JP2000178441A - Polyamide resin composition, and formed product thereof - Google Patents
Polyamide resin composition, and formed product thereofInfo
- Publication number
- JP2000178441A JP2000178441A JP35783998A JP35783998A JP2000178441A JP 2000178441 A JP2000178441 A JP 2000178441A JP 35783998 A JP35783998 A JP 35783998A JP 35783998 A JP35783998 A JP 35783998A JP 2000178441 A JP2000178441 A JP 2000178441A
- Authority
- JP
- Japan
- Prior art keywords
- polyamide resin
- weight
- aspect ratio
- glass fiber
- resin composition
- 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
- 229920006122 polyamide resin Polymers 0.000 title claims abstract description 78
- 239000011342 resin composition Substances 0.000 title claims abstract description 36
- 239000003365 glass fiber Substances 0.000 claims abstract description 91
- 239000000835 fiber Substances 0.000 claims abstract description 38
- 238000002425 crystallisation Methods 0.000 claims abstract description 14
- 230000008025 crystallization Effects 0.000 claims abstract description 14
- NAQMVNRVTILPCV-UHFFFAOYSA-N hexane-1,6-diamine Chemical compound NCCCCCCN NAQMVNRVTILPCV-UHFFFAOYSA-N 0.000 claims description 46
- QQVIHTHCMHWDBS-UHFFFAOYSA-N isophthalic acid Chemical compound OC(=O)C1=CC=CC(C(O)=O)=C1 QQVIHTHCMHWDBS-UHFFFAOYSA-N 0.000 claims description 32
- WNLRTRBMVRJNCN-UHFFFAOYSA-N adipic acid Chemical compound OC(=O)CCCCC(O)=O WNLRTRBMVRJNCN-UHFFFAOYSA-N 0.000 claims description 24
- 239000000203 mixture Substances 0.000 claims description 23
- 229920001577 copolymer Polymers 0.000 claims description 19
- 235000011037 adipic acid Nutrition 0.000 claims description 12
- 239000001361 adipic acid Substances 0.000 claims description 12
- 238000002347 injection Methods 0.000 claims description 6
- 239000007924 injection Substances 0.000 claims description 6
- FQLAJSQGBDYBAL-UHFFFAOYSA-N 3-(azepane-1-carbonyl)benzamide Chemical compound NC(=O)C1=CC=CC(C(=O)N2CCCCCC2)=C1 FQLAJSQGBDYBAL-UHFFFAOYSA-N 0.000 claims description 5
- DJZKNOVUNYPPEE-UHFFFAOYSA-N tetradecane-1,4,11,14-tetracarboxamide Chemical compound NC(=O)CCCC(C(N)=O)CCCCCCC(C(N)=O)CCCC(N)=O DJZKNOVUNYPPEE-UHFFFAOYSA-N 0.000 claims description 5
- 239000000047 product Substances 0.000 description 30
- 239000008188 pellet Substances 0.000 description 25
- 229920002302 Nylon 6,6 Polymers 0.000 description 20
- 238000011156 evaluation Methods 0.000 description 15
- 238000004519 manufacturing process Methods 0.000 description 14
- 238000012360 testing method Methods 0.000 description 14
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 12
- 239000004677 Nylon Substances 0.000 description 12
- 229920001778 nylon Polymers 0.000 description 12
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 10
- KKEYFWRCBNTPAC-UHFFFAOYSA-N Terephthalic acid Chemical compound OC(=O)C1=CC=C(C(O)=O)C=C1 KKEYFWRCBNTPAC-UHFFFAOYSA-N 0.000 description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 10
- 238000001746 injection moulding Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 8
- 229920000642 polymer Polymers 0.000 description 8
- 238000000465 moulding Methods 0.000 description 7
- 230000000379 polymerizing effect Effects 0.000 description 7
- 229910052757 nitrogen Inorganic materials 0.000 description 6
- 150000003839 salts Chemical class 0.000 description 6
- 238000006116 polymerization reaction Methods 0.000 description 5
- 230000003746 surface roughness Effects 0.000 description 5
- 229920000007 Nylon MXD6 Polymers 0.000 description 4
- 239000004952 Polyamide Substances 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 238000010438 heat treatment Methods 0.000 description 4
- 229920001519 homopolymer Polymers 0.000 description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 4
- 229920002647 polyamide Polymers 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- -1 For example Polymers 0.000 description 3
- 229920003189 Nylon 4,6 Polymers 0.000 description 3
- 229920002292 Nylon 6 Polymers 0.000 description 3
- 238000005452 bending Methods 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000009826 distribution Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 239000007790 solid phase Substances 0.000 description 3
- JCUZDQXWVYNXHD-UHFFFAOYSA-N 2,2,4-trimethylhexane-1,6-diamine Chemical compound NCCC(C)CC(C)(C)CN JCUZDQXWVYNXHD-UHFFFAOYSA-N 0.000 description 2
- DPQHRXRAZHNGRU-UHFFFAOYSA-N 2,4,4-trimethylhexane-1,6-diamine Chemical compound NCC(C)CC(C)(C)CCN DPQHRXRAZHNGRU-UHFFFAOYSA-N 0.000 description 2
- IGSBHTZEJMPDSZ-UHFFFAOYSA-N 4-[(4-amino-3-methylcyclohexyl)methyl]-2-methylcyclohexan-1-amine Chemical compound C1CC(N)C(C)CC1CC1CC(C)C(N)CC1 IGSBHTZEJMPDSZ-UHFFFAOYSA-N 0.000 description 2
- FDLQZKYLHJJBHD-UHFFFAOYSA-N [3-(aminomethyl)phenyl]methanamine Chemical compound NCC1=CC=CC(CN)=C1 FDLQZKYLHJJBHD-UHFFFAOYSA-N 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000004455 differential thermal analysis Methods 0.000 description 2
- SNRUBQQJIBEYMU-UHFFFAOYSA-N dodecane Chemical compound CCCCCCCCCCCC SNRUBQQJIBEYMU-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- JBKVHLHDHHXQEQ-UHFFFAOYSA-N epsilon-caprolactam Chemical compound O=C1CCCCCN1 JBKVHLHDHHXQEQ-UHFFFAOYSA-N 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 230000009477 glass transition Effects 0.000 description 2
- 230000001771 impaired effect Effects 0.000 description 2
- 238000004898 kneading Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 2
- 230000003287 optical effect Effects 0.000 description 2
- 239000002244 precipitate Substances 0.000 description 2
- KIDHWZJUCRJVML-UHFFFAOYSA-N putrescine Chemical compound NCCCCN KIDHWZJUCRJVML-UHFFFAOYSA-N 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- CXMXRPHRNRROMY-UHFFFAOYSA-N sebacic acid Chemical compound OC(=O)CCCCCCCCC(O)=O CXMXRPHRNRROMY-UHFFFAOYSA-N 0.000 description 2
- RNFJDJUURJAICM-UHFFFAOYSA-N 2,2,4,4,6,6-hexaphenoxy-1,3,5-triaza-2$l^{5},4$l^{5},6$l^{5}-triphosphacyclohexa-1,3,5-triene Chemical compound N=1P(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP(OC=2C=CC=CC=2)(OC=2C=CC=CC=2)=NP=1(OC=1C=CC=CC=1)OC1=CC=CC=C1 RNFJDJUURJAICM-UHFFFAOYSA-N 0.000 description 1
- JZUHIOJYCPIVLQ-UHFFFAOYSA-N 2-methylpentane-1,5-diamine Chemical compound NCC(C)CCCN JZUHIOJYCPIVLQ-UHFFFAOYSA-N 0.000 description 1
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 1
- 101000576320 Homo sapiens Max-binding protein MNT Proteins 0.000 description 1
- JHWNWJKBPDFINM-UHFFFAOYSA-N Laurolactam Chemical compound O=C1CCCCCCCCCCCN1 JHWNWJKBPDFINM-UHFFFAOYSA-N 0.000 description 1
- 229920006065 Leona® Polymers 0.000 description 1
- 239000004594 Masterbatch (MB) Substances 0.000 description 1
- 229920000571 Nylon 11 Polymers 0.000 description 1
- 229920000299 Nylon 12 Polymers 0.000 description 1
- 229920000305 Nylon 6,10 Polymers 0.000 description 1
- 229920003776 Reny® Polymers 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 239000002216 antistatic agent Substances 0.000 description 1
- 239000006229 carbon black Substances 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- 230000001143 conditioned effect Effects 0.000 description 1
- 239000007822 coupling agent Substances 0.000 description 1
- 238000006731 degradation reaction Methods 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 229920006351 engineering plastic Polymers 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000011152 fibreglass Substances 0.000 description 1
- 239000003063 flame retardant Substances 0.000 description 1
- 239000004088 foaming agent Substances 0.000 description 1
- 235000019253 formic acid Nutrition 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 239000011256 inorganic filler Substances 0.000 description 1
- 229910003475 inorganic filler Inorganic materials 0.000 description 1
- 239000000314 lubricant Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 239000002667 nucleating agent Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920006131 poly(hexamethylene isophthalamide-co-terephthalamide) Polymers 0.000 description 1
- 229920006110 poly(m-benzoyl4,4'-methylenebis(cyclohexylamine)) Polymers 0.000 description 1
- 229920001225 polyester resin Polymers 0.000 description 1
- 239000004645 polyester resin Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 239000012779 reinforcing material Substances 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 230000035939 shock Effects 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000003381 stabilizer Substances 0.000 description 1
- 230000002087 whitening effect Effects 0.000 description 1
- 229910052724 xenon Inorganic materials 0.000 description 1
- FHNFHKCVQCLJFQ-UHFFFAOYSA-N xenon atom Chemical compound [Xe] FHNFHKCVQCLJFQ-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Manufacture Of Macromolecular Shaped Articles (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、表面平滑性、機械
的特性および耐候性に優れるポリアミド樹脂組成物およ
びそれによる成形品に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a polyamide resin composition having excellent surface smoothness, mechanical properties, and weather resistance, and a molded article formed therefrom.
【0002】[0002]
【従来の技術】ポリアミド樹脂は、優れた機械的特性を
有し、特にガラス繊維で補強した際に強度、剛性の向上
効果が著しいことから、様々な用途に利用されている。
しかしながら、強度、剛性を向上させるために比較的高
含有量にガラス繊維を配合して用いた場合、例えば、射
出成形して得られる成形品は、その表面にガラス繊維が
露出し、成形品外観が低下するために、その用途が限定
される等の問題点がある。2. Description of the Related Art Polyamide resins have been used in various applications because they have excellent mechanical properties and, particularly when reinforced with glass fibers, have a remarkable effect of improving strength and rigidity.
However, when glass fibers are blended with a relatively high content in order to improve strength and rigidity, for example, a molded product obtained by injection molding has glass fiber exposed on its surface and the appearance of the molded product , There is a problem that its use is limited.
【0003】これらの問題を解決する方法として、例え
ば、ポリアミド樹脂の中でも比較的結晶化温度の低いア
ジピン酸とメタキシリレンジアミンを重合してなるポリ
アミド(以下ナイロンMXD6という)、アジピン酸、
イソフタル酸、ヘキサメチレンジアミンを共重合してな
るポリアミド(以下、ナイロン66/6I共重合体とい
う)等を用い、これらのポリアミドをガラス繊維で強化
した組成物が提案されている。[0003] As a method for solving these problems, for example, polyamide (hereinafter referred to as nylon MXD6) obtained by polymerizing adipic acid and meta-xylylenediamine having relatively low crystallization temperature among polyamide resins, adipic acid,
A composition in which a polyamide obtained by copolymerizing isophthalic acid and hexamethylenediamine (hereinafter, referred to as a nylon 66 / 6I copolymer) or the like and which is reinforced with a glass fiber has been proposed.
【0004】また、成形品外観を改良する別の方法とし
て、例えば特開昭56−30460号公報や、特開昭6
3−156856号公報には、ポリエステル樹脂や、ナ
イロン46樹脂にガラス繊維を配合した組成物におい
て、ガラス繊維長を規定して、外観と機械的特性のバラ
ンスを改良した樹脂組成物が開示されている。しかしな
がら、上記の様なガラス繊維強化樹脂組成物は、ある程
度ガラス繊維の露出を防止でき、優れた外観を有する成
形品を得られるが、更に優れた外観を有する成形品、例
えば、成形品表面に発生する約1〜5mm周期の凹凸
(以下うねりという)がない成形品を要求される用途に
は不充分であり、さらには機械的特性が劣る等、充分満
足できるものではなかった。特に、ナイロン46は、結
晶化温度が250℃と高く、外観の良い成形品を得るこ
とが困難であり、良外観の成形品が得られる成形条件幅
が狭いために、成形が難しいという問題があった。Further, as another method for improving the appearance of a molded article, for example, Japanese Patent Application Laid-Open Nos. Sho 56-30460 and
JP-A-3-156856 discloses a resin composition in which a glass fiber is blended with a polyester resin or a nylon 46 resin to improve the balance between appearance and mechanical properties by defining the glass fiber length. I have. However, the glass fiber reinforced resin composition as described above can prevent the glass fiber from being exposed to some extent, and can obtain a molded article having an excellent appearance. It was not sufficient for applications requiring molded articles without irregularities (hereinafter referred to as undulations) having a period of about 1 to 5 mm, and was not sufficiently satisfactory such as poor mechanical properties. In particular, nylon 46 has a problem that the crystallization temperature is as high as 250 ° C., and it is difficult to obtain a molded article with good appearance, and molding is difficult because the molding condition range for obtaining a molded article with good appearance is narrow. there were.
【0005】前記問題を解決すべく本発明者等は、ガラ
ス繊維強化ポリアミド樹脂中のガラス繊維に着目し、そ
の平均アスペクト比と、アスペクト比の大きいガラス繊
維の含有量を規定することによって、表面平滑性、およ
び機械的特性のバランスに優れるポリアミド樹脂組成物
を見いだし、特開平10−120900号公報に記載す
る発明を先に出願するに至った。In order to solve the above-mentioned problems, the present inventors focused on glass fibers in a glass fiber reinforced polyamide resin, and defined the average aspect ratio and the content of glass fibers having a large aspect ratio to thereby improve the surface area. A polyamide resin composition having an excellent balance between smoothness and mechanical properties has been found, and the invention described in JP-A-10-120900 has been filed first.
【0006】しかしながら、前記ポリアミド樹脂組成物
は、より高いレベルの機械的特性、特に高いレベルの衝
撃強度、外観(光沢性および表面平滑性)および耐候性
(特に、使用される環境下で、紫外線や、雨(水)によ
って劣化し、ガラス繊維が表面に露出し、光沢を失うこ
とによる白化する現象に対する耐性が求められる)が求
められる用途においては、まだ充分満足できるものでは
なかった。However, the polyamide resin composition has a higher level of mechanical properties, especially a higher level of impact strength, appearance (gloss and surface smoothness) and weatherability (particularly, in the environment in which it is used, ultraviolet light). However, it is not sufficiently satisfactory in applications in which it is required to be resistant to the phenomenon of deterioration due to rain (water), glass fibers being exposed on the surface, and whitening due to loss of gloss.
【0007】[0007]
【発明が解決しようとする課題】本発明は、上述した従
来のポリアミド樹脂組成物が有する諸問題を解消するこ
と、すなわち、機械的特性(特に耐衝撃性)および耐候
性に優れ、かつ、表面光沢および表面平滑性に優れた成
形品が得られるポリアミド樹脂組成物、およびその成形
品を提供することを目的とする。SUMMARY OF THE INVENTION The present invention solves the above-mentioned problems of the conventional polyamide resin composition, that is, it is excellent in mechanical properties (particularly impact resistance) and weather resistance, and has an excellent surface property. An object of the present invention is to provide a polyamide resin composition from which a molded article excellent in gloss and surface smoothness can be obtained, and a molded article thereof.
【0008】[0008]
【課題を解決するための手段】本発明者等は上記課題を
達成するために、ポリアミド樹脂組成物およびそれを構
成する成分についてさらに詳しく検討した結果、より優
れた成形品外観を有し、更に衝撃強度と耐候性にも優れ
るポリアミド樹脂成形品が存在することを見い出した。Means for Solving the Problems In order to achieve the above object, the present inventors have studied the polyamide resin composition and the components constituting the same in more detail, and as a result, have a better appearance of the molded product. It has been found that there is a polyamide resin molded product excellent in impact strength and weather resistance.
【0009】特に、本発明者等は、従来にはない太い径
のガラス繊維を用いることで、驚くべき事に、耐衝撃性
(ノッチつきIzod特性)や耐候性が飛躍的に向上す
ることを見い出し、本発明に至った。すなわち、本発明
は下記の通りである。 1)結晶化温度が210℃以下であるポリアミド樹脂3
0〜70重量%とガラス繊維70〜30重量%を含有
し、該ガラス繊維の平均繊維径が15〜30μmであ
り、かつ平均アスペクト比が10〜20であることを特
徴とするポリアミド樹脂組成物。 2)アスペクト比が5以下であるガラス繊維の含有率が
全ガラス繊維含有量の15重量%以下であることを特徴
とする上記1記載のポリアミド樹脂組成物。 3)ポリアミド樹脂が、(a)アジピン酸およびヘキサ
メチレンジアミンから得られるヘキサメチレンアジパミ
ド成分70〜95重量%と(b)イソフタル酸およびヘ
キサメチレンジアミンから得られるヘキサメチレンイソ
フタラミド成分30〜5重量%からなる共重合体である
ことを特徴とする上記1または2記載のポリアミド樹脂
組成物。 4)ポリアミド樹脂30〜70重量%とガラス繊維70
〜30重量%からなり、該ガラス繊維の平均アスペクト
比が9〜18であり、平均繊維径が15〜30μmであ
り、該ポリアミド樹脂の結晶化温度が210℃以下であ
ることを特徴とするポリアミド樹脂成形品。 5)アスペクト比が5以下であるガラス繊維の含有率が
全ガラス繊維含有量の15重量%以下であることを特徴
とする上記4記載のポリアミド樹脂成形品。 6)ポリアミド樹脂が(a)アジピン酸およびヘキサメ
チレンジアミンから得られるヘキサメチレンアジパミド
成分70〜95重量%と(b)イソフタル酸およびヘキ
サメチレンジアミンから得られるヘキサメチレンイソフ
タラミド成分30〜5重量%からなる共重合体であるこ
とを特徴とする上記4または5記載のポリアミド樹脂成
形品。 7)ポリアミド樹脂成形品が射出成形品であることを特
徴とする上記4、5または6記載のポリアミド樹脂成形
品。[0009] In particular, the present inventors have surprisingly found that the use of glass fibers having an unprecedently large diameter significantly improves the shock resistance (notched Izod characteristic) and the weather resistance. Have found the present invention. That is, the present invention is as follows. 1) Polyamide resin 3 having a crystallization temperature of 210 ° C. or lower
A polyamide resin composition comprising 0 to 70% by weight and 70 to 30% by weight of glass fiber, wherein the glass fiber has an average fiber diameter of 15 to 30 µm and an average aspect ratio of 10 to 20. . 2) The polyamide resin composition as described in 1 above, wherein the content of glass fibers having an aspect ratio of 5 or less is 15% by weight or less of the total glass fiber content. 3) A polyamide resin comprising: (a) 70 to 95% by weight of a hexamethylene adipamide component obtained from adipic acid and hexamethylenediamine; and (b) 30 to 95% by weight of a hexamethylene isophthalamide component obtained from isophthalic acid and hexamethylenediamine. 3. The polyamide resin composition as described in 1 or 2 above, which is a copolymer comprising 5% by weight. 4) 30-70% by weight of polyamide resin and glass fiber 70
A polyamide having an average aspect ratio of the glass fiber of 9 to 18, an average fiber diameter of 15 to 30 μm, and a crystallization temperature of the polyamide resin of 210 ° C. or less. Resin molded products. (5) The polyamide resin molded product as described in (4) above, wherein the content of glass fibers having an aspect ratio of 5 or less is 15% by weight or less of the total glass fiber content. 6) The polyamide resin is (a) 70 to 95% by weight of a hexamethylene adipamide component obtained from adipic acid and hexamethylene diamine, and (b) a hexamethylene isophthalamide component obtained from (b) an isophthalic acid and hexamethylene diamine. 6. The polyamide resin molded product according to the above item 4 or 5, wherein the molded product is a copolymer composed of at least 1% by weight. 7) The polyamide resin molded product according to the above 4, 5 or 6, wherein the polyamide resin molded product is an injection molded product.
【0010】以下に本発明を詳細に説明する。本発明に
よるポリアミド樹脂組成物はポリアミド樹脂とガラス繊
維より成る。本発明では、結晶化温度が210℃以下の
ポリアミド樹脂を用いる必要がある。本発明におけるポ
リアミド樹脂の結晶化温度は、示差熱分析器(DSC)
を用い、融点+20℃の温度で試料を5分間保持した
後、20℃/minの降温速度で測定した示差熱分析チ
ャートにおける結晶化ピークのピークトップ温度をい
う。Hereinafter, the present invention will be described in detail. The polyamide resin composition according to the present invention comprises a polyamide resin and glass fibers. In the present invention, it is necessary to use a polyamide resin having a crystallization temperature of 210 ° C. or lower. The crystallization temperature of the polyamide resin in the present invention is determined by a differential thermal analyzer (DSC).
And the peak top temperature of the crystallization peak in the differential thermal analysis chart measured at a temperature lowering rate of 20 ° C./min after holding the sample at a temperature of melting point + 20 ° C. for 5 minutes.
【0011】本発明において、結晶化温度が210℃以
下のポリアミド樹脂としては、例えば、ε−カプロラク
タム、アジピン酸、セバシン酸、ドデカン二酸、イソフ
タル酸、テレフタル酸、ヘキサメチレンジアミン、テト
ラメチレンジアミン、2−、メチルペンタメチレンジア
ミン、2,2,4−トリメチルヘキサメチレンジアミ
ン、2,4,4−トリメチルヘキサメチレンジアミン、
メタキシリレンジアミン、ビス(3ーメチルー4アミノ
シクロヘキシル)メタン等のナイロン形成性モノマーを
適宜組み合わせて得られるホモポリマー単独、共重合体
単独、ホモポリマー同士の混合物、共重合体同士の混合
物、共重合体とホモポリマーの混合物等を用いることが
できる。このようなポリアミド樹脂の具体例としては、
例えば、ナイロン6、ナイロン610、ナイロン61
2、ナイロン11、ナイロン12、ナイロンMXD6、
ヘキサメチレンジアミンとイソフタル酸を重合してなる
ナイロン(ナイロン6I)、イソフタル酸とビス(3−
メチル−4アミノシクロヘキシル)メタンを重合してな
るナイロン(ナイロンPACMI)などのホモポリマ
ー、アジピン酸とイソフタル酸とへキサメチレンジアミ
ンを重合してなるナイロン(ナイロン66/6I共重合
体)、イソフタル酸とテレフタル酸とヘキサメチレンジ
アミンを重合してなるナイロン(ナイロン6I/6T共
重合体)、テレフタル酸と2,2,4−トリメチルヘキ
サメチレンジアミンと2,4,4−トリメチルヘキサメ
チレンジアミンを重合してなるナイロン(ナイロンTM
DT共重合体)、イソフタル酸とテレフタル酸とヘキサ
メチレンジアミンとビス(3ーメチルー4アミノシクロ
ヘキシル)メタンを重合してなる共重合ナイロン、およ
びイソフタル酸とテレフタル酸とヘキサメチレンジアミ
ンとビス(3ーメチルー4アミノシクロヘキシル)メタ
ンを重合してなる共重合ナイロンとナイロン6の混合
物、MXD6ナイロンとナイロン66のブレンド物等が
挙げられるが、本発明はこれらに限定されるものではな
い。In the present invention, polyamide resins having a crystallization temperature of 210 ° C. or lower include, for example, ε-caprolactam, adipic acid, sebacic acid, dodecane diacid, isophthalic acid, terephthalic acid, hexamethylene diamine, tetramethylene diamine. 2-, methylpentamethylenediamine, 2,2,4-trimethylhexamethylenediamine, 2,4,4-trimethylhexamethylenediamine,
A homopolymer alone, a copolymer alone, a mixture of homopolymers, a mixture of copolymers, and a copolymer obtained by appropriately combining nylon-forming monomers such as meta-xylylenediamine and bis (3-methyl-4-aminocyclohexyl) methane. A mixture of the union and the homopolymer can be used. As a specific example of such a polyamide resin,
For example, nylon 6, nylon 610, nylon 61
2, nylon 11, nylon 12, nylon MXD6,
Nylon (nylon 6I) obtained by polymerizing hexamethylenediamine and isophthalic acid, isophthalic acid and bis (3-
Homopolymers such as nylon (nylon PACMI) obtained by polymerizing methyl-4aminocyclohexyl) methane, nylon (nylon 66 / 6I copolymer) obtained by polymerizing adipic acid, isophthalic acid and hexamethylenediamine, isophthalic acid (Nylon 6I / 6T copolymer) obtained by polymerizing terephthalic acid and hexamethylenediamine, and terephthalic acid, 2,2,4-trimethylhexamethylenediamine and 2,4,4-trimethylhexamethylenediamine Nylon (Nylon TM
DT copolymer), copolymerized nylon obtained by polymerizing isophthalic acid, terephthalic acid, hexamethylenediamine and bis (3-methyl-4-aminocyclohexyl) methane, and isophthalic acid, terephthalic acid, hexamethylenediamine and bis (3-methyl-4 Examples thereof include a mixture of nylon 6 and a copolymerized nylon obtained by polymerizing aminocyclohexyl) methane, and a blend of nylon 66 and MXD6, but the present invention is not limited thereto.
【0012】ポリアミド樹脂および/またはポリアミド
樹脂成形品の結晶化温度が210℃を越えると、得られ
る成形品の表面にガラス繊維の露出が多くなり、優れた
外観を有する成形品が得られない。本発明における特に
好ましいポリアミド樹脂としては、(a)アジピン酸お
よびヘキサメチレンジアミンから得られるヘキサメチレ
ンアジパミド成分(以下66成分)70〜95重量%と
(b)イソフタル酸およびヘキサメチレンジアミンから
得られるヘキサメチレンイソフタラミド成分(以下6I
成分)30〜5重量%からなる共重合体であり、このポ
リアミド樹脂を用いて得られる成形品は、吸水時の機械
的特性の低下がより少なく、外観(光沢性)、機械的特
性(強度、剛性、耐衝撃性)、耐候性のバランスが特に
優れる。When the crystallization temperature of the polyamide resin and / or the molded product of the polyamide resin exceeds 210 ° C., the surface of the obtained molded product is exposed to glass fibers so much that a molded product having an excellent appearance cannot be obtained. Particularly preferred polyamide resins in the present invention include (a) 70 to 95% by weight of a hexamethylene adipamide component (hereinafter referred to as 66 components) obtained from adipic acid and hexamethylene diamine and (b) an isophthalic acid and hexamethylene diamine. Hexamethylene isophthalamide component (hereinafter referred to as 6I
Component) 30 to 5% by weight of a copolymer. A molded article obtained by using this polyamide resin has less decrease in mechanical properties when absorbing water, and has an appearance (glossiness) and mechanical properties (strength). , Rigidity, impact resistance) and weather resistance are particularly excellent.
【0013】前記6I成分が5重量%より少ないと、成
形品の表面へのガラス繊維の露出が著しく、特にガラス
繊維を高含有量で配合する際は、必ずしも十分に良好な
外観が得られず、さらに、吸水時の機械的特性が劣る可
能性がある。また、6I成分が30重量%より多いと、
実質的に非晶性となり熱時の機械的特性が必ずしも十分
ではなく、また、金型温度を100℃以上に上げないと
良外観が得られない恐れがある等の成形上の制限を生じ
る。When the content of the 6I component is less than 5% by weight, the glass fiber is extremely exposed to the surface of the molded product, and a sufficiently good appearance is not always obtained, especially when a high content of glass fiber is blended. Further, the mechanical properties at the time of water absorption may be inferior. When the 6I component is more than 30% by weight,
It is substantially amorphous and mechanical properties during heating are not always sufficient, and there is a limitation on molding that a good appearance may not be obtained unless the mold temperature is raised to 100 ° C. or higher.
【0014】また、本発明では使用するポリアミド樹脂
の分子量を特に制限しないが、硫酸相対粘度(ηr:ポ
リマー1g/95.5%硫酸100ml 25℃測定)
が1.5〜3.5であることが好ましく、2.0〜3.
0の範囲のものが特に好ましく使用できる。本発明に使
用できるガラス繊維は、通常強化材として使用されるガ
ラス繊維であれば特に制限はない。例えば、0.2〜6
mmの長さにあらかじめカットされたチョップドストラ
ンドや、あらかじめ規定の繊維長分布に粉砕または切断
されたミルドファイバー、カットファイバーなどのいず
れでも用いることができる。また必要により、集束剤や
カップリング剤で表面処理されたガラス繊維を用いてよ
い。In the present invention, the molecular weight of the polyamide resin used is not particularly limited, but the relative viscosity of sulfuric acid (ηr: 1 g of polymer / 95.5% sulfuric acid 100 ml, measured at 25 ° C.)
Is preferably from 1.5 to 3.5, and more preferably from 2.0 to 3.
Those having a range of 0 can be particularly preferably used. The glass fiber that can be used in the present invention is not particularly limited as long as it is a glass fiber usually used as a reinforcing material. For example, 0.2-6
Any of chopped strands previously cut to a length of mm, milled fibers or cut fibers that have been ground or cut into a predetermined fiber length distribution can be used. If necessary, glass fibers surface-treated with a sizing agent or a coupling agent may be used.
【0015】本発明のポリアミド樹脂組成物は、その中
に含まれるガラス繊維の平均アスペクト比が10〜20
の範囲にあり、かつ平均繊維径が15〜30μmの範囲
にあることが必要である。さらに加えて、アスペクト比
が5以下のガラス繊維の含有率が全ガラス繊維含有量の
15重量%以下であることが特に好ましい。より好まし
い平均アスペクト比は12〜19であり、かつより好ま
しい平均繊維径は20〜25μmである。平均アスペク
トクト比が10未満であると、ガラス繊維の配合量に応
じて期待される機械的特性を充分に発現させることがで
きない。また平均アスペクト比が20を越えると成形品
表面にうねりが著しく発生する恐れがある。平均繊維径
が15μm未満の場合は、平均アスペクト比を10〜2
0に制御しても、耐衝撃性、耐候性の点で充分満足でき
るレベルにすることが困難である。平均繊維径が30μ
mを越える場合は、ガラス繊維の配合量に応じて期待さ
れる機械的特性を充分に発現し得ない。また、平均繊維
径が30μmを越えるガラス繊維は生産性や、ハンドリ
ング性等の点でも問題があり好ましくない。アスペクト
比が5以下のガラス繊維の含有率が15重量%よりも多
いと、耐衝撃性(ノッチ付きIzod特性)が十分でな
い場合がある。The polyamide resin composition of the present invention has an average aspect ratio of glass fibers contained therein of 10 to 20.
And the average fiber diameter must be in the range of 15 to 30 μm. In addition, the content of glass fibers having an aspect ratio of 5 or less is particularly preferably 15% by weight or less of the total glass fiber content. A more preferable average aspect ratio is 12 to 19, and a more preferable average fiber diameter is 20 to 25 μm. If the average aspect ratio is less than 10, the mechanical properties expected according to the amount of the glass fiber cannot be sufficiently exhibited. If the average aspect ratio exceeds 20, undulation may be significantly generated on the surface of the molded product. When the average fiber diameter is less than 15 μm, the average aspect ratio is 10 to 2
Even if it is controlled to 0, it is difficult to achieve a sufficiently satisfactory level of impact resistance and weather resistance. Average fiber diameter is 30μ
If it exceeds m, the mechanical properties expected according to the amount of the glass fiber cannot be sufficiently exhibited. Further, glass fibers having an average fiber diameter of more than 30 μm are not preferable because they have problems in productivity and handling properties. If the content of glass fibers having an aspect ratio of 5 or less is more than 15% by weight, impact resistance (notched Izod characteristics) may not be sufficient.
【0016】本発明のポリアミド樹脂成形品は、その中
に含まれるガラス繊維の平均アスペクト比が9〜18の
範囲にあり、かつ平均繊維径が15〜30μmの範囲に
あることが必要である。さらに加えて、アスペクト比が
5以下のガラス繊維の含有率が全ガラス繊維含有量の1
5重量%以下であることが特に好ましい。より好ましい
平均アスペクト比は11〜16であり、かつより好まし
い平均繊維径は20〜25μmである。平均アスペクト
クト比が9未満であると、ガラス繊維の配合量に応じて
期待される機械的特性を充分に発現させることがきな
い。また平均アスペクト比が18を越えると成形品表面
にうねりが著しく発生する恐れがある。平均繊維径が1
5μm未満の場合は、平均アスペクト比を10〜20に
制御しても、耐衝撃性、耐候性の点で充分満足できるレ
ベルにすることが困難である。平均繊維径が30μmを
越える場合は、ガラス繊維の配合量に応じて期待される
機械的特性を充分に発現し得ない。また、平均繊維径が
30μmを越えるガラス繊維は生産性や、ハンドリング
性等の点でも問題があり好ましくない。アスペクト比が
5以下のガラス繊維の含有率が15重量%よりも多い
と、耐衝撃性(ノッチ付きIzod特性)が十分でなく
なる恐れがある。In the polyamide resin molded article of the present invention, the average aspect ratio of the glass fibers contained therein must be in the range of 9 to 18, and the average fiber diameter must be in the range of 15 to 30 μm. In addition, the content of glass fibers having an aspect ratio of 5 or less is 1% of the total glass fiber content.
It is particularly preferred that the content be 5% by weight or less. A more preferable average aspect ratio is 11 to 16, and a more preferable average fiber diameter is 20 to 25 μm. If the average aspect ratio is less than 9, the mechanical properties expected according to the blending amount of the glass fiber cannot be sufficiently exhibited. On the other hand, if the average aspect ratio exceeds 18, undulations may be remarkably generated on the surface of the molded product. Average fiber diameter is 1
When it is less than 5 μm, even if the average aspect ratio is controlled to 10 to 20, it is difficult to obtain a sufficiently satisfactory level of impact resistance and weather resistance. If the average fiber diameter exceeds 30 μm, the mechanical properties expected according to the amount of the glass fiber cannot be sufficiently exhibited. Further, glass fibers having an average fiber diameter of more than 30 μm are not preferable because they have problems in productivity and handling properties. If the content of glass fibers having an aspect ratio of 5 or less is more than 15% by weight, impact resistance (notched Izod characteristics) may not be sufficient.
【0017】先に本願発明者等は、既述のように、ガラ
ス繊維強化ポリアミド樹脂中のガラス繊維の平均アスペ
クト比と、アスペクト比の大きいガラス繊維の含有量を
規定することによって、表面平滑性、および機械的特性
のバランスに優れるポリアミド樹脂組成物を見いだし、
特開平10−120900号公報記載の発明に至った
が、本発明は、同号公報記載の発明をさらに著しく改良
したものであり、本発明によって初めて、機械的特性
(特にノッチ付きIzod特性)、外観(光沢性、表面
平滑性)、耐候性のバランスに優れるポリアミド樹脂組
成物を提供できる様になったのである。First, as described above, the inventors of the present invention determined the average aspect ratio of the glass fibers in the glass fiber reinforced polyamide resin and the content of the glass fibers having a large aspect ratio to thereby improve the surface smoothness. , And a polyamide resin composition having an excellent balance of mechanical properties,
Although the invention described in Japanese Patent Application Laid-Open No. 10-120900 has been reached, the present invention is a further remarkable improvement of the invention described in the Japanese Patent Application Laid-Open No. H10-120900. This makes it possible to provide a polyamide resin composition having an excellent balance between appearance (glossiness, surface smoothness) and weather resistance.
【0018】本発明における、ポリアミド樹脂組成物の
ガラス繊維の平均繊維径、平均アスペクト比、およびア
スペクト比が5以下のガラス繊維の含有率は、ポリアミ
ド樹脂組成物ペレット中のガラス繊維を300〜100
0本無作為に抽出し、光学顕微鏡下にて実測して求める
ものであり、数平均繊維径をもって平均ガラス繊維径と
する。また、重量平均繊維長を数平均繊維径で除した値
を平均アスペクト比とする。また抽出した300〜10
00本のガラス繊維の繊維径および繊維長の分布データ
に基づき、全ガラス繊維量に対する、アスペクト比が5
以下のガラス繊維の含有率を求める。また、ポリアミド
樹脂成形品の場合には、成形品を実質的にガラス繊維長
に影響を及ぼさない程度の大きさ(例えば3mm角程)
のペレット状に切削し、ポリアミド樹脂組成物の場合と
全く同様にして、平均繊維径、平均アスペクト比、およ
びアスペクト比が5以下のガラス繊維の含有率を求める
こととする。In the present invention, the average fiber diameter and average aspect ratio of the glass fibers of the polyamide resin composition, and the content of the glass fibers having an aspect ratio of 5 or less are such that the glass fibers in the polyamide resin composition pellets are 300 to 100.
0 is randomly extracted and measured by actual measurement under an optical microscope. The number average fiber diameter is defined as the average glass fiber diameter. The value obtained by dividing the weight average fiber length by the number average fiber diameter is defined as the average aspect ratio. 300 to 10
Based on the distribution data of the fiber diameter and fiber length of 00 glass fibers, the aspect ratio with respect to the total glass fiber amount was 5
The following glass fiber content is determined. In the case of a polyamide resin molded product, the molded product is of a size that does not substantially affect the glass fiber length (for example, about 3 mm square).
And the average fiber diameter, the average aspect ratio, and the content of glass fibers having an aspect ratio of 5 or less are determined in the same manner as in the case of the polyamide resin composition.
【0019】本発明のポリアミド樹脂とガラス繊維の配
合割合は、ポリアミド樹脂30〜70重量%とガラス繊
維70〜30重量%である。ポリアミド樹脂が30重量
%より少ないと、ガラス繊維が成形品表面に露出し外観
を著しく損ねる。またポリアミド樹脂が70重量%より
多いと、機械的特性が満足なレベルに達しない。またこ
のようなガラス繊維の配合量が少ない領域においては、
特にガラス繊維のアスペクト比を規定しなくとも、うね
りが少ない、比較的良外観の成形品が得られる。The compounding ratio of the polyamide resin of the present invention and the glass fiber is 30 to 70% by weight of the polyamide resin and 70 to 30% by weight of the glass fiber. If the amount of the polyamide resin is less than 30% by weight, the glass fibers are exposed on the surface of the molded product, and the appearance is significantly impaired. If the amount of the polyamide resin is more than 70% by weight, the mechanical properties do not reach a satisfactory level. In the region where the amount of such glass fibers is small,
In particular, even if the aspect ratio of the glass fiber is not specified, a molded article having a relatively good appearance with little undulation can be obtained.
【0020】本発明におけるポリアミド樹脂組成物は、
その製造方法を、特に制限するものではないが、通常用
いられる単軸または2軸押出機を用いて、ポリアミド樹
脂とガラス繊維を溶融混練してペレットを得ることがで
きる。ガラス繊維の平均アスペクト比を本発明記載の範
囲に制御するには、例えば、適切なアスペクト比のガラ
ス繊維を用い、前記溶融混練の温度、吐出量、スクリュ
ーデザインおよび回転数、原料供給位置を適宜選択する
ことで、制御することができる。The polyamide resin composition according to the present invention comprises:
Although the production method is not particularly limited, pellets can be obtained by melting and kneading the polyamide resin and the glass fibers using a commonly used single-screw or twin-screw extruder. In order to control the average aspect ratio of the glass fiber to the range described in the present invention, for example, using a glass fiber having an appropriate aspect ratio, the temperature of the melt-kneading, the discharge rate, the screw design and the number of revolutions, the raw material supply position are appropriately set By selecting, you can control.
【0021】本発明によるポリアミド樹脂組成物は通常
ペレット状にて得られ、このペレットを用いて、例えば
圧縮成形、射出成形、押出成形等の各種の成形方法によ
って成形品とすればよい。本発明のポリアミド樹脂組成
物を用いることによる効果は、特に射出成形品に現れ
る。本発明における射出成形品は、通常の射出成形の他
に本発明の目的を損なわない範囲で、ガスアシスト成形
・2色成形などの特殊な射出成形によって得られる成形
品をも含む。The polyamide resin composition according to the present invention is usually obtained in the form of pellets, and the pellets may be formed into molded articles by various molding methods such as compression molding, injection molding and extrusion molding. The effect of using the polyamide resin composition of the present invention appears particularly in injection molded articles. The injection molded product in the present invention includes a molded product obtained by a special injection molding such as gas assist molding and two-color molding in addition to ordinary injection molding within a range not to impair the object of the present invention.
【0022】その場合の射出成形条件としては、例え
ば、成形温度が250〜310℃の範囲、金型温度が4
0〜120℃の範囲とすればよい。本発明のポリアミド
樹脂組成物には、本発明の目的を損なわない範囲で、1
種またはそれ以上の通常の添加剤を添加してよく、例え
ば、酸化、熱、および紫外線劣化に対する安定剤および
禁止剤、潤滑剤および離型剤、染料および顔料を含む着
色剤、核形成剤、発泡剤、可塑剤、無機充填材、難燃
剤、帯電防止剤などを適宜添加することができる。The injection molding conditions in this case include, for example, a molding temperature in the range of 250 to 310 ° C. and a mold temperature of 4
What is necessary is just to let it be the range of 0-120 degreeC. The polyamide resin composition of the present invention contains 1 as long as the object of the present invention is not impaired.
One or more conventional additives may be added, such as stabilizers and inhibitors against oxidation, heat, and UV degradation, lubricants and release agents, coloring agents including dyes and pigments, nucleating agents, A foaming agent, a plasticizer, an inorganic filler, a flame retardant, an antistatic agent and the like can be appropriately added.
【0023】[0023]
【発明の実施の形態】以下に本発明を実施例・比較例に
より具体的に説明する。なお、樹脂組成物、成形品の評
価方法、使用したポリアミド樹脂およびガラス繊維、ペ
レット作成法等は次の通りである。 A〕樹脂組成物、成形品の評価方法 (1)樹脂組成物中の平均ガラス繊維径、平均アスペク
ト比、およびアスペクト比が5以下のガラス繊維含有
率:蟻酸中にポリアミド樹脂組成物のペレットを入れ、
ポリアミドを溶解させ、ガラス繊維を沈殿させる。得ら
れた沈殿物を光学顕微鏡下で観察し、無作為に選んだ3
00〜1000本のガラス繊維の長さおよび直径を旭化
成工業(株)製画像解析装置IP−1000を用いて測
定し、重量平均繊維長および数平均繊維径を求めた。得
られた結果から、数平均繊維径を平均繊維径とし、重量
平均繊維長を数平均繊維径で除した値を平均アスペクト
比とした。また、繊維長、繊維径の分布データからアス
ペクト比が5以下のガラス繊維の含有率を求めた。 (2)結晶化温度:ポリアミド樹脂組成物の場合は使用
した原料ポリマーのペレットまたは粉砕品を試料とし、
ポリアミド樹脂成形品の場合は後述する(3)引張特性
を評価した成形品を3mm角程度に切削して試料とし、
パーキンエルマー社製示差熱分析器DSC7を用い融点
+20℃の温度で5分間保持した後、20℃/minの
降温速度で測定した示差熱分析チャートにおける結晶化
ピークのピークトップ温度を結晶化温度とした。 (3)引張特性:東芝機械(株)社製IS50EP射出
成形機を用い、シリンダー温度290℃で、充填時間が
約1秒になるように射出圧力、速度を適宜調整して試験
片を得た。尚、金型温度は、80〜120℃の範囲で組
成物のガラス転位温度に応じて適宜設定した。得られた
試験片を用い、ASTM D638に準じて引張強度、
引張伸度を測定した。 (4)曲げ特性:前記(3)の引張特性に用いた試験片
と同様の方法で試験片を得、ASTMD790に準じて
曲げ強度、曲げ弾性率を測定した。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be specifically described below with reference to examples and comparative examples. In addition, the resin composition, the evaluation method of a molded article, the used polyamide resin and glass fiber, the pellet preparation method, etc. are as follows. A] Evaluation method of resin composition and molded article (1) Average glass fiber diameter, average aspect ratio, and glass fiber content with aspect ratio of 5 or less in resin composition: pellet of polyamide resin composition in formic acid Get in,
Dissolve the polyamide and precipitate the glass fibers. The obtained precipitate was observed under an optical microscope and randomly selected 3
The length and diameter of 00 to 1000 glass fibers were measured using an image analyzer IP-1000 manufactured by Asahi Kasei Corporation to determine the weight average fiber length and the number average fiber diameter. From the obtained results, the number average fiber diameter was defined as the average fiber diameter, and the value obtained by dividing the weight average fiber length by the number average fiber diameter was defined as the average aspect ratio. The content ratio of glass fibers having an aspect ratio of 5 or less was determined from distribution data of fiber length and fiber diameter. (2) Crystallization temperature: In the case of a polyamide resin composition, pellets or pulverized products of the raw material polymer used as a sample,
In the case of a polyamide resin molded product, a molded product obtained by evaluating the tensile properties described later (3) is cut into about 3 mm square to obtain a sample,
After holding at a temperature of melting point + 20 ° C. for 5 minutes using a differential thermal analyzer DSC7 manufactured by Perkin Elmer, the peak top temperature of the crystallization peak in the differential thermal analysis chart measured at a temperature lowering rate of 20 ° C./min is defined as did. (3) Tensile properties: Using an IS50EP injection molding machine manufactured by Toshiba Machine Co., Ltd., a test piece was obtained by appropriately adjusting the injection pressure and speed so that the filling time was about 1 second at a cylinder temperature of 290 ° C. . The mold temperature was appropriately set in the range of 80 to 120 ° C. according to the glass transition temperature of the composition. Using the obtained test piece, tensile strength according to ASTM D638,
The tensile elongation was measured. (4) Bending properties: Test pieces were obtained in the same manner as the test pieces used for the tensile properties of (3), and the bending strength and the flexural modulus were measured according to ASTM D790.
【0024】吸水時の曲げ特性評価においては、試験片
を23℃、相対湿度50%の雰囲気下で、成形品の水分
率が平衡に達するまで調湿した後、測定した。 (5)Izod衝撃性:前記(3)の引張特性に用いた
試験片と同様の方法で試験片を得、ASTMD256に
準じてノッチ付きIzod衝撃強度を測定した。 (6)表面光沢性:東芝機械(株)社製IS150E射
出成形機を用い、シリンダー温度290℃とし、充填時
間が約1.5秒になるように射出圧力、速度を適宜調整
して100x90x3mmの平板状試験片を得た。尚、
金型温度は、80〜120℃の範囲で組成物のガラス転
位温度に応じて適宜設定した。また、より感度良く表面
光沢性を評価するため、本発明のポリアミド樹脂組成物
ペレット100重量部に対し、2.5重量部の大日本イ
ンキ(株)社製 カーボンブラック系ナイロンマスター
バッチF−36600B−20Sを射出成形前にブレン
ドし黒着色成形品とした。In the evaluation of the bending characteristics during water absorption, the test pieces were conditioned in an atmosphere of 23 ° C. and 50% relative humidity until the moisture content of the molded article reached equilibrium, and then measured. (5) Izod impact strength: A test piece was obtained in the same manner as the test piece used for the tensile properties of the above (3), and the notched Izod impact strength was measured according to ASTM D256. (6) Surface gloss: using an IS150E injection molding machine manufactured by Toshiba Machine Co., Ltd., setting the cylinder temperature to 290 ° C. and adjusting the injection pressure and speed as appropriate so that the filling time is about 1.5 seconds, and measuring 100 × 90 × 3 mm. A flat test piece was obtained. still,
The mold temperature was appropriately set in the range of 80 to 120 ° C. according to the glass transition temperature of the composition. Further, in order to evaluate surface glossiness with higher sensitivity, 2.5 parts by weight of carbon black nylon masterbatch F-36600B manufactured by Dainippon Ink Co., Ltd. per 100 parts by weight of the polyamide resin composition pellets of the present invention. -20S was blended before injection molding to obtain a black colored molded product.
【0025】得られた試験片の中央部を堀場製ハンディ
ー光沢計IG320を用いてJIS−K7150に準じ
てGs60°を測定した。 (7)表面平滑性:前記(6)に記載の平板状試験片を
用い、表面のうねりの発生状況を目視で評価した。評価
基準は、うねりが全面に渡り認められないものを◎、う
ねりが極僅かまたは極一部に認められるものを○、うね
りが全面に渡り顕著に認められるものをXとした。 (8)表面粗度:前記(6)記載の平板状試験片を、
(株)小坂研究所製表面粗さ測定器SE30Kおよび表
面粗さ解析装置AY−31を用いて、表面粗さRa(中
心線平均粗さ)およびRmax(最大高さ)をJIS
B 0601に準じて求めた。Ra、Rmaxともに数
値の大きい方が表面粗度が大きい。 (9)耐候性:前記(6)に記載の平板状試験片を、A
TLAS社製キセノンウエザオメター、Xnotest
1200LMを用いて83℃、300時間、降雨サイク
ル10分/60分の条件で促進暴露した。日本電色社製
色差計ND−300Aを用い暴露前後の色差(△E)を
求めた。色差(△E)の小さい方が耐候性が良い。 (10)成形品中の平均ガラス繊維径、平均アスペクト
比、およびアスペクト比が5以下のガラス繊維含有率:
評価方法(6)記載の平板状成形品を3mm角程度に切
削して試料とした以外は、評価方法(1)記載と同様の
方法で測定した。 B〕使用したポリアミド樹脂およびガラス繊維 (1)ポリアミド樹脂 ナイロン66:旭化成工業(株)社製レオナ1300 ナイロン6:宇部興産(株)社製SF1013A ナイロンMXD6:三菱エンジニアリングプラスチッ
ク(株)社製レニー6002 ナイロン66/6I共重合体:製造例1〜3に従って
作成した。The center of the obtained test piece was measured for Gs 60 ° according to JIS-K7150 using a handy gloss meter IG320 manufactured by Horiba. (7) Surface smoothness: The occurrence of undulation on the surface was visually evaluated using the flat test piece described in (6) above. The evaluation criteria were。 when no undulation was observed over the entire surface, ○ when the undulation was extremely or partially observed, and X when the undulation was significantly observed over the entire surface. (8) Surface roughness: the plate-shaped test piece according to the above (6),
The surface roughness Ra (center line average roughness) and Rmax (maximum height) were measured by JIS using a surface roughness measuring device SE30K and a surface roughness analyzer AY-31 manufactured by Kosaka Laboratory Co., Ltd.
B0601. The larger the value of both Ra and Rmax, the greater the surface roughness. (9) Weather resistance: The plate-shaped test piece described in (6)
Xenon Weatherometa, Xnotest, manufactured by TLAS
Accelerated exposure was performed using 1200 LM under the conditions of 83 ° C., 300 hours, and a rain cycle of 10 minutes / 60 minutes. The color difference (ΔE) before and after exposure was determined using a color difference meter ND-300A manufactured by Nippon Denshoku Co., Ltd. The smaller the color difference (ΔE), the better the weather resistance. (10) The average glass fiber diameter, the average aspect ratio, and the glass fiber content of the aspect ratio of 5 or less in the molded article:
The measurement was performed in the same manner as in the evaluation method (1) except that the flat molded product described in the evaluation method (6) was cut into a sample of about 3 mm square to obtain a sample. B] Polyamide resin and glass fiber used (1) Polyamide resin Nylon 66: Leona 1300 nylon 6 manufactured by Asahi Kasei Kogyo Co., Ltd. SF1013A nylon MXD6 manufactured by Ube Industries, Ltd .: Reny 6002 manufactured by Mitsubishi Engineering-Plastics Corporation Nylon 66 / 6I copolymer: produced according to Production Examples 1 to 3.
【0026】ナイロン46:帝人(株)社製ナイロン
46C2000 (2)ガラス繊維 旭ファイバーグラス(株)社製CS03MA416 平均繊維径 13μm 旭ファイバーグラス(株)社製 試作材 平均繊維径 18μm 旭ファイバーグラス(株)社製 CS03TA416 平均繊維径 23μm 旭ファイバーグラス(株)社製 試作材 平均繊維径 28μm 旭ファイバーグラス(株)社製 試作材 平均繊維径 36μm C〕ポリアミド樹脂組成物のペレットの作成法 前記の各種ポリアミド樹脂とガラス繊維を適宜組み合わ
せ、東芝機械(株)社製2軸押出機TEM35を用いて
溶融混練し、ペレットを得た。Nylon 46: Nylon 46C2000 manufactured by Teijin Limited (2) Glass fiber CS03MA416 manufactured by Asahi Fiber Glass Co., Ltd. Average fiber diameter: 13 μm Prototype material manufactured by Asahi Fiber Glass Co., Ltd. Average fiber diameter: 18 μm Asahi Fiber Glass ( Co., Ltd. CS03TA416 Average fiber diameter 23 μm Asahi Fiberglass Co., Ltd. Prototype material Average fiber diameter 28 μm Asahi Fiberglass Co., Ltd. Prototype material Average fiber diameter 36 μm C] Method for preparing pellets of polyamide resin composition Various polyamide resins and glass fibers were appropriately combined and melt-kneaded using a twin screw extruder TEM35 manufactured by Toshiba Machine Co., Ltd. to obtain pellets.
【0027】この際、得られたペレット中のガラス繊維
のアスペクト比を調整するためにガラス繊維のフィード
位置・吐出量(30〜90kg/hrの範囲)・温度(25
0〜300℃の範囲)・スクリュー回転数(250〜4
50rpmの範囲)を適宜選択した。At this time, in order to adjust the aspect ratio of the glass fiber in the obtained pellet, the feed position, discharge amount (range of 30 to 90 kg / hr) and temperature (25%) of the glass fiber are used.
Screw rotation speed (250-4 ° C)
(Range of 50 rpm) was appropriately selected.
【0028】[0028]
【製造例】(ナイロン66/6I共重合体の製造例1)
アジピン酸とヘキサメチレンジアミンの等モル塩2.0
kgとイソフタル酸とヘキサメチレンジアミンの等モル
塩0.5kgおよび純水2.5kgを5リットルオート
クレーブに仕込み良く攪拌しながら、充分に窒素置換し
た。攪拌を継続しながら温度を室温から220℃まで約
1時間で昇温した。この後、オートクレーブの内圧を1
8kg/cm2−Gになるように、水を反応系外に除去
しながら約2時間かけて温度を260℃に昇温した。そ
の後加熱をやめ、オートクレーブを密閉し、約8時間か
けて室温まで冷却し、ナイロン66/6I(組成重量
比:78.5/21.5)ポリマーを約2kg得た。得
られたポリマーを粉砕し、10リットルのエバポレータ
を用い、窒素気流下200℃で10時間固相重合して分
子量をさらに上げた。固相重合によって硫酸相対粘度η
rは、1.38から2.30に上昇した。 (ナイロン66/6I共重合体の製造例2)アジピン酸
とヘキサメチレンジアミンの等モル塩2.0kgとイソ
フタル酸とヘキサメチレンジアミンの等モル塩0.32
kgおよび純水2.32kgを5リットルオートクレー
ブに仕込み良く攪拌しながら、充分に窒素置換した。攪
拌を継続しながら温度を室温から220℃まで約1時間
で昇温した。この後、オートクレーブの内圧を18kg
/cm2−Gになるように、水を反応系外に除去しなが
ら約2時間かけて温度を260℃に昇温した。その後加
熱をやめ、オートクレーブを密閉し、約8時間かけて室
温まで冷却し、ナイロン66/6I(組成重量比:85
/15)ポリマーを約2kg得た。得られたポリマーを
粉砕し、10リットルのエバポレータを用い、窒素気流
下200℃で10時間固相重合して分子量をさらに上げ
た。固相重合によって硫酸相対粘度ηrは、1.38か
ら2.30に上昇した。 (ナイロン66/6I共重合体の製造例3)アジピン酸
とヘキサメチレンジアミンの等モル塩2.426kgと
イソフタル酸とヘキサメチレンジアミンの等モル塩0.
074kgおよび純水2.5kgを5リットルオートク
レーブに仕込み良く攪拌しながら、充分に窒素置換し
た。攪拌を継続しながら温度を室温から220℃まで約
1時間で昇温した。この後、オートクレーブの内圧を1
8kg/cm2−Gになるように、水を反応系外に除去
しながら約2時間かけて温度を260℃に昇温した。そ
の後加熱をやめ、オートクレーブを密閉し、約8時間か
けて室温まで冷却し、ナイロン66/6I(組成重量
比:97/3)ポリマーを約2kg得た。得られたポリ
マーを粉砕し、10リットルのエバポレータを用い、窒
素気流下200℃で10時間固相重合して分子量をさら
に上げた。固相重合によって硫酸相対粘度ηrは、1.
38から2.30に上昇した。[Production example] (Production example 1 of nylon 66 / 6I copolymer)
Equimolar salt of adipic acid and hexamethylenediamine 2.0
kg, 0.5 kg of equimolar salt of isophthalic acid and hexamethylenediamine and 2.5 kg of pure water were charged into a 5-liter autoclave and sufficiently purged with nitrogen. The temperature was raised from room temperature to 220 ° C. in about 1 hour while stirring was continued. Thereafter, the internal pressure of the autoclave is reduced to 1
The temperature was raised to 260 ° C. over about 2 hours while removing water from the reaction system so as to be 8 kg / cm 2 -G. Thereafter, the heating was stopped, the autoclave was closed, and the mixture was cooled to room temperature over about 8 hours to obtain about 2 kg of a nylon 66 / 6I (composition weight ratio: 78.5 / 21.5) polymer. The obtained polymer was pulverized and subjected to solid-phase polymerization at 200 ° C. for 10 hours under a nitrogen stream using a 10-liter evaporator to further increase the molecular weight. Sulfuric acid relative viscosity η by solid state polymerization
r increased from 1.38 to 2.30. (Production Example 2 of Nylon 66 / 6I Copolymer) 2.0 kg of equimolar salt of adipic acid and hexamethylenediamine and 0.32 of equimolar salt of isophthalic acid and hexamethylenediamine
kg and 2.32 kg of pure water were charged into a 5 liter autoclave and sufficiently purged with nitrogen. The temperature was raised from room temperature to 220 ° C. in about 1 hour while stirring was continued. After that, the internal pressure of the autoclave is reduced to 18 kg.
The temperature was raised to 260 ° C. over about 2 hours while removing water from the reaction system so as to be / cm 2 -G. Thereafter, the heating was stopped, the autoclave was closed, and the mixture was cooled to room temperature over about 8 hours, and then nylon 66 / 6I (composition weight ratio: 85
/ 15) About 2 kg of polymer was obtained. The obtained polymer was pulverized and subjected to solid-phase polymerization at 200 ° C. for 10 hours under a nitrogen stream using a 10-liter evaporator to further increase the molecular weight. The sulfuric acid relative viscosity ηr increased from 1.38 to 2.30 due to solid-state polymerization. (Production Example 3 of Nylon 66 / 6I Copolymer) 2.426 kg of equimolar salt of adipic acid and hexamethylenediamine and equimolar salt of isophthalic acid and hexamethylenediamine 0.
074 kg and pure water 2.5 kg were charged into a 5-liter autoclave and sufficiently purged with nitrogen while stirring well. The temperature was raised from room temperature to 220 ° C. in about 1 hour while stirring was continued. Thereafter, the internal pressure of the autoclave is reduced to 1
The temperature was raised to 260 ° C. over about 2 hours while removing water from the reaction system so as to be 8 kg / cm 2 -G. Thereafter, the heating was stopped, the autoclave was closed, and the mixture was cooled to room temperature over about 8 hours to obtain about 2 kg of nylon 66 / 6I (composition weight ratio: 97/3) polymer. The obtained polymer was pulverized and subjected to solid-phase polymerization at 200 ° C. for 10 hours under a nitrogen stream using a 10-liter evaporator to further increase the molecular weight. The relative viscosity ηr of sulfuric acid is 1.
It increased from 38 to 2.30.
【0029】[0029]
【実施例1】製造例(ナイロン66/6I共重合体の製
造1)に示す方法で得られたナイロン66/6I粉砕品
を、東芝機械(株)社製2軸押出機TEM35のメイン
フィード口より、ガラス繊維(CS03TA416)を
サイドフィード口より表1に示す組成比になるように、
定重量式フィーダーで投入し、吐出量50kg/hr、
シリンダー温度設定290℃、スクリュー回転数450
rpmで溶融混練し、ペレットを得た。得られたペレッ
トおよびそれを用いた成形品の評価結果を表1に示す。Example 1 Nylon 66 / 6I pulverized product obtained by the method shown in Production Example (Production of Nylon 66 / 6I Copolymer 1) was used as a main feed port of a twin screw extruder TEM35 manufactured by Toshiba Machine Co., Ltd. Thus, the glass fiber (CS03TA416) was supplied from the side feed port so as to have a composition ratio shown in Table 1.
Feeding by constant weight feeder, discharge rate 50kg / hr,
Cylinder temperature setting 290 ° C, screw rotation speed 450
The mixture was melt-kneaded at rpm to obtain pellets. Table 1 shows the evaluation results of the obtained pellets and molded articles using the pellets.
【0030】[0030]
【実施例2】製造例(ナイロン66/6I共重合体の製
造2)に示す方法で得られたナイロン66/6I粉砕品
を用いた他は実施例1と同様の方法でペレットを得た。
得られたペレットおよびそれを用いた成形品の評価結果
を表1に示す。Example 2 Pellets were obtained in the same manner as in Example 1 except that the pulverized nylon 66 / 6I obtained by the method shown in the Production Example (Production of Nylon 66 / 6I copolymer 2) was used.
Table 1 shows the evaluation results of the obtained pellets and molded articles using the pellets.
【0031】[0031]
【実施例3〜11】表1〜3に示す組成物からなるペレ
ットおよび試験片を作成し、それらを評価し、評価結果
を併せて表1〜3に示した。Examples 3 to 11 Pellets and test pieces made of the compositions shown in Tables 1 to 3 were prepared, evaluated, and the evaluation results are shown in Tables 1 to 3.
【0032】[0032]
【実施例12】製造例(ナイロン66/6I共重合体の
製造1)に示す方法で得られたナイロン66/6I粉砕
品およびガラス繊維(CS03TA416)を、東芝機
械(株)社製2軸押出機TEM35のメインフィード口
より、表1に示す組成になるように定重量式フィーダー
で投入し、吐出量50kg/hr、シリンダー温度29
0℃、スクリュー回転数250rpmで溶融混練しペレ
ットを得た。得られたペレットおよびそれを用いた成形
品の評価結果を表4に示す。Example 12 Nylon 66 / 6I pulverized product and glass fiber (CS03TA416) obtained by the method shown in the Production Example (Production of Nylon 66 / 6I Copolymer 1) were twin-screw extruded from Toshiba Machine Co., Ltd. From the main feed port of the TEM35 machine, feed by a constant weight feeder so as to have the composition shown in Table 1, discharge rate 50 kg / hr, cylinder temperature 29
The mixture was melt-kneaded at 0 ° C. and a screw rotation speed of 250 rpm to obtain pellets. Table 4 shows the obtained pellets and the evaluation results of the molded articles using the pellets.
【0033】上記した、実施例1〜12のいずれの組成
物も、成形片の表面にうねりがほとんど認められず、ま
た機械的特性に優れ、外観、機械的特性、耐候性のバラ
ンスが良いことが表1〜3より明らかである。また、実
施例1と12の評価結果をを比較するとアスペクト比が
5以下のガラス繊維の含有率が15%を越える実施例1
2の方がノッチ付きIzod特性がより劣ることが理解
される。Each of the above-mentioned compositions of Examples 1 to 12 has almost no undulation on the surface of the molded piece, excellent mechanical properties, and a good balance of appearance, mechanical properties and weather resistance. Is clear from Tables 1 to 3. Comparing the evaluation results of Examples 1 and 12, the content of the glass fiber having an aspect ratio of 5 or less exceeds 15%.
It is understood that No. 2 is inferior in notched Izod characteristics.
【0034】さらに、実施例1と実施例10の評価結果
を比較するとナイロン66/6Iを用いた実施例1の方
が引張伸度およびノッチ付きIzod特性の点でより優
れる。加えて、実施例1および実施例6〜10の評価結
果が示す通り、平均ガラス繊維径が20〜25μm、平
均アスペクト比が12〜19の場合に、特に機械的特
性、表面平滑性、耐候性のバランスに優れる。Further, comparing the evaluation results of Example 1 and Example 10, Example 1 using nylon 66 / 6I is more excellent in terms of tensile elongation and notched Izod characteristics. In addition, as shown by the evaluation results of Example 1 and Examples 6 to 10, when the average glass fiber diameter is 20 to 25 μm and the average aspect ratio is 12 to 19, the mechanical properties, surface smoothness, and weather resistance are particularly high. Excellent balance.
【0035】[0035]
【比較例1】製造例(ナイロン66/6I共重合体の製
造3)に示す方法で得られたナイロン66/6I粉砕品
を用いた他は実施例1と同様の方法でペレットを得た。
得られたペレットおよびそれを用いた成形品の評価結果
を表4に示す。Comparative Example 1 Pellets were obtained in the same manner as in Example 1 except that the pulverized nylon 66 / 6I obtained by the method shown in Production Example (Production of Nylon 66 / 6I Copolymer 3) was used.
Table 4 shows the obtained pellets and the evaluation results of the molded articles using the pellets.
【0036】[0036]
【比較例2〜7】表4および5に示す組成物からなるペ
レットおよび試験片を作成し、それらを評価した。評価
結果を表4および5に示す。これらの比較例におけるい
ずれの組成においても、得られる成形品の表面にうねり
が発生するか、あるいは、うねりがないものはその機械
的特性、特に耐衝撃性および/または耐候性に劣り、成
形品外観、機械的特性、耐候性のバランスが悪いことが
表4および5より明らかである。Comparative Examples 2 to 7 Pellets and test pieces comprising the compositions shown in Tables 4 and 5 were prepared and evaluated. The evaluation results are shown in Tables 4 and 5. In any of the compositions in these comparative examples, the surface of the obtained molded product has undulation, or those having no undulation have poor mechanical properties, particularly impact resistance and / or weather resistance. It is clear from Tables 4 and 5 that the balance between appearance, mechanical properties and weather resistance is poor.
【0037】[0037]
【表1】 [Table 1]
【0038】[0038]
【表2】 [Table 2]
【0039】[0039]
【表3】 [Table 3]
【0040】[0040]
【表4】 [Table 4]
【0041】[0041]
【表5】 [Table 5]
【0042】[0042]
【発明の効果】以上詳述したように、本発明によるポリ
アミド樹脂組成物およびそれによる成形品は、従来のも
のと比べ、機械的特性(特に耐衝撃性)、成形品の外観
特性(表面光沢性、平滑性、粗さ)、耐候性が飛躍的に
向上するという顕著な効果を有する。As described above in detail, the polyamide resin composition according to the present invention and the molded article made therefrom have higher mechanical properties (particularly impact resistance) and appearance properties (surface gloss) than the conventional ones. , Smoothness, and roughness) and weather resistance are significantly improved.
Claims (7)
ミド樹脂30〜70重量%とガラス繊維70〜30重量
%を含有し、該ガラス繊維の平均アスペクト比が10〜
20であり、かつ平均繊維径が15〜30μmであるこ
とを特徴とするポリアミド樹脂組成物。1. A composition comprising 30 to 70% by weight of a polyamide resin having a crystallization temperature of 210 ° C. or lower and 70 to 30% by weight of a glass fiber, wherein the glass fiber has an average aspect ratio of 10 to 10.
20. The polyamide resin composition having an average fiber diameter of 15 to 30 μm.
の含有率が全ガラス繊維含有量の15重量%以下である
ことを特徴とする請求項1記載のポリアミド樹脂組成
物。2. The polyamide resin composition according to claim 1, wherein the content of glass fibers having an aspect ratio of 5 or less is 15% by weight or less of the total glass fiber content.
びヘキサメチレンジアミンから得られるヘキサメチレン
アジパミド成分70〜95重量%と(b)イソフタル酸
およびヘキサメチレンジアミンから得られるヘキサメチ
レンイソフタラミド成分30〜5重量%からなる共重合
体であることを特徴とする請求項1または2記載のポリ
アミド樹脂組成物。3. A polyamide resin comprising (a) 70 to 95% by weight of a hexamethylene adipamide component obtained from adipic acid and hexamethylene diamine and (b) a hexamethylene isophthalamide component obtained from isophthalic acid and hexamethylene diamine. 3. The polyamide resin composition according to claim 1, which is a copolymer comprising 30 to 5% by weight.
ス繊維70〜30重量%からなり、該ガラス繊維の平均
アスペクト比が9〜18であり、平均繊維径が15〜3
0μmであり、該ポリアミド樹脂の結晶化温度が210
℃以下であることを特徴とするポリアミド樹脂成形品。4. A glass fiber comprising 30 to 70% by weight of a polyamide resin and 70 to 30% by weight of a glass fiber, wherein the glass fiber has an average aspect ratio of 9 to 18 and an average fiber diameter of 15 to 3%.
0 μm, and the crystallization temperature of the polyamide resin is 210
A polyamide resin molded product having a temperature of at most ℃.
の含有率が全ガラス繊維含有量の15重量%以下である
ことを特徴とする請求項4記載のポリアミド樹脂成形
品。5. The polyamide resin molded article according to claim 4, wherein the content of glass fibers having an aspect ratio of 5 or less is 15% by weight or less of the total glass fiber content.
びヘキサメチレンジアミンから得られるヘキサメチレン
アジパミド成分70〜95重量%と(b)イソフタル酸
およびヘキサメチレンジアミンから得られるヘキサメチ
レンイソフタラミド成分30〜5重量%からなる共重合
体であることを特徴とする請求項4または5記載のポリ
アミド樹脂成形品。6. A polyamide resin comprising: (a) 70 to 95% by weight of a hexamethylene adipamide component obtained from adipic acid and hexamethylene diamine; and (b) a hexamethylene isophthalamide component obtained from (b) isophthalic acid and hexamethylene diamine. The polyamide resin molded product according to claim 4 or 5, which is a copolymer comprising 30 to 5% by weight.
ることを特徴とする請求項4、5または6記載のポリア
ミド樹脂成形品。7. The polyamide resin molded product according to claim 4, wherein the polyamide resin molded product is an injection molded product.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP35783998A JP2000178441A (en) | 1998-12-16 | 1998-12-16 | Polyamide resin composition, and formed product thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP35783998A JP2000178441A (en) | 1998-12-16 | 1998-12-16 | Polyamide resin composition, and formed product thereof |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2000178441A true JP2000178441A (en) | 2000-06-27 |
Family
ID=18456196
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP35783998A Pending JP2000178441A (en) | 1998-12-16 | 1998-12-16 | Polyamide resin composition, and formed product thereof |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2000178441A (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002105312A (en) * | 2000-10-04 | 2002-04-10 | Asahi Kasei Corp | Reinforced semi-aromatic polyamide resin composition and molded article |
| JP2005263828A (en) * | 2004-03-16 | 2005-09-29 | Asahi Kasei Chemicals Corp | Long fiber reinforced polyamide resin material |
| WO2008053911A1 (en) | 2006-11-01 | 2008-05-08 | Mitsubishi Engineering-Plastics Corporation | Pellet blend of polyamide resin composition, molded article, and process for producing pellet blend |
| CN102341450A (en) * | 2009-03-04 | 2012-02-01 | 帝斯曼知识产权资产管理有限公司 | Process for preparing injection molded parts with reduced glass fiber development |
-
1998
- 1998-12-16 JP JP35783998A patent/JP2000178441A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002105312A (en) * | 2000-10-04 | 2002-04-10 | Asahi Kasei Corp | Reinforced semi-aromatic polyamide resin composition and molded article |
| JP2005263828A (en) * | 2004-03-16 | 2005-09-29 | Asahi Kasei Chemicals Corp | Long fiber reinforced polyamide resin material |
| WO2008053911A1 (en) | 2006-11-01 | 2008-05-08 | Mitsubishi Engineering-Plastics Corporation | Pellet blend of polyamide resin composition, molded article, and process for producing pellet blend |
| CN102341450A (en) * | 2009-03-04 | 2012-02-01 | 帝斯曼知识产权资产管理有限公司 | Process for preparing injection molded parts with reduced glass fiber development |
| CN106239818A (en) * | 2009-03-04 | 2016-12-21 | 帝斯曼知识产权资产管理有限公司 | For the method preparing the injection molded that the glass fibre with minimizing manifests |
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