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JP4770265B2 - Melt polymerization / compression molding system - Google Patents
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JP4770265B2 - Melt polymerization / compression molding system - Google Patents

Melt polymerization / compression molding system Download PDF

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JP4770265B2
JP4770265B2 JP2005145143A JP2005145143A JP4770265B2 JP 4770265 B2 JP4770265 B2 JP 4770265B2 JP 2005145143 A JP2005145143 A JP 2005145143A JP 2005145143 A JP2005145143 A JP 2005145143A JP 4770265 B2 JP4770265 B2 JP 4770265B2
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compression molding
flow path
melt polymerization
resin flow
discharge
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JP2006321085A (en
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恒夫 今谷
明彦 諸藤
卓哉 藤川
弘之 橋本
秀人 門前
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Toyo Seikan Group Holdings Ltd
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Toyo Seikan Kaisha Ltd
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Description

本発明は、熱可塑性ポリエステルの如き樹脂を溶融重合し、次いで溶融重合された樹脂を圧縮成形して所要成形品、例えば後にブロー成形を加えることによって容器にせしめられる前成形体、にせしめる溶融重合・圧縮成形システムに関する。   The present invention provides melt polymerization of a resin such as a thermoplastic polyester, and then compression molding the melt polymerized resin to give the required molded product, for example, a pre-molded body that is subsequently placed in a container by adding blow molding. -It relates to a compression molding system.

下記特許文献1には、熱可塑性ポリエステルを溶融重合し、溶融重合した樹脂を硬化せしめることなくそのまま射出成形手段に供給し、後にブロー成形を加えることによって容器にせしめられる前成形体(一般にプリフォームとも称されている)を射出成形することが開示されている。更に、溶融重合した樹脂を射出成形手段ではなく圧縮成形手段に供給し前成形体に圧縮成形することも開示されている。
特開2000−117819公報
In Patent Document 1 below, a thermoplastic polyester is melt-polymerized, and the melt-polymerized resin is supplied as it is to an injection molding means without being cured, and then blow molded to give a preform (generally a preform). Which is also referred to as injection molding). Furthermore, it is also disclosed that the melt-polymerized resin is supplied not to the injection molding means but to the compression molding means and compression molded into the preform.
JP 2000-117819 A

圧縮成形手段への樹脂の供給は、所要吐出口から所要圧力で樹脂を連続的に吐出すことによって好都合に実施される。前成形体の圧縮成形に好都合に適用される圧縮成形手段は複数個の成形型を含んだ圧縮成形機と共に切断・搬送機構を含んでおり、吐出口から吐出された樹脂を切断して次々に開状態にある成形型に供給する。溶融重合した樹脂はアセトアルデヒドの発生を可及的に回避する等の見地から、可及的に短い径路を定常的に流動せしめて供給せしめることが望ましく、従って溶融重合した樹脂を圧縮成形手段に供給して所要成形品に圧縮成形する場合、溶融重合した樹脂を溶融重合手段から連続的に吐出し、かかる樹脂をアキュムレータ等に一旦貯留することなく連続的に圧縮成形手段に供給することが望まれる。   The supply of the resin to the compression molding means is conveniently performed by continuously discharging the resin from the required discharge port at the required pressure. The compression molding means conveniently applied to the compression molding of the pre-molded body includes a cutting / conveying mechanism together with a compression molding machine including a plurality of molding dies, and cuts the resin discharged from the discharge port one after another. Supply to mold in open state. From the standpoint of avoiding the generation of acetaldehyde as much as possible, it is desirable for melt-polymerized resin to be supplied by constantly flowing as short a path as possible, and therefore supplying the melt-polymerized resin to the compression molding means. In the case of compression molding into a required molded product, it is desirable to continuously discharge the melt-polymerized resin from the melt polymerization means and continuously supply the resin to the compression molding means without temporarily storing it in an accumulator or the like. .

然るに、圧縮成形手段におけるトラブルの発生等に起因して圧縮成形手段の作動を停止せしめる場合には、圧縮成形手段への樹脂の供給を停止せしめることが必要である。一方、溶融重合手段の作動は、通常、停止することなく継続することが必要である。従って、圧縮成形手段の作動を停止した時に、溶融重合手段から連続的に吐出される樹脂を無駄に破棄することなく有効に利用することができ、そしてまた圧縮成形手段の作動を再開した時には遅滞なく圧縮成形手段への連続的な樹脂の供給を再開することができるようになすことが望まれる。   However, when the operation of the compression molding means is stopped due to the occurrence of trouble in the compression molding means, it is necessary to stop the resin supply to the compression molding means. On the other hand, the operation of the melt polymerization means usually needs to be continued without stopping. Therefore, when the operation of the compression molding means is stopped, the resin continuously discharged from the melt polymerization means can be effectively used without being wasted, and when the operation of the compression molding means is resumed, there is a delay. It is desirable that the continuous resin supply to the compression molding means can be resumed.

本発明は上記事実に鑑みてなされたものであり、その主たる技術的課題は、溶融重合手段から連続的に吐出される樹脂を圧縮成形手段に連続的に供給することができることに加えて、溶融重合手段の作動を継続しながら圧縮成形手段の作動を停止せしめた場合にも、溶融重合手段から連続的に吐出される樹脂を無駄に破棄することなく有効に利用することができ、そして圧縮成形手段の作動を再開した場合には圧縮成形手段への連続的な樹脂の供給を直に再開することができる、新規且つ改良された溶融重合・圧縮成形システムを提供することである。   The present invention has been made in view of the above-mentioned facts, and its main technical problem is that in addition to being able to continuously supply the resin continuously discharged from the melt polymerization means to the compression molding means, Even when the operation of the compression molding means is stopped while continuing the operation of the polymerization means, the resin continuously discharged from the melt polymerization means can be effectively used without being wasted, and the compression molding is performed. To provide a new and improved melt polymerization / compression molding system capable of resuming the continuous resin supply to the compression molding means immediately when the operation of the means is resumed.

本発明によれば、所定圧力で連続的に供給することが必ずしも重要ではない付加成形手段を付設し、圧縮成形手段への樹脂の供給における変動に応じて付加成形手段への樹脂の供給を適宜に制御することによって上記主たる技術的課題が達成される。   According to the present invention, the additional molding means which is not necessarily important to supply continuously at a predetermined pressure is attached, and the resin is appropriately supplied to the additional molding means in accordance with the fluctuation in the resin supply to the compression molding means. The main technical problem can be achieved by controlling to the above.

即ち、本発明によれば、上記主たる技術的課題を達成する溶融重合・圧縮成形システムとして、溶融重合手段、少なくとも1個の圧縮成形手段、該溶融重合手段と該圧縮成形手段との間に配設された主樹脂流路、及び作動制御手段を具備する溶融重合・圧縮成形システムにおいて、
該主樹脂流路の上流端には該溶融重合手段から樹脂を連続的に流出せしめる第一の吐出手段が配設され、該主樹脂流路の下流端には該主樹脂流路を通して流動せしめられた樹脂を該圧縮成形手段に連続的に供給する第二の吐出手段が配設されており、
更に、付加成形手段が装備されており、該主樹脂流路における分岐部位と該付加成形手段との間には副樹脂流路が配設されており、該副樹脂流路の下流端には該副樹脂流路を通して流動せしめられた樹脂を該付加成形手段に供給する吐出量可変吐出手段が配設されており、該吐出量可変吐出手段の吐出量は該作動制御手段によって制御される、
ことを特徴とする溶融重合・圧縮成形システムが提供される。
That is, according to the present invention, as a melt polymerization / compression molding system that achieves the main technical problems described above, a melt polymerization means, at least one compression molding means, and between the melt polymerization means and the compression molding means are arranged. In the melt polymerization / compression molding system comprising the main resin flow path and the operation control means,
First discharge means for continuously flowing out the resin from the melt polymerization means is disposed at the upstream end of the main resin flow path, and the first resin flow path is flowed through the main resin flow path at the downstream end of the main resin flow path. A second discharge means for continuously supplying the obtained resin to the compression molding means,
Furthermore, an additional molding means is provided, and a sub resin flow path is disposed between the branch portion of the main resin flow path and the additional molding means, and at the downstream end of the sub resin flow path. Discharge amount variable discharge means for supplying the resin flowed through the sub resin flow path to the additional molding means is disposed, and the discharge amount of the discharge amount variable discharge means is controlled by the operation control means.
A melt polymerization / compression molding system is provided.

好ましくは、該分岐部位よりも下流である圧力検出部位において該主樹脂流路中の樹脂圧力を検出する圧力検出手段が配設されており、該作動制御手段は該圧力検出手段が検出する樹脂圧力に応じて吐出量可変吐出手段の吐出量を制御し、該圧力検出手段が検出する圧力を一定に維持する。該主樹脂流路における該圧力検出部位よりも下流には開閉弁手段が配設されているのが好都合である。上記圧力検出手段該検出する樹脂圧力に代えて、該該第二の吐出手段の作動状態に応じて、或いは該主樹脂流路における該分岐部位と該第二の吐出手段との間に配設された開閉弁手段の作動状態に応じて該吐出量可変吐出手段の吐出量を制御することもできる。複数個の圧縮成形手段が装備されており、該主樹脂流路の下流部は該複数個の圧縮成形手段の各々に対応して複数個の分岐樹脂流路に分岐されており、該分岐樹脂流路の各々に該開閉弁手段及び該第二の吐出手段が配設されているのが好適である。該溶融重合手段において溶融重合される樹脂はポリエステルであり、該圧縮成形手段は、後にブロー成形を加えることによって容器にせしめられる前成形体を圧縮成形するものでよい。   Preferably, pressure detection means for detecting a resin pressure in the main resin flow path is disposed at a pressure detection portion downstream of the branch portion, and the operation control means is a resin detected by the pressure detection means. The discharge amount of the discharge amount variable discharge means is controlled according to the pressure, and the pressure detected by the pressure detection means is kept constant. Conveniently, an on-off valve means is disposed downstream of the pressure detection site in the main resin flow path. In place of the pressure detection means and the detected resin pressure, the pressure detection means is arranged according to the operating state of the second discharge means, or between the branch portion of the main resin flow path and the second discharge means. The discharge amount of the discharge amount variable discharge means can be controlled according to the operating state of the open / close valve means. A plurality of compression molding means are provided, and a downstream portion of the main resin flow path is branched into a plurality of branch resin flow paths corresponding to each of the plurality of compression molding means. It is preferable that the opening / closing valve means and the second discharge means are disposed in each of the flow paths. The resin that is melt polymerized in the melt polymerization means is polyester, and the compression molding means may be a compression molding of a pre-molded body that is later put into a container by adding blow molding.

本発明の溶融重合・圧縮成形システムにおいては、圧縮成形手段への樹脂の供給における変動に応じて、付加成形手段への樹脂の供給を適宜に制御することができ、従って溶融重合手段から連続的に吐出される樹脂を圧縮成形手段に連続的に供給することができることに加えて、溶融重合手段の作動を継続しながら圧縮成形手段の作動を停止せしめた場合にも、溶融重合手段から連続的に吐出される樹脂を無駄に破棄することなく付加成形手段に供給して有効に利用することができ、そして圧縮成形手段の作動を再開した場合には圧縮成形手段への連続的な樹脂の供給を直に再開することができる。   In the melt polymerization / compression molding system of the present invention, the resin supply to the additional molding means can be appropriately controlled in accordance with the fluctuation in the resin supply to the compression molding means, and therefore the melt polymerization means continuously from the melt polymerization means. In addition to being able to continuously supply the resin discharged to the compression molding means, when the operation of the compression molding means is stopped while continuing the operation of the melt polymerization means, The resin discharged to the resin can be supplied to the additional molding means without being wasted and used effectively, and when the operation of the compression molding means is resumed, continuous resin supply to the compression molding means Can be resumed immediately.

以下、本発明に従って構成された溶融重合・圧縮成形システムの好適実施形態を簡略に図示している図1を参照して、更に詳述する。   The preferred embodiment of a melt polymerization and compression molding system constructed in accordance with the present invention will now be described in further detail with reference to FIG.

本発明に従って構成された図示の溶融重合・圧縮成形システムは、1個の溶融重合手段2、4個の圧縮成形手段4a、4b、4c及び4d並びに1個の付加成形手段6を具備している。   The illustrated melt polymerization / compression molding system constructed in accordance with the present invention comprises one melt polymerization means 2, four compression molding means 4a, 4b, 4c and 4d and one additional molding means 6. .

溶融重合手段2は、例えばポリエチレンテレフタレート(PET)或いはポリエチレンナフタレート(PEN)の如きポリエステルである合成樹脂を連続方式で溶融重合することができるそれ自体は周知の多段方式溶融重合装置から構成されているのが好都合である。圧縮成形手段4a、4b、4c及び4dの各々もそれ自体は周知の形態のものでよく、周方向に間隔をおいて配設された複数の圧縮成形型を有する圧縮成形機と、後述する吐出手段の吐出口から連続的に吐き出される溶融樹脂を切断して所要経路を通して搬送し圧縮成形機の圧縮成形型の各々に次々と供給する切断・搬送機構とから構成されているのが好都合である。圧縮成形手段を攻勢する圧縮成形機及び切断・搬送機構の好適形態としては、特開2000−25729号公報或いは特開平2000−108127号公報に開示されている形態のものを挙げることができる。圧縮成形機は、例えば後にブロー成形を加えることによって容器せしめられる前成形体を圧縮成形する。付加成形手段6は、所定圧力で連続的に樹脂を供給することが必要でなく樹脂の供給状態を適宜に変動せしめることができる形態の成形手段であれば任意の形態の成形手段でよく、例えば供給される溶融樹脂からペレットを成形するそれ自体は周知のペレタイザーでよい。   The melt polymerization means 2 is composed of a well-known multistage melt polymerization apparatus which can melt polymerize a synthetic resin such as polyethylene terephthalate (PET) or polyethylene naphthalate (PEN) in a continuous manner. It is convenient to be. Each of the compression molding means 4a, 4b, 4c, and 4d may be of a well-known form, and includes a compression molding machine having a plurality of compression molds arranged at intervals in the circumferential direction, and a discharge described later. It is advantageous to comprise a cutting / conveying mechanism that cuts the molten resin continuously discharged from the discharge port of the means, conveys it through a required path, and supplies it successively to each compression molding die of the compression molding machine. . Preferable forms of the compression molding machine and the cutting / conveying mechanism for attacking the compression molding means include those disclosed in Japanese Patent Application Laid-Open No. 2000-25729 or Japanese Patent Application Laid-Open No. 2000-108127. The compression molding machine compresses and molds a pre-molded body that can be put into a container by adding blow molding later. The additional molding means 6 may be a molding means of any form as long as it is a molding means in a form that does not need to continuously supply resin at a predetermined pressure and can appropriately change the resin supply state. The pelletizer may be formed from the supplied molten resin by a well-known pelletizer.

図1を参照して説明を続けると、溶融重合手段2と圧縮成形手段4との間には全体を番号8で示す主樹脂流路が配設されている。この主樹脂流路8は共通樹脂流路10と4個の圧縮成形手段4の夫々に対応する4個の分岐流路12a、12b、12c及び12dから構成されている。圧縮成形手段4aは共通樹脂流路10及び分岐樹脂流路12aを介して溶融重合手段2に接続されており、圧縮成形手段4bは共通樹脂流路10及び分岐樹脂流路12bを介して溶融重合手段2に接続されており、圧縮成形手段4cは共通樹脂流路10及び分岐樹脂流路12cを介して溶融重合手段2に接続されており、圧縮成形手段4dは共通樹脂流路10及び分岐樹脂流路12dを介して溶融重合手段2に接続されている。   Continuing with reference to FIG. 1, a main resin flow path generally indicated by numeral 8 is disposed between the melt polymerization means 2 and the compression molding means 4. The main resin flow path 8 is composed of four branch flow paths 12a, 12b, 12c and 12d corresponding to the common resin flow path 10 and the four compression molding means 4, respectively. The compression molding means 4a is connected to the melt polymerization means 2 via the common resin flow path 10 and the branch resin flow path 12a, and the compression molding means 4b is melt polymerization via the common resin flow path 10 and the branch resin flow path 12b. The compression molding means 4c is connected to the melt polymerization means 2 via the common resin flow path 10 and the branched resin flow path 12c, and the compression molding means 4d is connected to the common resin flow path 10 and the branched resin. It is connected to the melt polymerization means 2 through a flow path 12d.

主樹脂流路8の上流端、従って共通樹脂流路10の上流端には第一の吐出手段14が配設されている。ギアポンプから構成されているのが好適である吐出手段14は、溶融重合手段2において溶融重合された例えばポリエステル樹脂である溶融樹脂を溶融重合手段2から連続的に定量吐き出しする。主樹脂流路8の共通樹脂流路10にはそこを流動せしめられる樹脂の圧力を検出するための圧力検出手段16も配設されている。   A first discharge means 14 is disposed at the upstream end of the main resin flow path 8, and hence at the upstream end of the common resin flow path 10. The discharge means 14, which is preferably composed of a gear pump, continuously discharges a molten resin, for example, a polyester resin melt-polymerized in the melt-polymerization means 2 from the melt-polymerization means 2. The common resin flow path 10 of the main resin flow path 8 is also provided with a pressure detection means 16 for detecting the pressure of the resin flowing therethrough.

主樹脂流路8の分岐流路12a、12b、12c及び12dの各々の下流端には第二の吐出手段18a、18b、18c及び18dが配設されている。かかる吐出手段18a、18b、18c及び18dもギアポンプから好都合に構成することができ、分岐流路12a、12b、12c及び12dを通して流動せしめられた溶融樹脂を連続的に定量吐き出しして圧縮成形手段4a、4b、4c及び4dに供給する。分岐流路12a、12b、12c及び12dの各々には、適宜の形態の開閉弁部材から構成することができる開閉弁手段20a、20b、20c及び20dも配設されている。   Second discharge means 18a, 18b, 18c and 18d are disposed at the downstream ends of the branch flow paths 12a, 12b, 12c and 12d of the main resin flow path 8, respectively. Such discharge means 18a, 18b, 18c and 18d can also be advantageously constructed from a gear pump, and the molten resin flowed through the branch flow paths 12a, 12b, 12c and 12d is continuously and quantitatively discharged to compress and form the compression means 4a. 4b, 4c and 4d. On / off valve means 20a, 20b, 20c and 20d, each of which can be constituted by an appropriate form of on-off valve member, are also disposed in each of the branch flow paths 12a, 12b, 12c and 12d.

主樹脂流路8の共通樹脂流路10における吐出手段14が配設されている位置と圧力検出手段16が配設されている位置との間に位置する分岐部位22と上記付加成形手段6との間には副樹脂流路24が配設されている。そして、この副樹脂流路24の下流端には吐出量が可変である吐出手段26が配設されている。かかる吐出手段26も吐出量が適宜に変動せしめられるギアポンプから構成されているのが好適である。図示の溶融重合・圧縮成形システムは、更に、圧力検出手段16が検出する圧力に応じて吐出手段26の作動を制御する作動制御手段28が配設されている。かかる作動制御手段28はマイクロプロセッサから構成することができる。   The branch portion 22 located between the position where the discharge means 14 is disposed in the common resin flow path 10 of the main resin flow path 8 and the position where the pressure detection means 16 is disposed, and the additional molding means 6. A sub-resin channel 24 is disposed between them. Discharge means 26 having a variable discharge amount is disposed at the downstream end of the sub resin flow path 24. It is preferable that the discharge means 26 is also composed of a gear pump whose discharge amount can be appropriately changed. The illustrated melt polymerization / compression molding system is further provided with an operation control means 28 for controlling the operation of the discharge means 26 in accordance with the pressure detected by the pressure detection means 16. Such operation control means 28 can be constituted by a microprocessor.

上述したとおりの溶融重合・圧縮成形システムの作動様式は次のとおりである。溶融重合手段2は連続的に作動せしめられ、例えばポリエステルである樹脂を連続的に溶融重合する。そして、溶融重合された樹脂が吐出手段14によって連続的に定量吐き出しされる。吐出手段14が連続的に吐き出す量は、4個の圧縮成形手段4a、4b、4c及び4dが必要とする合計量よりも所定量だけ大きく設定されているのが好ましい。所望ならば、溶融重合手段2内に存在する溶融重合された樹脂量を、例えば液面検出手段の如き適宜の検出手段(図示していない)によって検出し、かかる検出樹脂量に応じて吐出手段14の作動を適宜に制御することもできる。溶融重合される吐出手段14が吐き出す溶融樹脂は主樹脂流路8の共通樹脂流路10並びに分岐樹脂流路12a、12b、12c及び12dを通して流動せしめられ、そして吐出手段18a、18b、18c及び18dの各々によって連続的に圧縮成形手段4a、4b、4c及び4dの各々に定量供給される。   The operation mode of the melt polymerization / compression molding system as described above is as follows. The melt polymerization means 2 is continuously operated, and continuously melt polymerizes a resin, for example, polyester. Then, the melt-polymerized resin is continuously discharged quantitatively by the discharge means 14. The amount that the discharge means 14 continuously discharges is preferably set larger than the total amount required by the four compression molding means 4a, 4b, 4c, and 4d by a predetermined amount. If desired, the amount of melt-polymerized resin present in the melt-polymerization means 2 is detected by an appropriate detection means (not shown) such as a liquid level detection means, and the discharge means according to the detected resin amount. It is also possible to appropriately control the operation of 14. The molten resin discharged from the discharge means 14 to be melt-polymerized is caused to flow through the common resin flow path 10 of the main resin flow path 8 and the branched resin flow paths 12a, 12b, 12c and 12d, and the discharge means 18a, 18b, 18c and 18d. Are continuously supplied to each of the compression molding means 4a, 4b, 4c and 4d.

吐出手段14によって主樹脂流路8の共通樹脂流路10に吐出される溶融樹脂は副樹脂流路24にも流動せしめられる。副樹脂流路24に配設されている吐出手段26の作動は、圧力検出手段16が検出する共通樹脂流路10内の樹脂圧力に応じて制御される。更に詳述すると、圧力検出手段16が検出する樹脂圧力を所定値に維持するように、吐出手段26の作動が制御される。従って、圧縮成形手段4a、4b、4c及び4dの全てが正常に作動せしめられている時には、吐出手段14が吐き出す樹脂量から4個の圧縮成形手段4a、4b、4c及び4dが消費する樹脂量を引いた量の樹脂量が副樹脂流路24を通して流動せしめられ、吐出手段26によって付加成形手段6に供給される。   The molten resin discharged into the common resin flow path 10 of the main resin flow path 8 by the discharge means 14 is also caused to flow into the sub resin flow path 24. The operation of the discharge means 26 disposed in the sub resin flow path 24 is controlled according to the resin pressure in the common resin flow path 10 detected by the pressure detection means 16. More specifically, the operation of the discharge means 26 is controlled so that the resin pressure detected by the pressure detection means 16 is maintained at a predetermined value. Accordingly, when all of the compression molding means 4a, 4b, 4c and 4d are operating normally, the amount of resin consumed by the four compression molding means 4a, 4b, 4c and 4d from the amount of resin discharged by the discharge means 14 The amount of the resin obtained by subtracting is made to flow through the sub resin flow path 24 and supplied to the additional molding means 6 by the discharge means 26.

一方、例えば圧縮成形手段4aにおいて不具合が発生し修理の必要が発生した場合、或いは圧縮成形手段4aにおいて点検乃至成形型変更等の必要が発生した場合には、主樹脂流路8の分岐樹脂流路12aに配設されている開閉弁手段20aが閉状態に切り換えられると共に吐出手段18aの作動が停止される。開閉弁手段20b、20c及び20dは開状態に維持され、吐出手段18b、18c及び18dは作動され続け、従って圧縮成形手段4b、4c及び4dにおいては圧縮成形が継続される。   On the other hand, for example, when a failure occurs in the compression molding means 4a and a repair is necessary, or when there is a need for inspection or a mold change in the compression molding means 4a, the branched resin flow in the main resin flow path 8 is reduced. The on-off valve means 20a disposed in the passage 12a is switched to the closed state and the operation of the discharge means 18a is stopped. The on-off valve means 20b, 20c and 20d are maintained in the open state, and the discharge means 18b, 18c and 18d continue to be operated, so that compression molding is continued in the compression molding means 4b, 4c and 4d.

分岐樹脂流路12aにおける開閉弁手段20aが閉状態にせしめられると、主樹脂流路8の共通樹脂流路10内の樹脂圧力が増大せしめられる。かくすると、作動制御手段28は副樹脂流路24に配設されている吐出手段26の作動能力を増大せしめて吐出量を増大せしめる。これによって、付加成形手段6に供給される溶融樹脂量が圧縮成形手段4aに供給されていた溶融樹脂量分だけ増大せしめられる。従って、溶融重合手段2の作動を継続しても溶融重合・圧縮成形システム全体は特に問題を発生せしめることなく作動を継続することができ、溶融重合された樹脂が無駄に破棄されることもない。   When the on-off valve means 20a in the branched resin flow path 12a is closed, the resin pressure in the common resin flow path 10 of the main resin flow path 8 is increased. Thus, the operation control means 28 increases the operation capacity of the discharge means 26 disposed in the sub resin flow path 24 and increases the discharge amount. As a result, the amount of molten resin supplied to the additional molding means 6 is increased by the amount of molten resin supplied to the compression molding means 4a. Accordingly, even if the operation of the melt polymerization means 2 is continued, the entire melt polymerization / compression molding system can continue to operate without causing any particular problems, and the melt polymerized resin is not wasted. .

圧縮成形手段4aの作動を再開する際には、分岐樹脂流路12aに配設されている開閉弁手段20aを開状態に戻すと共に吐出手段18aの作動を再開し、圧縮成形手段4aへの溶融樹脂の供給を再開する。かくすると、主樹脂流路8の共通樹脂流路10における樹脂圧力が低減せしめられる。従って、作動制御手段28は副樹脂流路24に配設されている吐出手段26の作動能力を低減せしめて吐出量を低減せしめる。これによって、付加成形手段6に供給される溶融樹脂量が圧縮成形手段4aに供給される溶融樹脂量分だけ低減せしめられる。かくして溶融重合・圧縮成形システム全体に問題を発生せしめることなく円滑に圧縮成形手段4aの作動を再開することができる。   When restarting the operation of the compression molding means 4a, the on-off valve means 20a disposed in the branch resin flow path 12a is returned to the open state and the operation of the discharge means 18a is restarted to melt into the compression molding means 4a. Resin supply resumed. Thus, the resin pressure in the common resin flow path 10 of the main resin flow path 8 is reduced. Therefore, the operation control means 28 reduces the operation capacity of the discharge means 26 disposed in the sub resin flow path 24 to reduce the discharge amount. As a result, the amount of molten resin supplied to the additional molding means 6 is reduced by the amount of molten resin supplied to the compression molding means 4a. Thus, the operation of the compression molding means 4a can be resumed smoothly without causing problems in the entire melt polymerization / compression molding system.

圧縮成形手段4aのみならず圧縮成形手段4a、4b、4c及び4dの全ての作動が停止され、開閉制御弁20a、20b、20c及び20dの全てが閉状態に切り換えられ、吐出手段18a、18b、18c及び18dの全ての作動が停止された場合でも、特に不都合を発生せしめることなく、作動制御手段28によって吐出手段26の作動が制御され、この場合には吐出手段14によって溶融重合手段2から主樹脂流路8の共通樹脂流路10に吐出される樹脂の実質上全ては付加成形手段6に供給される。   All the operations of not only the compression molding means 4a but also the compression molding means 4a, 4b, 4c and 4d are stopped, all the open / close control valves 20a, 20b, 20c and 20d are switched to the closed state, and the discharge means 18a, 18b, Even when all the operations of 18c and 18d are stopped, the operation of the discharge means 26 is controlled by the operation control means 28 without causing any particular inconvenience, and in this case, the main means from the melt polymerization means 2 is controlled by the discharge means 14. Substantially all of the resin discharged into the common resin flow path 10 of the resin flow path 8 is supplied to the additional molding means 6.

上述した実施形態においては、作動制御手段28は圧力検出手段16が検出する樹脂圧力に応じて吐出手段26の作動を制御しているが、所望ならばこれに代えて、例えば第二の吐出手段18a、18b、18c及び18dの作動状態(連続定量吐出状態又は作動停止状態)を適宜の検出手段によって検出し、第二の吐出手段18a、18b、18c及び18dの作動状態に応じて、或いは開閉弁手段20a、20b、20c及び20dの作動状態(開状態又は閉状態)を適宜の検出手段によって検出し、開閉弁手段20a、20b、20c及び20dの作動状態に応じて、吐出手段26の作動を制御することもできる。   In the embodiment described above, the operation control means 28 controls the operation of the discharge means 26 in accordance with the resin pressure detected by the pressure detection means 16, but if desired, instead of this, for example, the second discharge means 18a, 18b, 18c and 18d operating states (continuous quantitative discharge state or operation stop state) are detected by appropriate detecting means, and depending on the operating state of the second discharging means 18a, 18b, 18c and 18d, or open / close The operation state (open state or closed state) of the valve means 20a, 20b, 20c and 20d is detected by an appropriate detection means, and the operation of the discharge means 26 is performed according to the operation state of the on-off valve means 20a, 20b, 20c and 20d. Can also be controlled.

本発明に従って構成された溶融重合・圧縮成形システムの好適実施形態を示す簡略図。1 is a simplified diagram illustrating a preferred embodiment of a melt polymerization / compression molding system constructed in accordance with the present invention.

符号の説明Explanation of symbols

2:溶融重合手段
4a、4b、4c及び4d:圧縮成形手段
6:付加成形手段
8:主樹脂流路
10:主樹脂流路の共通樹脂流路
12a、12b、12c及び12d:分岐樹脂流路
14:第一の吐出手段
16:圧力検出手段
18a、18b、18c及び18d:第二の吐出手段
20a、20b、20c及び20d:開閉弁手段
22:分岐部位
24:副樹脂流路
26:吐出量可変吐出手段
28:作動制御手段
2: Melt polymerization means 4a, 4b, 4c and 4d: Compression molding means 6: Additional molding means 8: Main resin flow path 10: Common resin flow path of main resin flow path 12a, 12b, 12c and 12d: Branched resin flow path 14: First discharge means 16: Pressure detection means 18a, 18b, 18c and 18d: Second discharge means 20a, 20b, 20c and 20d: On-off valve means 22: Branch portion 24: Sub resin flow path 26: Discharge amount Variable discharge means 28: Operation control means

Claims (9)

溶融重合手段、少なくとも1個の圧縮成形手段、該溶融重合手段と該圧縮成形手段との間に配設された主樹脂流路、及び作動制御手段を具備する溶融重合・圧縮成形システムにおいて、
該主樹脂流路の上流端には該溶融重合手段から樹脂を連続的に流出せしめる第一の吐出手段が配設され、該主樹脂流路の下流端には該主樹脂流路を通して流動せしめられた樹脂を該圧縮成形手段に連続的に供給する第二の吐出手段が配設されており、
更に、付加成形手段が装備されており、該主樹脂流路における分岐部位と該付加成形手段との間には副樹脂流路が配設されており、該副樹脂流路の下流端には該副樹脂流路を通して流動せしめられた樹脂を該付加成形手段に供給する吐出量可変吐出手段が配設されており、該吐出量可変吐出手段の吐出量は該作動制御手段によって制御される、
ことを特徴とする溶融重合・圧縮成形システム。
In a melt polymerization / compression molding system comprising a melt polymerization means, at least one compression molding means, a main resin flow path disposed between the melt polymerization means and the compression molding means, and an operation control means,
First discharge means for continuously flowing out the resin from the melt polymerization means is disposed at the upstream end of the main resin flow path, and the first resin flow path is flowed through the main resin flow path at the downstream end of the main resin flow path. A second discharge means for continuously supplying the obtained resin to the compression molding means,
Furthermore, an additional molding means is provided, and a sub resin flow path is disposed between the branch portion of the main resin flow path and the additional molding means, and at the downstream end of the sub resin flow path. Discharge amount variable discharge means for supplying the resin flowed through the sub resin flow path to the additional molding means is disposed, and the discharge amount of the discharge amount variable discharge means is controlled by the operation control means.
A melt polymerization / compression molding system characterized by this.
該分岐部位よりも下流である圧力検出部位において該主樹脂流路中の樹脂圧力を検出する圧力検出手段が配設されており、該作動制御手段は該圧力検出手段が検出する樹脂圧力に応じて吐出量可変吐出手段の吐出量を制御し、該圧力検出手段が検出する圧力を一定に維持する、請求項1記載の溶融重合・圧縮成形システム。   Pressure detection means for detecting the resin pressure in the main resin flow path is disposed at the pressure detection part downstream from the branch part, and the operation control means is responsive to the resin pressure detected by the pressure detection means. The melt polymerization / compression molding system according to claim 1, wherein the discharge amount of the discharge amount variable discharge means is controlled to maintain a constant pressure detected by the pressure detection means. 該主樹脂流路における該圧力検出部位よりも下流には開閉弁手段が配設されている、請求項記載の溶融重合・圧縮成形システム。
The melt polymerization / compression molding system according to claim 2 , wherein an on-off valve means is disposed downstream of the pressure detection portion in the main resin flow path.
複数個の圧縮成形手段が装備されており、該主樹脂流路の下流部は該複数個の圧縮成形手段の各々に対応して複数個の分岐樹脂流路に分岐されており、該分岐樹脂流路の各々に該開閉弁手段及び該第二の吐出手段が配設されている、請求項3記載の溶融重合・圧縮成形システム。   A plurality of compression molding means are provided, and a downstream portion of the main resin flow path is branched into a plurality of branch resin flow paths corresponding to each of the plurality of compression molding means. The melt polymerization / compression molding system according to claim 3, wherein the on-off valve means and the second discharge means are disposed in each of the flow paths. 該作動制御手段は該第二の吐出手段の作動状態に応じて該吐出量可変吐出手段の吐出量を制御する、請求項1記載の溶融重合・圧縮成形システム。   The melt polymerization / compression molding system according to claim 1, wherein the operation control means controls the discharge amount of the variable discharge amount discharge means in accordance with the operating state of the second discharge means. 該主樹脂流路における該分岐部位と該第二の吐出手段との間には開閉弁手段が配設されており、該作動制御手段は該開閉弁手段の作動状態に応じて該吐出量可変吐出手段の吐出量を制御する、請求項1記載の溶融重合・圧縮成形システム。   On-off valve means is disposed between the branch portion in the main resin flow path and the second discharge means, and the operation control means can change the discharge amount according to the operating state of the on-off valve means. The melt polymerization / compression molding system according to claim 1, wherein the discharge amount of the discharge means is controlled. 複数個の圧縮成形手段が装備されており、該主樹脂流路の下流部は該複数個の圧縮成形手段の各々に対応して複数個の分岐樹脂流路に分岐されており、該分岐樹脂流路の各々に該開閉弁手段及び該第二の吐出手段が配設されている、請求項6記載の溶融重合・圧縮成形システム。   A plurality of compression molding means are provided, and a downstream portion of the main resin flow path is branched into a plurality of branch resin flow paths corresponding to each of the plurality of compression molding means. The melt polymerization / compression molding system according to claim 6, wherein the on-off valve means and the second discharge means are disposed in each of the flow paths. 該溶融重合手段において溶融重合される樹脂はポリエステル樹脂である、請求項1から7までのいずれかに記載の溶融重合・圧縮成形システム。   The melt polymerization / compression molding system according to any one of claims 1 to 7, wherein the resin to be melt polymerized in the melt polymerization means is a polyester resin. 該圧縮成形手段は、後にブロー成形を加えることによって容器にせしめられる前成形体を圧縮成形する、請求項1から8までのいずれかに記載の溶融重合・圧縮成形システム。   The melt polymerization / compression molding system according to any one of claims 1 to 8, wherein the compression molding means performs compression molding of a pre-molded body to be put into a container by adding blow molding later.
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