JP2001150512A - Foaming method and apparatus therefor - Google Patents

Foaming method and apparatus therefor

Info

Publication number
JP2001150512A
JP2001150512A JP33771899A JP33771899A JP2001150512A JP 2001150512 A JP2001150512 A JP 2001150512A JP 33771899 A JP33771899 A JP 33771899A JP 33771899 A JP33771899 A JP 33771899A JP 2001150512 A JP2001150512 A JP 2001150512A
Authority
JP
Japan
Prior art keywords
cylinder
pressure
inert gas
foam molding
nozzle
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.)
Granted
Application number
JP33771899A
Other languages
Japanese (ja)
Other versions
JP3979758B2 (en
Inventor
Atsuo Teraoka
淳男 寺岡
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.)
Japan Steel Works Ltd
Original Assignee
Japan Steel Works 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 Japan Steel Works Ltd filed Critical Japan Steel Works Ltd
Priority to JP33771899A priority Critical patent/JP3979758B2/en
Publication of JP2001150512A publication Critical patent/JP2001150512A/en
Application granted granted Critical
Publication of JP3979758B2 publication Critical patent/JP3979758B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • 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
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/34Auxiliary operations
    • B29C44/3469Cell or pore nucleation
    • B29C44/348Cell or pore nucleation by regulating the temperature and/or the pressure, e.g. suppression of foaming until the pressure is rapidly decreased
    • 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
    • B29C44/00Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles
    • B29C44/02Shaping by internal pressure generated in the material, e.g. swelling or foaming ; Producing porous or cellular expanded plastics articles for articles of definite length, i.e. discrete articles
    • B29C44/12Incorporating or moulding on preformed parts, e.g. inserts or reinforcements

Landscapes

  • Injection Moulding Of Plastics Or The Like (AREA)
  • Extrusion Moulding Of Plastics Or The Like (AREA)
  • Molding Of Porous Articles (AREA)

Abstract

PROBLEM TO BE SOLVED: To enable low pressure foaming by setting the pressure in a cylinder to definite pressure, which exceeds supercritical pressure, or more by controlling the opening degree of the throttle means of a nozzle part. SOLUTION: In a method and an apparatus for performing foaming, the opening degree of the throttle means 11 of the nozzle part 12 is controlled so that the internal pressure of a cylinder 1 during injection does not become supercritical pressure or less and the supply amount of inert gas 18a is controlled corresponding to the rotational speed of a screw 3.

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、発泡成形方法及び
装置に関し、特に、ノズル部に絞り手段を設けて、射出
等のシリンダ内が超臨界圧力以下とならないようにして
低圧発泡成形を可能とすると共に、流量制御弁を設けて
スクリュの回転速度に応じて不活性ガスの供給量を制御
するための新規な改良に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for foam molding, and more particularly, to a method for forming a nozzle by providing a throttle means so that the inside of a cylinder for injection or the like can be kept at a supercritical pressure or less, thereby enabling low pressure foam molding. In addition, the present invention relates to a novel improvement for providing a flow control valve to control a supply amount of an inert gas according to a rotation speed of a screw.

【0002】[0002]

【従来の技術】従来、用いられていたこの種の発泡成形
方法及び装置としては、例えば、熱可塑性樹脂に化学的
発泡剤を混合させて発泡成形する第1方法、熱可塑性樹
脂に物理的発泡剤を用いて発泡成形する第2方法が採用
されていた。また、特許第2625576号公報に開示
されているように、超臨界状態の二酸化炭素を溶融樹脂
中に注入して発泡成形を行う第3方法が採用されてい
た。
2. Description of the Related Art Conventionally, foam molding methods and apparatuses of this kind include, for example, a first method in which a thermoplastic resin is mixed with a chemical foaming agent and foam molding is performed; A second method of foam molding using an agent has been employed. Further, as disclosed in Japanese Patent No. 2625576, a third method of injecting carbon dioxide in a supercritical state into a molten resin and performing foam molding has been adopted.

【0003】[0003]

【発明が解決しようとする課題】従来の発泡成形方法及
び装置は以上のように構成されていたため、次のような
課題が存在していた。すなわち、前述の第1の方法にお
いては、化学発泡剤を熱分解させて発泡成形を行う方法
であるが、発泡剤のコストが高いこと、又分解ガスの残
留物のため、異臭の発生、食品衛生上の問題、成形機、
金型の汚れ等による成形品の品質問題が発生していた。
これに対し、第2の方法である物理的発泡法は、成形機
で溶融した樹脂に、ブタン、ベタン、フロン等を混練し
た後、金型内に射出して発泡成形品を得る方法である
が、これらの発泡剤は、コストが高いことに加え、オゾ
ン層破壊等の環境汚染を引き起こす。また、第3の方法
の場合、二酸化炭素等の不活性ガスを用いるため、コス
トも安く、地球環境に有害となる物質の発生はなく、か
つ、発泡セルサイズも10μm以下となって成形性も良
好な上、成形品強度も低下しない等の特長があるが、射
出前の工程でシリンダ内を超臨界状態に保持することが
難しく、この超臨界圧力が保持されないと、シリンダ内
でガスが分離、金型内で充分な発泡成形品が得られな
い。
Since the conventional foam molding method and apparatus have been constructed as described above, the following problems exist. That is, in the first method described above, the foaming is performed by thermally decomposing the chemical foaming agent. However, since the cost of the foaming agent is high and the residue of the decomposed gas generates an unpleasant odor, Hygiene issues, molding machines,
There was a quality problem of the molded product due to contamination of the mold and the like.
On the other hand, the physical foaming method, which is the second method, is a method of kneading butane, betan, freon, and the like into a resin melted by a molding machine, and then injecting the kneaded resin into a mold to obtain a foam molded product. However, these foaming agents are expensive and cause environmental pollution such as depletion of the ozone layer. Further, in the case of the third method, since an inert gas such as carbon dioxide is used, the cost is low, there is no generation of substances harmful to the global environment, and the foam cell size is 10 μm or less, and the moldability is low. Although it has good characteristics and the strength of the molded product does not decrease, it is difficult to maintain the inside of the cylinder in a supercritical state in the process before injection, and if this supercritical pressure is not maintained, the gas will be separated in the cylinder. In addition, a sufficient foam molded product cannot be obtained in the mold.

【0004】本発明は、以上のような課題を解決するた
めになされたもので、特に、ノズル部に絞り手段を設け
て射出前のシリンダ内が超臨界圧力以下とならないよう
にして低圧発泡成形を可能とすると共に、流量制御弁を
設けてスクリュの回転速度に応じて不活性ガスの供給量
を制御するようにした発泡成形方法及び装置を提供する
ことを目的とする。
SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and in particular, a low-pressure foam molding method is provided in which a nozzle portion is provided with a throttling means so that the inside of a cylinder before injection does not become lower than supercritical pressure. It is another object of the present invention to provide a method and an apparatus for foam molding in which a flow control valve is provided and a supply amount of an inert gas is controlled according to a rotation speed of a screw.

【0005】[0005]

【課題を解決するための手段】本発明による発泡成形方
法は、不活性ガスを溶融樹脂に溶解させてスクリュによ
りシリンダの先端のノズル部から射出し、発泡成形体を
成形するようにした発泡成形方法において、前記ノズル
部に絞り手段を設け、射出中に前記シリンダの内圧が超
臨界圧力以下とならないように前記絞り手段の絞り量を
可変とする方法であり、また、前記シリンダ内への不活
性ガスの供給量を前記シリンダに接続した流量制御弁に
より、前記スクリュの回転速度に応じて制御する方法で
あり、また、前記射出の射出圧力を検出し、この射出圧
力に応じて前記絞り手段の開度を制御する方法であり、
また、前記超臨界圧力状態の圧力が7.5MPa以上と
する方法である。また、本発明による発泡成形装置は、
不活性ガスを溶融樹脂に溶解させてスクリュによりシリ
ンダの先端のノズル部から射出し、発泡成形体を成形す
るようにした発泡成形装置において、前記ノズル部に絞
り手段が設けられている構成であり、また、前記シリン
ダと前記不活性ガスのタンクとの間に流量制御弁を有す
る構成であり、また、前記ノズル部には射出圧力センサ
が設けられている構成である。
A foam molding method according to the present invention is a foam molding method in which an inert gas is dissolved in a molten resin and injected from a nozzle at the tip of a cylinder by a screw to form a foam molded article. A throttle means provided in the nozzle portion, wherein the throttle amount of the throttle means is made variable so that the internal pressure of the cylinder does not become lower than the supercritical pressure during injection. A method of controlling the supply amount of the active gas by a flow rate control valve connected to the cylinder in accordance with the rotation speed of the screw, detecting an injection pressure of the injection, and controlling the throttle means in accordance with the injection pressure. Is a method of controlling the opening of
Further, the method is such that the pressure in the supercritical pressure state is 7.5 MPa or more. Further, the foam molding device according to the present invention,
In a foam molding apparatus in which an inert gas is dissolved in a molten resin and injected by a screw from a nozzle portion at a tip of a cylinder to form a foam molded article, the nozzle portion is provided with a squeezing means. Further, a flow control valve is provided between the cylinder and the inert gas tank, and an injection pressure sensor is provided in the nozzle portion.

【0006】[0006]

【発明の実施の形態】以下、図面と共に本発明による発
泡成形方法及び装置の好適な実施の形態について説明す
る。図1において符号1で示されるものは全体形状が長
手筒状をなすと共にヒータ1Aを有するシリンダであ
り、このシリンダ1の内部に形成された内腔2にはスク
リュ3がエンコーダ等の回転検出器Eを有するモータM
によって回転自在に配設されている。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the foam molding method and apparatus according to the present invention will be described below with reference to the drawings. In FIG. 1, a cylinder denoted by reference numeral 1 is a cylinder having an overall shape of a longitudinal cylinder and having a heater 1A. A screw 3 is provided in a bore 2 formed inside the cylinder 1 with a rotation detector such as an encoder. Motor M with E
It is arranged so that it can rotate freely.

【0007】前記スクリュ3は、その長手方向に沿っ
て、ホッパ4が設けられた原料供給口5側からスクリュ
ヘッド部6側へ向けて供給部7、第1溶融部8、低圧部
9及び第2溶融部10が順次形成されている。前記スク
リュヘッド部6の先端側には絞り弁又は絞りノズル等か
らなる絞り手段11を有すると共にヒータ12Aを備え
たノズル部12が設けられている。なお、この絞り手段
11は後述の制御部14からの絞り指令14bに基づい
て絞り状態を可変できるように構成されている。
The screw 3 has a supply section 7, a first melting section 8, a low-pressure section 9, and a first section from the raw material supply port 5 side provided with the hopper 4 to the screw head section 6 along the longitudinal direction. Two fusion parts 10 are sequentially formed. At the tip end of the screw head 6, there is provided a nozzle unit 12 having a throttle means 11 comprising a throttle valve or a throttle nozzle and a heater 12A. The aperture means 11 is configured to be able to change the aperture state based on an aperture command 14b from the control unit 14 described later.

【0008】前記シリンダ1の前記スクリュヘッド部6
には、このスクリュヘッド部6内の圧力を検出するため
の射出圧力センサ13が設けられ、この射出圧力センサ
13で検出された射出圧力13aが制御部14に取込ま
れるように構成されている。また、前記シリンダ1のほ
ぼ中央位置に設けられた圧力センサ15の内圧15aは
前記制御部14に取込まれるように構成されている。
The screw head 6 of the cylinder 1
Is provided with an injection pressure sensor 13 for detecting the pressure in the screw head section 6, and the injection pressure 13 a detected by the injection pressure sensor 13 is taken into the control section 14. . The internal pressure 15 a of the pressure sensor 15 provided at a substantially central position of the cylinder 1 is configured to be taken into the control unit 14.

【0009】前記シリンダ1のほぼ中央部位置に設けら
れた注入口16には、可変電磁型の流量制御弁17が接
続され、この流量制御弁17は二酸化炭素、窒素等の液
体又は気体からなる不活性ガスを内蔵したタンク18に
接続されており、この流量制御弁17の開度は、前記制
御部14からの制御信号14aによって可変式に制御さ
れるように構成されている。
A variable electromagnetic type flow control valve 17 is connected to an injection port 16 provided at a substantially central position of the cylinder 1, and the flow control valve 17 is made of a liquid or gas such as carbon dioxide and nitrogen. The flow control valve 17 is connected to a tank 18 containing an inert gas. The opening of the flow control valve 17 is variably controlled by a control signal 14 a from the control unit 14.

【0010】前記モータMに設けられた回転検出器Eで
検出されたスクリュ3の回転速度Vは、前記制御部14
に取込まれ、このスクリュ回転速度Vに基づいて、制御
部14からのモータ速度指令VcomによってモータM
すなわちスクリュ3の回転速度を所要の速度に制御する
ことができるように構成されている。
The rotation speed V of the screw 3 detected by the rotation detector E provided on the motor M is
And based on the screw rotation speed V, the motor M is controlled by a motor speed command Vcom from the control unit 14.
That is, the rotation speed of the screw 3 is controlled to a required speed.

【0011】次に、動作について述べる。まず、図1の
状態で、ホッパ4からシリンダ1の供給口5を介してシ
リンダ1内へ送られた樹脂原料20は、制御部14から
のモータ速度指令Vcomに基づいて回転するスクリュ
3により送られ、この樹脂原料20は、ヒータ1Aによ
る加熱とスクリュ3による剪断熱によって溶融しつつ下
流側へ送られる。この場合、ノズル部12の絞り手段1
1は閉状態に保持され、スクリュ3の先端側のスクリュ
ヘッド部6の内室4内へ可塑化されて蓄積される。
Next, the operation will be described. First, in the state of FIG. 1, the resin raw material 20 sent from the hopper 4 into the cylinder 1 through the supply port 5 of the cylinder 1 is sent by the screw 3 rotating based on the motor speed command Vcom from the control unit 14. The resin raw material 20 is sent to the downstream side while being melted by heating by the heater 1A and shearing heat insulation by the screw 3. In this case, the throttle unit 1 of the nozzle unit 12
1 is held in a closed state, and is plasticized and accumulated in the inner chamber 4 of the screw head portion 6 on the tip side of the screw 3.

【0012】前述の場合、制御部14からの制御信号1
4aによって開弁され、不活性ガス18aが注入口16
を介してシリンダ1内へ供給され、溶融樹脂内へ不活性
ガス18aが混合される。この場合、不活性ガス18a
の溶融樹脂中への混合量は、5〜20W%が好適である
ため、図2で示されるように、スクリュ回転速度Vに応
じて制御部14によって演算し、制御信号14aのレベ
ルを制御し、例えば、図2の段階特性に見られるような
制御を行って、流量制御弁17の開度を制御している。
たとえば、図2において、スクリュ回転速度を100
%、たとえば可塑化能力を100Kg/Hr、60%
(30100Kg/Hr)、20%(20Kg/Hr)
と変化させた場合、それぞれ、この回転速度に対応した
ガス供給量を制御し、溶融樹脂へのガス供給量を一定に
保つ。
In the case described above, the control signal 1 from the control unit 14
4a, the inert gas 18a is opened by the injection port 16a.
And the inert gas 18a is mixed into the molten resin. In this case, the inert gas 18a
Since the mixing amount in the molten resin is preferably 5 to 20 W%, as shown in FIG. 2, the control unit 14 calculates according to the screw rotation speed V and controls the level of the control signal 14 a. For example, the opening degree of the flow control valve 17 is controlled by performing control as shown in the step characteristics of FIG.
For example, in FIG.
%, For example, a plasticizing ability of 100 kg / hr, 60%
(30100 kg / hr), 20% (20 kg / hr)
Is changed, the gas supply amount corresponding to the rotation speed is controlled, and the gas supply amount to the molten resin is kept constant.

【0013】また、溶融樹脂内へ注入して混合された不
活性ガスは、シリンダ1内の内圧15aが一定レベル
(例えば、7.5Ma以上)よりも低下すると超臨界状
態とならなくなるため、この一定レベルを保持して超臨
界圧力以下とならないように図3のようにノズル部12
を金型30のタッチ部31にタッチして射出できるよう
に、内圧15aを制御部14に取込んで絞り手段11の
アクチュエータ(開示せず)を絞り指令14bによって
制御しつつ射出を行う。前述のように、超臨界圧力状態
を保持して射出することにより、シリンダ1内では発泡
状態とならずに、金型30のキャビティ33内で発泡す
るため、微細発泡の成形品(たとえば、10μm以下の
セル径)が得られ、成形品強度も低下しない。又樹脂の
流動性も向上するため、低圧成形が可能となり、たとえ
ば、ICカード成形においてのIC、コイル等の電子部
品の破損や損傷を防止することができる。また、前述の
場合、スクリュヘッド部6に設けた射出圧力センサ13
によって、射出時の射出圧力13aを検出し、この射出
圧力13aに応じて絞り指令14bにより前記絞り手段
11の開度を可変制御している。なお、前述のシリンダ
1を前進させてノズル部12を金型30のタッチ部31
にタッチさせる動作は、図示していないが、周知のシリ
ンダ台(図示せず)を前進させるシリンダ手段によって
前進動作が行われる。
The inert gas injected and mixed into the molten resin does not enter a supercritical state when the internal pressure 15a in the cylinder 1 falls below a certain level (for example, 7.5 Ma or more). As shown in FIG. 3, the nozzle 12 is maintained at a certain level so that the pressure does not become lower than the supercritical pressure.
Injection is performed by taking the internal pressure 15a into the control unit 14 and controlling the actuator (not shown) of the squeezing means 11 by the squeezing command 14b so that the squeezing can be performed by touching the touch unit 31 of the mold 30. As described above, by injecting while maintaining the supercritical pressure state, since the foam is formed in the cavity 33 of the mold 30 without being in the foamed state in the cylinder 1, a molded product of fine foam (for example, 10 μm The following cell diameter) is obtained, and the strength of the molded product does not decrease. Further, since the fluidity of the resin is also improved, low-pressure molding becomes possible. For example, breakage or damage of electronic components such as ICs and coils in IC card molding can be prevented. In the case described above, the injection pressure sensor 13 provided on the screw head 6
Thus, the injection pressure 13a at the time of injection is detected, and the opening of the throttle means 11 is variably controlled by the throttle command 14b according to the injection pressure 13a. The aforementioned cylinder 1 is advanced and the nozzle part 12 is moved to the touch part 31 of the mold 30.
Although not shown, the operation of touching is performed by a well-known cylinder means for moving a cylinder table (not shown) forward.

【0014】[0014]

【発明の効果】本発明による発泡成形方法及び装置は、
以上のように構成されているため、次のような効果を得
ることができる。すなわち、発泡成形時に、シリンダ内
の圧力が常に超臨界圧力以下とならないように、かつ射
出時も射出圧力をフィードバック制御して絞り手段の開
度を制御することによって、シリンダ内の内圧を一定以
上として、シリンダ内での発泡を制御しているため、金
型内で微細発泡の成形品が得られ強度の強い成形品が得
られ、又低圧成形が可能となるため、例えば、ICカー
ド等のインサート成形時の電子部品の損傷等を防止する
ことができる。また、スクリュ回転速度に応じて流量制
御弁の開度を制御しているため、溶融樹脂中の不活性ガ
スの混合量を一定の範囲内に制御することができ、成形
目的に応じた発泡状態の制御が可能であリ、一定した、
発泡の成形品が得られる。
The foam molding method and apparatus according to the present invention include:
With the configuration described above, the following effects can be obtained. That is, at the time of foam molding, the internal pressure in the cylinder is kept at a certain level or more by controlling the opening of the throttle means by feedback control of the injection pressure during injection so that the pressure in the cylinder does not always fall below the supercritical pressure. As the foaming in the cylinder is controlled, a molded product of fine foam is obtained in the mold, and a molded product having a high strength is obtained, and low-pressure molding is possible. It is possible to prevent electronic components from being damaged during insert molding. In addition, since the opening of the flow control valve is controlled in accordance with the screw rotation speed, the amount of inert gas mixed in the molten resin can be controlled within a certain range. Control is possible, constant,
A foamed molded product is obtained.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明による発泡成形方法及び装置を示す断面
構成図である。
FIG. 1 is a sectional view showing a foam molding method and apparatus according to the present invention.

【図2】図1におけるスクリュ回転速度に応じて流量制
御を行う場合の特性図である。
FIG. 2 is a characteristic diagram when a flow rate is controlled according to a screw rotation speed in FIG.

【図3】図1のノズルタッチ状態の拡大構成図である。FIG. 3 is an enlarged configuration diagram of a nozzle touch state in FIG. 1;

【符号の説明】[Explanation of symbols]

1 シリンダ 3 スクリュ 11 絞り手段 12 ノズル部 13a 射出圧力 18a 不活性ガス 18 タンク 17 流量制御弁 13 射出圧力センサ DESCRIPTION OF SYMBOLS 1 Cylinder 3 Screw 11 Throttle means 12 Nozzle part 13a Injection pressure 18a Inert gas 18 Tank 17 Flow control valve 13 Injection pressure sensor

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 不活性ガス(18a)を溶融樹脂に溶解させ
てスクリュ(3)によりシリンダ(1)の先端のノズル部(12)
から射出し、発泡成形体を成形するようにした発泡成形
方法において、前記ノズル部(12)に絞り手段(11)を設
け、射出中に前記シリンダ(1)の内圧が超臨界圧力以下
とならないように前記絞り手段(11)の絞り量を可変とす
ることを特徴とする発泡成形方法。
An inert gas (18a) is dissolved in a molten resin, and a screw (3) is used to dissolve an inert gas (18a) in a nozzle (12) at a tip of a cylinder (1).
In the foam molding method in which a foaming molded body is molded from the above, a nozzle means (12) is provided with a squeezing means (11), and the internal pressure of the cylinder (1) does not become lower than the supercritical pressure during the injection. Thus, the foaming method is characterized in that the drawing amount of the drawing means (11) is made variable.
【請求項2】 前記シリンダ(1)内への不活性ガス(18a)
の供給量を前記シリンダ(1)に接続した流量制御弁(17)
により、前記スクリュ(3)の回転速度に応じて制御する
ことを特徴とする請求項1記載の発泡成形方法。
2. An inert gas (18a) into the cylinder (1).
Flow control valve (17) connected to the cylinder (1)
The foam molding method according to claim 1, wherein the control is performed in accordance with the rotation speed of the screw (3).
【請求項3】 前記射出の射出圧力(13a)を検出し、こ
の射出圧力(13a)に応じて前記絞り手段(11)の開度を制
御することを特徴とする請求項1又は2記載の発泡成形
方法。
3. The method according to claim 1, wherein an injection pressure (13a) of the injection is detected, and an opening degree of the throttle means (11) is controlled according to the injection pressure (13a). Foam molding method.
【請求項4】 前記超臨界圧力状態の圧力が7.5MP
a以上とすることを特徴とする請求項1ないし3の何れ
かに記載の発泡成形方法。
4. The pressure in the supercritical pressure state is 7.5MP.
The foam molding method according to any one of claims 1 to 3, wherein the value is not less than a.
【請求項5】 不活性ガス(18a)を溶融樹脂に溶解させ
てスクリュ(3)によりシリンダ(1)の先端のノズル部(12)
から射出し、発泡成形体を成形するようにした発泡成形
装置において、前記ノズル部(12)に絞り手段(11)が設け
られていることを特徴とする発泡成形装置。
5. A nozzle (12) at the tip of a cylinder (1) by dissolving an inert gas (18a) in a molten resin and using a screw (3).
A foaming molding apparatus, which is formed by injecting from a nozzle to form a foamed molded article, characterized in that the nozzle portion (12) is provided with a squeezing means (11).
【請求項6】 前記シリンダ(1)と前記不活性ガス(18a)
のタンク(18)との間に流量制御弁(17a)を有することを
特徴とする請求項5記載の発泡成形装置。
6. The cylinder (1) and the inert gas (18a).
6. A foam molding apparatus according to claim 5, further comprising a flow control valve (17a) between said tank and said tank (18).
【請求項7】 前記ノズル部(12)には射出圧力センサ(1
3)が設けられていることを特徴とする請求項5又は6記
載の発泡成形装置。
7. An injection pressure sensor (1) is provided at said nozzle portion (12).
7. The foam molding apparatus according to claim 5, wherein 3) is provided.
JP33771899A 1999-11-29 1999-11-29 Foam molding method Expired - Fee Related JP3979758B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33771899A JP3979758B2 (en) 1999-11-29 1999-11-29 Foam molding method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33771899A JP3979758B2 (en) 1999-11-29 1999-11-29 Foam molding method

Publications (2)

Publication Number Publication Date
JP2001150512A true JP2001150512A (en) 2001-06-05
JP3979758B2 JP3979758B2 (en) 2007-09-19

Family

ID=18311322

Family Applications (1)

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

Country Link
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Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003008172A1 (en) * 2001-07-16 2003-01-30 Siemens Aktiengesellschaft Method for the injection moulding of plastic workpieces
KR100641599B1 (en) 2004-07-02 2006-11-10 주식회사 프라코 The Adjustable Method for Gas
KR100654620B1 (en) 2004-06-28 2006-12-08 주식회사 프라코 The Adjustable Method for Gas
KR100654619B1 (en) 2004-06-29 2006-12-08 주식회사 프라코 The Adjustable Method for Gas
JP2019051631A (en) * 2017-09-14 2019-04-04 株式会社神戸製鋼所 Kneader

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003008172A1 (en) * 2001-07-16 2003-01-30 Siemens Aktiengesellschaft Method for the injection moulding of plastic workpieces
KR100654620B1 (en) 2004-06-28 2006-12-08 주식회사 프라코 The Adjustable Method for Gas
KR100654619B1 (en) 2004-06-29 2006-12-08 주식회사 프라코 The Adjustable Method for Gas
KR100641599B1 (en) 2004-07-02 2006-11-10 주식회사 프라코 The Adjustable Method for Gas
JP2019051631A (en) * 2017-09-14 2019-04-04 株式会社神戸製鋼所 Kneader

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