JPH0584576B2 - - Google Patents

Info

Publication number
JPH0584576B2
JPH0584576B2 JP61301401A JP30140186A JPH0584576B2 JP H0584576 B2 JPH0584576 B2 JP H0584576B2 JP 61301401 A JP61301401 A JP 61301401A JP 30140186 A JP30140186 A JP 30140186A JP H0584576 B2 JPH0584576 B2 JP H0584576B2
Authority
JP
Japan
Prior art keywords
propane
bis
phosgene
torr
mol
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP61301401A
Other languages
Japanese (ja)
Other versions
JPS63227390A (en
Inventor
Tatsuya Sugano
Ikuo Takahashi
Kenichi Sasaki
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Daicel Corp
Original Assignee
Daicel Chemical Industries Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Daicel Chemical Industries Ltd filed Critical Daicel Chemical Industries Ltd
Priority to JP61301401A priority Critical patent/JPS63227390A/en
Publication of JPS63227390A publication Critical patent/JPS63227390A/en
Publication of JPH0584576B2 publication Critical patent/JPH0584576B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B41PRINTING; LINING MACHINES; TYPEWRITERS; STAMPS
    • B41MPRINTING, DUPLICATING, MARKING, OR COPYING PROCESSES; COLOUR PRINTING
    • B41M5/00Duplicating or marking methods; Sheet materials for use therein
    • B41M5/26Thermography ; Marking by high energetic means, e.g. laser otherwise than by burning, and characterised by the material used

Landscapes

  • Physics & Mathematics (AREA)
  • Optics & Photonics (AREA)
  • Thermal Transfer Or Thermal Recording In General (AREA)
  • Polyesters Or Polycarbonates (AREA)
  • Optical Record Carriers And Manufacture Thereof (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

(産業上の利用分野) この発明はレーザー光線により信号を記録しあ
るいはレーザー光線の反射又は透過により記録さ
れた信号の読み出しを行なう光学式情報記録デイ
スクに用いられるポリカーボネート共重合体から
成る光学式デイスクに関する。 (従来の技術) レーザー光線のスポツトビームをデイスクにあ
て、デイスクに微細なピツトで信号を記録あるい
はこのようなピツトによつて記録された信号をレ
ーザー光線の反射又は透過光量を検出することに
よつて読み出すDRAW(ダイレクト・リード・ア
フター・ライト),Erasable−DRAW(イレーザ
ブル−ダイレクト・リード・アフター・ライト)
型光学式情報記録再生方式は著しく記録密度を上
げることができ特にErasable−DRAW型では記
録の消去.書き込みも可能であり、且つそれらか
ら再生される画像や音質が優れた特性を有するこ
とから画像や音質の記録又は記録再生、多量の情
報記録再生等に広く実用されることが期待されて
いる。この記録再生方式に利用されるデイスクに
はデイスク本体をレーザー光線が透過するために
透明であることは勿論のこと読み取り誤差を少な
くするために光学的均質性が強く求められる。デ
イスク本体形成時の樹脂の冷却及び流動過程にお
いて生じた熱応力、分子配向、ガラス転移点付近
の容積変化による残留応力が主な原因となり、レ
ーザー光線がデイスク本体を通過する際に複屈折
が生ずる。この複屈折に起因する光学的不均一性
が大きいことは光学式デイスクとしては致命的欠
陥である。 (発明が解決しようとする問題点) このようにデイスク成形時の樹脂の冷却及び流
動過程において生じた熱応力、分子配向、残留応
力が主原因で生ずる複屈折は形成条件を選ぶこと
によつて得られるデイスクの複屈折はかなり小さ
くすることができるが、成形樹脂自身のもつ固有
の複屈折、すなわち光弾性定数に大きく依存して
いる。 (問題点を解決するための手段) 複屈折は光弾性定数と残留応力の積として下記
(1)式で表すことができる。 n1−n2=C(σ1−σ2) (1) n1−n2:複屈折 σ1−σ2:残留応力 C:光弾性定数 (1)式から光弾性定数を小さくすれば成形条件が
同じでも得られるデイスクの複屈折が小さくなる
ことは明らかである。そこで発明者らは2,2−
ビス−(4−ヒドロキシフエニル)プロパンと2,
2−ビス−(4−ヒドロキシ−3−ターシヤリー
ブチルフエニル)プロパンをカーボネート結合に
よつて共重合させることによつて芳香族ポリカー
ボネートの機械的特性を損ねることなく光弾性定
数の小さな樹脂が得られる事実を見出し、本発明
に至つたものである。 (発明の構成) 本発明は2,2−ビス−(4−ヒドロキシフエ
ニル)プロパン(I)95〜5モル%と2,2−ビ
ス−(4−ヒドロキシ−3−ターシヤリーブチル
フエニル)プロパン()5〜95モル%とをカー
ボネート結合して得られる芳香族ポリカーボネー
ト共重合体から成る光学式デイスクに関する。か
くして、この発明によれば、下記の式(I),
()で示されるビスフエノールがカーボネート
結合により共重合してなる芳香族ポリカーボネー
ト共重合体が提供される。
(Industrial Application Field) The present invention relates to an optical disk made of a polycarbonate copolymer used in an optical information recording disk that records a signal using a laser beam or reads out the recorded signal by reflecting or transmitting the laser beam. (Prior art) A spot beam of a laser beam is applied to a disk, and signals are recorded on the disk using minute pits, or signals recorded by such pits are read out by detecting the amount of reflected or transmitted light of the laser beam. DRAW (Direct Read After Write), Erasable-DRAW (Erasable-Direct Read After Write)
The optical information recording and reproducing method can significantly increase the recording density, especially with the Erasable-DRAW type, which allows erasure of records. Since it is possible to write on it, and the images and sound quality reproduced from them have excellent characteristics, it is expected that it will be widely put to practical use in recording and reproducing images and sound quality, recording and reproducing large amounts of information, etc. The disks used in this recording/reproducing system are required not only to be transparent because the laser beam passes through the disk body, but also to have optical homogeneity to reduce reading errors. Birefringence occurs when the laser beam passes through the disk body, mainly due to thermal stress generated during the cooling and flow process of the resin during disk body formation, molecular orientation, and residual stress due to volume changes near the glass transition point. This large optical non-uniformity caused by birefringence is a fatal defect for optical disks. (Problems to be Solved by the Invention) As described above, birefringence mainly caused by thermal stress, molecular orientation, and residual stress generated during the cooling and flow process of the resin during disk molding can be controlled by selecting the forming conditions. Although the birefringence of the resulting disk can be considerably reduced, it is highly dependent on the inherent birefringence of the molded resin itself, that is, the photoelastic constant. (Means to solve the problem) Birefringence is expressed as the product of photoelastic constant and residual stress as follows:
It can be expressed by equation (1). n 1 - n 2 = C (σ 1 - σ 2 ) (1) n 1 - n 2 : Birefringence σ 1 - σ 2 : Residual stress C: Photoelastic constant From equation (1), if the photoelastic constant is made smaller, It is clear that the birefringence of the disc obtained is smaller even if the molding conditions are the same. Therefore, the inventors 2,2-
bis-(4-hydroxyphenyl)propane and 2,
By copolymerizing 2-bis-(4-hydroxy-3-tertiarybutylphenyl)propane through carbonate bonds, a resin with a small photoelastic constant can be obtained without impairing the mechanical properties of aromatic polycarbonate. The present invention was developed based on the discovery of the fact that (Structure of the Invention) The present invention comprises 95 to 5 mol% of 2,2-bis-(4-hydroxyphenyl)propane (I) and 2,2-bis-(4-hydroxy-3-tert-butylphenyl). This invention relates to an optical disc made of an aromatic polycarbonate copolymer obtained by carbonate bonding with 5 to 95 mol% of propane (). Thus, according to the invention, the following formula (I),
An aromatic polycarbonate copolymer obtained by copolymerizing bisphenols represented by () through carbonate bonds is provided.

【化】[ka]

【化】 また、式()の構成単位は10〜90モル%が好
ましい。というのは、式()の構成単位が10モ
ル%未満のものであると得られる芳香族ポリカー
ボネートの光弾性定数は式(I)よりなるホモポ
リカーボネートとあまり変わらない。また、式
()の構成単位が90モル%を超えると得られる
芳香族ポリカーボネートのガラス転移点が式
(I)よりなるホモポリカーボネートに較べて著
しく低下する。なお、本発明の共重合体の粘度平
均分子量は13000〜50000が好ましい。13000未満
では共重合体がもろくなり50000を越えると共重
合体の流れが悪くなり成形性が劣る。 さらに、第3成分を共重合体させることも可能
である。本発明のポリカーボネート共重合体の製
造法としては、次の2つのの方法がある。 エステル交換法 2,2−ビス−(4−ヒドロキシフエニル)プ
ロパンと2,2−ビス−(4−ヒドロキシ−3−
ターシヤリーブチルフエニル)プロパンの混合物
に対し化学量論的に当量よりやや過剰のジフエニ
ルカーボネートに通常のカーボネート化触媒の存
在下約160〜180℃の温度下で常圧下、不活性ガス
を導入した条件下で約30分反応させ約2時間〜3
時間かけて徐々に減圧しながら180〜220℃の温度
下で最終的に10Torr,220℃下で前縮合を終了す
る。その後、10Torr,270℃下で30分,5Torr,
270℃下で20分反応し、対で0.5Torr以下好まし
くは0.3Torr〜0.1Torrの減圧下で270℃下で1.5時
間〜2.0時間後縮合を進める。尚、カーボネート
結合のためカーボネート化触媒としてはリチウム
系触媒、カリウム系触媒、ナトリウム系触媒、カ
ルシウム系触媒、錫系触媒等のアルカリ金属、ア
ルカリ土類金属触媒が適しており例えば水酸化リ
チウム、炭酸リチウム、水素化ホウ素カリウム、
リン酸水素カリウム、水酸化ナトリウム、水素化
ホウ素ナトリウム、水素化カルシウム、ジブチル
錫オキシド、酸化第1錫が挙げられる。これらの
うち、カリウム系触媒を用いることが好ましい。 ホスゲン法 三つ口フラスコにかき混ぜ機、温度計、ガス導
入管、排気管をつける。2,2−ビス−(4−ヒ
ドロキシフエニル)プロパンと2,2−ビス−
(4−ヒドロキシ−3−ターシヤリーブチルフエ
ニル)プロパンの混合物をピリジンに溶かしこれ
を激しくかき混ぜながらホスゲンガスを導入する
のであるが、ホスゲンは猛毒であるから強力なド
ラフト中で操作する。また、排気末端には水酸化
ナトリウム10%水溶液で余剰ホスゲンを分解無毒
化するユニツトをつける。ホスゲンはボンベから
の洗気びん、パラフインを入れた洗気びん(泡数
を数える)、空の洗気びんを通してフラスコに導
入する。ガラス導入管はかき混ぜ機の上に差し込
むようにし、析出するピリジン塩によつてつまら
ないようにするため先端を漏斗状に広げておく。
ガス導入に伴いピリジンの塩酸塩が析出して内容
な濁つてくる。反応温度は30℃以下になるように
水冷する。縮合の進行とともに粘ちようになつて
くる。ホスゲン−塩化水素錯体の黄色が消えなく
なるまでホスゲンを通じる。反応終了後、メタノ
ールを加えて重合体を沈殿せしめ、ろ別乾燥す
る。生成するポリカーボネートは塩化メチレン、
ピリジン、クロロホルム、テトラヒドロフランな
どに溶けるから、これらの溶液からメタノールで
再沈殿して精製する。このようにして得られるポ
リカーボネート共重合体は、レーザー光線により
信号を記録し、あるいは、レーザー光線の反射又
は透過により記録された信号の読み出しをおこな
うDRAW,Erasable−DRAW光学式情報記録用
デイスクに有用である。以下に本発明を実施例に
ついて説明するが、本発明は、これらの実施例に
よつて限定されるものではない。 実施例 1 2,2−ビス−(4−ヒドロキシフエニル)プ
ロパン192重量部(50mol%)と2,2−ビス−
(4−ヒドロキシ−3−ターシヤリーブチルフエ
ニル)プロパン122重量部(50mol%)とジフエ
ニルカーボネート264重量部を3三つ口フラス
コに入れ脱気、N2パージを5回繰り返した後、
シリコンバス160℃で窒素を導入しながら溶融さ
せた。溶融したら、カーボネート化触媒である水
素化ホウ素カリウムを予めフエノールに溶かした
溶液(仕込んだビスフエノール全量に対して10-3
mol%量)を加え、160℃、N2下、30分攪はん醸
成した。次に、同温度下、100Torrにし30分攪は
んした後、同温度下でさらに50Torrに減圧し60
分反応させた。次に徐々に温度を220℃まで上げ
60分反応させここまでの反応でフエノール留出理
論量の80%を留出させた。しかるのち、同温度下
で10Torrに減圧し30分反応させ温度を徐々に270
℃に上げ、30分反応させた。さらに同温度下で
5Torrに減圧し30分反応させ、フエノール留出理
論量のほぼ全量を留出させ前縮合を終えた。次に
同温度下で0.1〜0.3Toorで2時間後縮合させた。
窒素下にて生成物のポリマーを取り出し冷却した
後ジクロルメタンを溶媒に用いて20℃にて溶液粘
度を測定した。この値から算出した粘度平均分子
量はv=23000であつた。 実施例 2 三つ口フラスコに攪はん機、温度計、ガス導入
管、排気管をつける。ジクロルメタンに2,2−
ビス−(4−ヒドロキシフエニル)プロパン192重
量部と2,2−ビス−(4−ヒドロキシ−3−タ
ーシヤリーブチルフエニル)プロパン122重量部
を溶かし、水酸化ナトリウム10重量%水溶液を加
えこれを激しく攪はんしながらホスゲンガスを導
入した。ホスゲンはボンベから空の洗気びん、水
を入れた洗気びん、空の洗気びんを通してフラス
コに導入した。ホスゲンガスを導入中の反応温度
は25℃以下になるように水冷した。縮合の進行と
ともに溶液は粘ちようになつてくる。さらにホス
ゲン−塩化水素錯体の黄色が消えてなくなるまで
ホスゲンを通じた。反応終了後、メタノールに反
応溶液を注ぎこみろ別し水洗を繰り返した。さら
に生成したポリカーボネートはジクロルメタンの
溶液からメタノールで再沈精製した。精製後よく
乾燥したのちジクロルメタンを溶媒に用いて20℃
にて溶液粘度を測定した。この値から算出した粘
度を測定した。この値から算出した粘度平均分子
量はv=26000であつた。 (記録特性の評価) 上記のようにして製造したポリカーボネート共
重合体に記録膜を付けて、光記録特性評価した。
即ち、実施例1,2に記載のポリカーボネート共
重合体を射出成形機(名機製作所製、ダイナメル
ター)を用いて直径130mm、厚さ1.2mmの円盤状基
板に成形し、この基板上にTb23.5Fe64.2Co12.3(原
子%)の合金ターゲツトを用いてスパツタリング
装置(RFスパツタリング装置、日本真空(株)製)
中で光磁気記録膜を1000Å形成した。この記録膜
上に本出願人による特開昭60−177449号に記載の
無機ガラスの保護膜1000Åを上記と同じスパツタ
リング装置を用いて形成した。得られた光磁気デ
イスクの性能をCN比、BERおよび60℃90RH%
の条件下でのCN比変化率で評価した。結果は表
1の通りであつた。
[Image Omitted] Furthermore, the structural unit of formula () is preferably 10 to 90 mol%. This is because when the structural unit of formula () is less than 10 mol %, the photoelastic constant of the resulting aromatic polycarbonate is not much different from that of the homopolycarbonate of formula (I). Moreover, when the structural unit of formula () exceeds 90 mol %, the glass transition point of the aromatic polycarbonate obtained is significantly lower than that of the homopolycarbonate of formula (I). In addition, the viscosity average molecular weight of the copolymer of the present invention is preferably 13,000 to 50,000. If it is less than 13,000, the copolymer will become brittle, and if it exceeds 50,000, the copolymer will have poor flow and poor moldability. Furthermore, it is also possible to copolymerize the third component. There are the following two methods for producing the polycarbonate copolymer of the present invention. Transesterification method 2,2-bis-(4-hydroxyphenyl)propane and 2,2-bis-(4-hydroxy-3-
An inert gas is introduced into a slightly stoichiometrically equivalent excess of diphenyl carbonate to a mixture of tert-butylphenyl (tertiary butyl phenyl) propane at a temperature of about 160 to 180° C. under normal pressure in the presence of a conventional carbonation catalyst. React for about 30 minutes under the same conditions for about 2 to 3 hours.
The precondensation is completed at a temperature of 180 to 220°C while gradually reducing the pressure over time, and finally at 10 Torr and 220°C. After that, 10 Torr, 30 minutes at 270℃, 5 Torr,
The reaction is carried out at 270° C. for 20 minutes, and the condensation is continued at 270° C. for 1.5 to 2.0 hours under reduced pressure of less than 0.5 Torr, preferably 0.3 Torr to 0.1 Torr. For carbonate bonding, alkali metal or alkaline earth metal catalysts such as lithium-based catalysts, potassium-based catalysts, sodium-based catalysts, calcium-based catalysts, and tin-based catalysts are suitable as carbonation catalysts, such as lithium hydroxide, carbonate, etc. Lithium, potassium borohydride,
Examples include potassium hydrogen phosphate, sodium hydroxide, sodium borohydride, calcium hydride, dibutyltin oxide, and stannous oxide. Among these, it is preferable to use a potassium catalyst. Phosgene method Attach a stirrer, thermometer, gas inlet pipe, and exhaust pipe to a three-necked flask. 2,2-bis-(4-hydroxyphenyl)propane and 2,2-bis-
A mixture of (4-hydroxy-3-tertiarybutylphenyl)propane is dissolved in pyridine, and the mixture is vigorously stirred while phosgene gas is introduced. Since phosgene is extremely poisonous, the process is carried out in a strong fume hood. Additionally, a unit is installed at the exhaust end to decompose and detoxify excess phosgene using a 10% sodium hydroxide aqueous solution. Phosgene is introduced into the flask through the air wash bottle from the cylinder, the air wash bottle containing paraffin (count the number of bubbles), and the empty air wash bottle. The glass introduction tube should be inserted into the top of the stirrer, and the tip should be widened into a funnel shape to prevent it from becoming clogged by precipitated pyridine salt.
As gas is introduced, pyridine hydrochloride precipitates out and the mixture becomes cloudy. Cool with water so that the reaction temperature is 30°C or less. As condensation progresses, it becomes sticky. Phosgene is passed through the mixture until the yellow color of the phosgene-hydrogen chloride complex no longer disappears. After the reaction is completed, methanol is added to precipitate the polymer, which is then filtered and dried. The polycarbonate produced is methylene chloride,
Since it is soluble in pyridine, chloroform, tetrahydrofuran, etc., it is purified by reprecipitation from these solutions with methanol. The polycarbonate copolymer thus obtained is useful for DRAW and Erasable-DRAW optical information recording disks that record signals using laser beams or read out recorded signals by reflection or transmission of laser beams. . EXAMPLES The present invention will be described below with reference to Examples, but the present invention is not limited to these Examples. Example 1 192 parts by weight (50 mol%) of 2,2-bis-(4-hydroxyphenyl)propane and 2,2-bis-
122 parts by weight (50 mol%) of (4-hydroxy-3-tert-butylphenyl)propane and 264 parts by weight of diphenyl carbonate were placed in a three-necked flask, and degassing and N2 purging were repeated five times.
It was melted in a silicon bath at 160°C while introducing nitrogen. Once melted, add a solution of potassium borohydride, which is a carbonation catalyst, dissolved in phenol (10 -3 based on the total amount of bisphenol charged).
(mol% amount) was added and stirred and incubated at 160°C under N 2 for 30 minutes. Next, at the same temperature, the pressure was increased to 100 Torr, and after stirring for 30 minutes, the pressure was further reduced to 50 Torr at the same temperature, and the pressure was reduced to 60 Torr.
It was allowed to react for a minute. Then gradually increase the temperature to 220℃
The reaction was continued for 60 minutes, and 80% of the theoretical amount of phenol was distilled out through the reaction up to this point. After that, the pressure was reduced to 10 Torr at the same temperature, and the reaction was allowed to proceed for 30 minutes, and the temperature was gradually increased to 270°C.
The mixture was raised to ℃ and allowed to react for 30 minutes. Furthermore, at the same temperature
The pressure was reduced to 5 Torr and the reaction was allowed to proceed for 30 minutes, and almost all of the theoretical amount of phenol was distilled out to complete the precondensation. Next, condensation was carried out at the same temperature for 2 hours at 0.1 to 0.3 Toor.
After the product polymer was taken out and cooled under nitrogen, the solution viscosity was measured at 20°C using dichloromethane as a solvent. The viscosity average molecular weight calculated from this value was v=23000. Example 2 A three-necked flask is equipped with a stirrer, a thermometer, a gas inlet pipe, and an exhaust pipe. 2,2- in dichloromethane
Dissolve 192 parts by weight of bis-(4-hydroxyphenyl)propane and 122 parts by weight of 2,2-bis-(4-hydroxy-3-tert-butylphenyl)propane, add a 10% by weight aqueous solution of sodium hydroxide, and dissolve. Phosgene gas was introduced while stirring vigorously. Phosgene was introduced from the cylinder into the flask through an empty air wash bottle, a water filled air wash bottle, and an empty air wash bottle. The reaction temperature during the introduction of phosgene gas was water-cooled so as to be below 25°C. As the condensation progresses, the solution becomes viscous. Further, phosgene was passed through the mixture until the yellow color of the phosgene-hydrogen chloride complex disappeared. After the reaction was completed, the reaction solution was poured into methanol, filtered, and washed with water repeatedly. Furthermore, the produced polycarbonate was purified by reprecipitation with methanol from a dichloromethane solution. After purification, dry thoroughly and heat at 20℃ using dichloromethane as a solvent.
The solution viscosity was measured. The viscosity calculated from this value was measured. The viscosity average molecular weight calculated from this value was v=26,000. (Evaluation of recording properties) A recording film was attached to the polycarbonate copolymer produced as described above, and the optical recording properties were evaluated.
That is, the polycarbonate copolymers described in Examples 1 and 2 were molded into a disc-shaped substrate with a diameter of 130 mm and a thickness of 1.2 mm using an injection molding machine (manufactured by Meiki Seisakusho, Dynamelter), and Tb was applied onto this substrate. Sputtering equipment (RF sputtering equipment, manufactured by Japan Vacuum Co., Ltd.) using an alloy target of 23.5 Fe 64.2 Co 12.3 (atomic%)
A magneto-optical recording film with a thickness of 1000 Å was formed inside. On this recording film, a protective film of 1000 Å of inorganic glass as described in Japanese Patent Application Laid-open No. 177449/1983 by the present applicant was formed using the same sputtering apparatus as above. The performance of the obtained magneto-optical disk was measured by CN ratio, BER and 60℃90RH%.
It was evaluated by the rate of change in CN ratio under the following conditions. The results were as shown in Table 1.

【表】 表1の結果から明らかなように、本発明によるポ
リカーボネート共重合体は複屈折値の低下により
CN比が大幅に向上しており、耐久性にも優れて
いることがわかる。
[Table] As is clear from the results in Table 1, the polycarbonate copolymer according to the present invention has a lower birefringence value.
It can be seen that the CN ratio has been significantly improved and the durability is also excellent.

Claims (1)

【特許請求の範囲】[Claims] 1 2,2−ビス−(4−ヒドロキシフエニル)
プロパン95〜5モル%と2,2−ビス−(4−ヒ
ドロキシ−3−ターシヤリーブチルフエニル)プ
ロパン5〜95モル%とをカーボネート結合して得
られる芳香族ポリカーボネート共重合体から成る
光学式デイスク。
1 2,2-bis-(4-hydroxyphenyl)
An optical formula consisting of an aromatic polycarbonate copolymer obtained by carbonate bonding of 95 to 5 mol% of propane and 5 to 95 mol% of 2,2-bis-(4-hydroxy-3-tert-butylphenyl)propane. disc.
JP61301401A 1986-12-19 1986-12-19 Optical disk Granted JPS63227390A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61301401A JPS63227390A (en) 1986-12-19 1986-12-19 Optical disk

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61301401A JPS63227390A (en) 1986-12-19 1986-12-19 Optical disk

Publications (2)

Publication Number Publication Date
JPS63227390A JPS63227390A (en) 1988-09-21
JPH0584576B2 true JPH0584576B2 (en) 1993-12-02

Family

ID=17896424

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61301401A Granted JPS63227390A (en) 1986-12-19 1986-12-19 Optical disk

Country Status (1)

Country Link
JP (1) JPS63227390A (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6269072B1 (en) * 1999-10-22 2001-07-31 Victor Company Of Japan, Ltd. Optical disc

Also Published As

Publication number Publication date
JPS63227390A (en) 1988-09-21

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