JPH11291304A - Manufacture of polycarbonate resin molding material and transparent molded product - Google Patents

Manufacture of polycarbonate resin molding material and transparent molded product

Info

Publication number
JPH11291304A
JPH11291304A JP10101144A JP10114498A JPH11291304A JP H11291304 A JPH11291304 A JP H11291304A JP 10101144 A JP10101144 A JP 10101144A JP 10114498 A JP10114498 A JP 10114498A JP H11291304 A JPH11291304 A JP H11291304A
Authority
JP
Japan
Prior art keywords
polycarbonate resin
resin
molding material
extruder
filter
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
JP10101144A
Other languages
Japanese (ja)
Inventor
Toshiaki Takada
聡明 高田
Kazuhiro Ando
和弘 安藤
Ko Tanabe
鋼 田辺
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 Gas Chemical Co Inc
Original Assignee
Mitsubishi Gas Chemical Co Inc
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 Gas Chemical Co Inc filed Critical Mitsubishi Gas Chemical Co Inc
Priority to JP10101144A priority Critical patent/JPH11291304A/en
Publication of JPH11291304A publication Critical patent/JPH11291304A/en
Pending legal-status Critical Current

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  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)

Abstract

PROBLEM TO BE SOLVED: To suppress the generation of a gelled material in a method for producing a polycarbonate resin molding material by extruding a polycarbonate resin powder in a molten state. SOLUTION: In a method for producing a polycarbonate resin molding material by extruding a polycarbonate resin powder in a molten state, the interior of the cylinder of an extruder and/or the housing and metal element of the resin filter provided to the extruder is filled and replaced with nitrogen and, thereafter, the molten resin is passed through the extruder to substantially suppress the generation of a gelled material caused by the resin filter.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明はポリカーボネート樹
脂成形材料の製造法と得られた成形材料を成形して得ら
れる透明成形品についてであり、押出機シリンダー内及
び/または押出機の樹脂フィルターについて、特定の前
処理を行った後に樹脂フィルターに溶融樹脂を通すこと
によるゲル化物の発生を抑えた樹脂の製造する方法及び
ゲル化物が無いか殆ど外観に影響しない透明成形品に関
する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a polycarbonate resin molding material and a transparent molded article obtained by molding the obtained molding material. The invention relates to a resin filter in an extruder cylinder and / or an extruder. The present invention relates to a method for producing a resin in which the generation of a gelled substance caused by passing a molten resin through a resin filter after a specific pretreatment is performed, and a transparent molded article having no gelled substance or having little effect on the appearance.

【0002】[0002]

【従来の技術】ポリカーボネート樹脂溶液から成形材料
の製造方法としては、溶液から樹脂を分離、乾燥し、押
出機でペレット化する方法が使用されている。
2. Description of the Related Art As a method of producing a molding material from a polycarbonate resin solution, a method of separating a resin from a solution, drying the resin, and pelletizing the resin with an extruder has been used.

【0003】しかし、ポリカーボネート樹脂の押出は高
温条件下で行われるため、原料の一部が熱分解し、ゲル
化物、炭化物等が生成することは避けられないものと思
われていた。
However, since extrusion of the polycarbonate resin is performed under high temperature conditions, it has been considered that a part of the raw material is thermally decomposed to generate a gel, a carbide, and the like.

【0004】ポリカーボネート樹脂は、透明性に優れる
特性から光学用途や医療用途、建材用シートに使用され
ており、光学ディスクではミクロンオーダーの異物は信
号の書き込みや読み取りにエラーを引き起こして情報の
信頼性を大きく低下させ、また医療用品や建材用シート
では目認できる異物は製品の強度低下や透明外観におい
て商品価値を低下させるため、異物除去を目的として、
溶融樹脂の濾過のために樹脂フィルターを取り付けてい
る。
Polycarbonate resins are used for optical and medical applications and as sheets for building materials because of their excellent transparency. For optical discs, foreign matter on the order of microns causes errors in signal writing and reading, resulting in information reliability. In addition, foreign substances that can be seen in medical supplies and building material sheets reduce the strength of the product and the commercial value of the product due to its transparent appearance.
A resin filter is installed for filtering the molten resin.

【0005】[0005]

【発明が解決しようとする課題】しかし、押出を開始し
てから運転状態が安定してゲル化物、炭化物等による異
物の発生が所定量以下になるまでには20時間以上の時
間を必要とし、生産効率を著しく悪化させていた。この
うち、樹脂フィルターでは捕捉除去されず押し出された
ポリカーボネート樹脂に残留するゲル化物は、その後の
成形品において金属異物や樹脂やけ炭化物等のように明
確な核のある異物とは異なり、目視又は顕微鏡の観察で
核は無いが、成形品にした場合、光線が散乱される現象
(シルバー)を起こすため、光学ディスクの信号エラー
及び医療用品や建材用シートの外観不良になる不良要因
となっていた。
However, it takes more than 20 hours from the start of the extrusion to the time when the operating condition is stabilized and the generation of foreign substances such as gels and carbides becomes less than a predetermined amount. Production efficiency was significantly deteriorated. Of these, the gelled material that remains in the extruded polycarbonate resin without being caught and removed by the resin filter is different from a foreign material having a clear nucleus such as a metal foreign material or a resin or carbonized carbide in a subsequent molded product, and is visually or microscopically. There was no nucleus in the observation, but when it was made into a molded product, the phenomenon of light scattering (silver) occurred, which was a cause of failure of signal errors of optical discs and poor appearance of medical supplies and building material sheets. .

【0006】特開平2−135222号には押出操作に
よるゲル化の発生や増加を抑えるため、ベントの減圧度
を調節してあまり高くしないようにすることで対処する
方法が記載されているが、ベントはポリカーボネート樹
脂中に含まれている低分子量体や溶媒等の不純物を除去
するためのものであり、その減圧度をあまり高くしない
ことは不純物の除去が不十分となり、結果として成形品
を射出成形するときに成形品の外観不良や金型汚染を引
き起こして、成形品の製造に著しい生産性の低下を引き
起こすため、完全な解決策にはなっていない。
Japanese Patent Application Laid-Open No. Hei 2-135222 discloses a method for controlling the occurrence and increase of gelation due to an extrusion operation by adjusting the degree of depressurization of a vent so as not to make it too high. The vent is for removing impurities such as low molecular weight substances and solvents contained in the polycarbonate resin.If the degree of pressure reduction is not too high, the removal of impurities becomes insufficient, and as a result, the molded product is injected. This is not a complete solution because it causes poor appearance of the molded article and mold contamination during molding, causing a significant decrease in productivity in the production of the molded article.

【0007】そこで、本発明者等はゲル化物の発生を低
減すべく、押出機、樹脂フィルター等を検討した結果、
押出機シリンダー内及び樹脂フィルターに滞留した空気
が溶融樹脂と接触して樹脂の熱分解を生じ、このことが
ゲル化物発生の原因になること、及び特定の方法で押出
機シリンダーと樹脂フィルターの処理を行えば、ゲル化
物の発生が実質的に抑制されることを見出し、本発明に
到達した。
Therefore, the present inventors studied an extruder, a resin filter, and the like in order to reduce the generation of a gelled product.
The air that has accumulated in the extruder cylinder and in the resin filter comes into contact with the molten resin and causes thermal decomposition of the resin, which causes the formation of gelled substances, and the treatment of the extruder cylinder and resin filter in a specific manner The present inventors have found that the formation of a gelled substance is substantially suppressed by carrying out the method, and arrived at the present invention.

【0008】[0008]

【課題を解決するための手段】即ち本発明は、ポリカー
ボネート樹脂の素材粉末を溶融押出ししてポリカーボネ
ート成形材料を製造する方法において、押出機シリンダ
ー内及び/または押出機に装着する樹脂フィルターのハ
ウジングと金属エレメントを窒素で充満置換したところ
で、溶融樹脂を通すことによる、ゲル化物の発生を実質
的に抑制したポリカーボネート樹脂成形材料の製造方法
である。
That is, the present invention relates to a method for producing a polycarbonate molding material by melt-extruding a raw material powder of a polycarbonate resin, comprising a resin filter housing mounted in an extruder cylinder and / or mounted on the extruder. This is a method for producing a polycarbonate resin molding material in which generation of a gelled substance by passing a molten resin when a metal element is filled with nitrogen is substantially suppressed.

【0009】[0009]

【発明の実施の形態】本発明においてポリカーボネート
樹脂は、ビスフェノールをモノマーとし、ホスゲン法、
エステル交換法、ピリジン法、その他によりビスフェノ
ールを炭酸エステル結合して製造される芳香族ポリカー
ポネート樹脂である。
BEST MODE FOR CARRYING OUT THE INVENTION In the present invention, a polycarbonate resin comprises bisphenol as a monomer,
Aromatic polycarbonate resin produced by transesterification, pyridine method, or the like, by bonding bisphenol to carbonic acid ester.

【0010】ビスフェノールの代表的な例を挙げると、
2,2-ビス(4-ヒドロキシフェニル)プロパン、1,1-ビス
(4-ヒドロキシフェノル)エタン、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
ロキシフェニル)シクロヘキサン等がある。好ましいビ
スフェノールはビス(4-ヒドロキシフェニル)アルカン
系化合物、特に2,2-ビス(4-ヒドロキシフェニル)プロ
パン(以下、ビスフェノールAと記す。)である。ビス
フェノールは単独で又は2種以上混合して使用する事が
できる。また、このポリカーボネート樹脂と他の樹脂と
のグラフト共重合体などの透明樹脂にも適用可能であ
る。
[0010] Representative examples of bisphenols include:
2,2-bis (4-hydroxyphenyl) propane, 1,1-bis (4-hydroxyphenol) ethane, 2,2-bis (4-hydroxy-3-methylphenyl) propane, 1,1-bis ( 4-hydroxyphenyl) cyclohexane and the like. Preferred bisphenols are bis (4-hydroxyphenyl) alkane-based compounds, particularly 2,2-bis (4-hydroxyphenyl) propane (hereinafter referred to as bisphenol A). Bisphenols can be used alone or in combination of two or more. Further, the present invention can be applied to a transparent resin such as a graft copolymer of the polycarbonate resin and another resin.

【0011】本発明においてポリカーボネート樹脂粉末
は、例えばホスゲン法の場合、重合溶液からポリカーボ
ネート樹脂溶液を分離し、洗浄精製した後、更に精密濾
過、遠心分離等により、異物やイオン性の不純物を除去
して精製されたポリカーボネート樹脂の溶液を得る。
In the present invention, for example, in the case of the phosgene method, the polycarbonate resin powder is obtained by separating the polycarbonate resin solution from the polymerization solution, washing and purifying, and further removing foreign substances and ionic impurities by microfiltration, centrifugation and the like. To obtain a solution of the purified polycarbonate resin.

【0012】次いで行われる樹脂の分離方法としては、
樹脂溶液をそのままあるいはこれに貧溶媒を沈殿が生
じない程度に加えた樹脂溶液を濃縮ゲル化する方法(”
ゲル濃縮法”:溶媒留去ゲル化、フラッシュ濃縮ゲル化
等)、又は該樹脂溶液を温水中に滴下し溶媒を留去しゲ
ル化する”温水滴下法”、貧溶媒中にポリカーボネー
ト樹脂溶液を滴下するか或いは該樹脂溶液中に貧溶媒を
滴下する方法である”沈澱法”等が採用される。
[0012] The following resin separation method includes:
A method of concentrating and gelling a resin solution as it is or a resin solution to which a poor solvent is added to such an extent that precipitation does not occur ("
"Gel concentration method": solvent evaporation gelation, flash concentration gelation, etc.), or "hot water dropping method" in which the resin solution is dropped into warm water to evaporate the solvent and gel. For example, a "precipitation method", which is a method of dropping or adding a poor solvent to the resin solution, is employed.

【0013】ポリカーボネート樹脂粉末とは、”温水滴
下法”により得られた湿潤粉末、或いは沈澱法により得
た粉末に水を加え、適宜湿式粉砕をしながら加熱して溶
媒を留去する方法等により製造される湿潤粉末である。
湿潤粉末をベント部よりの揮発成分の除去の容易な押出
機に導入し、押出と共に溶媒を留去する方法は、乾燥工
程における熱履歴がないので熱劣化の防止からも好まし
い。
[0013] Polycarbonate resin powder is defined as a method in which water is added to a wet powder obtained by the "hot water dropping method" or a powder obtained by the precipitation method, and the solvent is distilled off by heating while appropriately performing wet grinding. It is a wet powder produced.
A method in which the wet powder is introduced into an extruder from which a volatile component can be easily removed from the vent portion and the solvent is distilled off together with the extrusion is preferable from the viewpoint of preventing thermal deterioration since there is no heat history in the drying step.

【0014】本発明において押出機としてはベント付き
単軸押出機、ベント付き2軸押出機、ベント付き多軸押
出機、あるいはコ・ニーダ、プラネタリ−スクリュー押
出機などの特殊押出機等各種のものを用いることができ
る。
In the present invention, various extruders such as a single-screw extruder with a vent, a twin-screw extruder with a vent, a multi-screw extruder with a vent, or a special extruder such as a co-kneader or a planetary screw extruder are used. Can be used.

【0015】本発明で用いる押出機バレル内面は、クロ
ムタングステン鋼(SKS)、クロムバナジウム鋼(S
KD)、ニッケルクロム鋼(SNC)、ニッケルクロム
モリブデン鋼(SNCM)、クロムモリブデン鋼(SC
M)又はアルミニウムクロムモリブデン鋼(SACM)
等の高強度鋼材の窒化処理したものを挙げることができ
るが、特に、ステライト、ハステロイ又はコルモノイを
溶射したものが好適に使用される。また、スクリューと
しては、クロムタングステン鋼(SKS)、クロムバナ
ジウム鋼(SKD)、ニッケルクロム鋼(SNC)、ニ
ッケルクロムモリブデン鋼(SNCM)、クロムモリブ
デン鋼(SCM)に硬質クロムメッキあるいはNiカニ
ゼンメッキしたもの、マルテンサイト系ステンレス鋼を
熱処理したもの、又はクロムタングステン鋼(SK
S)、クロムバナジウム鋼(SKD)、ニッケルクロム
鋼(SNC)、ニッケルクロムモリブデン鋼(SNC
M)、クロムモリブデン鋼(SCM)を基材として山材
にステライトを肉盛りしたものが用いられる。特に、ク
ロムバナジウム鋼(SKD)、ニッケルクロム鋼(SN
C)、クロムモリブデン鋼(SCM)またはニッケルク
ロムモリブデン鋼(SNCM)に硬質クロムメッキある
いはNiカニゼンメッキしたもが好ましい。
The inner surface of the extruder barrel used in the present invention is made of chrome tungsten steel (SKS) or chrome vanadium steel (S
KD), nickel chrome steel (SNC), nickel chrome molybdenum steel (SNCM), chromium molybdenum steel (SC
M) or aluminum chrome molybdenum steel (SACM)
And the like. Nitriding of a high-strength steel material such as Stellite, Hastelloy, or Colmonoy is particularly preferable. Further, as the screw, chromium tungsten steel (SKS), chromium vanadium steel (SKD), nickel chrome steel (SNC), nickel chromium molybdenum steel (SNCM), and chromium molybdenum steel (SCM) were hard chromium plated or Ni Kanigen plated. Steel, heat-treated martensitic stainless steel, or chrome tungsten steel (SK
S), chrome vanadium steel (SKD), nickel chrome steel (SNC), nickel chrome molybdenum steel (SNC)
M), chromium molybdenum steel (SCM) as a base material, and stellite overlaid on a mountain material is used. In particular, chrome vanadium steel (SKD), nickel chrome steel (SN)
C), preferably, hard chromium plating or Ni Kanigen plating on chromium molybdenum steel (SCM) or nickel chromium molybdenum steel (SNCM).

【0016】本発明の樹脂フィルターエレメントは、通
常オーステナイト系ステンレス鋼が使用される。例え
ば、SUS304、SUS304L、SUS316、S
US316L、SUS309S、SUS310S、SU
S317およびSUS317L等を挙げることができ
る。樹脂フィルターの公称濾過口径は通常1〜100μ
m、好ましくは1〜60μm、さらに好ましくは2〜4
0μmである。フィルターはディスクフィルター、リー
フディスクフィルター、円筒フィルター、チューブ型フ
ィルター等の各種のものかあげられるが、特にリーフデ
ィスクフィルター、ディスクフィルターが好ましい。フ
ィルターメディアは金属の繊維を不織布とし、該不織布
を焼結して多孔体とした金属繊維焼結体が望ましい。
Austenitic stainless steel is usually used for the resin filter element of the present invention. For example, SUS304, SUS304L, SUS316, S
US316L, SUS309S, SUS310S, SU
S317 and SUS317L can be mentioned. Nominal filter diameter of resin filter is usually 1-100μ
m, preferably 1 to 60 μm, more preferably 2 to 4
0 μm. Examples of the filter include various types such as a disk filter, a leaf disk filter, a cylindrical filter, and a tube type filter, and a leaf disk filter and a disk filter are particularly preferable. The filter medium is desirably a metal fiber sintered body in which a metal fiber is formed into a nonwoven fabric and the nonwoven fabric is sintered to be a porous body.

【0017】樹脂フィルターはフィルターエレメントを
ハウジング内に固定し、押出機に装着する前か、装着後
に窒素を常圧または微加圧で流通充満させて、さらに押
出機シリンダー内が樹脂の全くない場合やあっても空隙
率が高い場合にはシリンダー内にも窒素流通し、残留す
る空気を置換することで、その後溶融ポリカーボネート
樹脂が押出機シリンダー内やフィルター部分にやってき
ても空気と接触することがなく、熱分解によるゲル化が
抑制される。
In the case of a resin filter, the filter element is fixed in a housing, and before or after being mounted on the extruder, nitrogen is flowed and filled at normal pressure or slightly pressurized. Even if the porosity is high, even if nitrogen is circulated in the cylinder and displaces the remaining air, even if the molten polycarbonate resin subsequently comes into the extruder cylinder or the filter part, it will come into contact with the air. In addition, gelation due to thermal decomposition is suppressed.

【0018】ゲル化物の判定は、ポリカーボネート樹脂
ペレット1Kgを50〜200μmのフィルム成形を行
い、CCD光学カメラによる50μm以上の異物検出を
行い、その中で目視ないしは顕微鏡観察によりゲル化物
に識別されるものを確認する方法によった。ゲル化物の
個数は、フィルムの厚みにより若干の差はあるが、30
個/Kg以下、好ましくは10個/Kg以下、さらに好
ましくは5個/Kg以下である。
The determination of the gelled product is performed by forming a film of 50 kg to 200 μm from 1 kg of the polycarbonate resin pellets, detecting a foreign material of 50 μm or more by a CCD optical camera, and discriminating the gelled product by visual or microscopic observation. How to confirm. Although the number of gelled substances slightly differs depending on the thickness of the film,
Pcs / Kg or less, preferably 10 pcs / Kg or less, more preferably 5 pcs / Kg or less.

【0019】[0019]

【実施例】以下、実施例等により本発明を説明するが、
本発明はこれらの例によってなんら限定されるものでは
ない。
Hereinafter, the present invention will be described with reference to examples and the like.
The present invention is not limited in any way by these examples.

【0020】実施例等におけるゲル化物の測定は、ポリ
カーボネート樹脂ペレット1Kgを150〜200μm
のフィルム成形を行い、CCD光学カメラによる50μ
m以上の異物検出を行い、その中で目視によりゲル化物
に識別されるものを確認する方法によった。
In the measurement of the gelled product in Examples and the like, 1 kg of the polycarbonate resin pellet was measured at 150 to 200 μm.
Of 50μ with a CCD optical camera
m or more foreign substances were detected, and among them, those which were visually identified as gelled substances were confirmed.

【0021】実施例1 50mmφベント付き押出機(バレル内面:コルモノイ溶
射処理、スクリュー:クロムモリブデン鋼に硬質クロム
メッキ処理)を用い、樹脂フィルターとして公称濾過口
径40μmのSUS316L製フィルターエレメントを
用いてハウジングにセットし、フィルターエレメントと
ハウジング内を窒素置換をした後押出機に取り付けた。
さらに押出機シリンダー内の空隙部を窒素置換するため
窒素を流通させた後、ポリカーボネート樹脂粉末を高温
(330℃)で押出し始め、ベントの真空度20Torr以
下にし、3時間後得られたペレットをフィルム成形、異
物検査によりゲル化物の個数測定を行った。また、上記
ペレットを射出成形機により直径120mm、厚さ1.2
mmのディスクを200枚成形し、ゲル化物に起因するシ
ルバーの発生枚数を測定した。結果を表1に示す。
Example 1 Using a 50 mmφ vented extruder (barrel inner surface: spraying Colmonoy, screw: hard chrome plating on chromium molybdenum steel), using a filter element made of SUS316L having a nominal filtration diameter of 40 μm as a resin filter, and mounting it on the housing After setting, the inside of the filter element and the housing were replaced with nitrogen, and then attached to an extruder.
Further, after flowing nitrogen to replace the voids in the extruder cylinder with nitrogen, the polycarbonate resin powder is extruded at a high temperature (330 ° C.), and the degree of vacuum of the vent is reduced to 20 Torr or less. The number of gelled materials was measured by molding and foreign matter inspection. In addition, the above-mentioned pellet was prepared by an injection molding machine to have a diameter of 120 mm and a thickness of 1.2 mm.
200 mm disks were molded, and the number of generated silver due to the gel was measured. Table 1 shows the results.

【0022】比較例1 比較のためフィルタ―エレメントとハウジング内、さら
に押出機シリンダー内の窒素置換を行わない以外は、実
施例1と同様にして得られたペレットの異物検査および
ペレットを射出成形して得られたディスクのゲル化物に
起因するシルバー検査を実施例1と同様に行った。結果
を表1に示した。
COMPARATIVE EXAMPLE 1 For the purpose of comparison, the pellets obtained in the same manner as in Example 1 except that nitrogen replacement in the filter element, the housing, and the extruder cylinder were not performed, and the pellets were subjected to injection molding. A silver test was performed in the same manner as in Example 1 due to the gelation of the obtained disk. The results are shown in Table 1.

【0023】[0023]

【表1】 窒素置換 ゲル化物数(個/Kg) シルバー発生率(枚/枚) ─────────────────────────────────── 実施例1 有り 5 1.5% 比較例1 無し 299 13 %[Table 1] Number of nitrogen-substituted gels (pieces / kg) Silver generation rate (sheets / sheet) ──────────────────────────── ─────── Example 1 Yes 5 1.5% Comparative Example 1 No 299 13%

【0024】[0024]

【発明の効果】本発明によれば、ポリカーボネート樹脂
粉末を溶融押出ししてポリカーボネート樹脂成形材料を
製造する方法において、非常に簡単な操作で、樹脂フィ
ルターによって除去出来なかったゲル化物を実質的に含
まないポリカーボネート樹脂成形材料を製造することが
でき、光ディスク、医療用品あるいは建材用シートの成
形材料として好適に使用される。
According to the present invention, in a method for producing a polycarbonate resin molding material by melt-extruding a polycarbonate resin powder, a gelled material which cannot be removed by a resin filter by a very simple operation is substantially contained. Polycarbonate resin molding materials can be manufactured, and are suitably used as molding materials for optical disks, medical supplies, or sheets for building materials.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 ポリカーボネート樹脂粉末を溶融押出し
してポリカーボネート樹脂成形材料を製造する方法にお
いて、押出機シリンダー内及び/または押出機に装着す
る樹脂フィルターのハウジングと金属エレメントを窒素
で充満置換した後、溶融樹脂を通すことによりフィルタ
ーによるゲル化物の発生を実質的に抑制することを特徴
とするポリカーボネート樹脂成形材料の製造方法。
1. A method for producing a polycarbonate resin molding material by melt-extruding a polycarbonate resin powder, wherein a housing and a metal element of a resin filter mounted in an extruder cylinder and / or the extruder are filled and replaced with nitrogen. A method for producing a polycarbonate resin molding material, wherein the generation of a gelled substance by a filter is substantially suppressed by passing a molten resin.
【請求項2】 樹脂フィルターエレメントがオーステナ
イト系ステンレス鋼である請求項1に記載のポリカーボ
ネート樹脂成形材料の製造方法。
2. The method according to claim 1, wherein the resin filter element is austenitic stainless steel.
【請求項3】 樹脂フィルターエレメントがSUS30
4、SUS304L、SUS316、SUS316L、
SUS309S、SUS310S、SUS317および
SUS317Lから選ばれた少なくとも1種である請求
項2に記載のポリカーボネート樹脂成形材料の製造方
法。
3. The resin filter element is made of SUS30.
4, SUS304L, SUS316, SUS316L,
The method for producing a polycarbonate resin molding material according to claim 2, wherein the method is at least one selected from SUS309S, SUS310S, SUS317, and SUS317L.
【請求項4】 請求項1ないし3の製造方法により得ら
れたポリカーボネート樹脂成形材料を、射出成形、押出
成形および圧縮成形の少なくとも1種の方法で成形して
得られる透明成形品。
4. A transparent molded article obtained by molding the polycarbonate resin molding material obtained by the production method according to claim 1 by at least one of injection molding, extrusion molding and compression molding.
JP10101144A 1998-04-13 1998-04-13 Manufacture of polycarbonate resin molding material and transparent molded product Pending JPH11291304A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10101144A JPH11291304A (en) 1998-04-13 1998-04-13 Manufacture of polycarbonate resin molding material and transparent molded product

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10101144A JPH11291304A (en) 1998-04-13 1998-04-13 Manufacture of polycarbonate resin molding material and transparent molded product

Publications (1)

Publication Number Publication Date
JPH11291304A true JPH11291304A (en) 1999-10-26

Family

ID=14292893

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JPH11291304A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008169401A (en) * 1999-12-21 2008-07-24 Mitsubishi Chemicals Corp Method for producing aromatic polycarbonate
EP1156071B2 (en) 2000-05-17 2008-08-06 General Electric Company A method for manufacturing polycarbonate

Citations (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51108382A (en) * 1975-03-19 1976-09-25 Toyo Boseki Seikeiyoryutaino renzokurokaho
JPS60107319A (en) * 1983-11-16 1985-06-12 Nissan Chem Ind Ltd Molding method of thermoplastic resin
JPS60184813A (en) * 1984-03-05 1985-09-20 Mitsubishi Gas Chem Co Inc Manufacture of polycarbonate resin molding material for disc body
JPS61180706U (en) * 1985-04-27 1986-11-11
JPS63288732A (en) * 1987-05-20 1988-11-25 Fuji Photo Film Co Ltd Apparatus for exchanging filter for extrusion molding machine
JPH01192528A (en) * 1988-01-29 1989-08-02 Mitsubishi Gas Chem Co Inc Manufacture of optical polycarbonate resin molding material
JPH02212529A (en) * 1989-02-10 1990-08-23 Toray Ind Inc Cleaning of filter and filter apparatus
JPH0376623A (en) * 1989-08-21 1991-04-02 Fujikura Ltd Extrusion of resin incorporated with crosslinking agent
JPH0497819A (en) * 1990-08-13 1992-03-30 Japan Steel Works Ltd:The Molding method of polycarbonate resin
JPH054270A (en) * 1991-06-28 1993-01-14 Hitachi Zosen Sangyo Kk Screen changing device of extruder
JPH06304982A (en) * 1993-04-26 1994-11-01 Kobe Steel Ltd Composite cylinder and its manufacture
JPH07171873A (en) * 1991-05-16 1995-07-11 Mitsubishi Gas Chem Co Inc Manufacture of polycarbonate resin molding material
JPH0939073A (en) * 1995-08-03 1997-02-10 Toray Ind Inc Apparatus and method for producing thermoplastic resin film
JPH0939072A (en) * 1995-08-03 1997-02-10 Toray Ind Inc Thermoplastic resin film and manufacture thereof
JPH0957818A (en) * 1995-08-29 1997-03-04 Furukawa Electric Co Ltd:The Screen mesh for extruding resin composition and manufacture of extrusion using the same
JPH09254151A (en) * 1996-01-16 1997-09-30 Asahi Chem Ind Co Ltd Polycarbonate pellet and its production

Patent Citations (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS51108382A (en) * 1975-03-19 1976-09-25 Toyo Boseki Seikeiyoryutaino renzokurokaho
JPS60107319A (en) * 1983-11-16 1985-06-12 Nissan Chem Ind Ltd Molding method of thermoplastic resin
JPS60184813A (en) * 1984-03-05 1985-09-20 Mitsubishi Gas Chem Co Inc Manufacture of polycarbonate resin molding material for disc body
JPS61180706U (en) * 1985-04-27 1986-11-11
JPS63288732A (en) * 1987-05-20 1988-11-25 Fuji Photo Film Co Ltd Apparatus for exchanging filter for extrusion molding machine
JPH01192528A (en) * 1988-01-29 1989-08-02 Mitsubishi Gas Chem Co Inc Manufacture of optical polycarbonate resin molding material
JPH02212529A (en) * 1989-02-10 1990-08-23 Toray Ind Inc Cleaning of filter and filter apparatus
JPH0376623A (en) * 1989-08-21 1991-04-02 Fujikura Ltd Extrusion of resin incorporated with crosslinking agent
JPH0497819A (en) * 1990-08-13 1992-03-30 Japan Steel Works Ltd:The Molding method of polycarbonate resin
JPH07171873A (en) * 1991-05-16 1995-07-11 Mitsubishi Gas Chem Co Inc Manufacture of polycarbonate resin molding material
JPH054270A (en) * 1991-06-28 1993-01-14 Hitachi Zosen Sangyo Kk Screen changing device of extruder
JPH06304982A (en) * 1993-04-26 1994-11-01 Kobe Steel Ltd Composite cylinder and its manufacture
JPH0939073A (en) * 1995-08-03 1997-02-10 Toray Ind Inc Apparatus and method for producing thermoplastic resin film
JPH0939072A (en) * 1995-08-03 1997-02-10 Toray Ind Inc Thermoplastic resin film and manufacture thereof
JPH0957818A (en) * 1995-08-29 1997-03-04 Furukawa Electric Co Ltd:The Screen mesh for extruding resin composition and manufacture of extrusion using the same
JPH09254151A (en) * 1996-01-16 1997-09-30 Asahi Chem Ind Co Ltd Polycarbonate pellet and its production

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008169401A (en) * 1999-12-21 2008-07-24 Mitsubishi Chemicals Corp Method for producing aromatic polycarbonate
EP1156071B2 (en) 2000-05-17 2008-08-06 General Electric Company A method for manufacturing polycarbonate

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