JPH07324138A - Method of molding optical component - Google Patents

Method of molding optical component

Info

Publication number
JPH07324138A
JPH07324138A JP6797595A JP6797595A JPH07324138A JP H07324138 A JPH07324138 A JP H07324138A JP 6797595 A JP6797595 A JP 6797595A JP 6797595 A JP6797595 A JP 6797595A JP H07324138 A JPH07324138 A JP H07324138A
Authority
JP
Japan
Prior art keywords
polycarbonate
powder
optical component
bis
silver
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
Application number
JP6797595A
Other languages
Japanese (ja)
Inventor
Seiichiro Maruyama
征一郎 丸山
Hiroyuki Kawasaki
博行 河崎
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.)
Mitsubishi Chemical Corp
Original Assignee
Mitsubishi Chemical Corp
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 Mitsubishi Chemical Corp filed Critical Mitsubishi Chemical Corp
Priority to JP6797595A priority Critical patent/JPH07324138A/en
Publication of JPH07324138A publication Critical patent/JPH07324138A/en
Pending legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B9/00Making granules
    • B29B9/12Making granules characterised by structure or composition
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C2045/0091Pellets or granules, e.g. their structure, composition, length, height, width
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2069/00Use of PC, i.e. polycarbonates or derivatives thereof, as moulding material

Abstract

PURPOSE:To provide an optical component-molding method whereby the formation of a silver streak on an optical component can be prevented, and the percentage of rejects can be markedly lowered. CONSTITUTION:An optical component reduced in the formation of silver streak is molded from pellets made of a polycarbonate of a molecular weight of 10000-18000 and having a content of a powdery polymer of a mean particle diameter of 0.5mm or below of 2.0-wt.% or below.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明はシルバーの発生の少ない
光ディスク等の光学用部品の成形方法に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method of molding an optical component such as an optical disk which rarely produces silver.

【0002】[0002]

【従来の技術】ポリカーボネート樹脂は透明性、耐熱
性、低吸水性が優れているために、光学用途特に最近は
光ディスク用成形材料として使用されはじめた。光ディ
スクではミクロンオーダーの信号をレーザー光線で読取
り書き込む必要があるため、光ディスクの基板中にミク
ロンオーダー以上の欠陥があると読み取り、書き込みが
出来なくエラーレートの悪化をまねく。このような欠陥
としては樹脂の熱劣化による黒点が有名であるが、それ
以外にシルバー(銀条)といわれる線状欠陥がある。黒
点についてはポリカーボネート樹脂中に有機亜リン酸エ
ステルを含有させることによる対策が行なわれている
(特開昭58−126119号公報参照)。
2. Description of the Related Art Polycarbonate resins are excellent in transparency, heat resistance, and low water absorption, and have been used as molding materials for optical applications, especially optical discs recently. Since it is necessary to read and write signals of micron order with a laser beam in an optical disk, if there is a defect of micron order or more in the substrate of the optical disk, reading and writing cannot be performed and the error rate deteriorates. Black spots due to heat deterioration of the resin are well known as such defects, but there are other linear defects called silver. Regarding the black spots, countermeasures have been taken by incorporating an organic phosphite into a polycarbonate resin (see JP-A-58-126119).

【0003】[0003]

【発明が解決しようとする課題】一方シルバーについて
は一般に形状も大きいこともあって問題視されてきた
が、原因として成形直前ペレットの水分の含有率が0.
01%以上の乾燥不充分、又は成形条件の不適正等が考
えられ種々の対策がほどこされてきた。しかしシルバー
による不良率を1%以下にすることは未だ出来てないの
が現状である。
On the other hand, silver has been regarded as a problem because it generally has a large shape, but the cause is that the moisture content of the pellets immediately before molding is 0.
Various measures have been taken in consideration of insufficient drying of 01% or more, or inadequate molding conditions. However, the current situation is that it has not been possible to reduce the defective rate due to silver to 1% or less.

【0004】[0004]

【課題を解決するための手段】本発明者らは、光学的部
品である光ディスク基板の成形においてシルバーの発生
を抑制するために、原因検討を行ったところ、意外にも
粒状体中に粒径1mm以下の微粉が存在することが原因
であることを見い出し本発明に到達した。すなわち、本
願発明の要旨は、分子量が10000〜18000のポ
リカーボネートペレット中における平均粒径0.5mm
以下の粉末状重合体含有量が2.0重量%以下であるポ
リカーボネートペレットを用いることを特徴とするシル
バー発生の少ない光学用部品の成形方法に存する。
Means for Solving the Problems The inventors of the present invention have investigated the cause in order to suppress the generation of silver in the molding of an optical disk substrate which is an optical component. The inventors have found that the cause is the presence of fine powder having a size of 1 mm or less, and have reached the present invention. That is, the gist of the present invention is that the average particle diameter in a polycarbonate pellet having a molecular weight of 10,000 to 18,000 is 0.5 mm.
The present invention resides in a method for molding an optical component with less silver generation, which comprises using a polycarbonate pellet having a powdery polymer content of 2.0% by weight or less.

【0005】 〔発明の詳細な説明〕以下本発明を具体的に説明する。
本発明におけるポリカーボネート樹脂は、種々のジヒド
ロキシジアリール化合物とホスゲンとを反応させるホス
ゲン法、またはジヒドロキシジアリール化合物とジフェ
ニルカーボネートなどの炭酸エステルとを反応させるエ
ステル交換法によって得られる重合体または共重合体で
あり、代表的なものとしては、2,2−ビス(4−ヒド
ロキシフェニル)プロパン(ビスフェノールA)から製
造されたポリカーボネート樹脂があげられる。
DETAILED DESCRIPTION OF THE INVENTION The present invention will be specifically described below.
The polycarbonate resin in the present invention is a polymer or copolymer obtained by a phosgene method of reacting various dihydroxydiaryl compounds with phosgene, or a transesterification method of reacting a dihydroxydiaryl compound with a carbonic acid ester such as diphenyl carbonate. A typical example thereof is a polycarbonate resin produced from 2,2-bis (4-hydroxyphenyl) propane (bisphenol A).

【0006】上記ジヒドロキシジアリール化合物として
は、ビスフェノールAの他、ビス(4−ヒドロキシフェ
ニル)メタン、1,1−ビス(4−ヒドロキシフェニ
ル)エタン、2,2−ビス(4−ヒドロキシフェニル)
ブタン、2,2−ビス(4−ヒドロキシフェニル)オク
タン、ビス(4−ヒドロキシフェニル)フェニルメタ
ン、2,2−ビス(4−ヒドロキシ−3−メチルフェニ
ル)プロパン、1,1−ビス(4−ヒドロキシ−3−第
3ブチルフェニル)プロパン、2,2−ビス(4−ヒド
ロキシ−3−ブロモフェニル)プロパン、2,2−ビス
(4−ヒドロキシ−3,5ジブロモフェニル)プロパ
ン、2,2−ビス(4−ヒドロキシ−3,5ジクロロフ
ェニル)プロパンのようなビス(ヒドロキシアリール)
アルカン類、1,1−ビス(4−ヒドロキシフェニル)
シクロペンタン、1,1−ビス(4−ヒドロキシフェニ
ル)シクロヘキサンのようなビス(ヒドロキシアリー
ル)シクロアルカン類、4,4′−ジヒドロキシジフェ
ニルエーテル、4,4′−ジヒドロキシ−3,3′−ジ
メチルジフェニルエーテル、のようなジヒドロキシジア
リールエーテル類、4,4′−ジヒドロキシジフェニル
スルフィド、4,4′−ジヒドロキシ−3,3′−ジメ
チルジフェニルスルフィドのようなジヒドロキシジアリ
ールスルフィド類、4,4′−ジヒドロキシジフェニル
スルホキシド、4,4′−ジヒドロキシ−3,3′−ジ
メチルジフェニルスルホキシドのようなジヒドロキシジ
アリールスルホキシド類、4,4′−ジヒドロキシジフ
ェニルスルホン、4,4′−ジヒドロキシ−3,3′−
ジメチルジフェニルスルホンのようなジヒドロキシジア
リールスルホン類等があげられる。
Examples of the dihydroxydiaryl compound include bisphenol A, bis (4-hydroxyphenyl) methane, 1,1-bis (4-hydroxyphenyl) ethane, and 2,2-bis (4-hydroxyphenyl).
Butane, 2,2-bis (4-hydroxyphenyl) octane, bis (4-hydroxyphenyl) phenylmethane, 2,2-bis (4-hydroxy-3-methylphenyl) propane, 1,1-bis (4- Hydroxy-3-tert-butylphenyl) propane, 2,2-bis (4-hydroxy-3-bromophenyl) propane, 2,2-bis (4-hydroxy-3,5dibromophenyl) propane, 2,2- Bis (hydroxyaryl) such as bis (4-hydroxy-3,5dichlorophenyl) propane
Alkanes, 1,1-bis (4-hydroxyphenyl)
Cyclopentane, bis (hydroxyaryl) cycloalkanes such as 1,1-bis (4-hydroxyphenyl) cyclohexane, 4,4′-dihydroxydiphenyl ether, 4,4′-dihydroxy-3,3′-dimethyldiphenyl ether, Dihydroxy diaryl ethers such as 4,4'-dihydroxy diphenyl sulfide, dihydroxy diaryl sulfides such as 4,4'-dihydroxy-3,3'-dimethyldiphenyl sulfide, 4,4'-dihydroxy diphenyl sulfoxide, , 4'-Dihydroxy-3,3'-dimethyldiphenyl sulfoxide, such as dihydroxydiaryl sulfoxides, 4,4'-dihydroxydiphenyl sulfone, 4,4'-dihydroxy-3,3'-
Examples thereof include dihydroxydiaryl sulfones such as dimethyldiphenyl sulfone.

【0007】これらは単独でまたは2種以上混合して使
用されるが、これらの他にピペラジン、ジピペリジル、
ハイドロキノン、レゾルシン、4,4′−ジヒドロキシ
ジフェニル等を混合して使用してもよい。光ディスク等
の光学用部品には光学的ひずみのないことが要求される
ので、分子量は10000〜18000、好ましくは1
1000〜17000の範囲にする必要がある。なお、
ここでいう分子量(M)はオストワルド粘度計を用い塩
化メチレンを溶媒とする溶液の極限粘度〔η〕を求め、
Schnellの粘度式
These may be used alone or in admixture of two or more, but in addition to these, piperazine, dipiperidyl,
Hydroquinone, resorcin, 4,4'-dihydroxydiphenyl and the like may be mixed and used. Since optical components such as optical disks are required to have no optical distortion, the molecular weight is 10,000 to 18,000, preferably 1
It should be in the range of 1000 to 17000. In addition,
The molecular weight (M) as used herein is determined by using an Ostwald viscometer to obtain the intrinsic viscosity [η] of a solution containing methylene chloride as a solvent
Schnell's viscosity formula

【0008】[0008]

【数1】〔η〕=1.23×10-50.83 [Equation 1] [η] = 1.23 × 10 −5 M 0.83

【0009】から求められる。光ディスク等の光学用部
品に用いられるポリカーボネート成形材料には低粘度の
ものが使用されるので、成形機のスクリューによるせん
断発熱が少なく、通常2〜4mmの粒径の粒状体(ペレ
ット)中の1mm径以下の微粉の重合体はシリンダーか
らの熱でしか溶融されない。しかしポリカーボネートな
どの重合体の熱伝導性は低いので、微粉の重合体は未溶
融状態で射出成形され、成形品中にシルバー状欠陥とし
て観察される。したがって粉末状重合体の含有量が2.
0重量%より多いと未溶融粉末となる可能性が大きくシ
ルバーの発生が多く、2.0重量%以下、好ましくは
1.0重量%以下ならばシルバーによる不良率を1〜2
%以下におさえられ、光学用途としても要求される目標
に達成される。
[0009] Polycarbonate molding materials used for optical parts such as optical discs have low viscosity, so there is little shear heat generation by the screw of the molding machine, and it is usually 1 mm in granules (pellets) with a particle size of 2 to 4 mm. A finely divided polymer having a diameter not larger than that can be melted only by heat from the cylinder. However, since a polymer such as polycarbonate has a low thermal conductivity, a finely divided polymer is injection-molded in an unmelted state and is observed as a silver-like defect in a molded product. Therefore, the content of the powdery polymer is 2.
If it is more than 0% by weight, unmelted powder is likely to occur and silver is often generated. If it is 2.0% by weight or less, preferably 1.0% by weight or less, the defective rate due to silver is 1-2.
%, And the target required for optical applications is achieved.

【0010】本発明におけるポリカーボネート成形材料
において、平均粒径が0.5mm以下のポリカーボネー
ト粉末含有量を2%以下にするためには、溶融ポリマー
を冷却してペレット化するカッティング工程でのカッテ
ィング条件を最適化し粉末発生量を極小化すること、ペ
レット化以降についても全工程にわたりペレットに加わ
る機械的剪断力をできるだけ小さくし粉末の発生を極力
抑える必要がある。特に乾燥工程、配合工程、包装工程
などの各工程、およびこれら工程間を結ぶ空送等のペレ
ット輸送工程におけるペレット同志、ペレットと装置器
壁との衝突を極小化し、またすべての単位操作において
回転式攪拌機などの強度の剪断履歴を与える手段を用い
ないことが重要である。本発明で使用するような10,
000〜18,000の比較的低分子量のポリカーボネ
ートは強度が弱くなるためペレット化するカッティング
工程において粉末が発生しやすい。従ってペレット化時
のカッター刃の摩耗、ストランドの温度などが粉末の発
生に大きな要因となる。また製造工程において不可避的
に発生したポリカーボネート粉末については、製造工程
の最終段階において該粉末を低減せしめることも可能で
ある。粉末除去の方法としては振動篩など機械的方法が
よく知られている。ただしペレット表面に付着した微細
な粉末は機械的方法では満足に除去し難く、また水洗等
の特殊な粉末除去を行なうときは、工程の煩雑化、生産
能率の低下を招く。したがって製造工程で粉末の発生量
を極小化し、さらに最終工程で粉末量を低減することが
より好ましい。
In the polycarbonate molding material of the present invention, in order to reduce the content of the polycarbonate powder having an average particle diameter of 0.5 mm or less to 2% or less, the cutting conditions in the cutting step of cooling and pelletizing the molten polymer are set. It is necessary to optimize the generation amount of the powder to the minimum and to suppress the mechanical shearing force applied to the pellet as much as possible in the whole process even after the pelletization to suppress the generation of the powder as much as possible. In particular, minimizes collision between pellets, pellets and equipment walls in each process such as drying process, compounding process, packaging process, and pellet transport process such as empty transportation that connects these processes, and rotates in all unit operations. It is important not to use means such as a mechanical stirrer to provide a strong shear history. 10, as used in the present invention,
Since a polycarbonate having a relatively low molecular weight of 000 to 18,000 has low strength, powder is likely to be generated in the pelletizing cutting process. Therefore, the abrasion of the cutter blade during pelletization, the temperature of the strand, etc. are major factors in the generation of powder. Further, regarding the polycarbonate powder which is inevitably generated in the manufacturing process, it is possible to reduce the powder at the final stage of the manufacturing process. A mechanical method such as a vibrating screen is well known as a method for removing powder. However, it is difficult to satisfactorily remove the fine powder adhering to the pellet surface by a mechanical method, and when performing special powder removal such as washing with water, the process becomes complicated and the production efficiency is lowered. Therefore, it is more preferable to minimize the amount of powder generated in the manufacturing process and further reduce the amount of powder in the final process.

【0011】本発明におけるポリカーボネートペレット
中の全粉末量の測定は、次の方法により行なう。ポリカ
ーボネートペレット100〜200gを秤量した後、3
0メッシュのステンレス金網容器に入れ、300〜40
0ccのメタノール中でよく振盪してペレットを洗浄
し、粉末をメタノール中に分離せしめる。ここで分離さ
れる粉末は通常粒径1mm以下である。
The total amount of powder in the polycarbonate pellets of the present invention is measured by the following method. After weighing 100 to 200 g of polycarbonate pellets, 3
Put in 0 mesh stainless wire mesh container, 300-40
The pellet is washed by shaking well in 0 cc of methanol and the powder is separated in methanol. The powder separated here usually has a particle size of 1 mm or less.

【0012】この洗浄液をG4ガラスフィルターで濾別
する。この操作をメタノール中に浮遊物が認められなく
なるまで繰り返す。通常4〜5回の操作で濾取された残
渣の重量は恒量に達する。この残渣の重量は粉末重量と
する。以上はペレットに添加剤が表面付着されていない
場合であるが、通常ポリカーボネートは添加剤が全て練
込まれていることが多く、特に光ディスクなどのように
成形室のクリーン度をクラス1000以下に保持するに
は添加剤が全て練込まれている方が好ましい。添加剤が
表面添着されている場合には、メタノール中に添加剤も
移行するため添加剤の定性、定量を行なわなければなら
ない。分析の具体的方法については添加剤の種類により
それぞれ異なるので個々の添加剤について各々最適の定
量方法を選定すればよい。
The washing solution is filtered with a G4 glass filter. This operation is repeated until no suspended substance is observed in methanol. Usually, the weight of the residue collected by filtration after 4 to 5 times reaches a constant weight. The weight of this residue is the weight of the powder. The above is the case where the additive is not attached to the surface of the pellet, but usually the additive is usually mixed in polycarbonate, and the cleanliness of the molding chamber is maintained below class 1000, especially for optical discs. To this end, it is preferable that all the additives are kneaded. When the additive is surface-attached, the additive also migrates into methanol, so the additive must be qualitatively and quantitatively determined. Since the specific method of analysis differs depending on the type of additive, it is only necessary to select the optimum quantification method for each additive.

【0013】ポリカーボネートペレットは通常2.0〜
3.5mm径の球状又は直径および長さが2.0〜4.
0mmの円柱の粒状体になっており、直径又は長さが
2.0mm以上ならば形状は特に問題ではない。粉末の
平均粒径の測定は前述のようにして採集した粒径1mm
以下の粉末を光学顕微鏡を用い、視野内の200〜10
00個の粉末粒子について粒子の最大幅(粒子の投影像
をその面内の二平行線によって挟むときその距離の最大
のもの)を測定し、算術平均をとったものとする。本発
明における成形材料はスクリュー等の剪断力で可塑化す
る成形機、すなわち射出成形機、射出圧縮成形機、押出
成形機において有効で、ディスク、レンズ、ミラー、銘
板、シート、プレートなどの種々のものに加工される。
Polycarbonate pellets are usually 2.0-
3.5 mm diameter spherical or diameter and length 2.0-4.
It is a cylindrical granular body of 0 mm, and if the diameter or the length is 2.0 mm or more, the shape does not matter. The average particle size of the powder is measured by the particle size of 1 mm collected as described above.
Using an optical microscope, the following powders were used in a field of view of 200 to 10
It is assumed that the maximum width of the particles (the maximum distance between the projected images of the particles when they are sandwiched by the two parallel lines in the surface) is measured for 00 powder particles, and the arithmetic mean is taken. The molding material in the present invention is effective in a molding machine that plasticizes by shearing force such as a screw, that is, an injection molding machine, an injection compression molding machine, and an extrusion molding machine, and can be used for various materials such as disks, lenses, mirrors, nameplates, sheets and plates. Processed into a thing.

【0014】[0014]

【実施例】以下本発明について実施例により更に詳しく
説明するが、本発明はこれらの実施例に限定されるもの
ではない。 実施例1、2、比較例1 常法によりビスフェノールAとホスゲンを界面重合法で
重合して、得られた分子量15000のポリカーボネー
ト粉末に、有機亜リン酸エステル(トリスノニルフェニ
ルフォスファイト、アデカアーガス社製 Mark 1
178)を0.05%をブレンド後、40mmφベント
押出機にて250℃でストランド状に押出し、ペレット
化のためカッティングし、2.5mm径、3.0mm長
さの円柱状ペレットを得た。この粒状体を前述に記載の
方法で粉末状重合体の平均粒径及び含有量の測定をし
た。結果はそれぞれ0.41mm、2.8重量%であっ
た。このペレットをさらに振動ぶるいあるいは水洗する
ことにより表−1に示すような粉末を含有するペレット
を得た。
The present invention will be described in more detail with reference to the following examples, but the present invention is not limited to these examples. Examples 1, 2 and Comparative Example 1 Bisphenol A and phosgene were polymerized by an interfacial polymerization method by a conventional method to obtain a polycarbonate powder having a molecular weight of 15,000, and organic phosphite (trisnonylphenyl phosphite, manufactured by ADEKA ARGUS CORPORATION) was added. Made Mark 1
178) was blended with 0.05%, extruded in a strand shape at 250 ° C. with a 40 mmφ vent extruder, and cut for pelletization to obtain a cylindrical pellet having a diameter of 2.5 mm and a length of 3.0 mm. The average particle size and content of the powdery polymer of this granular material were measured by the method described above. The results were 0.41 mm and 2.8% by weight, respectively. The pellets containing the powder as shown in Table 1 were obtained by further subjecting the pellets to vibration sieving or washing with water.

【0015】これらペレットをカールフィッシャー法に
よる水分含有率が50ppmになるまで乾燥して、射出
成形機(名機製 M−100DM)で120mm径、
1.2mm厚みのコンパクトディスクの成形を実施し
た。条件は樹脂温度340℃、金型温度95℃、射出率
105cc/secの射出スピードであった。このコン
パクトディスクを連続して200枚成形し、シルバーの
発生したディスクを目視で観察し、その枚数を測定し、
そのシルバー発生ディスクの比率を不良率として測定し
た。結果を表−1に示す。これより、微粉が少なくなれ
ば急激にシルバーの発生が少なくなくことが示される。
These pellets were dried by the Karl Fischer method until the water content became 50 ppm, and the diameter was 120 mm with an injection molding machine (M-100DM manufactured by Meiki).
A 1.2 mm thick compact disc was molded. The conditions were a resin temperature of 340 ° C., a mold temperature of 95 ° C., and an injection speed of an injection rate of 105 cc / sec. 200 compact disks were continuously molded, the disks with silver were visually observed, and the number was measured.
The ratio of the silver-generated disc was measured as a defective rate. The results are shown in Table-1. From this, it is shown that the generation of silver is not abrupt when the amount of fine powder decreases.

【0016】[0016]

【表1】 [Table 1]

【0017】[0017]

【発明の効果】本発明の成形方法によれば、光学的部品
のシルバーの発生を防止でき、不良率を著しく低下出来
るため商業上の利用価値は極めて高い。
According to the molding method of the present invention, the occurrence of silver in optical parts can be prevented and the defective rate can be remarkably reduced, so that it has a very high commercial utility value.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C08L 69:00 ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display area C08L 69:00

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 分子量が10000〜18000のポリ
カーボネートペレット中における平均粒径0.5mm以
下の粉末状重合体含有量が2.0重量%以下であるポリ
カーボネートペレットを用いることを特徴とするシルバ
ー発生の少ない光学用部品の成形方法。
1. A polycarbonate pellet having a molecular weight of 10,000 to 18,000, wherein a polycarbonate pellet having an average particle diameter of 0.5 mm or less and a powdery polymer content of 2.0% by weight or less is used. Molding method for few optical parts.
【請求項2】 ポリカーボネートペレットが実質的に粒
径2mm以上の粒状体である特許請求の範囲第1項記載
の成形方法。
2. The molding method according to claim 1, wherein the polycarbonate pellets are substantially granular particles having a particle diameter of 2 mm or more.
【請求項3】 粉末状重合体が粒径1mm以下であるこ
とを特徴とする特許請求の範囲第1項記載の成形方法。
3. The molding method according to claim 1, wherein the powdery polymer has a particle diameter of 1 mm or less.
JP6797595A 1995-03-27 1995-03-27 Method of molding optical component Pending JPH07324138A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP6797595A JPH07324138A (en) 1995-03-27 1995-03-27 Method of molding optical component

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6797595A JPH07324138A (en) 1995-03-27 1995-03-27 Method of molding optical component

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP61146559A Division JPH0618890B2 (en) 1986-06-23 1986-06-23 Polycarbonate molding material

Publications (1)

Publication Number Publication Date
JPH07324138A true JPH07324138A (en) 1995-12-12

Family

ID=13360508

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6797595A Pending JPH07324138A (en) 1995-03-27 1995-03-27 Method of molding optical component

Country Status (1)

Country Link
JP (1) JPH07324138A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6066398A (en) * 1997-07-23 2000-05-23 Mitsubishi Engineering-Plastics Corporation Polycarbonate moulding material for optical discs
JP2001310935A (en) * 2000-02-25 2001-11-06 Mitsubishi Chemicals Corp Aromatic polycarbonate resin composition and its production method
JP2002265623A (en) * 2001-03-07 2002-09-18 Teijin Chem Ltd Polycarbonate resin molding material for optical use
JP2006247950A (en) * 2005-03-09 2006-09-21 Toyo Mach & Metal Co Ltd Injection molding machine
JP2013252975A (en) * 2007-03-20 2013-12-19 Mitsubishi Chemicals Corp Aromatic polycarbonate pellet transport method and pneumatic transport method
JP2014131864A (en) * 2012-06-08 2014-07-17 Mitsubishi Gas Chemical Co Inc Method of manufacturing polycarbonate resin molding, and polycarbonate resin molding
CN105431487A (en) * 2013-06-30 2016-03-23 三菱瓦斯化学株式会社 Polycarbonate resin composition, and fluorescence detection/analysis substrate produced using polycarbonate resin composition

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0618890A (en) * 1992-06-30 1994-01-28 Ricoh Co Ltd Liquid crystal display device

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0618890A (en) * 1992-06-30 1994-01-28 Ricoh Co Ltd Liquid crystal display device

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6066398A (en) * 1997-07-23 2000-05-23 Mitsubishi Engineering-Plastics Corporation Polycarbonate moulding material for optical discs
JP2001310935A (en) * 2000-02-25 2001-11-06 Mitsubishi Chemicals Corp Aromatic polycarbonate resin composition and its production method
JP2002265623A (en) * 2001-03-07 2002-09-18 Teijin Chem Ltd Polycarbonate resin molding material for optical use
JP2006247950A (en) * 2005-03-09 2006-09-21 Toyo Mach & Metal Co Ltd Injection molding machine
JP2013252975A (en) * 2007-03-20 2013-12-19 Mitsubishi Chemicals Corp Aromatic polycarbonate pellet transport method and pneumatic transport method
JP2014131864A (en) * 2012-06-08 2014-07-17 Mitsubishi Gas Chemical Co Inc Method of manufacturing polycarbonate resin molding, and polycarbonate resin molding
CN105431487A (en) * 2013-06-30 2016-03-23 三菱瓦斯化学株式会社 Polycarbonate resin composition, and fluorescence detection/analysis substrate produced using polycarbonate resin composition
JPWO2015001971A1 (en) * 2013-06-30 2017-02-23 三菱瓦斯化学株式会社 Polycarbonate resin composition and fluorescent detection analysis substrate using the polycarbonate resin composition
US9670315B2 (en) 2013-06-30 2017-06-06 Mitsubishi Gas Chemical Company, Inc. Polycarbonate resin composition, and fluorescence detection/analysis substrate produced using polycarbonate resin composition

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