JPH0511729B2 - - Google Patents

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Publication number
JPH0511729B2
JPH0511729B2 JP25343587A JP25343587A JPH0511729B2 JP H0511729 B2 JPH0511729 B2 JP H0511729B2 JP 25343587 A JP25343587 A JP 25343587A JP 25343587 A JP25343587 A JP 25343587A JP H0511729 B2 JPH0511729 B2 JP H0511729B2
Authority
JP
Japan
Prior art keywords
resin
mold
plasticization
molten resin
supply
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
JP25343587A
Other languages
Japanese (ja)
Other versions
JPH0195014A (en
Inventor
Shohei Masui
Masato Matsumoto
Nobuhiro Usui
Shigeyoshi Matsubara
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.)
Sumitomo Chemical Co Ltd
Original Assignee
Sumitomo Chemical Co 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 Sumitomo Chemical Co Ltd filed Critical Sumitomo Chemical Co Ltd
Priority to JP25343587A priority Critical patent/JPH0195014A/en
Publication of JPH0195014A publication Critical patent/JPH0195014A/en
Publication of JPH0511729B2 publication Critical patent/JPH0511729B2/ja
Granted 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)

Description

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

〔産業上の利用分野〕 本発明は熱可塑性樹脂のプレス成形方法に関す
る。 〔従来の技術〕 熱可塑性樹脂を可塑化溶融し、金型間に供給し
てプレス・冷却して成形品を得る熱可塑性樹脂の
プレス成形方法は一般の射出成形方法と比較して
次のような特徴がある。未閉鎖の金型間に溶融樹
脂を供給し、型締めによる圧力で金型面を一様に
流動させて賦形するので、射出成形と比較して低
供給圧力、低型締圧力で成形ができるとともに、
キヤビテイ間流動過程での剪断応力が低く配向歪
が小さいので、成形品のねじれ、ゆがみなどの変
形が少ない。また、製品の厚み方向に加圧するた
めリブの充填性が良好で、さらに冷却中の一様な
加圧で歪を残すことなくヒケ防止の効果がある。 しかしながら、この種の成形方法で良品を得る
ためには型締め方法で、上・下金型間への溶融樹
脂の供給方法、タイミング等が重要で、既に本発
明者等は特開昭60−31929号公報、特開昭61−
22917号公報等の出願をしている。かかる方法に
より、外観品質の良好な製品を低コストで成形で
き、既に自動車部品、家電部品、住宅部品、事務
機器部品等の生産に利用されている。 前記した従来の方法は溶融樹脂の供給口付近に
シヤツトオフノズル等の開閉自在のホツトノズル
を設けたり、樹脂通路途中に切替弁を設けたりあ
るいは供給口を相対的に移動させる機構を設け、
溶融樹脂の供給完了後、樹脂通路の閉鎖を行な
い、加圧時の溶融樹脂の逆流防止、可塑化時の樹
脂の前方への移動による樹脂のわき出し、供給口
付近での成形品の冷却遅れによる外観下良の防
止、可塑化終了後の樹脂通路内の残圧による樹脂
のわき出し防止を行なつていた。 〔発明が解決しようとする問題点〕 しかし前記のいずれの方法も開閉のための手段
や機構が必要であり、コストアツプの要因となる
ばかりでなく、材料替えに時間がかかり、さらに
開閉部付近の温度の均一性をはかりにくく、これ
により供給口付近等で外観不良をおこしやすかつ
た。 本発明はかかる従来方法の実用上の問題点を解
決する方法を提供するものである。 〔問題点を解決するための手段〕 本発明は垂直方向に運動するプレス機の上・下
プラテンに成形用上・下金型を取付け、該上・下
金型間に、上・下金型が未閉鎖の状態にて、上・
下金型内に設けた樹脂通路を通じて、樹脂可塑化
供給装置から溶融樹脂を供給後、型閉めを完了さ
せて加圧、冷却、型開きをして成形品を得る熱可
塑性樹脂のプレス成形方法において、溶融樹脂の
供給後、樹脂通路の閉鎖を行なうことなく、型閉
めを完了させて加圧力が設定圧に達した後、前記
樹脂可塑化供給装置内の樹脂の可塑化を開始し、
可塑化の終了時にスクリユーまたはプランジヤー
を適量強制後退させた後、型開きを開始すること
を特徴とする熱可塑性樹脂のプレス成形方法であ
る。 さらに上記本発明の方法を実施するより好まし
い方法は、金型の型閉め動作を途中で停止または
減速して上・下金型のキヤビテイのクリアランス
が50mm以下で溶融樹脂の供給を開始し、かつ、成
形品の厚さをtmmとしたときt+0.1mm以上(t
5.0mmのとき)、またはt+1/2tmm以上(5.0>
t1.0mmのとき)、または1.5mm以上(t<1.0mm
のとき)で終了するように行なう方法である。 以下、図面により本発明の方法について詳しく
説明する。第1図は本発明に使用する成形装置の
概略図、第2図は本発明の成形方法の工程を、1
つの成形サイクルにおける上金型とスクリユーの
位置関係により説明する図である。 図面において1は型締装置、2は上金型、3は
下金型、4は上プラテン、5は下プラテン、6は
溶融樹脂供給通路、7は溶融樹脂、11は樹脂可
塑化供給装置、12はスクリユーである。 上金型2.をa点から高速で降下させ、b点で
降下速度を減速させる。b点の位置信号を受けて
遅延タイマーがタイムアツプ後スクリユー12.
が後退位置から前進限まで移動して溶融樹脂
を下金型3.に設けた樹脂通路6を通じて上・下
金型キヤビテイ間に供給する。のスクリユー1
2.の位置信号を受けて上金型2.の降下速度を
増速してd点からe点まで降下させて、供給され
た溶融樹脂7を加圧し、その加圧力が設定圧力に
達するとその信号を受けて遅延タイマーのタイム
アツプ後、スクリユー12.をからまで強制
後退させ、その後スクリユー12.の回転を開始
して樹脂材料の可塑化を開始する。スクリユー1
2.は樹脂材料を可塑化しながら前方に送りつ
つ、からまで後退させる。の位置信号を受
け、スクリユー12.をからまで強制後退さ
せる。 他方上金型2.は上記のスクリユー12.の
位置信号を受けて遅延タイマーのタイムアツプ
後、f点から上昇を開始し元の位置h点に戻る。 ここにおいて溶融樹脂の供給は、上・下金型間
のキヤビテイクリヤランスが50mm以下で開始し、
かつ成形品の厚さをtmmとしたとき、t+0.1mm
以上(t5.0mmのとき)またはt+1/2tmm以上
(5.0>t1.0mmのとき)、または、1.5mm以上(t
<1.0mmのとき)で終了するようにb点の位置、
b点からd点への上金型の降下速度、点から
点への溶融樹脂の供給速度を設定するのが好まし
い。 溶融樹脂の供給を上・下金型キヤビテイクリヤ
ランスが50mm以下と狭いところで開始するのは、
溶融樹脂が上・下金型キヤビテイ面に適切な加圧
力で接触するように供給するためであり、これよ
り広いと上・下金型キヤビテイ面に適切な加圧力
で接触せず、このような状態で溶融樹脂が供給さ
れると冷却時に金型接触面に小じわ等の外観不良
(以下コールドマークと称する)が発生する。該
コールドマークは金型温度を上げることにより改
良できるが、金型温度をあげると長い冷却時間を
必要とし、好ましくない。また、溶融樹脂の供給
を上記のクリヤランスで終了するのは、材料供給
時の溶融樹脂のキヤビテイ流動時の剪断応力を低
いレベルにおさえるためであり、該数値より小さ
いクリヤランスで材料を供給すると剪断応力が大
きくなり、ねじれ、反り等の変形をおこしやす
く、かつ、より大きな供給圧力が必要となりより
大きな能力の供給装置が必要となる。さらに製品
の厚み方向への加圧の実質的な効果がなくなり、
リブの充填性等の利点がなくなる。 型閉め動作を途中で停止または減速するのは溶
融樹脂の供給を上記の位置で確実に行なうためで
ある。上記の説明においては溶融樹脂供給完了の
位置信号を受けて上金型の降下速度をアツプし
て、上金型をさらに低下させる例を示したが、上
金型の降下を連続で行なつているとき(以下連続
法と称する)は必ずしもこの再増速を必要としな
い。また、該再増速または上金型を一時停止させ
て溶融樹脂を供給する(以下一時停止法と称す
る)ときの上金型降下の再開は本説明のように、
溶融樹脂の供給完了信号をもらつて行なつてもよ
いし、溶融樹脂の供給とは独立させて例えばb点
信号からのタイマーのタイムアツプで行なつても
よい。ただし、一時停止法でスクリユーが点に
達して溶融樹脂の供給が終了後、上金型の降下開
始までにタイムラグがあると溶融樹脂の金型キヤ
ビテイ間での拡がりが一時停止し、その部分にリ
ング状のムラ(以下リングマークと称する)が発
生するので好しくない。 本発明では樹脂通路の閉鎖を行なうことなく樹
脂の可塑化を行なうが、可塑化は型閉めして加圧
力が設定圧に達した後に開始し、可塑化終了時ス
クリユーまたはプランジヤーを適量強制後退さ
せ、かつ該可塑化ならびに強制後退後に型開きさ
せることにより溶融樹脂加圧時の逆流防止、可塑
化時の材料の前方への移動による樹脂のわき出
し、成形品の供給口付近での冷却遅れの防止、な
らびに可塑化終了後の樹脂通路内の残圧による樹
脂のわき出し防止を行なうことができる。逆に、
可塑化を型閉めして、加圧力が設定圧に達した後
に行なうことおよび可塑化終了時スクリユーまた
はプランジヤーを適量強制後退させること、該可
塑化ならびに強制後退終了後に型開きを行なうこ
との三条件のうちのいずれかの条件を満たさない
ときは上記問題が発生する。該三条件のうちまず
可塑化を型閉めして加圧力が設定圧に達した後に
行なうことにより昇圧完了までスクリユーまたは
プランジヤーを前進位置に保持し(第2図〜
)、加圧時の溶融樹脂の逆流を防止する。また、
可塑化を型閉め昇圧完了後に開始し、型開き前に
終了することにより可塑化時の成形品の供給口か
らの樹脂のわき出しまたは供給口付近での冷却遅
れによる外観不良等を防止する。さらに可塑化終
了時にスクリユーまたはプランジヤーを適量強制
後退させること、該可塑化ならびに強制後退後に
型開きすることにより、型開き時の樹脂のわき出
しによるゲート付近の外観不良の防止ならびに型
開き後の樹脂のわき出しを防止する。 上記の説明においては可塑化開始前にもスクリ
ユーまたはプランジヤーを適量強制後退させる例
を示したが、場合により省略してもよい。 次により具体的な実施例ならびに比較例につい
て説明する。 〔実施例 1〜7〕 図面で説明した装置を用い、本発明の方法でポ
リプロピレン(PP)、ABS樹脂(ABS)、ポリメ
チルメタクリレート樹脂(PMMA)を使用して、
直径300mmで厚さ1.0,2.0,5.0mmの成形品を成形
した。いずれも加圧時の溶融樹脂のバツクフロ
ー、可塑化時ならびに可塑化後の成形品供給口付
近での顕著な冷却遅れ、樹脂のわき出しがなく、
得られた成形品は変形もなく表面外観も良好であ
つた。 〔比較例 1〜3〕 可塑化の開始を昇圧前に行なうことを除いて
(比較例1)あるいはスクリユーの強制後退を行
なわないことを除いて(比較例2)、あるいは型
開きを可塑化中に開始することを除いて(比較例
3)実施例3と同一の方法で成形を行なつた。 比較例1では溶融樹脂のバツクフローがあり、
ゲート付近にヒケが発生し、比較例2,3では型
開き時に樹脂のわき出しがあり、ゲート付近の外
観が悪くなり、さらに型開き後にも樹脂のわき出
しが認められた。 〔比較例 4,5〕 溶融樹脂の供給開始時のキヤビテイクリヤラン
スが55mmと大きいことを除いて(比較例4)、あ
るいは供給終了時のキヤビテイクリヤランスが2
mmと小さいことを除いて(比較例5)、実施例3
と同一の方法で成形を行なつた。いずれも溶融樹
脂のバツクフロー、樹脂のわき出しはないが比較
例4では表面外観が不良で、比較例5では成形品
のねじれ(変形)が大きかつた。 上記実施例及び比較例の成形条件及び成形品の
評価結果等を第1表にまとめて記した。
[Industrial Field of Application] The present invention relates to a method for press molding thermoplastic resin. [Prior art] The press molding method for thermoplastic resin, in which a molded product is obtained by plasticizing and melting a thermoplastic resin, supplying it between molds, pressing and cooling it, has the following advantages compared to the general injection molding method. There are some characteristics. Molten resin is supplied between unclosed molds, and the pressure from mold clamping causes the mold surface to uniformly flow and shape, so molding can be performed with lower supply pressure and lower mold clamping pressure compared to injection molding. As well as being able to
Since the shear stress and orientation strain during the inter-cavity flow process is low, there is little deformation such as twisting or distortion of the molded product. In addition, since the pressure is applied in the thickness direction of the product, the filling properties of the ribs are good, and the uniform pressure during cooling prevents sink marks without leaving any distortion. However, in order to obtain a good product using this type of molding method, the method and timing of supplying molten resin between the upper and lower molds in the mold clamping method are important, and the present inventors have already reported that Publication No. 31929, JP-A-61-
We have filed applications such as Publication No. 22917. By this method, products with good appearance quality can be molded at low cost, and are already used in the production of automobile parts, home appliance parts, housing parts, office equipment parts, etc. The conventional methods described above include providing a hot nozzle such as a shut-off nozzle that can be opened and closed near the molten resin supply port, providing a switching valve in the middle of the resin passage, or providing a mechanism for relatively moving the supply port.
After the supply of molten resin is completed, the resin passage is closed to prevent backflow of molten resin when pressurized, to prevent resin from flowing out due to forward movement of resin during plasticization, and to prevent cooling delays of molded products near the supply port. This was done to prevent poor appearance due to plasticization and to prevent the resin from oozing out due to residual pressure in the resin passage after plasticization. [Problems to be solved by the invention] However, all of the above methods require means and mechanisms for opening and closing, which not only increases costs, but also takes time to change materials, and furthermore, It was difficult to measure the uniformity of temperature, and this often resulted in poor appearance near the supply port. The present invention provides a method for solving the practical problems of such conventional methods. [Means for Solving the Problems] The present invention is characterized in that upper and lower molding molds are attached to the upper and lower platens of a press machine that moves in the vertical direction, and the upper and lower molds are placed between the upper and lower molds. When the is not closed, the upper and
A thermoplastic resin press molding method in which a molded product is obtained by supplying molten resin from a resin plasticization supply device through a resin passage provided in the lower mold, completing mold closing, applying pressure, cooling, and opening the mold. After supplying the molten resin, without closing the resin passage, after the mold closing is completed and the pressurizing force reaches the set pressure, plasticization of the resin in the resin plasticization supply device is started,
This is a thermoplastic resin press molding method characterized in that the screw or plunger is forcibly retreated by an appropriate amount at the end of plasticization, and then mold opening is started. Furthermore, a more preferable method for carrying out the above method of the present invention is to stop or decelerate the closing operation of the mold midway and start supplying the molten resin when the cavity clearance of the upper and lower molds is 50 mm or less, and , when the thickness of the molded product is tmm, t+0.1mm or more (t
5.0mm) or t+1/2tmm or more (5.0>
When t1.0mm) or 1.5mm or more (t<1.0mm
In this method, the process ends when Hereinafter, the method of the present invention will be explained in detail with reference to the drawings. Figure 1 is a schematic diagram of the molding apparatus used in the present invention, and Figure 2 shows the steps of the molding method of the present invention.
FIG. 3 is a diagram illustrating the positional relationship between the upper mold and the screw in one molding cycle. In the drawings, 1 is a mold clamping device, 2 is an upper mold, 3 is a lower mold, 4 is an upper platen, 5 is a lower platen, 6 is a molten resin supply passage, 7 is a molten resin, 11 is a resin plasticization supply device, 12 is a screw. Upper mold 2. is descended from point a at high speed, and the descending speed is decelerated at point b. After receiving the position signal of point b and the delay timer times up, screw 12.
moves from the retracted position to the forward limit and transfers the molten resin to the lower mold 3. The resin is supplied between the upper and lower mold cavities through a resin passage 6 provided in the upper and lower mold cavities. Screw 1
2. Upon receiving the position signal, the upper mold 2. The screw 12 is increased in descending speed and lowered from point d to point e to pressurize the supplied molten resin 7. When the applied pressure reaches the set pressure, the screw 12 receives the signal and after the delay timer times up. .. 12. The rotation of the resin material is started to start plasticizing the resin material. Screw 1
2. The resin material is sent forward while being plasticized, and then retracted until it reaches the bottom. After receiving the position signal of screw 12. Forced to retreat until the end. On the other hand, the upper mold 2. The above screw 12. After receiving the position signal and time-up of the delay timer, it starts to rise from point f and returns to its original position at point h. Here, the supply of molten resin starts when the cavity clearance between the upper and lower molds is 50 mm or less,
And when the thickness of the molded product is tmm, t+0.1mm
or more (when t5.0mm), or more than t+1/2tmm (when 5.0>t1.0mm), or more than 1.5mm (t
< 1.0mm) position of point b so that it ends at
It is preferable to set the lowering speed of the upper mold from point b to point d and the supply speed of molten resin from point to point. The reason for starting the supply of molten resin is when the upper and lower mold cavity clearances are narrow, less than 50 mm.
This is to supply the molten resin so that it comes into contact with the upper and lower mold cavity surfaces with an appropriate pressure. If it is wider than this, it will not come into contact with the upper and lower mold cavity surfaces with an appropriate pressure. If molten resin is supplied in this state, poor appearance such as fine wrinkles (hereinafter referred to as cold marks) will occur on the contact surface of the mold during cooling. The cold mark can be improved by increasing the mold temperature, but increasing the mold temperature requires a long cooling time, which is not preferable. In addition, the reason why the supply of molten resin is ended at the above clearance is to suppress the shear stress when the molten resin flows into the cavity during material supply to a low level.If the material is supplied with a clearance smaller than this value, shear stress As a result, deformations such as twisting and warping are likely to occur, and a larger supply pressure is required, which requires a supply device with a larger capacity. Furthermore, there is no practical effect of applying pressure in the thickness direction of the product.
Advantages such as rib filling properties are lost. The reason why the mold closing operation is stopped or decelerated midway is to ensure that the molten resin is supplied at the above-mentioned position. In the above explanation, an example was shown in which the lowering speed of the upper mold is increased and the upper mold is further lowered in response to a position signal indicating completion of molten resin supply, but it is also possible to lower the upper mold continuously. (hereinafter referred to as continuous method), this re-speed increase is not necessarily required. In addition, when speeding up again or temporarily stopping the upper mold to supply molten resin (hereinafter referred to as the "temporary stop method"), restarting the lowering of the upper mold is as described in this explanation.
This may be done by receiving a molten resin supply completion signal, or may be carried out independently of the molten resin supply by, for example, timing up a timer from the point b signal. However, in the temporary stop method, if there is a time lag between the screw reaching the point and the supply of molten resin ending and the upper mold starting to descend, the molten resin will temporarily stop spreading between the mold cavities, and the This is not preferable because ring-shaped unevenness (hereinafter referred to as ring mark) occurs. In the present invention, the resin is plasticized without closing the resin passage, but plasticization starts after the mold is closed and the pressurizing force reaches the set pressure, and the screw or plunger is forcibly retracted by an appropriate amount at the end of plasticization. , and by opening the mold after plasticization and forced retreat, it prevents backflow when pressurizing molten resin, prevents resin from flowing out due to forward movement of the material during plasticization, and prevents cooling delays near the supply port of the molded product. In addition, it is possible to prevent the resin from oozing out due to the residual pressure in the resin passage after plasticization is completed. vice versa,
Three conditions: plasticization is performed after the mold is closed and the pressurizing force reaches the set pressure, the screw or plunger is forcibly retracted by an appropriate amount at the end of plasticization, and the mold is opened after the plasticization and forced retraction are completed. If any of these conditions is not met, the above problem occurs. Among these three conditions, plasticization is first performed after the mold is closed and the pressurizing force reaches the set pressure, so that the screw or plunger is held in the forward position until the pressure rise is completed (Fig.
), to prevent backflow of molten resin when pressurized. Also,
Plasticization is started after the mold is closed and pressurized and completed before the mold is opened, thereby preventing resin from seeping out from the supply port of the molded product during plasticization or appearance defects due to delayed cooling in the vicinity of the supply port. Furthermore, by forcibly retracting the screw or plunger by an appropriate amount at the end of plasticization, and opening the mold after the plasticization and forced retraction, it is possible to prevent poor appearance near the gate due to the resin gushing out when the mold is opened, and to prevent the resin after the mold is opened. Prevents bulges. In the above description, an example has been shown in which the screw or plunger is forcibly retracted by an appropriate amount even before the start of plasticization, but this may be omitted depending on the case. Next, more specific examples and comparative examples will be described. [Examples 1 to 7] Using the apparatus illustrated in the drawings and the method of the present invention, polypropylene (PP), ABS resin (ABS), and polymethyl methacrylate resin (PMMA) were used.
Molded products with a diameter of 300 mm and thicknesses of 1.0, 2.0, and 5.0 mm were molded. In both cases, there is no backflow of molten resin during pressurization, no noticeable cooling delay near the molded product supply port during plasticization or after plasticization, and no resin leakage.
The obtained molded product was free from deformation and had a good surface appearance. [Comparative Examples 1 to 3] Except for starting plasticization before increasing the pressure (Comparative Example 1), or excluding forced retraction of the screw (Comparative Example 2), or starting mold opening during plasticizing. (Comparative Example 3) Molding was carried out in the same manner as in Example 3, except starting at (Comparative Example 3). In Comparative Example 1, there was a backflow of molten resin,
Sink marks occurred near the gate, and in Comparative Examples 2 and 3, resin oozed out when the mold was opened, resulting in poor appearance around the gate, and furthermore, resin oozed out even after the mold was opened. [Comparative Examples 4 and 5] Except that the cavity clearance at the start of supply of molten resin was as large as 55 mm (Comparative Example 4), or the cavity clearance at the end of supply was 2.
Example 3 except that it is small (comparative example 5)
Molding was carried out in the same manner as. Although there was no backflow of molten resin or seepage of resin in either case, the surface appearance of Comparative Example 4 was poor, and the molded product of Comparative Example 5 was highly twisted (deformed). The molding conditions and evaluation results of the molded products of the above Examples and Comparative Examples are summarized in Table 1.

【表】【table】

【表】【table】 【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明に使用する成形装置の概略図、
第2図は本発明の成形方法の工程における上金型
の位置とスクリユーの位置の時間による変化の関
係を説明する図である。 1:型締装置、2:上金型、3:下金型、4:
上プラテン、5:下プラテン、6:溶融樹脂通
路、7:溶融樹脂、11:材料可塑化、供給装
置、12:スクリユー。
FIG. 1 is a schematic diagram of a molding device used in the present invention;
FIG. 2 is a diagram illustrating the relationship between changes over time in the position of the upper mold and the position of the screw in the process of the molding method of the present invention. 1: Mold clamping device, 2: Upper mold, 3: Lower mold, 4:
Upper platen, 5: Lower platen, 6: Molten resin passage, 7: Molten resin, 11: Material plasticization, supply device, 12: Screw.

Claims (1)

【特許請求の範囲】 1 垂直方向に運動する成形用上・下金型間に、
上・下金型が未閉鎖の状態にて、上・下金型内に
設けた樹脂通路を通じて、樹脂可塑化供給装置か
ら溶融樹脂を供給後、型閉めを完了させて加圧、
冷却、型開きをして成形品を得る熱可塑性樹脂の
プレス成形方法において、溶融樹脂の供給後、樹
脂通路の閉鎖を行なうことなく、型閉めを完了さ
せて加圧力が設定圧に達した後、前記樹脂可塑化
供給装置内の樹脂の可塑化を開始し、可塑化の終
了時にスクリユーまたはブランジヤーを適量強制
後退させた後、型開きを開始することを特徴とす
る熱可塑性樹脂のプレス成形方法。 2 前記溶融樹脂の供給を、金型の型閉め動作を
途中で停止または減速して上・下金型のキヤビテ
イのクリアランスが50mm以下で開始し、かつ、成
形品の厚さをtmmとしたときt+0.1mm以上(t
5.0mmのとき)、またはt+1/2tmm以上(5.0>
t1.0mmのとき)、または1.5mm以上(t<1.0mm
のとき)で終了するように行なうことを特徴とす
る特許請求の範囲第1項記載の方法。
[Claims] 1. Between the upper and lower molding molds that move in the vertical direction,
While the upper and lower molds are not closed, molten resin is supplied from the resin plasticization supply device through the resin passages provided in the upper and lower molds, and the molds are closed and pressurized.
In a thermoplastic resin press molding method in which a molded product is obtained by cooling and opening the mold, after supplying the molten resin, the mold is closed without closing the resin passage and the pressurizing force reaches the set pressure. , a method for press molding a thermoplastic resin, characterized in that plasticization of the resin in the resin plasticization supply device is started, and upon completion of plasticization, a screw or a plunger is forcibly retracted by an appropriate amount, and then opening of the mold is started. . 2 When the supply of the molten resin is started when the mold closing operation of the mold is stopped or decelerated midway and the cavity clearance of the upper and lower molds is 50 mm or less, and the thickness of the molded product is t mm. t+0.1mm or more (t
5.0mm) or t+1/2tmm or more (5.0>
When t1.0mm) or 1.5mm or more (t<1.0mm
The method according to claim 1, characterized in that the method is carried out in such a way that the process ends at the time of .
JP25343587A 1987-10-06 1987-10-06 Press molding method for thermoplastic resin Granted JPH0195014A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25343587A JPH0195014A (en) 1987-10-06 1987-10-06 Press molding method for thermoplastic resin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25343587A JPH0195014A (en) 1987-10-06 1987-10-06 Press molding method for thermoplastic resin

Publications (2)

Publication Number Publication Date
JPH0195014A JPH0195014A (en) 1989-04-13
JPH0511729B2 true JPH0511729B2 (en) 1993-02-16

Family

ID=17251359

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25343587A Granted JPH0195014A (en) 1987-10-06 1987-10-06 Press molding method for thermoplastic resin

Country Status (1)

Country Link
JP (1) JPH0195014A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20080011599A1 (en) 2006-07-12 2008-01-17 Brabender Dennis M Sputtering apparatus including novel target mounting and/or control
JP5213106B2 (en) 2008-01-17 2013-06-19 デクセリアルズ株式会社 Flat cable

Also Published As

Publication number Publication date
JPH0195014A (en) 1989-04-13

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