JPH0153618B2 - - Google Patents
Info
- Publication number
- JPH0153618B2 JPH0153618B2 JP6883984A JP6883984A JPH0153618B2 JP H0153618 B2 JPH0153618 B2 JP H0153618B2 JP 6883984 A JP6883984 A JP 6883984A JP 6883984 A JP6883984 A JP 6883984A JP H0153618 B2 JPH0153618 B2 JP H0153618B2
- Authority
- JP
- Japan
- Prior art keywords
- resin
- gate
- amount
- passing
- pressure
- 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
Links
- 239000011347 resin Substances 0.000 claims description 45
- 229920005989 resin Polymers 0.000 claims description 45
- 238000002347 injection Methods 0.000 claims description 25
- 239000007924 injection Substances 0.000 claims description 25
- 238000000034 method Methods 0.000 claims description 11
- 238000000748 compression moulding Methods 0.000 claims description 8
- 238000000465 moulding Methods 0.000 description 3
- 238000005266 casting Methods 0.000 description 2
- 229920003023 plastic Polymers 0.000 description 2
- 239000004033 plastic Substances 0.000 description 2
- 238000001816 cooling Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 238000001746 injection moulding Methods 0.000 description 1
- 238000010125 resin casting Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/17—Component parts, details or accessories; Auxiliary operations
- B29C45/26—Moulds
- B29C45/27—Sprue channels ; Runner channels or runner nozzles
- B29C45/30—Flow control means disposed within the sprue channel, e.g. "torpedo" construction
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/17—Component parts, details or accessories; Auxiliary operations
- B29C45/46—Means for plasticising or homogenising the moulding material or forcing it into the mould
- B29C45/56—Means for plasticising or homogenising the moulding material or forcing it into the mould using mould parts movable during or after injection, e.g. injection-compression moulding
- B29C45/561—Injection-compression moulding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/17—Component parts, details or accessories; Auxiliary operations
- B29C45/76—Measuring, controlling or regulating
- B29C45/77—Measuring, controlling or regulating of velocity or pressure of moulding material
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/17—Component parts, details or accessories; Auxiliary operations
- B29C45/26—Moulds
- B29C45/27—Sprue channels ; Runner channels or runner nozzles
- B29C45/2701—Details not specific to hot or cold runner channels
- B29C2045/2722—Nozzles or runner channels provided with a pressure sensor
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/17—Component parts, details or accessories; Auxiliary operations
- B29C45/26—Moulds
- B29C45/27—Sprue channels ; Runner channels or runner nozzles
- B29C2045/279—Controlling the flow of material of two or more nozzles or gates to a single mould cavity
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
- B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
- B29C45/17—Component parts, details or accessories; Auxiliary operations
- B29C45/26—Moulds
- B29C45/27—Sprue channels ; Runner channels or runner nozzles
- B29C45/30—Flow control means disposed within the sprue channel, e.g. "torpedo" construction
- B29C2045/304—Adjustable torpedoes
Landscapes
- Engineering & Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- Mechanical Engineering (AREA)
- Moulds For Moulding Plastics Or The Like (AREA)
- Injection Moulding Of Plastics Or The Like (AREA)
Description
【発明の詳細な説明】
本発明はプラスチツク等の射出圧縮成形におい
て、多点ゲートを有する成形機のゲート通過樹脂
量を最適に制御する制御方法に関するものであ
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a control method for optimally controlling the amount of resin passing through a gate of a molding machine having multiple gates in injection compression molding of plastics and the like.
従来1台の成形機より例えば長尺製品、大型製
品、或は異なる大きさの製品の射出圧縮成形によ
る多数個取りを行う場合は、複数のゲートを設け
て樹脂の鋳込みを行つていた。この多点ゲートの
場合、個々のゲートの通過樹脂量を適切に選ぶこ
とが製品の品質を維持する上で重要なことである
が、その径路の長さが異なれば通過樹脂量に変化
をきたし、従つて個々のゲートの通過樹脂量を適
正にすることは非常に困難であつた。この通過樹
脂量を調整するため、従来は、その径路の面積を
種々変化させて、その量の均一化を図つている
が、この方法によると通過樹脂量はゲートの半径
の4乗に比例する値となるために、半径の僅かの
変化が通過量に大きく影響し、これを調整するた
めのテストを繰返し多くの時間を必要としてい
た。更には大型製品などの場合は、成型の為の金
型の温度分布の変化が大きいために、通過樹脂の
粘性が変化し、これに伴い通過樹脂量も変化する
ということがあり、又、製品によつては、冷却
管、エアピン等によりゲートの位置が制約される
ものがあり、更には多数個取りにてその製品に大
小がある場合などにおいて、任意にゲートの通過
樹脂量を変化させたい場合は、その都度多くの時
間を要し、手数を掛けてゲートの径の調整が行な
われていた。 Conventionally, when a single molding machine is used to produce a large number of long products, large products, or products of different sizes by injection compression molding, a plurality of gates are provided to perform resin casting. In the case of multi-point gates, it is important to appropriately select the amount of resin passing through each gate in order to maintain product quality, but if the length of the path differs, the amount of resin passing through each gate will change. Therefore, it has been extremely difficult to make the amount of resin passing through each gate appropriate. In order to adjust the amount of resin passing through, conventionally, the area of the path is varied in order to equalize the amount, but according to this method, the amount of resin passing through is proportional to the fourth power of the radius of the gate. In order to obtain the correct value, a slight change in the radius has a large effect on the amount of passage, and it takes a lot of time to repeat tests to adjust this. Furthermore, in the case of large products, the temperature distribution of the mold used for molding changes greatly, so the viscosity of the resin passing through changes, and the amount of resin passing through changes accordingly. In some cases, the position of the gate may be restricted by cooling pipes, air pins, etc., and furthermore, in cases where multiple pieces are produced and the products have different sizes, it is desirable to arbitrarily change the amount of resin passing through the gate. In this case, it took a lot of time and effort to adjust the diameter of the gate each time.
本発明による樹脂量の制御方法は、上記の問題
点を解消し、容易に通過樹脂量を調整できると共
に多点ゲートにおける通過樹脂量の不均一性の問
題をも解決し、射出圧縮成形作業の効率化を図り
得る樹脂量制御方法を提供するために為されたも
のであり、その方法は、射出機より型窩に到る径
路の途中に樹脂の流量調整用ゲートを設けてなる
射出圧縮成形装置の、射出機の出口とゲートの出
口に設けた感圧センサより両方の圧力差を検出
し、該圧力差より通過樹脂量を算出し、該算出結
果に基づき流量調整用ゲートを開閉してゲートの
通過樹脂量を制御することを特徴とする樹脂量の
制御方法であり、以下実施例によりその詳細を説
明する。 The method for controlling the amount of resin according to the present invention solves the above problems, makes it possible to easily adjust the amount of resin passing through, and also solves the problem of non-uniformity in the amount of resin passing through multi-point gates, thereby improving the efficiency of injection compression molding operations. This method was developed to provide a method for controlling the amount of resin that can improve efficiency, and the method is injection compression molding in which a gate for adjusting the resin flow rate is provided in the path from the injection machine to the mold cavity. A pressure-sensitive sensor installed at the exit of the injection machine and the exit of the gate of the device detects the pressure difference between the two, calculates the amount of resin passing through from the pressure difference, and opens and closes the flow rate adjustment gate based on the calculation result. This is a resin amount control method characterized by controlling the amount of resin passing through a gate, and details thereof will be explained below using examples.
第1図は本発明の制御方法の実施例を説明する
装置の略側断面図であり、1は上金型、2は下金
型であり、この間に製品となる型窩3が形成され
る。4は樹脂の射出機であり、型窩3に到る径路
は射出機4のノズル4′出口にて2方向に分岐さ
れ、径路5および6により構成される。夫々の径
路5,6の途中には樹脂の流量を制御するための
ゲート7,8が設けられ、ゲート7,8は夫々油
圧シリンダ9,10により予め設定された通過樹
脂量Q1,Q2に達した時に閉鎖する。11,12,
13は感圧センサであり、夫々射出機4のノズル
4′の出口、ゲート7,8の出口に設けられる。 FIG. 1 is a schematic side sectional view of an apparatus for explaining an embodiment of the control method of the present invention, in which 1 is an upper mold, 2 is a lower mold, and a mold cavity 3 to be a product is formed between them. . Reference numeral 4 denotes a resin injection machine, and the path leading to the mold cavity 3 is branched into two directions at the exit of the nozzle 4' of the injection machine 4, and is constituted by paths 5 and 6. Gates 7 and 8 are provided in the middle of each of the paths 5 and 6 to control the flow rate of the resin, and the gates 7 and 8 control the amounts of passing resin Q 1 and Q 2 set in advance by hydraulic cylinders 9 and 10, respectively. Closes when reached. 11, 12,
Reference numeral 13 denotes a pressure sensor, which is provided at the outlet of the nozzle 4' of the injection machine 4 and the outlet of the gates 7 and 8, respectively.
射出圧縮成形装置は以上の如く構成されてお
り、ここで射出機4に射出された樹脂は、ノズル
4′の出口にて径路5および6にわかれ、夫々ゲ
ート7,8を径由して型窩3に鋳込まれるが、こ
の場合夫々のゲート7,8の通過樹脂量はハーゲ
ン・ポアゼイユの法則によれば、次式にて求めら
れる。即ち
Q=πR4(P1−P2)/8μL×t×η ……(1)
ここでQは通過樹脂量、μはその粘性係数、Rは
ゲートの半径、P1は感圧センサ11にて検知し
た圧力、P2は感圧センサ12または13にて検
知した圧力、Lは樹脂の移動距離、tは時間、η
は補正係数、(樹脂温度、樹脂の通過する穴径の
形状及び表面の加工あらさ等により補正される係
数)である。この(1)式を第1図の装置に適用すれ
ば、樹脂の粘性係数μ、径路の距離L、ゲートの
夫々の半径R、は既知の値であり、ここで時間t
を定めれば、径路Lの2点間の樹脂圧力P1,P2
を検出することにより、通過樹脂量Qを求めるこ
とができるものである。即ち感圧センサ11,1
2,13の夫々の検知した圧力をP1,P2,P2′と
すれば圧力差(P1−P2)よりゲート7の通過樹
脂量Q1を、また圧力差(P1−P2′)よりゲート8
の通過樹脂量Q2を求めることができる。即ちゲ
ートを通過して鋳込まれる樹脂の総量Qaは、前
記(1)式より次の如く表わすことができる。 The injection compression molding apparatus is constructed as described above, and the resin injected into the injection machine 4 is divided into paths 5 and 6 at the exit of the nozzle 4', and is sent to the mold via gates 7 and 8, respectively. In this case, the amount of resin passing through each of the gates 7 and 8 is determined by the following equation according to the Hagen-Poiseuille law. That is, Q = πR 4 (P 1 - P 2 ) / 8 μL × t × η ... (1) where Q is the amount of passing resin, μ is its viscosity coefficient, R is the radius of the gate, and P 1 is the pressure sensor 11 P 2 is the pressure detected by pressure sensor 12 or 13, L is the distance the resin moves, t is time, η
is a correction coefficient (a coefficient corrected based on the resin temperature, the shape of the hole through which the resin passes, the roughness of the surface processing, etc.). If this equation (1) is applied to the apparatus shown in FIG. 1, the viscosity coefficient μ of the resin, the path distance L, and the radius R of each gate are known values, and the time
If , the resin pressures P 1 , P 2 between the two points on the path L are determined.
By detecting this, the amount Q of resin passing through can be determined. That is, the pressure sensor 11,1
2 and 13 are respectively detected as P 1 , P 2 , and P 2 ′, the amount of resin passing through the gate 7 Q 1 can be determined from the pressure difference (P 1 − P 2 ), and the pressure difference (P 1 − P 2 ′) from gate 8
The amount of resin passing through Q2 can be determined. That is, the total amount Q a of the resin that passes through the gate and is cast can be expressed as follows from the above equation (1).
Qa=C∫t 0ΔPdt ……(2)
ここでCは定数でC=πR4/8μL・ηであり、また
ΔPはP1−P2である。従つてノズル4′の出口圧
力とゲート7または8との圧力差を時間により積
分演算することにより夫々のゲートを通過する樹
脂の総量Qaを求め、この総量Qaが一定の値、例
えば計画の鋳込量に達すれば油圧シリンダ9また
は10を作動させてゲートを閉鎖し、鋳込み行程
を終了することができる。 Q a =C∫ t 0 ΔPdt (2) Here, C is a constant, C=πR 4 /8μL·η, and ΔP is P 1 −P 2 . Therefore, by integrating the pressure difference between the outlet pressure of the nozzle 4' and the gate 7 or 8 with respect to time, the total amount Q a of resin passing through each gate is determined, and this total amount Q a is set to a constant value, for example, as planned. When the casting amount reaches , the hydraulic cylinder 9 or 10 is operated to close the gate and the casting process can be completed.
また第2の実施例として、第2図に示す如く上
記差圧ΔPを一定にするべく油圧シリンダ9およ
び10を加減してゲート7および8にて流路面積
を調整することにより通過樹脂量Qbを制御する
ことができる。 In addition, as a second embodiment, as shown in FIG. 2, in order to keep the differential pressure ΔP constant, the hydraulic cylinders 9 and 10 are adjusted to adjust the passage area with the gates 7 and 8, so that the amount of resin passing through Q can be adjusted. b can be controlled.
前記(1)式より
Qb=C′∫t 0dt ……(3)
ここにC′は定数でありC′=πR4(P1−P2)/8μL・
η
である。従つて差圧ΔP=P1−P2を一定にするよ
うにR値、即ちゲート7,8にて開度を制御し
て、通過樹脂量Qbを制御することができる。こ
のようにして例えば多点ゲートを有する場合は、
夫々のゲート出口の圧力を一定にすることによ
り、各ゲートの通過樹脂量の均一化を図ることが
できる。 From the above formula (1), Q b = C′∫ t 0 dt ...(3) where C′ is a constant and C′ = πR 4 (P 1 − P 2 )/8μL・
η. Therefore, by controlling the R value, that is, the opening degree of the gates 7 and 8, so as to keep the differential pressure ΔP=P 1 −P 2 constant, the amount of resin passing Q b can be controlled. In this way, for example, if you have a multi-point gate,
By keeping the pressure at each gate outlet constant, it is possible to equalize the amount of resin passing through each gate.
第3図は第3の実施例を示す図面であり、ここ
で14は第1図における射出機4に設けられた樹
脂押出用の油圧シリンダであり、この内部に設け
られた油圧ピストン15は、射出機4の出口のノ
ズル4′の手前に設けられた射出シリンダ16内
の射出ピストン17に連結されている。以上の構
成において、油圧ピストン15側の断面積をSと
し、射出ピストン17側の断面積をS′とすれば、
このピストン系の増圧比はその断面積の比に等し
くS/S′にてあらわすことができ、従つて油圧シ
リンダ14の油圧室18に、例えばP3の油圧力
が加えられれば、出口のノズル4′点における圧
力P1は
P1=P3×増圧比=P3×S/S′ ……(4)
にて表わすことができ、圧力P1はP3を測定する
ことにより求めることができる。従つて、第1お
よび第2の実施例において説明したノズル4′の
出口における圧力P1は油圧シリンダ14に加え
られる油圧力P3を測定することにより求められ、
第1および第2の実施例において述べたノズル
4′出口における感圧センサ11を省略すること
ができるものである。 FIG. 3 is a drawing showing a third embodiment, where 14 is a hydraulic cylinder for resin extrusion provided in the injection machine 4 in FIG. 1, and a hydraulic piston 15 provided inside this cylinder is It is connected to an injection piston 17 in an injection cylinder 16 provided in front of the nozzle 4' at the outlet of the injection machine 4. In the above configuration, if the cross-sectional area on the hydraulic piston 15 side is S and the cross-sectional area on the injection piston 17 side is S', then
The pressure increase ratio of this piston system is equal to the ratio of its cross-sectional area and can be expressed as S/S'. Therefore, if a hydraulic pressure of, for example, P 3 is applied to the hydraulic chamber 18 of the hydraulic cylinder 14, the outlet nozzle The pressure P 1 at point 4' can be expressed as P 1 = P 3 × pressure increase ratio = P 3 × S/S' (4), and the pressure P 1 can be obtained by measuring P 3 . can. Therefore, the pressure P 1 at the outlet of the nozzle 4' described in the first and second embodiments is determined by measuring the hydraulic pressure P 3 applied to the hydraulic cylinder 14,
The pressure sensor 11 at the outlet of the nozzle 4' described in the first and second embodiments can be omitted.
以上説明した如く本発明による樹脂量の制御方
法は射出機出口とゲート出口の圧力を検知すると
いう簡単な操作により、目的とする通過樹脂量を
知ると共に通過量を制御出来るものであり、多点
ゲートを有する場合、各ゲートの不均一性を解決
できると共に、大型製品、長大物、などについて
も適切な樹脂量の鋳込みを行うことが出来、成形
品の内部密度や精密度が要求される射出圧縮成形
によるプラスチツク製品の品質の維持と、作業の
効率化を図ることができる。 As explained above, the resin amount control method according to the present invention is capable of knowing the target amount of passing resin and controlling the amount of passing resin by a simple operation of detecting the pressure at the injection machine outlet and the gate outlet. If the gate is provided, it is possible to resolve the non-uniformity of each gate, and it is also possible to cast an appropriate amount of resin for large products, long items, etc., and it is suitable for injection molding that requires internal density and precision of the molded product. It is possible to maintain the quality of plastic products and improve work efficiency through compression molding.
第1図は制御方法を説明する装置の略側断面
図、第2図は第2の実施例を説明するゲート部の
略側断面図、第3図は第3の実施例を説明する油
圧シリンダおよび射出機出口ノズル部の略側断面
図である。
1,2……金型、3……型窩、4……射出機、
4′……ノズル、5,6……径路、7,8……ゲ
ート、9,10……油圧シリンダ、11,12,
13……感圧センサ、14……油圧シリンダ、1
5……油圧ピストン、16……射出シリンダ、1
7……射出ピストン、18……油圧室。
FIG. 1 is a schematic side sectional view of the device to explain the control method, FIG. 2 is a schematic side sectional view of the gate part to explain the second embodiment, and FIG. 3 is a hydraulic cylinder to explain the third embodiment. FIG. 3 is a schematic side sectional view of an injection machine outlet nozzle section. 1, 2... Mold, 3... Mold cavity, 4... Injection machine,
4'... Nozzle, 5, 6... Path, 7, 8... Gate, 9, 10... Hydraulic cylinder, 11, 12,
13...Pressure sensor, 14...Hydraulic cylinder, 1
5...Hydraulic piston, 16...Injection cylinder, 1
7...Injection piston, 18...Hydraulic chamber.
Claims (1)
量調整用ゲートを設けてなる射出圧縮成形装置
の、射出機の出口とゲートの出口に設けた感圧セ
ンサより両方の圧力差を検出し、該圧力差より通
過樹脂量を算出し、該算出結果に基づき流量調整
用ゲートを開閉してゲートの通過樹脂量を制御す
ることを特徴とする射出圧縮成形における樹脂量
制御方法。1. In an injection compression molding device that has a gate for adjusting the flow rate of resin in the middle of the path from the injection machine to the mold cavity, the pressure difference between both is detected by the pressure sensor installed at the exit of the injection machine and the exit of the gate. A method for controlling the amount of resin in injection compression molding, comprising: calculating the amount of resin passing through the pressure difference; and controlling the amount of resin passing through the gate by opening and closing a flow rate adjusting gate based on the calculation result.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6883984A JPS60212321A (en) | 1984-04-06 | 1984-04-06 | Quantity control of resin for injection compression molding |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6883984A JPS60212321A (en) | 1984-04-06 | 1984-04-06 | Quantity control of resin for injection compression molding |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60212321A JPS60212321A (en) | 1985-10-24 |
JPH0153618B2 true JPH0153618B2 (en) | 1989-11-15 |
Family
ID=13385260
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6883984A Granted JPS60212321A (en) | 1984-04-06 | 1984-04-06 | Quantity control of resin for injection compression molding |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60212321A (en) |
Families Citing this family (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6315723A (en) * | 1986-07-08 | 1988-01-22 | Toshiba Mach Co Ltd | Injection molding method |
JPH03275315A (en) * | 1990-03-27 | 1991-12-06 | Japan Steel Works Ltd:The | Extrusion molding method and device for multi-layer parison |
JP2949317B2 (en) * | 1993-05-11 | 1999-09-13 | 鐘淵化学工業株式会社 | Mold structure for injection molding |
US5556582A (en) * | 1995-02-17 | 1996-09-17 | Stanford University | Injection molding gate flow control |
US6001296A (en) * | 1997-03-27 | 1999-12-14 | The Whitaker Corporation | Apparatuses and methods for controlling the fill of tooling cavities |
US6464909B1 (en) | 1998-04-21 | 2002-10-15 | Synventive Molding Solutions, Inc. | Manifold system having flow control |
US6638049B1 (en) | 1997-06-13 | 2003-10-28 | Synventive Molding Solutions, Inc. | Apparatus and method for proportionally controlling fluid delivery to readily replaceable mold inserts |
US6514440B1 (en) | 1998-04-21 | 2003-02-04 | Synventive Molding Solutions, Inc. | Apparatus and method for purging injection molding system |
US6585505B2 (en) | 1998-04-21 | 2003-07-01 | Synventive Molding Solutions, Inc. | Machine for proportionally controlling fluid delivery to a mold |
US6361300B1 (en) * | 1998-04-21 | 2002-03-26 | Synventive Molding Solutions, Inc. | Manifold system having flow control |
US6632079B1 (en) * | 1998-04-21 | 2003-10-14 | Synventive Molding Solutions, Inc. | Dynamic feed control system |
US6309208B1 (en) | 1997-06-13 | 2001-10-30 | Synventive Molding Solutions, Inc. | Apparatus for proportionally controlling fluid delivery to a mold |
US6287107B1 (en) | 1997-09-02 | 2001-09-11 | Synventive Molding Solutions, Inc. | Apparatus for proportionally controlling fluid delivery to a mold |
US7234929B2 (en) | 1999-09-21 | 2007-06-26 | Synventive Molding Solutions, Inc. | Injection molding flow control apparatus and method |
US6824379B2 (en) | 1998-04-21 | 2004-11-30 | Synventive Molding Solutions, Inc. | Apparatus for utilizing an actuator for flow control valve gates |
US6589039B1 (en) | 1998-04-21 | 2003-07-08 | Synventive Molding Solutions, Inc. | Controlled injection using manifold having multiple feed channels |
JP2002515362A (en) * | 1998-05-15 | 2002-05-28 | オットー ホフシュテッテル アクチェン ゲゼルシャフト ベルクゾイグ−ウント フォルメンバウ | Injection molding tools |
DE19918532A1 (en) * | 1999-04-23 | 2000-10-26 | Zahoransky Formenbau Gmbh | Injection molded preform production, especially for toothbrushes, in which materials are metered independently at different injection points in a molding cavity |
WO2003057448A1 (en) | 2001-12-26 | 2003-07-17 | Synventive Molding Solutions, Inc. | Non-coaxial injection molding valve flow control |
US6683283B2 (en) | 2002-05-10 | 2004-01-27 | Dynisco Hot Runners Inc. Canada | Apparatus and method for heating injection molding fluid |
US6884061B2 (en) | 2002-09-18 | 2005-04-26 | Mold-Masters Limited | Metering device for a nozzle of an injection molding apparatus |
CA2451898C (en) | 2002-12-03 | 2011-04-26 | Mold-Masters Limited | Hot runner co-injection nozzle |
EP1447200B1 (en) | 2003-02-13 | 2012-04-11 | Mold-Masters (2007) Limited | Valve gated injection molding system with independant flow control |
DE102014114874A1 (en) * | 2013-11-22 | 2015-05-28 | Christopherus Bader | Method for regulating the filling of at least one cavity |
JP6240114B2 (en) * | 2014-03-18 | 2017-11-29 | イングラス ソシエタ ペル アチオニINGLASS S.p.A. | Injection molding method of resin material |
WO2018210391A1 (en) * | 2017-05-16 | 2018-11-22 | Coloplast A/S | A method and an apparatus for injection moulding of a urinary catheter |
-
1984
- 1984-04-06 JP JP6883984A patent/JPS60212321A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS60212321A (en) | 1985-10-24 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JPH0153618B2 (en) | ||
US3807914A (en) | Cavity pressure control system | |
US5441680A (en) | Method and apparatus for injection molding | |
DK2212086T3 (en) | A method and device for monitoring, documenting, and / or controlling an injection molding machine | |
US4559991A (en) | Method and system of controlling injection molding machines | |
US3977255A (en) | Evaluating pressure profile of material flowing to mold cavity | |
US10449707B2 (en) | Method of injection molding using one or more strain gauges as a virtual sensor | |
JPS63249613A (en) | Method for controlling injection process in injection molder | |
JP2004525794A (en) | Method of controlling shrinkage of member to be formed | |
JP3277961B2 (en) | Injection mold | |
US4508670A (en) | Method and apparatus for controlling the temperature in thermoforming machines | |
SE508097C2 (en) | Method and apparatus for making a hollow plastic detail | |
JP4299009B2 (en) | Centering control method in injection molding using a series of diaphragms provided in the base wall channel | |
US11718008B2 (en) | Method of injection molding with down cavity detection | |
EP0630731A1 (en) | Method for molding a plastic article using a multi-point volume control system | |
JP3219308B2 (en) | Injection molding method | |
JPS61175008A (en) | Balisong wall thickness control device in blow molding equipment | |
JPH06262646A (en) | Mold assembly injection molder and the like | |
JP2607961B2 (en) | Injection molding method | |
JPS62227617A (en) | Process change-over control device in injection molder | |
JP2009208229A (en) | Method for adjusting pressure loss of mold for injection molding | |
JP2010228157A (en) | Injection molding method and injection molding machine | |
US8168111B2 (en) | Injection moulding method | |
JPS62227616A (en) | Detecting of in-mold resin pressure in injection molding | |
JPS5892510A (en) | Injection molding device for ceramic product |