JPH0798901B2 - Polyphenylene sulfide composition - Google Patents
Polyphenylene sulfide compositionInfo
- Publication number
- JPH0798901B2 JPH0798901B2 JP61084175A JP8417586A JPH0798901B2 JP H0798901 B2 JPH0798901 B2 JP H0798901B2 JP 61084175 A JP61084175 A JP 61084175A JP 8417586 A JP8417586 A JP 8417586A JP H0798901 B2 JPH0798901 B2 JP H0798901B2
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- pps
- chlorine
- polymer
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- ppm
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- Polymers With Sulfur, Phosphorus Or Metals In The Main Chain (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 本発明はポリマー中の結合塩素含有量が500ppm以下であ
るポリフェニレンスルフィド(以下PPSと略す)と無機
充てん剤から成る組成物に関するものである。本発明の
組成物は電気特性に優れ、電気,電子部品類の被覆や封
止材料として特に有用である。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a composition comprising polyphenylene sulfide (hereinafter abbreviated as PPS) having a bound chlorine content of 500 ppm or less in a polymer and an inorganic filler. The composition of the present invention has excellent electrical properties and is particularly useful as a coating material or sealing material for electric and electronic parts.
従来の成形用PPS組成物としては特公昭45−3368号公報
に開示されている方法によって製造した低重合度のPPS
を酸化架橋することにより見かけの溶融粘度を上昇させ
たものを原料ポリマーとし、これに充てん剤を加えた組
成物が知られている。As a conventional PPS composition for molding, PPS having a low degree of polymerization produced by the method disclosed in JP-B-45-3368.
There is known a composition in which a material having an apparent melt viscosity increased by oxidative crosslinking is used as a raw material polymer and a filler is added thereto.
一方、重合時に助剤を使用したり、分子中に3個以上の
ハロゲンを有するポリハロベンゼンを共重合させること
により酸化架橋せずに高分子量化したPPSを原料ポリマ
ーとし、これに充てん剤を加えた組成物も知られてい
る。On the other hand, by using an auxiliary agent at the time of polymerization or by copolymerizing polyhalobenzene having 3 or more halogens in the molecule, PPS which has not been oxidatively crosslinked and has a high molecular weight is used as a raw material polymer, and a filler is added to this. Additive compositions are also known.
しかしながら、これら上記の組成物を電気,電子部品の
分野に適用しようとするとPPS中の食塩等の多量のナト
リウムおよび塩素による電気特性の低下が大きな障害と
なる。すなわち、ナトリウムおよび塩素を多量に含有す
るPPSを例えばIC等の電子部品の封止に使用した場合に
は、吸湿により回路の絶縁性を低下させたり、電極やリ
ードフレームなどが腐食されて断線するなどの素子の特
性劣化や故障を引き起こす原因となる。However, if the above-mentioned compositions are to be applied to the fields of electric and electronic parts, the deterioration of electric characteristics due to a large amount of sodium and chlorine such as salt in PPS becomes a serious obstacle. That is, when PPS containing a large amount of sodium and chlorine is used to seal electronic components such as ICs, the insulation of the circuit may be reduced due to moisture absorption, or the electrodes or lead frame may be corroded and broken. It may cause the deterioration of the characteristics of the element such as the above and the failure.
そこで、これらの欠点を改善するための方法として、熱
水でPPS粉末を数回抽出することにより、水抽出可能な
ナトリウム量を100ppm以下にするという方法が特開昭55
−156342号公報に開示されている。しかし、本発明者ら
の研究によれば、この方法においては、極めて長い時間
抽出をくり返したにもかかわらず、抽出されるナトリウ
ム量はポリマー粒子表面に付着しているものや、極く表
面層にあるものだけであり、依然ポリマー中には1000pp
m以上のナトリウムが存在しており、除去効果に乏しい
ものであった。さらにこの方法により精製したPPS中の
塩素含有量を定量してみると2000〜3000ppm程度存在し
ており、PPS中の塩素低減効果は全く見られなかった。Therefore, as a method for improving these drawbacks, a method of extracting the PPS powder several times with hot water so that the amount of sodium that can be extracted with water is 100 ppm or less is known.
-156342. However, according to the study by the present inventors, in this method, the amount of sodium extracted was such that the amount of sodium adhering to the surface of the polymer particles or the surface layer was extremely small, even though the extraction was repeated for an extremely long time. There is still only 1000 pp in the polymer.
There was sodium above m, and the removal effect was poor. Furthermore, when the chlorine content in PPS purified by this method was quantified, it was found to be about 2000 to 3000 ppm, and no chlorine reducing effect was found in PPS.
また、特開昭59−219331号公報には、PPSを芳香族溶媒
中で加熱処理してナトリウム含有量を低減する方法が開
示されている。この方法によれば、ナトリウム含有量に
ついては低減が可能であるが、塩素については処理後の
ポリマー中に2000〜3000ppm程度含まれており、除去効
果は見られなかった。Further, JP-A-59-219331 discloses a method of heating PPS in an aromatic solvent to reduce the sodium content. According to this method, the sodium content can be reduced, but chlorine was contained in the treated polymer in an amount of about 2000 to 3000 ppm, and no removal effect was observed.
このように、従来の技術でPPSの精製を試みてもナトリ
ウム含有量の低減は可能でも塩素含有量の低減は不可能
で、そのようなPPSを原料ポリマーとして用いた組成物
は、電気,電子部品類の被覆や封止材料として用いるの
に依然として満足すべき純度のものではない。Thus, even if attempts were made to purify PPS by conventional techniques, the sodium content could be reduced, but the chlorine content could not be reduced. It is not yet of satisfactory purity for use as a coating or sealing material for parts.
本発明は、これらの要望に答えるべく鋭意研究の結果、
PPS中にイオン結合性の塩素を実質的に含まず、ナトリ
ウム含有量のみならず共有結合性塩素含有量をも極度に
低減したPPSを原料ポリマーとし、これに無機充てん剤
を加えた組成物が、電気,電子部品分野に優れた適用性
を有することを見出し、本発明を完成した。The present invention, as a result of earnest research to answer these demands,
PPS, which does not substantially contain ionic bond chlorine in PPS and has extremely reduced not only sodium content but also covalent bond chlorine content, is used as a raw material polymer, and a composition obtained by adding an inorganic filler to it is prepared. The inventors have found that they have excellent applicability in the fields of electric and electronic parts, and have completed the present invention.
即ち本発明はPPSを処理することによりポリマー中の結
合塩素含有量が500ppm以下としたPPSを原料ポリマーと
し、これに無機充てん剤を加えたPPS組成物に関するも
のである。本発明で言う結合塩素とは、炭素原子に直接
結合した共有結合性の塩素であり、NaCl等としてポリマ
ー中に含まれているようなイオン結合性の塩素を意味す
るものではない。また、この共有結合性の塩素中には、
残存モノマーとしてのジクロルベンゼンの塩素は含まな
い。このようなポリマー中に含まれる共有結合性塩素の
定量はイオンクロマト等により共有結合性塩素とイオン
結合性塩素の総和を定量した後、ESCA(Electron Spect
roscopy for Chemical Analysis)により、共有結合性
塩素とイオン結合性塩素の比を求め、定量した。That is, the present invention relates to a PPS composition prepared by treating PPS with a combined chlorine content in the polymer of 500 ppm or less as a raw material polymer and adding an inorganic filler to the raw material polymer. The bound chlorine referred to in the present invention is a covalent chlorine directly bonded to a carbon atom, and does not mean an ionic chlorine contained in a polymer as NaCl or the like. In addition, in this covalent chlorine,
It does not contain chlorine of dichlorobenzene as a residual monomer. The amount of covalently bound chlorine contained in such a polymer is determined by quantifying the total amount of covalently bound chlorine and ionicly bound chlorine by ion chromatography, etc.
roscopy for Chemical Analysis), the ratio of covalently bound chlorine to ionicly bound chlorine was determined and quantified.
本発明において使用されるPPSは、高純度に精製されて
おり、PPS中にイオン結合性の塩素を実質的に含まず、
ナトリウム含有量のみならず結合塩素含有量をも500ppm
以下、好ましくは100ppm以下に低減されている。ここで
イオン結合性塩素を実質的に含まないとは、PPS中のイ
オン結合性塩素含有量が100ppm以下程度であることを意
味する。PPS used in the present invention has been purified to a high degree of purity, substantially free of ionic bond chlorine in PPS,
500ppm not only for sodium content but also for combined chlorine content
Below, it is preferably reduced to 100 ppm or less. The phrase "substantially free of ionic bond chlorine" means that the content of ionic bond chlorine in PPS is about 100 ppm or less.
本発明において使用されるPPSは、少なくとも90モル%
以上、さらに好ましくは95モル%以上が 構成単位からなるポリ(P−フェニレンスルフィド)で
あり、残りの構成単位は共重合可能な単位であればよ
く、例えばオルトおよびメタフェニレンスルフィド,ビ
フェニスルフィド,2,6−ナフタレンスルフィド,ジフェ
ニルスルホンスルフィド,ジフェニルケトンスルフィド
や分子中3個以上のハロゲンを有するモノマーを共重合
することによって導入される3価,4価のフェニレンスル
フィド等が挙げられる。さらに本発明で使用されるPPS
は酸素共存下に加熱処理することにより酸化架橋したも
のであってもよい。The PPS used in the present invention is at least 90 mol%
Or more, more preferably 95 mol% or more It is a poly (P-phenylene sulfide) composed of structural units, and the remaining structural units may be copolymerizable units such as ortho and metaphenylene sulfides, biphenyl sulfides, 2,6-naphthalene sulfides, diphenyl sulfone sulfides. Examples thereof include diphenyl ketone sulfide and trivalent or tetravalent phenylene sulfide introduced by copolymerizing a monomer having three or more halogens in the molecule. Further PPS used in the present invention
May be oxidatively crosslinked by heat treatment in the presence of oxygen.
また、本発明において使用されるPPSは高化式フローテ
スター(ダイス:穴径0.5mm,穴長2mm)により300℃,10k
g荷重で測定した溶融粘度が10〜50000ポイズの範囲にあ
ることが好ましい。In addition, the PPS used in the present invention uses a high-performance flow tester (die: hole diameter 0.5 mm, hole length 2 mm) at 300 ° C, 10 k
The melt viscosity measured by g-load is preferably in the range of 10 to 50,000 poise.
本発明の組成物に使用される高純度PPSは本発明者が先
に出願した特願昭60−245318号や特願昭60−277913号の
方法、即ち特公昭45−3368号公報等で開示されているよ
うな公知の方法によってPPSを製造した後、このように
して製造したPPSとメルカプト基含有化合物のアルカリ
金属塩またはメルカプト基含有化合物またはジスルフィ
ドと必要に応じて塩基とをPPSを溶解し得る溶媒中で加
熱処理することなどにより製造される。即ち、ポリフェ
ニレンスルフィドと一般式(1)で示されるメルカプト
基含有化合物 (Rは炭化水素基または複素環式化合物残基であり、M
は水素原子又はアルカリ金属であり、Aはカルボキシル
基または水酸基または置換,未置換アミノ基またはニト
ロ基であり、xは1〜6の整数、yは0〜6の整数であ
る)と一般式(2)で示されるジスルフィド (AxR−S−S−R′A)y (2) (R,R′は炭化水素基または複素環式化合物残基であ
り、RとR′は同一であってもよく、Aはカルボキシル
基または水酸基または置換,未置換アミノ基またはニト
ロ基であり、x,yは0〜6の整数である)とから選ばれ
る化合物と必要に応じて塩基とをポリフェニレンスルフ
ィドを溶解し得る溶媒中で加熱処理して製造される。例
えば公知法により製造したPPSと2−メルカプトベンズ
イミダゾール等のメルカプト基含有化合物と水酸化ナト
リウム等の塩基とをN−メチルピロリドン中で220〜260
℃にて0.5〜10時間反応させる等の方法である。このよ
うな処理により、PPS中のナトリウム含有量のみならず
結合塩素含有量をも500ppm以下、更には100ppm以下に低
減することができる。The high-purity PPS used in the composition of the present invention is disclosed in the method of Japanese Patent Application No. 60-245318 and Japanese Patent Application No. 60-277913 previously filed by the present inventor, that is, Japanese Patent Publication No. 45-3368. After producing PPS by a known method as described above, PPS and the alkali metal salt of the mercapto group-containing compound or the mercapto group-containing compound or disulfide thus produced and PPS are dissolved with a base as necessary. It is produced by heat treatment in the solvent to be obtained. That is, polyphenylene sulfide and a mercapto group-containing compound represented by the general formula (1) (R is a hydrocarbon group or a heterocyclic compound residue,
Is a hydrogen atom or an alkali metal, A is a carboxyl group or a hydroxyl group, a substituted or unsubstituted amino group or a nitro group, x is an integer of 1 to 6, and y is an integer of 0 to 6) and a general formula ( Disulfide represented by 2) (A x R-S-S-R'A) y (2) (R and R'are a hydrocarbon group or a heterocyclic compound residue, and R and R'are the same. A is a carboxyl group, a hydroxyl group, a substituted or unsubstituted amino group or a nitro group, and x and y are integers of 0 to 6) and a base, if necessary, with polyphenylene sulfide. Is produced by heat treatment in a solvent capable of dissolving. For example, PPS produced by a known method, a mercapto group-containing compound such as 2-mercaptobenzimidazole, and a base such as sodium hydroxide in N-methylpyrrolidone are used in an amount of 220 to 260
It is a method such as reacting at 0 ° C for 0.5 to 10 hours. By such a treatment, not only the sodium content in PPS but also the combined chlorine content can be reduced to 500 ppm or less, further 100 ppm or less.
本発明のPPS組成物は、上記の方法により得られた高純
度PPSと無機充てん剤とを配合することによって得られ
る。無機充てん剤は、例えば粉末,顆粒または繊維等の
形状で使用できる。本発明で使用することのできる無機
充てん剤の若干の例としては、ガラス繊維,アスベスト
繊維,セラミック繊維,炭素繊維,ガラスビーズ,ガラ
ス粉末,タルク,シリカ,クレー,雲母,アルミナ,硫
酸カルシウム,炭酸カルシウム,チタン酸カリウム,酸
化鉄,酸化亜鉛,酸化チタン等が挙げられる。これら無
機充てん剤の添加量は、5〜85重量%、好ましくは10〜
80重量%である。添加量が少なすぎると充分な充てん効
果が得られず、また多すぎると、成形性が劣ったり、成
形品とした時に脆くなる等の問題が生じ好ましくない。The PPS composition of the present invention can be obtained by blending the high-purity PPS obtained by the above method and the inorganic filler. The inorganic filler can be used, for example, in the form of powder, granules or fibers. Some examples of inorganic fillers that can be used in the present invention are glass fiber, asbestos fiber, ceramic fiber, carbon fiber, glass beads, glass powder, talc, silica, clay, mica, alumina, calcium sulfate, carbonic acid. Examples thereof include calcium, potassium titanate, iron oxide, zinc oxide and titanium oxide. The amount of these inorganic fillers added is 5 to 85% by weight, preferably 10 to
80% by weight. If the addition amount is too small, a sufficient filling effect cannot be obtained, and if the addition amount is too large, problems such as poor moldability and brittleness when formed into a molded product are not preferable.
以上のようにして得られた本発明のPPS組成物は、射出
成形,トランスファー成形,押出成形等により、各種成
形品,フィルム,シート,パイプ等に成形可能であり、
特に電気,電子部品類の被覆や封止材料として用いるの
に極めて有用である。The PPS composition of the present invention obtained as described above can be molded into various molded products, films, sheets, pipes, etc. by injection molding, transfer molding, extrusion molding, etc.
In particular, it is extremely useful for coating electric and electronic parts and as a sealing material.
以下、本発明を実施例によって具体的に説明するが、本
発明はこれら実施例のみに限定されるものではない。Hereinafter, the present invention will be specifically described by way of examples, but the present invention is not limited to these examples.
なお、以下の実施例および比較例中で使用されるPPS中
のナトリウム含有量は、約0.5gの試料を石英ビーカー中
で約10mlの硫酸および約10mlの硝酸で湿式分解させた
後、脱イオン水を加えて一定量に調製した液を原子吸光
分析により求めた。またPPS中の結合塩素含有量は約30m
gの試料をフラスコ燃焼法により灰化した後、N/100NaOH
aqに吸収、脱イオン水を加えて一定量に調製した液をイ
オンクロマトで測定し、塩素の全量を定量した後、ESCA
(島津製作所製ESCA−750)により共有結合性塩素とイ
オン結合性塩素の比を求め、これらの値より共有結合性
塩素を定量した。ESCAの測定は、X線源としてMgターゲ
ットを用い、エネルギー8KV,30mAで測定した。The sodium content in the PPS used in the following examples and comparative examples is about 0.5 g of a sample, which is deionized after wet decomposition with about 10 ml of sulfuric acid and about 10 ml of nitric acid in a quartz beaker. A solution prepared by adding water to a constant amount was determined by atomic absorption spectrometry. The combined chlorine content in PPS is about 30 m.
After ashing a sample of g by the flask combustion method, N / 100NaOH
After absorption and deionized water were added to aq and adjusted to a fixed amount, the liquid was measured by ion chromatography and the total amount of chlorine was quantified.
The ratio of covalent bond chlorine and ionic bond chlorine was obtained by (Shimadzu ESCA-750), and covalent bond chlorine was quantified from these values. ESCA was measured at a energy of 8 KV and 30 mA using a Mg target as an X-ray source.
PPSの溶融粘度は、高化式フローテスター(ダイス;穴
径0.5mm,穴長2mm)により、300℃,10kg荷重で測定し
た。The melt viscosity of PPS was measured with a Koka type flow tester (die; hole diameter 0.5 mm, hole length 2 mm) at 300 ° C. under a load of 10 kg.
実施例1 15l容量のオートクレープにNa2S・2.9H2O14.6モル,N−
メチルピロリドン4.9lを入れ、窒素気流下攪拌して210
℃まで昇温し、340gの主に水からなる留出液を留去し
た。その後系を170℃まで冷却し、P−ジクロルベンゼ
ン14.5モルを添加し、窒素気流下に系を封入、昇温して
250℃にて3時間重合した。重合終了後減圧下でN−メ
チルピロリドンを蒸留回収した後、水でポリマーを洗浄
し、乾燥,単離した。得られたポリマーの収量は1490
g、溶融粘度は210ポイズであり、ポリマー中のナトリウ
ムおよび塩素含有量はそれぞれ2200ppm,2900ppmであっ
た。Example 1 Into a 15 l autoclave was added Na 2 S.2.9H 2 O 14.6 mol, N-
Add 4.9 l of methylpyrrolidone and stir under a nitrogen stream to 210
The temperature was raised to 0 ° C., and 340 g of a distillate mainly composed of water was distilled off. After that, the system was cooled to 170 ° C, 14.5 mol of P-dichlorobenzene was added, the system was sealed under a nitrogen stream, and the temperature was raised.
Polymerization was carried out at 250 ° C for 3 hours. After completion of the polymerization, N-methylpyrrolidone was distilled and recovered under reduced pressure, and then the polymer was washed with water, dried and isolated. The yield of the obtained polymer is 1490.
g, melt viscosity was 210 poise, and sodium and chlorine contents in the polymer were 2200 ppm and 2900 ppm, respectively.
次いでこのPPS1400gと2−メルカプトベンズイミダゾー
ル0.65モル,NaOH0.65モル,N−メチルピロリドン5.0lを1
5l容量のオートクレーブに仕込み、系内を窒素で置換し
た後、昇温して260℃にて1時間反応を行った。反応終
了後減圧下でN−メチルピロリドンを蒸留回収した後、
水を添加しポリマーを200℃にて4時間洗浄し乾燥,単
離した。得られたポリマーの収量は1330g,溶融粘度は20
4ポイズであり、ポリマー中のナトリウム含有量は56pp
m,結合塩素含有量は100ppm以下であった。Next, 1400 g of this PPS, 0.65 mol of 2-mercaptobenzimidazole, 0.65 mol of NaOH, and 5.0 l of N-methylpyrrolidone were added to 1 part.
The autoclave having a capacity of 5 l was charged, the system was replaced with nitrogen, and the temperature was raised to carry out a reaction at 260 ° C. for 1 hour. After completion of the reaction, N-methylpyrrolidone was distilled and recovered under reduced pressure.
Water was added and the polymer was washed at 200 ° C. for 4 hours, dried and isolated. The yield of the obtained polymer was 1330 g and the melt viscosity was 20.
4 poise, sodium content in polymer is 56pp
The content of m and bound chlorine was less than 100 ppm.
このようにして得た高純度のPPSを260℃で3時間、酸素
共存下で加熱処理し、溶融粘度3070ポイズとした後、こ
のPPS60重量部とガラス繊維(直径13μm,長さ3mmのチョ
プドストランド)40重量部をVブレンダーにて均一に混
合してからスクリュー径40mmの押出機にてシリンダー温
度310℃で混練ペレット化した。次に射出成形機を用い
て前記ペレットをシリンダー温度310℃,射出圧力800kg
/cm2,金型温度135℃の条件においてあらかじめアルミ
製金具をインサートした金具に射出した。The high-purity PPS thus obtained was heated at 260 ° C. for 3 hours in the presence of oxygen to obtain a melt viscosity of 3070 poise, and 60 parts by weight of this PPS and glass fiber (diameter 13 μm, length 3 mm chopped 40 parts by weight of strand) were uniformly mixed in a V blender, and then kneaded into pellets at a cylinder temperature of 310 ° C. in an extruder having a screw diameter of 40 mm. Next, using an injection molding machine, the pellets were heated to a cylinder temperature of 310 ° C. and an injection pressure of 800 kg.
/ cm 2 and mold temperature of 135 ° C were injected into the metal fittings into which aluminum metal fittings were previously inserted.
得られた成形物から試料10個を任意に取出し、80℃,95
%RHふん囲気中に1000時間放置し、アルミ製金具の腐食
状況を調べた。その結果アルミ製金具の腐食は試料10個
中0個であった。10 samples were taken out from the obtained molded product at 80 ℃, 95
It was left to stand in% RH atmosphere for 1000 hours, and the corrosion state of aluminum metal fittings was examined. As a result, corrosion of aluminum metal fittings was 0 out of 10 samples.
実施例2 実施例1と同様の方法により重合、高純度化したPPS
(溶融粘度200ポイズ,ナトリウム含有量40ppm,結合塩
素含有量100ppm以下)を230℃で2時間酸素共存下で加
熱処理し、溶融粘度を550ポイズとした後、このPPS35重
量部とガラス繊維(直径13μm,長さ3mmのチョップドス
トランド)35重量部,炭酸カルシウム30重量部を実施例
1と同様に混練,ペレット化した。このペレットを用い
て実施例1と同様に射出成形によりインサート成形し、
得られた成形物について実施例1と同条件で耐湿性試験
を行った。その結果、アルミ製金具の腐食は試料10個中
0個であった。Example 2 Polymerized and highly purified PPS by the same method as in Example 1
(Melt viscosity 200 poise, sodium content 40ppm, bound chlorine content 100ppm or less) was heat-treated at 230 ° C for 2 hours in the presence of oxygen to make the melt viscosity 550 poise, and then 35 parts by weight of this PPS and glass fiber (diameter 35 parts by weight of chopped strands (13 μm, length 3 mm) and 30 parts by weight of calcium carbonate were kneaded and pelletized in the same manner as in Example 1. Using this pellet, insert molding was performed by injection molding in the same manner as in Example 1,
A moisture resistance test was conducted on the obtained molded product under the same conditions as in Example 1. As a result, the corrosion of the aluminum metal fittings was 0 out of 10 samples.
実施例3 実施例1と同様の方法により重合を行い、溶融粘度230
ポイズ,ナトリウム含有量2400ppm,塩素含有量3000ppm
のPPS1520gを得た。次いでこのPPS1400gと二硫化フェニ
ル0.65モル,NaOH0.65モル,N−メチルピロリドン5.0lを1
5l容量のオートクレーブに仕込み、系内を窒素で置換し
た後昇温して200℃にて2時間反応を行った。反応終了
後、減圧下でN−メチルピロリドンを蒸留回収した後水
を添加しポリマーを200℃にて4時間洗浄し、乾燥,単
離した。得られたポリマーの収量は1300g,溶融粘度は10
5ポイズであり、ポリマー中のナトリウム含有量は23pp
m,結合塩素含有量は100ppm以下であった。Example 3 Polymerization was carried out in the same manner as in Example 1 to obtain a melt viscosity of 230
Poise, sodium content 2400ppm, chlorine content 3000ppm
1520 g of PPS was obtained. Next, 1400 g of this PPS, 0.65 mol of phenyl disulfide, 0.65 mol of NaOH, and 5.0 l of N-methylpyrrolidone were added to 1 part.
The autoclave having a volume of 5 l was charged, the system was replaced with nitrogen, and the temperature was raised to carry out a reaction at 200 ° C. for 2 hours. After completion of the reaction, N-methylpyrrolidone was distilled and recovered under reduced pressure, water was added, and the polymer was washed at 200 ° C. for 4 hours, dried and isolated. The yield of the obtained polymer was 1300 g and the melt viscosity was 10
It is 5 poise and the sodium content in the polymer is 23 pp
The content of m and bound chlorine was less than 100 ppm.
このようにして得た高純度のPPSを260℃で4時間酸素共
存下で加熱処理し溶融粘度3140ポイズとした後、このPP
S60重量部とガラス繊維(直径13μm,長さ3mmのチョップ
ドストランド)40重量部を実施例1と同様に混練,ペレ
ット化した。このペレットを用いて実施例1と同様に射
出成形によりインサート成形し、得られた成形物につい
て実施例1と同条件で耐湿性試験を行った。その結果、
アルミ製金具の腐食は試料10個中0個であった。The high-purity PPS thus obtained was heated at 260 ° C. for 4 hours in the presence of oxygen to obtain a melt viscosity of 3140 poise,
In the same manner as in Example 1, 60 parts by weight of S and 40 parts by weight of glass fiber (chopped strand having a diameter of 13 μm and a length of 3 mm) were kneaded and pelletized. Using this pellet, insert molding was performed by injection molding in the same manner as in Example 1, and the obtained molded product was subjected to a moisture resistance test under the same conditions as in Example 1. as a result,
Corrosion of aluminum metal fittings was 0 out of 10 samples.
比較例1 実施例1と同様の公知法により重合を行い、溶融粘度21
0ポイズ,ナトリウム含有量2000ppm,塩素含有量2800ppm
のPSS1500gを得た。このPPSを260℃で3時間酸素共存下
で加熱処理し、溶融粘度を3140ポイズとした後、このPP
S60重量部とガラス繊維(直径13μm,長さ3mmのチョップ
ドストランド)40重量部を実施例1と同様に混練,ペレ
ット化した。このペレットを用いて実施例1と同様に射
出成形によりインサート成形し、得られた成形物につい
て実施例1と同条件で耐湿性試験を行った。その結果、
アルミ製金具の腐食は試料10個中10個すべてに認められ
た。Comparative Example 1 Polymerization was carried out by the same known method as in Example 1 to obtain a melt viscosity of 21
0 poise, sodium content 2000ppm, chlorine content 2800ppm
I got 1500g of PSS. After heat-treating this PPS at 260 ° C for 3 hours in the presence of oxygen to make the melt viscosity 3140 poise,
In the same manner as in Example 1, 60 parts by weight of S and 40 parts by weight of glass fiber (chopped strand having a diameter of 13 μm and a length of 3 mm) were kneaded and pelletized. Using this pellet, insert molding was performed by injection molding in the same manner as in Example 1, and the obtained molded product was subjected to a moisture resistance test under the same conditions as in Example 1. as a result,
Corrosion of aluminum metal fittings was found in all 10 of the 10 samples.
以上の説明から明らかなように、本発明のPPS組成物
は、電気,電子部品分野に優れた適用性を有し、電気,
電子部品類の被覆や封止材料として用いるのに極めて有
用である。As is clear from the above description, the PPS composition of the present invention has excellent applicability in the fields of electric and electronic parts.
It is extremely useful for coating electronic parts and as a sealing material.
───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 昭62−106929(JP,A) 特開 昭61−220446(JP,A) 特開 昭62−150752(JP,A) 特開 昭62−185717(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (56) Reference JP 62-106929 (JP, A) JP 61-220446 (JP, A) JP 62-150752 (JP, A) JP 62- 185717 (JP, A)
Claims (1)
500ppm以下であるポリフェニレンスルフィド15〜95重量
%と無機充てん剤5〜85重量%を含有することを特徴と
するポニフェニレンスルフィド組成物。1. (N: 20 or more) as a constituent unit
A poniphenylene sulfide composition comprising 15 to 95% by weight of polyphenylene sulfide which is 500 ppm or less and 5 to 85% by weight of an inorganic filler.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61084175A JPH0798901B2 (en) | 1986-04-14 | 1986-04-14 | Polyphenylene sulfide composition |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP61084175A JPH0798901B2 (en) | 1986-04-14 | 1986-04-14 | Polyphenylene sulfide composition |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS62241961A JPS62241961A (en) | 1987-10-22 |
| JPH0798901B2 true JPH0798901B2 (en) | 1995-10-25 |
Family
ID=13823151
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP61084175A Expired - Fee Related JPH0798901B2 (en) | 1986-04-14 | 1986-04-14 | Polyphenylene sulfide composition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0798901B2 (en) |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5015703A (en) * | 1989-06-29 | 1991-05-14 | General Electric Company | Reactively capped polyarylene sulfide and method and intermediates for their preparation |
| US5015704A (en) * | 1989-06-29 | 1991-05-14 | General Electric Company | Reactively capped polyarylene sulfide and method and intermediates for their preparation |
| JP2009155419A (en) * | 2007-12-26 | 2009-07-16 | Polyplastics Co | Polyarylene sulfide resin composition |
| JP2010030177A (en) * | 2008-07-30 | 2010-02-12 | Toray Ind Inc | Complex and process for manufacturing the same |
| JP5514532B2 (en) * | 2009-12-21 | 2014-06-04 | 株式会社ニックス | Sliding parts, resin composition for forming sliding parts, and spindle motor provided with sliding parts |
| US20130035440A1 (en) * | 2010-04-23 | 2013-02-07 | Polyplastics Co., Ltd. | Polyarylene sulfide resin composition |
| JP6504817B2 (en) * | 2011-09-20 | 2019-04-24 | ティコナ・エルエルシー | Low halogen content disulfide washed polyarylene sulfide |
| EP2758463A2 (en) * | 2011-09-20 | 2014-07-30 | Ticona LLC | Low chlorine filled melt processed polyarylene sulfide composition |
| US20180354900A1 (en) | 2015-12-07 | 2018-12-13 | Sumitomo Seika Chemicals Co., Ltd. | Composition containing anticaking agent |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61220446A (en) * | 1985-03-27 | 1986-09-30 | Toray Ind Inc | Resin sealed electronic device |
| JP2525357B2 (en) * | 1985-12-25 | 1996-08-21 | 東レ株式会社 | Resin-sealed electronic components |
-
1986
- 1986-04-14 JP JP61084175A patent/JPH0798901B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPS62241961A (en) | 1987-10-22 |
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