JP3479790B2 - Polycarbonate resin composition for injection molding - Google Patents
Polycarbonate resin composition for injection moldingInfo
- Publication number
- JP3479790B2 JP3479790B2 JP04608695A JP4608695A JP3479790B2 JP 3479790 B2 JP3479790 B2 JP 3479790B2 JP 04608695 A JP04608695 A JP 04608695A JP 4608695 A JP4608695 A JP 4608695A JP 3479790 B2 JP3479790 B2 JP 3479790B2
- Authority
- JP
- Japan
- Prior art keywords
- weight
- polycarbonate resin
- resin
- terpene
- injection molding
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Landscapes
- Compositions Of Macromolecular Compounds (AREA)
Description
【発明の詳細な説明】
【0001】
【産業上の利用分野】本発明は、成形加工性に優れた射
出成形用ポリカーボネート系樹脂組成物に関するもので
ある。
【0002】
【従来の技術】ポリカーボネート樹脂は耐熱性、機械的
強度(特に衝撃強度)、寸法安定性、電気的特性、透明
性、衛生性等に優れたエンジニアリングプラスチックと
して現在では電気、電子、OA、精密機械、自動車、医
療、保安、家庭用品等あらゆる分野に広く使用されてい
る。
【0003】このようにポリカーボネート樹脂はエンジ
ニアリングプラスチックとして必要な各種の特性を兼ね
備えている為、広い用途に使用できることが大きな特長
であるが、溶融粘度が高く成形加工性に劣る。
【0004】従来より、ポリカーボネート樹脂は溶融粘
度が高いため射出成形により成形品を得るためには30
0℃以上の高温で成形を行うか、ポリカーボネート樹脂
の分子量を下げる等の対策が取られてきた。しかし高温
での成形はポリカーボネート樹脂の分解は避けがたく樹
脂の色調が悪化するほか分子量低下も起こり、得られる
成形品の外観不良、強度不足の問題を引き起こす。また
樹脂の分子量を下げた場合は強度的な問題を起こす場合
が多い。
【0005】またポリカーボネート樹脂の溶融特性を改
良する方法として分岐を有するポリカーボネート樹脂を
用いたり、分子量の異なる2種のポリカーボネート樹脂
を混合する方法、さらにはポリカーボネート樹脂の変性
等(特開昭54−14633、同56−45945、同
58−138733、同64−74220、特開平3−
231919)の方法が提案されているが操作が煩雑で
あったり、成形性と物性のバランス必ずしも十分である
とはいえない。
【0006】
【発明が解決しようとする課題】本発明は、ポリカーボ
ネート樹脂の優れた諸特性を損なうことなく加熱溶融時
の流動性を改善し成形性の優れた射出成形用ポリカーボ
ネート系樹脂組成物を提供する事を目的とする。
【0007】
【課題を解決するための手段】本発明は上記課題を解決
するため、次のようなポリカーボネート系樹脂組成物を
提案した。すなわち、ポリカーボネート樹脂にテルペン
系樹脂1〜10重量%を含有させることを特長とする射
出成形用ポリカーボネート系樹脂組成物である。
【0008】本発明で用いられるポリカーボネート樹脂
はジヒドロキシ芳香族化合物とホスゲンとを反応して得
られる重合物(ホスゲン法)またはジヒドロキシ芳香族
化合物とジアリールカーボネートとを反応して得られる
重合物(エステル交換法)のいずれであってもよい。ま
たガラス繊維等の補強剤、充填剤を含有するポリカーボ
ネート樹脂も用いられる。
【0009】ここでジヒドロキシ芳香族化合物とは、芳
香核に2個のヒドロキシ基を有する芳香族化合物であっ
て、例えば、ビスフェノールA、ビスフェノールS、水
添ビスフェノールA、ビスフェノールF、2,2−ビス
(4−ヒドロキシ−3,5−ジメチルフェニル)プロパ
ン、ビス(4−ヒドロキシ−3,5−ジメチルフェニ
ル)スルホン、1,1−ビス(4−ヒドロキシフェニ
ル)シクロヘキサン等がある。
【0010】また、ジアリールカーボネートとはジフェ
ニルカーボネートのほか芳香核がカルボメトキシ基、ニ
トロ基、シアノ基、クロル基、イソプロピル基等で置換
された置換ジフェニルカーボネートなどを挙げることが
できる。
【0011】本発明で用いられるテルペン系樹脂は、有
機溶媒中でフリーデルクラフツ型触媒存在下、テルペン
単量体単独若しくは、テルペン単量体と芳香族単量体、
またはテルペン単量体とフェノール類を共重合して得ら
れたものをいう。また得られたテルペン系樹脂を水素添
加処理して得られた水添添加テルペン系樹脂であっても
よい。
【0012】テルペン単量体としてはα−ピネン、β−
ピネン、ジペンテン、d−リモネン等が挙げられ、芳香
族単量体としてはスチレン、α−メチルスチレン、ビニ
ルトルエンが挙げられる。またフェノール類としてはフ
ェノール、クレゾール、ビスフェノールA等が挙げられ
る。
【0013】この様にして得られたテルペン系樹脂は例
えばヤスハラケミカル(株)より”YSレジンPX”
(テルペン樹脂)、”YSレジンTO”(芳香族変性テ
ルペン樹脂)、”YSレジンTR”(芳香族変性テルペ
ン樹脂)、”クリアロン”(水添テルペン樹脂)、”Y
Sポリスター”(テルペンフェノール樹脂)、”マイテ
ィエース”(テルペンフェノール樹脂)の商品名で市販
されており容易に入手できる。
【0014】本発明で配合されるテルペン系樹脂の配合
量は1〜10重量%であり、好ましくは3〜5重量%で
ある。1重量%未満では、成形性(流動性)の改質効果
に乏しく、10重量%を越えると、熱的、機械的特性の
低下が著しい。
【0015】
【作用】本発明のポリカーボネート系樹脂組成物を射出
成形に使用するとポリカーボネート樹脂の優れた諸特性
を損なうことなく、成形性の優れた成形品を得ることが
できる。
【0016】
【実施例】以下実施例を挙げて本発明をさらに具体的に
説明する。
実施例1
帝人化成(株)製ポリカーボネート樹脂”パンライトK
−1300”(高粘度、高強度タイプ)を120℃で5
時間十分予備乾燥して、ヤスハラケミカル(株)製テル
ペン系樹脂”マイティエースG−150”(テルペンフ
ェノール樹脂)3重量%をドライブレンドし、2軸押出
機を用いて溶融混合してペレットとした。このペレット
を射出成形機を用いてスパイラルフロー金型による流動
性(成形性)の評価を行った。また、ASTMに準じた
各種試験片を射出成形し、機械的物性を評価した。結果
を表1に示した。なお、試験片の作製および評価方法の
詳細は以下の方法で行った。
(1)溶融混合条件
使用機器:ラボプラストミル((株)東洋精機製作所
製)
二軸押出機、D=20mm、L/D=25
混合条件:260〜290℃×70rpm
配合条件:ドライブレンド
(2)流動性試験(スパイラルフロー長、成形評価)
使用機器:射出成形機”日鉱N100B型”
1)シリンダー温度:H1/H2/H3/H4/H5/
ノズル=260/300/300/300/300/3
00℃
2)金型:2mmスパイラルフロー金型
3)金型温度:80℃
4)評価射出圧力:1220,980,730Kg/c
m2の3点
5)射出時間:20sec、冷却時間:20sec
6)計量位置:50mm、シリンダー余裕:5〜10m
m
(3)試験片の作成
使用機器:射出成形機”日鉱N100B型”
1)シリンダー温度:H1/H2/H3/H4/H5/
ノズル=260/300/300/300/300/3
00℃
2)金型温度:80℃
3)射出圧力:1220(ゲージ圧:100Kg/cm
2)
4)射出時間:20sec、冷却時間:20sec
5)計量位置:50mm、シリンダー余裕:5〜10m
m
6)成形試験片:ASTM引っ張り試験用ダンベル1
号、曲げ、アイゾット衝撃、熱変形用試験片
(4)機械物性試験
1)引張り強度(ASTM D638に準ずる)
装置:島津オートグラフAGS−10KND
引張り速度:50mm/min
測定温度、湿度:23℃、50%
2)曲げ強さおよび曲げ弾性率(ASTM D790に
準ずる)
装置:島津オートグラフAGS−10KND
曲げ速度:3mm/min
測定温度、湿度:23℃、50%
3)アイゾット衝撃強度(ASTM D256に準ず
る)
装置:IMPACT TESTAR(東洋精機製作所
製)
W=1.754Kg、R=17.957cm、α=12
5°58′
4)熱変形温度(ASTM D648に準ずる)
装置:全自動熱変形温度試験機(安田精機製作所製)
曲げ応力:4.6Kg・f/cm2
【0017】実施例2
実施例1において使用したマイティーエースG150の
使用量を3重量%から5重量%に変更した以外は実施例
1と全く同様の方法で評価した。結果を表1に示した。
【0018】実施例3
実施例1において使用したマイティーエースG150の
使用量を3重量%から10重量%に変更した以外は実施
例1と全く同様の方法で評価した。結果を表1に示し
た。
【0019】実施例4
実施例1において使用したマイティーエースG150の
使用量を3重量%から1重量%に変更した以外は実施例
1と全く同様の方法で評価した。結果を表2に示した。
【0020】実施例5
実施例1において使用したマイティーエースG150の
3重量%を水添テルペン樹脂、ヤスハラケミカル(株)
製クリアロンP−125の3重量%に変更した以外は実
施例1と全く同様の方法で評価した。結果を表2に示し
た。
【0021】実施例6
実施例1において使用したマイティーエースG150の
3重量%を水添テルペン樹脂、ヤスハラケミカル(株)
製クリアロンP−125の5重量%に変更した以外は実
施例1と全く同様の方法で評価した。結果を表2に示し
た。
【0022】実施例7
実施例1において使用したマイティーエースG150の
3重量%を芳香族変性テルペン樹脂”YSレジンTO−
125”(ヤスハラケミカル(株)製)の5重量%に変
更した以外は実施例1と全く同様の方法で評価した。結
果を表3に示した。
【0023】実施例8
実施例1において使用したマイティーエースG150の
3重量%をテルペン樹脂”YSレジンPX−1250”
(ヤスハラケミカル(株)製)の5重量%に変更した以
外は実施例1と全く同様の方法で評価した。結果を表3
に示した。
【0024】比較例1
実施例1において使用したマイティーエースG150の
3重量%を、全く用いなかった以外は実施例1と全く同
様の方法で評価した。結果を表4に示した。
【0025】比較例2
実施例1において使用したマイティーエースG150の
使用量を3重量%から0.5重量%に変更した以外は実
施例1と全く同様の方法で評価した。結果を表4に示し
た。
【0026】比較例3
実施例1において使用したマイティーエースG150の
使用量を3重量%から15重量%に変更した以外は実施
例1と全く同様の方法で評価した。結果を表4に示し
た。
【0027】
【表1】【0028】
【表2】【0029】
【表3】【0030】
【表4】【0031】表1〜表4に示した評価結果より、テルペ
ン系樹脂を1〜10重量%配合した本発明のポリカーボ
ネート系樹脂組成物では、各種機械的特性(引張り強
度、曲げ強さ、熱変形温度、衝撃強度)を大きく低下さ
せることなく流動性(成形性)が向上していることが判
る。
【0032】
【効果】本発明の射出成形用ポリカーボネート系樹脂組
成物は、コストアップとなる煩雑な化学的処理を必要と
せず単にテルペン系樹脂をブレンドするだけで、ポリカ
ーボネート樹脂の優れた諸特性を損なうことなく流動性
(成形性)の向上が達成でき工業的には極めて有用なも
のとなる。BACKGROUND OF THE INVENTION [0001] Field of the Invention The present invention is morphism excellent moldability
The present invention relates to a polycarbonate resin composition for out-molding . 2. Description of the Related Art Polycarbonate resins are currently used as engineering plastics having excellent heat resistance, mechanical strength (particularly impact strength), dimensional stability, electrical properties, transparency, hygiene, etc., and are currently used for electrical, electronic and OA applications. Widely used in various fields such as precision machinery, automobile, medical care, security, household goods, etc. As described above, a polycarbonate resin has various characteristics required as an engineering plastic, and thus has a great feature that it can be used for a wide range of applications, but has a high melt viscosity and is inferior in moldability. [0004] Conventionally, polycarbonate resins have a high melt viscosity, so that a molded product by injection molding requires 30 minutes.
Measures such as molding at a high temperature of 0 ° C. or higher or reducing the molecular weight of the polycarbonate resin have been taken. However, molding at a high temperature inevitably decomposes the polycarbonate resin, deteriorating the color tone of the resin and lowering the molecular weight, causing problems such as poor appearance and insufficient strength of the resulting molded product. Further, when the molecular weight of the resin is reduced, a problem in strength often occurs. As a method for improving the melting properties of the polycarbonate resin, a method of using a polycarbonate resin having a branch, a method of mixing two kinds of polycarbonate resins having different molecular weights, and a method of modifying the polycarbonate resin (JP-A-54-14633). JP-A-56-45945, JP-A-58-138733, JP-A-64-74220, and
231919) has been proposed, but the operation is complicated or the balance between moldability and physical properties is not always sufficient. SUMMARY OF THE INVENTION The present invention relates to a polycarbonate for injection molding which has improved flowability during heating and melting and has excellent moldability without impairing the excellent properties of the polycarbonate resin. An object of the present invention is to provide a resin composition. [0007] In order to solve the above problems, the present invention has proposed the following polycarbonate resin composition. That is, morphism that feature be contained 1 to 10% by weight terpene resin to a polycarbonate resin
It is a polycarbonate resin composition for out-molding . The polycarbonate resin used in the present invention is a polymer obtained by reacting a dihydroxy aromatic compound with phosgene (phosgene method) or a polymer obtained by reacting a dihydroxy aromatic compound with a diaryl carbonate (ester exchange). Method). Further, a polycarbonate resin containing a reinforcing agent such as glass fiber and a filler is also used. Here, the dihydroxy aromatic compound is an aromatic compound having two hydroxy groups in an aromatic nucleus. Examples thereof include bisphenol A, bisphenol S, hydrogenated bisphenol A, bisphenol F, and 2,2-bis. (4-hydroxy-3,5-dimethylphenyl) propane, bis (4-hydroxy-3,5-dimethylphenyl) sulfone, 1,1-bis (4-hydroxyphenyl) cyclohexane and the like. The diaryl carbonate includes, in addition to diphenyl carbonate, substituted diphenyl carbonate in which an aromatic nucleus is substituted with a carbomethoxy group, a nitro group, a cyano group, a chloro group, an isopropyl group and the like. The terpene resin used in the present invention may be a terpene monomer alone or a terpene monomer and an aromatic monomer in an organic solvent in the presence of a Friedel-Crafts catalyst.
Or it is obtained by copolymerizing a terpene monomer and a phenol. Further, a hydrogenated terpene-based resin obtained by subjecting the obtained terpene-based resin to a hydrogenation treatment may be used. As terpene monomers, α-pinene, β-
Examples include pinene, dipentene, and d-limonene, and examples of the aromatic monomer include styrene, α-methylstyrene, and vinyltoluene. Phenols include phenol, cresol, bisphenol A and the like. The terpene-based resin thus obtained is obtained, for example, from "Yasuhara Chemical Co., Ltd."
(Terpene resin), "YS resin TO" (aromatic modified terpene resin), "YS resin TR" (aromatic modified terpene resin), "Clearon" (hydrogenated terpene resin), "Y
S-Polyster "(terpene phenolic resin) and" Mighty Ace "(terpene phenolic resin) are commercially available and can be easily obtained.The compounding amount of the terpene resin compounded in the present invention is 1 to 10. If the amount is less than 1% by weight, the effect of modifying the moldability (flowability) is poor, and if it exceeds 10% by weight, the thermal and mechanical properties are reduced. When the polycarbonate resin composition of the present invention is used for injection molding, a molded article having excellent moldability can be obtained without impairing the excellent properties of the polycarbonate resin. The present invention will be described more specifically with reference to the following examples: Example 1 Polycarbonate resin "PANLITE K" manufactured by Teijin Chemicals Limited.
-1300 "(high viscosity, high strength type) at 120 ° C for 5
After sufficient preliminary drying for 3 hours, 3% by weight of a terpene resin “Mighty Ace G-150” (terpene phenol resin) manufactured by Yashara Chemical Co., Ltd. was dry-blended and melt-mixed using a twin-screw extruder to form pellets. The pellets were evaluated for fluidity (moldability) by a spiral flow mold using an injection molding machine. Further, various test pieces conforming to ASTM were injection-molded, and the mechanical properties were evaluated. The results are shown in Table 1. The details of the preparation and evaluation method of the test piece were performed by the following method. (1) Melt mixing conditions Equipment used: Labo Plast Mill (manufactured by Toyo Seiki Seisaku-sho, Ltd.) Twin screw extruder, D = 20 mm, L / D = 25 Mixing conditions: 260-290 ° C. × 70 rpm Compounding conditions: dry blending ( 2) Fluidity test (spiral flow length, molding evaluation) Equipment used: injection molding machine "Nikko N100B type" 1) Cylinder temperature: H1 / H2 / H3 / H4 / H5 /
Nozzle = 260/300/300/300/300/3
00 ° C 2) Mold: 2mm spiral flow mold 3) Mold temperature: 80 ° C 4) Evaluation injection pressure: 12,220,980,730Kg / c
3 points m 2 5) Injection time: 20sec, cooling time: 20sec 6) Weighing position: 50 mm, cylinder allowance: 5 to 10 m
m (3) Preparation of test piece Used equipment: injection molding machine "Nikko N100B type" 1) Cylinder temperature: H1 / H2 / H3 / H4 / H5 /
Nozzle = 260/300/300/300/300/3
00 ° C 2) Mold temperature: 80 ° C 3) Injection pressure: 1220 (gauge pressure: 100 kg / cm)
2 ) 4) Injection time: 20 sec, cooling time: 20 sec 5) Measuring position: 50 mm, cylinder allowance: 5 to 10 m
m 6) Molded test piece: dumbbell 1 for ASTM tensile test
No., bending, Izod impact, thermal deformation test specimen (4) Mechanical property test 1) Tensile strength (according to ASTM D638) Equipment: Shimadzu Autograph AGS-10KND Tensile speed: 50 mm / min Measurement temperature, humidity: 23 ° C. 50% 2) Flexural strength and flexural modulus (according to ASTM D790) Equipment: Shimadzu Autograph AGS-10KND Bending speed: 3 mm / min Measurement temperature, humidity: 23 ° C, 50% 3) Izod impact strength (as per ASTM D256) Apparatus) Device: IMPACT TESTAR (manufactured by Toyo Seiki Seisaku-sho, Ltd.) W = 1.754 Kg, R = 17.957 cm, α = 12
5 ° 58 ′ 4) Thermal deformation temperature (according to ASTM D648) Apparatus: Fully automatic thermal deformation temperature tester (manufactured by Yasuda Seiki Seisakusho) Bending stress: 4.6 kg · f / cm 2 Example 2 Example 1 Was evaluated in the same manner as in Example 1 except that the amount of Mighty Ace G150 used in Example 2 was changed from 3% by weight to 5% by weight. The results are shown in Table 1. Example 3 Evaluation was performed in the same manner as in Example 1 except that the amount of Mighty Ace G150 used in Example 1 was changed from 3% by weight to 10% by weight. The results are shown in Table 1. Example 4 Evaluation was performed in the same manner as in Example 1 except that the amount of Mighty Ace G150 used in Example 1 was changed from 3% by weight to 1% by weight. The results are shown in Table 2. Example 5 3% by weight of Mighty Ace G150 used in Example 1 was hydrogenated terpene resin, Yashara Chemical Co., Ltd.
Evaluation was performed in exactly the same manner as in Example 1 except that 3% by weight of Clearon P-125 was used. The results are shown in Table 2. Example 6 3% by weight of Mighty Ace G150 used in Example 1 was hydrogenated terpene resin, Yashara Chemical Co., Ltd.
Evaluation was performed in exactly the same manner as in Example 1 except that the amount was changed to 5% by weight of Clearon P-125. The results are shown in Table 2. Example 7 3% by weight of Mighty Ace G150 used in Example 1 was replaced with an aromatic modified terpene resin "YS Resin TO-".
Evaluation was performed in the same manner as in Example 1 except that the weight was changed to 5% by weight of 125 ″ (manufactured by Yashara Chemical Co., Ltd.). The results are shown in Table 3. Example 8 Example 8 was used in Example 1. 3 wt% of Mighty Ace G150 is a terpene resin “YS resin PX-1250”
(Yashara Chemical Co., Ltd.) was evaluated in the same manner as in Example 1 except that the weight was changed to 5% by weight. Table 3 shows the results
It was shown to. Comparative Example 1 Evaluation was performed in the same manner as in Example 1 except that 3% by weight of Mighty Ace G150 used in Example 1 was not used at all. The results are shown in Table 4. Comparative Example 2 Evaluation was performed in the same manner as in Example 1 except that the amount of Mighty Ace G150 used in Example 1 was changed from 3% by weight to 0.5% by weight. The results are shown in Table 4. Comparative Example 3 Evaluation was performed in the same manner as in Example 1 except that the amount of Mighty Ace G150 used in Example 1 was changed from 3% by weight to 15% by weight. The results are shown in Table 4. [Table 1] [Table 2] [Table 3] [Table 4] From the evaluation results shown in Tables 1 to 4, the polycarbonate resin composition of the present invention containing 1 to 10% by weight of a terpene resin shows various mechanical properties (tensile strength, flexural strength, thermal deformation). It can be seen that the fluidity (moldability) is improved without significantly lowering the temperature and impact strength. The polycarbonate resin composition for injection molding of the present invention does not require a complicated chemical treatment which increases the cost, and simply blends the terpene resin to obtain the excellent properties of the polycarbonate resin. An improvement in fluidity (moldability) can be achieved without impairment, and this is extremely useful industrially.
Claims (1)
を1〜10重量%配合してなる射出成形用ポリカーボネ
ート系樹脂組成物。(57) [Claim 1] A polycarbonate resin composition for injection molding comprising a polycarbonate resin and a terpene resin in an amount of 1 to 10% by weight.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP04608695A JP3479790B2 (en) | 1995-01-27 | 1995-01-27 | Polycarbonate resin composition for injection molding |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP04608695A JP3479790B2 (en) | 1995-01-27 | 1995-01-27 | Polycarbonate resin composition for injection molding |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH08199059A JPH08199059A (en) | 1996-08-06 |
JP3479790B2 true JP3479790B2 (en) | 2003-12-15 |
Family
ID=12737185
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP04608695A Expired - Fee Related JP3479790B2 (en) | 1995-01-27 | 1995-01-27 | Polycarbonate resin composition for injection molding |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3479790B2 (en) |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3398595B2 (en) * | 1998-05-20 | 2003-04-21 | 出光石油化学株式会社 | Polycarbonate resin composition and equipment housing using the same |
US7091267B2 (en) | 2002-03-19 | 2006-08-15 | General Electric Company | Resinous compositions, method of manufacture thereof and articles fabricated from the composition |
JP2006312670A (en) * | 2005-05-09 | 2006-11-16 | Sumitomo Dow Ltd | Flame-retardant polycarbonate resin composition |
JP4658726B2 (en) * | 2005-07-22 | 2011-03-23 | 出光興産株式会社 | Polycarbonate-polyterpene copolymer and method for producing the same |
JP5219490B2 (en) * | 2007-06-06 | 2013-06-26 | 住化スタイロンポリカーボネート株式会社 | Optical polycarbonate resin composition and optical molded article comprising the same |
WO2008149579A1 (en) * | 2007-06-06 | 2008-12-11 | Sumitomo Dow Limited | Optical polycarbonate resin composition and optical molded article comprising the same |
JP5219489B2 (en) * | 2007-06-06 | 2013-06-26 | 住化スタイロンポリカーボネート株式会社 | Optical polycarbonate resin composition and optical molded article comprising the same |
JP7218642B2 (en) * | 2019-03-26 | 2023-02-07 | 三菱ケミカル株式会社 | Polycarbonate resin composition and molded article thereof |
-
1995
- 1995-01-27 JP JP04608695A patent/JP3479790B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH08199059A (en) | 1996-08-06 |
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