JPH03167257A - Production of highly heat-resistant, glass fiber-reinforced polyamide composition - Google Patents
Production of highly heat-resistant, glass fiber-reinforced polyamide compositionInfo
- Publication number
- JPH03167257A JPH03167257A JP30858889A JP30858889A JPH03167257A JP H03167257 A JPH03167257 A JP H03167257A JP 30858889 A JP30858889 A JP 30858889A JP 30858889 A JP30858889 A JP 30858889A JP H03167257 A JPH03167257 A JP H03167257A
- Authority
- JP
- Japan
- Prior art keywords
- abs
- glass fiber
- polyamide
- reinforced
- mixing
- 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
- 239000000203 mixture Substances 0.000 title claims abstract description 29
- 239000011521 glass Substances 0.000 title claims abstract description 10
- 239000004952 Polyamide Substances 0.000 title claims description 33
- 229920002647 polyamide Polymers 0.000 title claims description 33
- 238000004519 manufacturing process Methods 0.000 title claims description 11
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 claims abstract description 45
- 239000003365 glass fiber Substances 0.000 claims abstract description 24
- 238000002156 mixing Methods 0.000 claims abstract description 15
- 230000007246 mechanism Effects 0.000 claims abstract description 11
- 238000001746 injection moulding Methods 0.000 claims abstract description 8
- 229920006122 polyamide resin Polymers 0.000 claims abstract description 8
- 229920000578 graft copolymer Polymers 0.000 claims abstract 3
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims description 11
- 229910045601 alloy Inorganic materials 0.000 abstract description 19
- 239000000956 alloy Substances 0.000 abstract description 19
- 238000000465 moulding Methods 0.000 abstract description 4
- 238000005457 optimization Methods 0.000 abstract description 3
- XECAHXYUAAWDEL-UHFFFAOYSA-N acrylonitrile butadiene styrene Chemical compound C=CC=C.C=CC#N.C=CC1=CC=CC=C1 XECAHXYUAAWDEL-UHFFFAOYSA-N 0.000 description 44
- 230000000704 physical effect Effects 0.000 description 9
- 229920005989 resin Polymers 0.000 description 9
- 239000011347 resin Substances 0.000 description 9
- 229920002292 Nylon 6 Polymers 0.000 description 7
- 238000000034 method Methods 0.000 description 7
- 229920000642 polymer Polymers 0.000 description 7
- 238000005516 engineering process Methods 0.000 description 6
- 238000009472 formulation Methods 0.000 description 6
- 238000004898 kneading Methods 0.000 description 6
- 230000000694 effects Effects 0.000 description 5
- 238000012360 testing method Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 239000002253 acid Substances 0.000 description 4
- 229920001577 copolymer Polymers 0.000 description 4
- 229920001971 elastomer Polymers 0.000 description 4
- 239000003925 fat Substances 0.000 description 4
- 239000011256 inorganic filler Substances 0.000 description 4
- 229910003475 inorganic filler Inorganic materials 0.000 description 4
- -1 polyhexamethylene sebacamide Polymers 0.000 description 4
- 239000005060 rubber Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- NLHHRLWOUZZQLW-UHFFFAOYSA-N Acrylonitrile Chemical compound C=CC#N NLHHRLWOUZZQLW-UHFFFAOYSA-N 0.000 description 3
- 229920002302 Nylon 6,6 Polymers 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 239000000835 fiber Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000011159 matrix material Substances 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 239000012779 reinforcing material Substances 0.000 description 3
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 206010011224 Cough Diseases 0.000 description 2
- 229920000299 Nylon 12 Polymers 0.000 description 2
- 229920000305 Nylon 6,10 Polymers 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 239000011324 bead Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 238000013329 compounding Methods 0.000 description 2
- 230000007547 defect Effects 0.000 description 2
- 238000001125 extrusion Methods 0.000 description 2
- 238000002347 injection Methods 0.000 description 2
- 239000007924 injection Substances 0.000 description 2
- FPYJFEHAWHCUMM-UHFFFAOYSA-N maleic anhydride Chemical compound O=C1OC(=O)C=C1 FPYJFEHAWHCUMM-UHFFFAOYSA-N 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 239000000178 monomer Substances 0.000 description 2
- 239000008188 pellet Substances 0.000 description 2
- 229920002285 poly(styrene-co-acrylonitrile) Polymers 0.000 description 2
- 238000006068 polycondensation reaction Methods 0.000 description 2
- 230000000379 polymerizing effect Effects 0.000 description 2
- 229920003048 styrene butadiene rubber Polymers 0.000 description 2
- 229910000838 Al alloy Inorganic materials 0.000 description 1
- KXDHJXZQYSOELW-UHFFFAOYSA-N Carbamic acid Chemical compound NC(O)=O KXDHJXZQYSOELW-UHFFFAOYSA-N 0.000 description 1
- 229920000049 Carbon (fiber) Polymers 0.000 description 1
- 241000219112 Cucumis Species 0.000 description 1
- 235000015510 Cucumis melo subsp melo Nutrition 0.000 description 1
- 229910000846 In alloy Inorganic materials 0.000 description 1
- JHWNWJKBPDFINM-UHFFFAOYSA-N Laurolactam Chemical compound O=C1CCCCCCCCCCCN1 JHWNWJKBPDFINM-UHFFFAOYSA-N 0.000 description 1
- 229920000571 Nylon 11 Polymers 0.000 description 1
- 239000005062 Polybutadiene Substances 0.000 description 1
- OFOBLEOULBTSOW-UHFFFAOYSA-N Propanedioic acid Natural products OC(=O)CC(O)=O OFOBLEOULBTSOW-UHFFFAOYSA-N 0.000 description 1
- 229920007962 Styrene Methyl Methacrylate Polymers 0.000 description 1
- FJJCIZWZNKZHII-UHFFFAOYSA-N [4,6-bis(cyanoamino)-1,3,5-triazin-2-yl]cyanamide Chemical compound N#CNC1=NC(NC#N)=NC(NC#N)=N1 FJJCIZWZNKZHII-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 238000012662 bulk polymerization Methods 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 239000004917 carbon fiber Substances 0.000 description 1
- 125000005521 carbonamide group Chemical group 0.000 description 1
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000007385 chemical modification Methods 0.000 description 1
- 239000003086 colorant Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 150000004985 diamines Chemical class 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000007720 emulsion polymerization reaction Methods 0.000 description 1
- 229920006351 engineering plastic Polymers 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 230000010006 flight Effects 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- UMORIIZQJQHCBX-UHFFFAOYSA-N furan-2,5-dione;methyl 2-methylprop-2-enoate;styrene Chemical compound COC(=O)C(C)=C.O=C1OC(=O)C=C1.C=CC1=CC=CC=C1 UMORIIZQJQHCBX-UHFFFAOYSA-N 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 150000003951 lactams Chemical class 0.000 description 1
- 239000004816 latex Substances 0.000 description 1
- 229920000126 latex Polymers 0.000 description 1
- VZCYOOQTPOCHFL-UPHRSURJSA-N maleic acid Chemical compound OC(=O)\C=C/C(O)=O VZCYOOQTPOCHFL-UPHRSURJSA-N 0.000 description 1
- 239000011976 maleic acid Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 1
- ADFPJHOAARPYLP-UHFFFAOYSA-N methyl 2-methylprop-2-enoate;styrene Chemical compound COC(=O)C(C)=C.C=CC1=CC=CC=C1 ADFPJHOAARPYLP-UHFFFAOYSA-N 0.000 description 1
- 239000010445 mica Substances 0.000 description 1
- 229910052618 mica group Inorganic materials 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 229920002857 polybutadiene Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 238000007151 ring opening polymerisation reaction Methods 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 239000000454 talc Substances 0.000 description 1
- 229910052623 talc Inorganic materials 0.000 description 1
- 229920001897 terpolymer Polymers 0.000 description 1
- VZCYOOQTPOCHFL-UHFFFAOYSA-N trans-butenedioic acid Natural products OC(=O)C=CC(O)=O VZCYOOQTPOCHFL-UHFFFAOYSA-N 0.000 description 1
- 239000010456 wollastonite Substances 0.000 description 1
- 229910052882 wollastonite Inorganic materials 0.000 description 1
Landscapes
- Injection Moulding Of Plastics Or The Like (AREA)
- Compositions Of Macromolecular Compounds (AREA)
Abstract
Description
【発明の詳細な説明】
《a》.産業上の利用分野
本発明は、改良されたガラス繊維強化ポリアミド組成物
に関する.aFL<は、ガラス山維弛化ポリアミドの物
性上の欠点を改良する方法を提示するものである.
山》.従来の技術
ポリアミド樹脂は、ta械的強度、剛性、耐薬品性など
の性質が優れているため、エンジニアリングプラスチッ
クとして各種の機械部品に使用されている.しかしポリ
アミド樹脂の欠点として、耐衝撃性、特にノフチ感度が
大きいこと、又吸水率が大きく、戒形品の寸法安定性が
劣るのみならず、吸水時に機械的特性特に曲げ弾性率が
著しく低下することが挙げられる.
この欠点を改良する手段として、{11種の高分子材料
を配合する所謂ポリマーアロイの方法が提案されている
.この中でボリアξドとアクリロニトリルースチレンー
ブタジエン共重合樹脂(以下ABSという)のアロイが
知られている.然し、一般にポリアミドとABSは相溶
性が劣る為、成形品とした時に機械的性質が期待したよ
うに出なかったり、或いは層状剥llII現象を生じた
りする欠点があった.その為、従来の技術改善の方向と
しては、両樹脂の相溶性を改良し、機械的強度、特に耐
衝撃性を向上させることが中心となっていた.例えば、
特開昭58−93745では、ポリアミドに一般の三元
組威(アクリロニトリル、スチレン、ブタジエン)のA
BSに不飽和カルボンアミドを0.5〜15%加えて共
重合させた変性ABSを配合し、二軸押出機により溶融
混練することにより、期待した耐衝撃性の向上を果たし
ている又米国特許4.777,211では、ポリアミド
樹脂とABSとの組或物に於いて、衝撃強さを改良する
為に、無水マレイン酸などの酸を含有するエチレンーア
ルキルアクリレートゴムを第三成分として、更に無水マ
レイン酸などの酸を含有するスチレン共重合体例えばス
チレンーメタクリル酸メチルー無水マレイン酸三元共重
合体を第四成分として配合することを必須条件としてい
る.又特開昭64−66255では、ポリアミドとAB
Sの相溶性を改良する為に、カルボン酸から誘導された
官能基を有するABS及びAs(スチレンーアクリロニ
トリル共重合体)、及びマレイン化エチレンプロピレン
共重合体の四成分系とし、これを二軸押出機により熔融
混合することにまり而4 (!i撃性の組成物をつくる
方法を提示している。[Detailed description of the invention] <<a>>. FIELD OF INDUSTRIAL APPLICATION This invention relates to improved glass fiber reinforced polyamide compositions. aFL< presents a method for improving the physical properties of glass fiber relaxed polyamide. Mountain". BACKGROUND OF THE INVENTION Polyamide resins have excellent properties such as mechanical strength, rigidity, and chemical resistance, so they are used as engineering plastics in various mechanical parts. However, the disadvantages of polyamide resins include high impact resistance, especially notch sensitivity, and high water absorption, which not only degrades the dimensional stability of shaped products, but also significantly reduces mechanical properties, especially flexural modulus, when water is absorbed. This can be mentioned. As a means to improve this drawback, a so-called polymer alloy method in which 11 types of polymer materials are blended has been proposed. Among these, an alloy of boria ξ-d and acrylonitrile-styrene-butadiene copolymer resin (hereinafter referred to as ABS) is known. However, since polyamide and ABS generally have poor compatibility, they have the disadvantage that when molded products are made, mechanical properties may not be as expected or the layer peeling phenomenon may occur. Therefore, conventional technological improvements have focused on improving the compatibility of both resins and improving mechanical strength, especially impact resistance. for example,
In JP-A No. 58-93745, A of a general ternary combination (acrylonitrile, styrene, butadiene) is used for polyamide.
The expected impact resistance was improved by blending BS with modified ABS, which was copolymerized by adding 0.5 to 15% of unsaturated carbonamide, and melt-kneading it using a twin-screw extruder. No. 777,211, in order to improve the impact strength of a combination of polyamide resin and ABS, an ethylene-alkyl acrylate rubber containing an acid such as maleic anhydride is used as a third component, and anhydrous It is an essential condition that a styrene copolymer containing an acid such as maleic acid, such as a styrene-methyl methacrylate-maleic anhydride terpolymer, be blended as the fourth component. Moreover, in JP-A-64-66255, polyamide and AB
In order to improve the compatibility of S, we created a four-component system of ABS and As (styrene-acrylonitrile copolymer), which have functional groups derived from carboxylic acid, and a maleated ethylene propylene copolymer, and used this as a biaxial It presents a method for making an aggressive composition by melt-mixing using an extruder.
又、特開平1−156355では、ポリア主ド20〜8
0重量部とABS等20〜80重量部との混合物100
重量部に対し無機充填材5〜100重量部を配合した組
成物に於いて、N置換マレイミドースチレン共重合体及
びAS或いはMS (スチレンーメタクリル酸メチル共
重合体)の存在を必須条件とし、これを一軸押出機、二
軸押出機、バンバリミキサー等で溶融混合することを提
案している.
このように従来技術に於いては、ボリアミト′とABS
の分散状態の改善や、基質と分散相の密着性の改善に重
点を置き、その為にABS成分中に他種成分を共重合さ
せたり、或いは第三、第四のボリマー成分を配合する手
段に頼っている。これはそれぞれ効果はうたわれており
、全般的に耐所撃性の改善の効果を強調しているが、反
面添加する第三、第四の戒分が原料の価格や少量生産に
起囚してコスト上昇を招いていることは避けられない.
更にこの組戒により犠牲となる性能としては従来技術が
ABSの酸変性やアミド変性を利用している為、必然的
に本来のABSに比べてIld湿性が低下することは明
らかであり、ポリアミドアロイをつくる一つの大きな目
的であるポリアミドの吸水時の物性低下が期待したほど
は改善されないことである.
更に、配合条件としては、汎用の一軸押出機、二軸押出
機等を提示しているだけで、配合条件による特別の効果
はうたわれていない.
更に従来技術に於いては、強化材配合の為の物性の最適
化の検討はなされていない。即ち、殆どの従来技術では
、組成物にガラス繊維、無機充填材等が配合出来るとし
ているだけで、か\る強化材や無機充填材を配合する時
に、提案された配合の利害得失については触れられてい
ないのである.即ち、従来のポリアミド−ABSアロイ
の技術は、特にガラス繊維強化材として見た場合、゛最
適の性能を発揮しているとはいえず、更にコスト上昇の
問題もあり、これらの改善が強く望まれていた。In addition, in JP-A-1-156355, Polya main do 20-8
100 parts by weight of a mixture of 0 parts by weight and 20 to 80 parts by weight of ABS, etc.
In a composition containing 5 to 100 parts by weight of an inorganic filler per part by weight, the presence of an N-substituted maleimide styrene copolymer and AS or MS (styrene-methyl methacrylate copolymer) is an essential condition, We propose melt-mixing this using a single-screw extruder, twin-screw extruder, Banbury mixer, etc. In this way, in the prior art, boria mite' and ABS
Emphasis is placed on improving the dispersion state of ABS and the adhesion between the substrate and the dispersed phase, and for this purpose, methods include copolymerizing other components into the ABS component, or blending third and fourth polymer components. I rely on it. Each of these is claimed to have an effect, and the overall effect of improving impact resistance is emphasized, but on the other hand, the third and fourth precepts of adding them are due to the price of raw materials and small-scale production. It is inevitable that costs will rise.
Furthermore, as for the performance sacrificed due to this combination, since conventional technology uses acid modification or amide modification of ABS, it is clear that Ild wettability is inevitably lower than that of original ABS, and polyamide alloy The problem is that the physical properties of polyamide, which is one of the major purposes for making it, do not improve as much as expected when it absorbs water. Furthermore, as for compounding conditions, a general-purpose single-screw extruder, a twin-screw extruder, etc. are only suggested, and no special effects of compounding conditions are mentioned. Furthermore, in the prior art, optimization of physical properties for reinforcing material formulation has not been considered. In other words, most conventional techniques only state that glass fibers, inorganic fillers, etc. can be added to the composition, but do not mention the benefits and disadvantages of the proposed combination when such reinforcing materials and inorganic fillers are added. It has not been done. In other words, the conventional polyamide-ABS alloy technology, especially when viewed as a glass fiber reinforced material, does not provide optimal performance, and there is also the problem of increased costs, so improvements in these areas are strongly desired. It was rare.
{C》.発明が解決しようとする問題点本発り1者らは
、従来技術に於.けるか覧る事1nに鑑み、ポリアミド
/ABSアロイのガラス級維配合に於ける配合処方、配
合技術、及び配合プロセスを通じて最適化を鋭意検討し
た結果、以下に詳記するように製品物性の最適化を達成
するのみならず、材料コストの上昇をも防ぎ得る手段を
見出し、本発明を完成するに至ったのである。{C}. Problems to be Solved by the Invention The inventors of the present invention have identified the problems that the invention seeks to solve in the prior art. As a result of intensive study on optimization through the formulation, formulation technology, and formulation process of the glass-grade fiber formulation of polyamide/ABS alloy, we have determined the optimum physical properties of the product as detailed below. They found a means to not only achieve this, but also prevent an increase in material costs, and have completed the present invention.
1d).問題点を解決するための手段 以下本発明を詳♀■に説明する。1d). Means to solve problems The present invention will be explained in detail below.
従来の技術では、ポリアミドとABSは相熔性が照ク、
何等かの化学的変性を行わないと強度、外観等を満足し
ないとされるのが一般的な知見であった。本発四者らは
、この問題を鋭意研究した結果、以下に詳記する特定の
溶融混合条件に於いて、一般のポリアミドとABSが充
分に混合分散することを見出し、且つこれにより従来技
術では達戒出来なかったガラス繊維強化ポリアミド−A
BSアロイの物性上の特徴を発揮させることに成功し、
この発明を完戒した.
こ覧でいうポリアミドとは、主鎖にアミド結合をもつ瓜
合体で、ジアミンと二塩基酸との重縮合、ラクタムの開
環重合、アミノカルボン酸の重縮合などにより得られる
線伏の高分子である.ポリアミドの例としては、ポリヘ
キサメチレンアジパミド(ナイロン66)、ポリへキサ
メチレンセバカミド(ナイロン610)、ポリカプロラ
クタム(ナイロン6)、ポリウンデカノアミド(ナイロ
ン11)、ポリラウリルラクタム(ナイロン12)等が
ある。本発明の配合物には、共重合体例えばナイロン6
−66、又ポリアミドの混合物例えばナイロン66とナ
イロン6の混合物も含まれる.本発明のポリアミドは、
好ましくはポリカブロラクタム(ナイロン6)である.
又こ\でいうABSとは、ゴム系重合体主幹にスチレン
、アクリロニトリルモノマーをグラフト重合させた材料
であり、ゴム系重合体とは主にポリプタジエンであり、
又スチレンーブタジエンゴムも使用される.一般に瓜合
体中のゴム成分はlO〜40重量部、スチレンは50〜
80重量部、アクリ口ニトリルは20〜50重量部であ
る。ABSの製造法としては、乳化重合法が最も汎用的
であり、ポリブタジエンラテックス中にスチレン、アク
リロニトリル両モノマーを添加し重合させることにより
製造する.従って、製品中には当然グラフトしていない
スチレンーアクリロニトリル共重合体も共存ずる.但し
、ABSの製造法としては、これに限定されるものでは
なく、塊状重合法、懸7Q重合法等によっても製造され
る.本発明で使用するABSには、実質的に化学的性質
、機械的性質、熱的性質を変化さセる量以上の第四威分
を含まないのである.
本発明は、ボリアミ■H脂30〜70重量部、AB34
M脂30〜?([1部より成る樹脂ペレット或いは粉体
の混合物100重量部に対しガラス繊維20〜100重
量部を混合し、以下の混合機構を備えた射出成形機によ
り戒形することによって、達威される。こ\で使用する
混合機構を備えたスクリュー式射出威形機の構造は次の
ようである。即ち、スクリューにはフィード部に続いて
複数のフライトで形威される可塑化・混練部が設けられ
ており、そのフライトは相対する.シリンダー内壁との
間にずり剪断がなされる程度の間隙があり、且つ咳シリ
ンダーには軸方向に連続して複数個の四部が形成されて
いる.か\る機構は、特公昭56−47847に開示さ
れている.この機構は同時にガラス繊維チョップドスト
ランドを溶融樹脂中に分散・混合させる作用も行う。In conventional technology, polyamide and ABS have poor compatibility;
It was a general knowledge that strength, appearance, etc. would not be satisfied unless some kind of chemical modification was performed. As a result of intensive research into this problem, the inventors of the present invention discovered that general polyamide and ABS can be sufficiently mixed and dispersed under specific melt-mixing conditions detailed below. Glass fiber reinforced polyamide-A that could not be achieved
Succeeded in demonstrating the physical characteristics of BS alloy,
I completely abandoned this invention. The polyamide referred to in this list is a polymer with an amide bond in the main chain, and is a linear polymer obtained by polycondensation of diamine and dibasic acid, ring-opening polymerization of lactam, polycondensation of aminocarboxylic acid, etc. It is. Examples of polyamides include polyhexamethylene adipamide (nylon 66), polyhexamethylene sebacamide (nylon 610), polycaprolactam (nylon 6), polyundecanoamide (nylon 11), polylauryllactam (nylon 12) etc. The formulations of the invention include copolymers such as nylon 6.
-66, and also mixtures of polyamides, such as mixtures of nylon 66 and nylon 6. The polyamide of the present invention is
Preferred is polycabrolactam (nylon 6). ABS referred to here is a material made by graft polymerizing styrene and acrylonitrile monomers to a rubber-based polymer, and the rubber-based polymer is mainly polyptadiene.
Styrene-butadiene rubber is also used. Generally, the rubber component in the melon mixture is 10~40 parts by weight, and the styrene is 50~40 parts by weight.
80 parts by weight, and 20 to 50 parts by weight of acrylic nitrile. Emulsion polymerization is the most commonly used method for producing ABS, and it is produced by adding both styrene and acrylonitrile monomers to polybutadiene latex and polymerizing them. Therefore, ungrafted styrene-acrylonitrile copolymer naturally coexists in the product. However, the method for producing ABS is not limited to this, and may also be produced by bulk polymerization, suspended 7Q polymerization, etc. The ABS used in the present invention does not contain a quaternary component in an amount that substantially alters its chemical, mechanical, or thermal properties. The present invention uses 30 to 70 parts by weight of Boreami ■H fat, AB34
M fat 30~? (Achieved by mixing 20 to 100 parts by weight of glass fiber with 100 parts by weight of a mixture of resin pellets or powder consisting of 1 part and molding the mixture using an injection molding machine equipped with the following mixing mechanism. The structure of the screw-type injection machine equipped with a mixing mechanism used here is as follows.In other words, the screw has a plasticizing/kneading section that is formed in multiple flights following the feed section. There is a gap between the cough cylinder and the inner wall of the cylinder that is large enough to create shear, and the cough cylinder has a plurality of four parts that are continuous in the axial direction. This mechanism is disclosed in Japanese Patent Publication No. 56-47847.This mechanism also functions to disperse and mix chopped glass fiber strands in a molten resin.
この機構が該アロイの混合に特に有効である理山は明確
でないが、以下のように推定される.即ち、一般の押出
機或いは射出威形機で使用されているスクリューの作用
は、主として樹脂に圧力を加え、フライト内を螺旋状に
流動させることにより可塑化と混合を行っているのに対
し、本発明で使用する機構では、フライト頂上とシリン
ダー内壁で樹脂に剪断力を作用させることにより可塑化
と異種成分の混合・分散を行い、これにより生成した熔
融樹脂塊をスクリューとシリンダー内面の凹部の間で切
り返しを繰り返して、分散状態の均一化を行うのである
.この作用によりABS熔融物は引きちぎられ、微細粒
子になってポリアミドマトリックス中に分散して行くの
である.その為、従来技術のように他種成分例えば有機
カルボン酸で変性した変性ABSを使川しなくてもAB
Sはポリアミドマトリックス中に充分分散するのである
。The reason why this mechanism is particularly effective for mixing the alloys is not clear, but it is presumed as follows. In other words, the action of a screw used in a general extruder or injection machine mainly applies pressure to the resin and causes it to flow spirally within the flight, thereby plasticizing and mixing it. The mechanism used in the present invention plasticizes and mixes and disperses different components by applying shearing force to the resin at the top of the flight and the inner wall of the cylinder, and the resulting molten resin mass is transferred between the screw and the recess on the inner surface of the cylinder. By repeatedly switching back and forth between the two, the distribution state is made uniform. This action causes the ABS melt to be torn apart and dispersed into fine particles in the polyamide matrix. Therefore, unlike the conventional technology, AB
S is well dispersed in the polyamide matrix.
本発明は、ガラス繊維強化ボリア主ドーABSアロイが
最高の物性を発揮させる方法を提示する.本発明者らは
前記のようにして非変性ABSを使用してつくったガラ
ス織維強化ポリアミドーABSアロイが、酸変性ABS
を使用した従来技術に比べ、機械的性能が優れるのみな
らず、特に熱変形温度に於いて優れた性能を与えること
を見出し、この発明を完威した.この理由は明確ではな
いが、次のように推定される.
即ち、ポリアミド樹脂はガラス機維に対して密着力が良
く、ガラス繊維の表面は完全にポリアξドで包まれる。The present invention presents a method to enable glass fiber reinforced boria-based ABS alloys to exhibit the best physical properties. The present inventors discovered that the glass woven fiber-reinforced polyamide ABS alloy produced using unmodified ABS as described above is similar to that of acid-modified ABS.
This invention has been perfected by discovering that it not only has superior mechanical performance, but also provides superior performance, especially at heat distortion temperatures, compared to conventional technology using The reason for this is not clear, but it is presumed as follows. That is, the polyamide resin has good adhesion to the glass fiber, and the surface of the glass fiber is completely covered with the polyamide resin.
非変性ABSを配合したアロイでは、ポリアミドマトリ
ックス中にABSが微細に分散した形態となり、ガラス
繊維にはポリアミドが優先して接触すると思われる.こ
の状態のポリアミドーABSアロイでは、ポリアミドに
比べガラス繊維との接着が弱いABSがポリアミドのガ
ラス繊維への接着を阻害することがなく、ポリアさド単
体を強化した場合に比べ熱変形温度の低下は小さいので
ある.一方、酸変性したABSを使用すると、ABSの
ガラス繊維への密着が良くなる為、ポリアミドのガラス
繊維への密着を阻害することになる.ABSがガラス繊
維に密着すると、組或物の熱変形温度はABSの影響を
受け、ポリアミド単体の強化品に比べて大幅に低下する
と推定出来る。この事実は後記の実施例により明確に説
明出来る.
本発明のガラス繊維強化ポリアミドアロイには、公知の
技術に従って、マイカ、タルク、炭酸カルシウム、ワラ
ストナイト、シリカ、ガラスビーズ,セラミックビーズ
、金fi粉末等の無機充填材、炭素繊維、アラ文ド繊維
などの強化材、着色剤等を配合しても良い.
本発明に係るガラス繊維強化ボリア文ドアロイは、以下
の実施例により明確に理解出来る。In alloys containing unmodified ABS, the ABS is finely dispersed in the polyamide matrix, and it is thought that the polyamide contacts the glass fibers preferentially. In this state of polyamide-ABS alloy, ABS, which has weaker adhesion to glass fibers than polyamide, does not inhibit the adhesion of polyamide to glass fibers, and the heat distortion temperature is lower than when polyamide alone is reinforced. It's small. On the other hand, if acid-modified ABS is used, the adhesion of ABS to glass fibers improves, which inhibits the adhesion of polyamide to glass fibers. When ABS is in close contact with glass fibers, the heat distortion temperature of the assembly is affected by ABS, and it can be estimated that it is significantly lower than that of a reinforced product made of polyamide alone. This fact can be clearly explained by the example below. The glass fiber-reinforced polyamide alloy of the present invention is prepared using inorganic fillers such as mica, talc, calcium carbonate, wollastonite, silica, glass beads, ceramic beads, gold fi powder, etc., carbon fiber, and aluminum alloy according to known techniques. Reinforcing materials such as fibers, coloring agents, etc. may be added. The glass fiber reinforced boria textured alloy according to the present invention can be clearly understood from the following examples.
《e》.作用
本発明は、ポリアミド、ABS,チョフプドストランド
ガラス鋤維混合物を、特公昭56−47847に記載さ
れた混練機構を備えた射出戒形機により射出成形するこ
とにより、従来技術では達成し得なかった物性特に熱変
形温度の高いガラス繊維強化ポリアミドABSアロイを
製造することを可能にしたものである.
(O.実施例
(1)参考例! (変性ABSの製造)A B S 4
A{脂(ダイセル化学工業f1!!!セピアンV300
パウダー)1500g,無水マレイン酸{三菱化成曲製
)15g,を2 0 0 0rrJ!スパルタノリユー
ザー(不ニパウダル側製}中で混合し、これにジターシ
中リフ゛チノレパーオキサイド(日本油脂■製)6g、
をトルエン15g、で希釈した溶液を添加し、500r
/mで3分間混合した。《e》. Function The present invention is achieved by injection molding a mixture of polyamide, ABS, and chopped strand glass plow fibers using an injection molding machine equipped with a kneading mechanism described in Japanese Patent Publication No. 56-47847, which could not be achieved with the prior art. This made it possible to produce a glass fiber reinforced polyamide ABS alloy with physical properties, particularly high heat distortion temperatures, that were previously unavailable. (O. Example (1) Reference example! (Production of modified ABS) AB S 4
A {fat (Daicel Chemical Industries f1!!! Sepian V300
Powder) 1500g, maleic anhydride (Mitsubishi Kasei Kyu) 15g, 2000rrJ! Mix in a Spartanori User (manufactured by Fuji Powder), add 6 g of Rifutinol Peroxide (manufactured by Nippon Oil & Fats Corporation) in a dither,
Add a solution diluted with 15 g of toluene, and boil for 500 r.
/m for 3 minutes.
この混合物を、同KCK製35mmφ連M混練押出機を
使用し、シリンダー温度250℃、スクリュー回転数6
Or/m、押出量10kg/hrsで押出し、ストラン
ドを水冷後ペレット化し、無水マレイン酸変性ABS
(以下M−ABS)を作成した.
(2)参考例2(ポリアミド/ABSボリマーアロイの
製造)
ポリアミド(宇部興産■製ナイロン6 10lIFB)
、ABS (上記)、及びM−ABSを表1に示すよ
うに所定量配合し、nKCK製35軸Φ連M混練押出機
を使用し、シリンダー温度250℃、スクリエー回転数
6Or/m,押出量lOkg/hrで押出し、ストラン
ドを水冷後ベレット化し、ポリアミド/ABSアロイを
作威した.作威したポリア主ド/ABSアロイは、新潟
鉄工91製NS75射出成形機を使用して、ASTMD
638及びD750試験片を戒形した.この試験片の物
性測定の結果は、表1に示す.この結果から明らかなよ
うに、M−ABSを配合した場合は特にアイゾフト衝撃
値が向上し、参考例で作成した変性ABSの効果が認め
られた。This mixture was mixed using a 35 mmφ continuous M kneading extruder manufactured by KCK at a cylinder temperature of 250°C and a screw rotation speed of 6.
Or/m, extrusion rate 10kg/hrs, strands were cooled with water, pelletized, maleic anhydride modified ABS
(hereinafter referred to as M-ABS) was created. (2) Reference example 2 (manufacture of polyamide/ABS polymer alloy) Polyamide (nylon 6 10l IFB manufactured by Ube Industries)
, ABS (above), and M-ABS were blended in predetermined amounts as shown in Table 1, and a 35-shaft Φ continuous M kneading extruder made by nKCK was used at a cylinder temperature of 250°C, a screw speed of 6 Or/m, and an extrusion amount. The strands were extruded at 10kg/hr, cooled with water, and then pelletized to produce a polyamide/ABS alloy. The produced polycarbonate/ABS alloy was manufactured using an NS75 injection molding machine made by Niigata Tekko 91, and was manufactured using ASTMD.
638 and D750 test pieces were prepared. The results of measuring the physical properties of this test piece are shown in Table 1. As is clear from the results, when M-ABS was blended, the Izoft impact value was particularly improved, and the effect of the modified ABS prepared in the reference example was recognized.
(3)ガラス繊維強化ボリア文ド/ABSアロイの製造
実施例1〜3、表2に記載した重量のポリアミドペレフ
ト(宇部興産■製ナイロン6 101 1FB) 、
ABS (ダイセル化学工業(I1J製セビアンv30
0ペレフト)、ガラス繊維(日東紡績Qli!13PE
−454)をドラムプレンダー中で混合し、特公昭56
−47847に記載された混練機構を備えた射出戒形機
(住友重機械工業nsi!!i00T)を使用し、混合
物が供給フィーダーから主スクリューの回転に連動して
供給されるようにして、ASTM D63B及びD7
50に規定する試験片を成形した.成形条件はシリンダ
ー温度260℃、スクリュー回転数100r/mである
.(ilれの試験片も樹脂分及びガラス繊維の分散は良
く、外観上の欠点は認められなかった.比較例1〜3、
実施例1〜3と同様にして、但しABSの代わりに参考
例で作成した無水マレイン酸変性ABS (M−ABS
)を使用して成形を行った.得られた試験片は、樹脂分
、ガラス繊維とも分散は良く、外観上の欠点は認められ
なかった.
実施例1〜3、比較例1〜3の物性測定の結果を表2に
示す.この結果アイゾント衝撃値、熱変形温度は非変性
のABSを配合した実施例が優れる結果となった.
(gl、発明の効果
本発明は、機械的強度及び熱変形温度の高いガラス機維
強化ポリアミド−ABSアロイをつくる製造法を開発し
たものであり、従来技術では必須条件としていた変性A
BSの使用や第三威分の添加を不必要とし、これにより
物性の向上のみならず製造コストの低減にも貢献する意
味で工業的に有益な発明である.
表1
表2
(1)
表2
(2)(3) Manufacturing Examples 1 to 3 of glass fiber-reinforced boria pattern/ABS alloy, polyamide pellets (nylon 6 101 1FB manufactured by Ube Industries ■) with the weights listed in Table 2,
ABS (Sevian v30 made by Daicel Chemical Industries (I1J)
0 PELEFT), glass fiber (Nittobo Qli!13PE
-454) in a drum blender and
Using an injection molding machine (Sumitomo Heavy Industries nsi!!i00T) equipped with a kneading mechanism described in -47847, the mixture is fed from the supply feeder in conjunction with the rotation of the main screw, and the ASTM D63B and D7
A test piece specified in No. 50 was molded. The molding conditions were a cylinder temperature of 260°C and a screw rotation speed of 100 r/m. (The resin content and glass fibers were well dispersed in the test specimens with no damage, and no defects were observed in appearance. Comparative Examples 1 to 3,
In the same manner as Examples 1 to 3, however, maleic anhydride-modified ABS (M-ABS) prepared in the reference example was used instead of ABS.
) was used for molding. In the obtained test piece, both the resin content and the glass fiber were well dispersed, and no defects were observed in appearance. Table 2 shows the results of physical property measurements of Examples 1 to 3 and Comparative Examples 1 to 3. As a result, the examples containing unmodified ABS were superior in terms of Izont impact value and heat distortion temperature. (gl, Effects of the Invention The present invention has developed a manufacturing method for producing a glass fiber-reinforced polyamide-ABS alloy with high mechanical strength and heat distortion temperature.
This is an industrially useful invention in the sense that it eliminates the need for the use of BS or the addition of a third component, thereby contributing not only to improving physical properties but also to reducing manufacturing costs. Table 1 Table 2 (1) Table 2 (2)
Claims (2)
レン系グラフト共重合体30〜70重量部の混合物10
0重量部に対しガラス繊維20〜100重量部を混合し
、特公昭56−47847に記載された混合分散機構を
備えたスクリュー式射出成形機で成形品を製造すること
を特徴とするガラス繊維強化ポリアミド組成物の製造法
。(1) Mixture 10 of 30 to 70 parts by weight of polyamide resin and 30 to 70 parts by weight of rubber-reinforced styrene graft copolymer
A glass fiber-reinforced product characterized by mixing 20 to 100 parts by weight of glass fiber to 0 parts by weight and producing a molded product using a screw injection molding machine equipped with a mixing and dispersing mechanism described in Japanese Patent Publication No. 56-47847. A method for producing a polyamide composition.
脂である請求項(1)記載のガラス繊維強化ポリアミド
組成物の製造法。(2) The method for producing a glass fiber-reinforced polyamide composition according to claim (1), wherein the rubber-reinforced styrenic graft copolymer is an ABS resin.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP30858889A JPH03167257A (en) | 1989-11-27 | 1989-11-27 | Production of highly heat-resistant, glass fiber-reinforced polyamide composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP30858889A JPH03167257A (en) | 1989-11-27 | 1989-11-27 | Production of highly heat-resistant, glass fiber-reinforced polyamide composition |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH03167257A true JPH03167257A (en) | 1991-07-19 |
Family
ID=17982844
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP30858889A Pending JPH03167257A (en) | 1989-11-27 | 1989-11-27 | Production of highly heat-resistant, glass fiber-reinforced polyamide composition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03167257A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101245171B (en) | 2007-02-13 | 2011-10-26 | 上海普利特复合材料有限公司 | Continuous fiber reinforcing vinyl cyanide-butadiene-vinyl benzene/polyamide composite material and manufacture method thereof |
-
1989
- 1989-11-27 JP JP30858889A patent/JPH03167257A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101245171B (en) | 2007-02-13 | 2011-10-26 | 上海普利特复合材料有限公司 | Continuous fiber reinforcing vinyl cyanide-butadiene-vinyl benzene/polyamide composite material and manufacture method thereof |
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