 | 1989-03-09 | ||
| JPH087078Y2 (en) * | 1987-09-16 | 1996-02-28 | 愛知機械工業株式会社 | Cylinder head cover |
| JP2518275Y2 (en) * | 1988-04-18 | 1996-11-27 | 内山工業 株式会社 | Cylinder head structure |
| JPH1058573A (en) * | 1996-08-20 | 1998-03-03 | Sumitomo Chem Co Ltd | Fiber-reinforced thermoplastic resin foam molded article and method for producing the same |
| KR20040020668A (en) * | 2002-08-31 | 2004-03-09 | 현대자동차주식회사 | Method for manufacturing intake manifold for noise reduction |
| EP2570454B1 (en) * | 2010-05-10 | 2019-09-18 | Nitto Boseki CO., LTD. | Method of foam molding of resin reinforced with flat glass fibers |
-
1985
- 1985-02-15 JP JP60026187A patent/JPS61188433A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61188433A (en) | 1986-08-22 |
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