JPS61121903A - Manufacture of molded product - Google Patents

Manufacture of molded product

Info

Publication number
JPS61121903A
JPS61121903A JP24518084A JP24518084A JPS61121903A JP S61121903 A JPS61121903 A JP S61121903A JP 24518084 A JP24518084 A JP 24518084A JP 24518084 A JP24518084 A JP 24518084A JP S61121903 A JPS61121903 A JP S61121903A
Authority
JP
Japan
Prior art keywords
mold
mixer
vacuum
component
mixed
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
JP24518084A
Other languages
Japanese (ja)
Other versions
JPH0527529B2 (en
Inventor
Kenichiro Suetsugu
憲一郎 末次
Takao Inoue
孝夫 井上
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP24518084A priority Critical patent/JPS61121903A/en
Publication of JPS61121903A publication Critical patent/JPS61121903A/en
Publication of JPH0527529B2 publication Critical patent/JPH0527529B2/ja
Granted 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
    • B29C67/00Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00
    • B29C67/24Shaping techniques not covered by groups B29C39/00 - B29C65/00, B29C70/00 or B29C73/00 characterised by the choice of material
    • B29C67/246Moulding high reactive monomers or prepolymers, e.g. by reaction injection moulding [RIM], liquid injection moulding [LIM]
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D3/00Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
    • B01D3/06Flash distillation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29BPREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B7/00Mixing; Kneading
    • B29B7/80Component parts, details or accessories; Auxiliary operations
    • B29B7/84Venting or degassing ; Removing liquids, e.g. by evaporating components
    • 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
    • B29C2791/00Shaping characteristics in general
    • B29C2791/004Shaping under special conditions
    • B29C2791/006Using vacuum
    • 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
    • B29C33/00Moulds or cores; Details thereof or accessories therefor
    • B29C33/38Moulds or cores; Details thereof or accessories therefor characterised by the material or the manufacturing process

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
  • Moulds For Moulding Plastics Or The Like (AREA)
  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)

Abstract

PURPOSE:To prevent the inclusion of voids produced upon mixing of A component and B component of nylon reactive injection molding material by employing a reduced pressure buffer adaptor. CONSTITUTION:Respective components are led out of tanks 1, 2, reserving A component and B component of the material for nylon RIM and a constituent, in which the A and B components are mixed by using a mixer 4 such as static mixer, power mixer, collision mixer or the like, is deaerated by the reduced pressure buffer adaptor 7, thereafter, is poured into a preheated rubber mold, ceramics mold, metal mold or hybrid mold, which is provided in a vacuum chamber, and is heated heated further to produce the molded product.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、構造材料用9機構部品材料用として、物性的
には耐衝撃性・熱変形温度にすぐれ、また成形の面では
外観に優れ、均質な品質を持ち、生産性が良好な少量多
品種材料に適した製造方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention is used as a material for nine mechanical parts for structural materials. Physically, it has excellent impact resistance and heat deformation temperature, and in terms of molding, it has an excellent appearance and a uniform shape. The present invention relates to a manufacturing method suitable for producing a wide variety of materials in small quantities with high quality and good productivity.

従来例の構成とその問題点 従来、ナイロンRIM用材料を用いて反応性射出成形す
る場合、ミキシングヘッド内部で衝突混合を行ない、こ
の混合液を金属型内に噴出して成形するというのが一般
的だった。しかしながら、この方法では、衝突混合する
ためには液が乱流になっていなければならず、そのため
にボイドをまきこみ、ボイドがぬけきらないという欠点
があった。このため、物性値にバラツキがみられ、特に
衝撃値については10%以上のバラツキがみられ3ベー
ジ た。さらに、この衝突混合ではボイドぬきをするために
も混合後に圧力をかける製造方法が多く、そのためにま
す型が金属である必要があった。このため金型コストが
、製造費に大きなウェイトを占め、生産性を考えるとコ
ストメリットを出しにくいのが一般的だった。また、こ
のような製造方法では、特に少量多品種には対応できな
い製造方法だった。
Conventional structure and its problems Conventionally, when performing reactive injection molding using nylon RIM materials, it is common practice to perform collision mixing inside a mixing head, and then spray this mixed liquid into a metal mold for molding. It was spot on. However, in this method, the liquid must be in a turbulent flow for collisional mixing, which has the disadvantage that voids are created and the voids cannot be completely removed. For this reason, variations in physical property values were observed, and in particular, variations of 10% or more were observed in impact values, which were 3 pages. Furthermore, in many manufacturing methods, pressure is applied after mixing in order to eliminate voids in this collision mixing, and for this reason, the molds had to be made of metal. For this reason, mold costs accounted for a large portion of manufacturing costs, and it was generally difficult to achieve cost benefits when considering productivity. In addition, this manufacturing method cannot be used especially for low-volume production of a wide variety of products.

発明の目的 本発明の目的は、上記問題点を解決し、成形物にボイド
の発生を防止でき、このため均一な物性値を得ることが
可能となり、さらにゴム型、セラミックス型、金属型を
用いることによって、少量多品種に対応できる有用な製
造方法を提供することである。
Purpose of the Invention The purpose of the present invention is to solve the above-mentioned problems, to prevent the occurrence of voids in the molded product, thereby making it possible to obtain uniform physical property values, and to use rubber molds, ceramic molds, and metal molds. By doing so, the purpose is to provide a useful manufacturing method that can handle a wide variety of products in small quantities.

発明の構成 ナイロンRIM用材料において、原材料のA成分、B成
分を加熱して得られたA液、B液を、スタティックミキ
サーによる混合か、パワーミキサーによる混合のうちい
ずれかの方法を用いて得られた混合液を、混合液吐出ノ
ズルから真空チャンバーにいたるまでいくつかの減圧緩
衝アダプターがあり、混合液がこの液だまりを経るごと
によって減圧度が高くなる減圧緩衝アダプターを経て真
空チャンバー内に導ひき、予備加熱したゴム型。
Components of the Invention In the material for nylon RIM, liquids A and B obtained by heating the raw materials A and B are mixed using either a static mixer or a power mixer. There are several vacuum buffer adapters from the mixed solution discharge nozzle to the vacuum chamber, and the mixed solution is guided into the vacuum chamber through the vacuum buffer adapters, which increase the degree of vacuum as the mixture passes through this liquid pool. Grind and preheat rubber molds.

セラミックス型、金属型かまたはハイブリット型内に流
しこみ、これをさらに加熱して作製するナイロンRIM
材料を用いた成形物の製造方法は、構造材料用1機構部
品材料用として、材料の物性の面では、耐衝撃性、熱変
形温度に優れ、成形面では外観にすぐれた、少量多品種
に対応できる、まったく新しい製造方法であることを発
見したのである。
Nylon RIM is produced by pouring it into a ceramic mold, metal mold, or hybrid mold and heating it further.
The method for manufacturing molded products using the material is for structural materials, mechanical parts materials, and has excellent impact resistance and thermal deformation temperature in terms of physical properties, and excellent appearance in terms of molding, and can be produced in a wide variety of products in small quantities. They discovered a completely new manufacturing method that could handle this problem.

この製造方法は、従来の真空注型9反応性射出成型など
の製造方法では、まったく用いられなかった減圧緩衝ア
ダプターを用いることにより、スタティックミキサー、
パワーミキサー、衝突混合のどの混合方法でも脱泡が完
全に行なえ、成形物に気泡がないというまったく新しい
改良がなされたものである。!、たこのアダプターをつ
けること6ページ より、衝突混合を用いていた大型成形物から、パワーミ
キサーさらにはスタディツクミキサーを用いた実験室レ
ベルの小型反応性射出成形機にいたるまですべてに汎用
できるまったく新しい改良がなされたものである。また
、ゴム型、セラミックス型を用いることにより、従来の
製造方法では得られなかったコストメリットの大きい少
量多品種に対応できるように改良できたものである。
This manufacturing method uses a vacuum buffer adapter, which is not used at all in conventional manufacturing methods such as vacuum casting and reactive injection molding.
This is a completely new improvement in that it can be completely defoamed using any mixing method, including power mixer or collision mixing, and there are no air bubbles in the molded product. ! , Attaching the Octopus Adapter From page 6, it is a completely versatile product that can be used for everything from large moldings using impingement mixing to small laboratory-level reactive injection molding machines using power mixers and even study mixers. New improvements have been made. In addition, by using a rubber mold or a ceramic mold, it has been improved to be able to handle a large variety of products in small quantities, which has a large cost advantage that could not be obtained with conventional manufacturing methods.

実施例の説明 以下、本発明の一実施例を図により説明する。Description of examples Hereinafter, one embodiment of the present invention will be described with reference to the drawings.

〔実施例1〕 1はナイロンRIM用材料のA成分(宇部興産■)製、
UX−BのA成分)を入れたタンクAであり、2はB成
分(UX−BのB成分)を入れたタンクBである。3は
、A液、B液をそれぞれのタンクより、流し出すパルプ
である。4は、2液を混合するためのスタティックミキ
サーである。5.8は、2液の混合液の量を調節するた
めのパルプである。7は、減圧緩衝アダプターであり、
6は、減圧緩衝アダプターをリークするためのパル6ペ
ーノ ブ、9は、減圧するための真空ホースである。1゜は、
真空チャンバーであり、11は、型12のゲート口であ
る。13は真空バルブである。
[Example 1] 1 is made of component A of nylon RIM material (Ube Industries ■),
Tank A contains the A component of UX-B, and tank B contains the B component (the B component of UX-B). 3 is pulp from which liquids A and B are poured out from their respective tanks. 4 is a static mixer for mixing two liquids. 5.8 is a pulp for adjusting the amount of the two liquid mixture. 7 is a vacuum buffer adapter;
6 is a Pal 6 pen knob for leaking the vacuum buffer adapter, and 9 is a vacuum hose for reducing pressure. 1° is
It is a vacuum chamber, and 11 is a gate opening of a mold 12. 13 is a vacuum valve.

マス、オイルバス中に、Aタンク、Bタンク。Mass, A tank, B tank during the oil bath.

スタティックミキサーなど浸漬して、オイルバスを90
℃に設定して、約2時間放置する。こののち、Aタンク
内、Bタンク内を完全にパージしたのち、90℃に保温
され、液化したナイロンRIM材料であるA液、B液を
それぞれのタンクに流しこむ。約1時間保温したのち、
パルプ3を開いて、スタティックミキサー4に流しこみ
、2液を混合する。これらを、6のパルプをあけ、7の
減圧緩衝アダプター内に流しこみ、約6分間、−76c
mHfで減圧にして保持したのち、8のパルプを開いて
、あらかじめ160℃の恒温槽で約3時間加温し、型内
部をN2パージしたシ1)コンゴム型のゲート口から混
合液を液しこみ、混合液を型内部に充てんする。これi
l 50Cの恒温槽中で約6分間放置したのち、脱型し
た。
Immerse in a static mixer, etc., and soak in an oil bath for 90 minutes.
℃ and leave it for about 2 hours. Thereafter, after completely purging the insides of tanks A and B, liquids A and B, which are nylon RIM materials kept at 90° C. and liquefied, are poured into the respective tanks. After keeping warm for about 1 hour,
Pulp 3 is opened, poured into static mixer 4, and the two liquids are mixed. Open the pulp in step 6, pour these into the vacuum buffer adapter in step 7, and hold them at -76c for about 6 minutes.
After reducing the pressure to mHf and maintaining it, open the pulp in step 8, preheat it in a constant temperature bath at 160°C for about 3 hours, and purge the inside of the mold with N2. 1) Pour the mixed solution through the gate opening of the rubber mold. , fill the inside of the mold with the mixed liquid. this i
After being left in a constant temperature bath at 50C for about 6 minutes, the mold was removed.

次に、ゴム型と同形状のセラミックス型(新来7ベーノ 工業(用膜、ポーラセラミックスR)を用いて、同様に
して成形した。
Next, molding was performed in the same manner using a ceramic mold having the same shape as the rubber mold (Shinrai 7 Beno Kogyo (Yomei, Polar Ceramics R)).

丑だ、ハイブリット型を第2図のように作製した。第2
図は、型の材質として、ゴム、セラミックス、金属を用
いたハイブリット型の断面図である。14はセラミック
スであり、16はシリコンゴムであり、17は金属で構
成されている。捷た16の線は、あわせ面を示した。こ
のハイブリット型を用いて、同様に成形した。
I made a hybrid type as shown in Figure 2. Second
The figure is a cross-sectional view of a hybrid mold using rubber, ceramics, and metal as the mold material. 14 is made of ceramics, 16 is made of silicone rubber, and 17 is made of metal. The 16 lines that were cut showed the mating surfaces. Molding was carried out in the same manner using this hybrid mold.

得られた成形物は、どれにも外観に気泡がみられず、成
形サイクルが10分以内で行なえ、型自体も、ゴム型、
セラミックス型などを用いるから、安価なものが得られ
ることがわかった。さらに、アイゾツト衝撃値(ノツチ
付き)も、13〜15(AI+−m/m)  となり、
H,D、Tも、180℃〜190℃の範囲でおさまり、
安定した品質かえられた。
None of the obtained molded products had any visible air bubbles, the molding cycle could be completed within 10 minutes, and the molds themselves were similar to rubber molds,
It was found that by using a ceramic mold, etc., it was possible to obtain an inexpensive product. Furthermore, the Izot impact value (with notch) is 13 to 15 (AI+-m/m),
H, D, and T also fall within the range of 180°C to 190°C,
Stable quality has been achieved.

〔実施例2〕 第3図においで、パワーミキサーを用いて攪拌する場合
を示している。18は攪拌機、19は、攪拌パイ・、2
0は、混合室、21は、減圧用真空ホース、22は減圧
緩衝アダプターである。
[Example 2] Fig. 3 shows a case where stirring is performed using a power mixer. 18 is a stirrer, 19 is a stirring pie, 2
0 is a mixing chamber, 21 is a vacuum hose for reducing pressure, and 22 is a reduced pressure buffer adapter.

実施例1と同様にして、A液、B液を溶解し、混合室2
0に導ひいたあと、攪拌機で15秒間攪拌した。これを
減圧アダプターD1でまず、−26cm Hflの状態
で5分脱泡し、つぎにD2で−76cn1Hfで5分間
脱泡したのち、160℃に加熱してあらかじめ準備され
た真空チャンバー内のゴム型に流しこんだ。混合液がみ
たされたゴム型をチャンバーからとりだし、150℃の
恒温槽中に、10分間放置したあと、とりだし、成形物
を脱型した。
In the same manner as in Example 1, liquid A and liquid B were dissolved and mixed in the mixing chamber 2.
After the temperature reached 0, the mixture was stirred for 15 seconds using a stirrer. This was first degassed for 5 minutes at -26 cm Hfl using vacuum adapter D1, then degassed for 5 minutes at -76 cm Hf using D2, heated to 160°C, and placed in a rubber mold in a vacuum chamber prepared in advance. I poured it into The rubber mold filled with the liquid mixture was taken out from the chamber and left in a constant temperature bath at 150° C. for 10 minutes, then taken out and the molded product was demolded.

得られた成形物は、常圧の場合に比べ、成形物の細かく
狭い部分にまでいきとどき、ボイドが1つたくみられな
かった。また真空中で流しこみ、常圧にもどすことから
、混合液が大気圧によって圧力をうけ、寸法精度が、0
.1〜0.5係以内におさめることができる結果となっ
た。この成形物の物性値は、均質で5係以内のバラツキ
がみられるだけとなった。
The resulting molded product reached fine and narrow parts of the molded product compared to the case under normal pressure, and no voids were observed. Also, since the mixture is poured in a vacuum and returned to normal pressure, the mixed liquid is pressurized by atmospheric pressure, resulting in dimensional accuracy of 0.
.. The result was that it could be kept within 1 to 0.5 units. The physical properties of this molded product were homogeneous with only variations within a factor of 5.

発明の効果 9ページ 以上、本発明は、ナイロンRIM用材料を用いるため、
従来のウレタンRIM用材料に比べて成形サイクルが1
/15〜1/2oに短縮でき、材料物性も、ウレタンR
IMに比べて、特にH,D、Tが1.5〜2.0倍も向
上したものが得られ、ゴム型。
Effects of the invention From page 9 onwards, the present invention uses nylon RIM material, so
1 molding cycle compared to conventional urethane RIM materials
/15 to 1/2o, and the material properties are also better than that of urethane R.
Compared to IM, in particular, H, D, and T are improved by 1.5 to 2.0 times, and it is a rubber type.

セラミックス型を用いるため、型が従来に比べ1150
以下の低価格で得られ、少量多品種に対応できる製造方
法として効果を発揮するものである。
Since a ceramic mold is used, the mold size is 1150 mm compared to conventional ones.
This method is effective as a manufacturing method that can be obtained at a low price as shown below and can be used to produce a wide variety of products in small quantities.

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

第1図は本発明の一実施例を示すスタティックミキサー
で混合し、減圧緩衝アダプターを1つ有し、真空チャン
バー内のゴム型に注液する装置を示した説明図、第2図
はハイブリット型の断面図、第3図は2液をパワーミキ
サーで混合し、減圧アダプター2個を直列につなぎ、真
空チャンバー内のゴム型に注液する装置を示した説明図
である。 1・・・・・・A成分用タンク、2・・・・・・B成分
用タンク、3 ・・・バルブ、4・・・・スタティック
ミキサー、5・・・・・・バルブ、6・・・・・・減圧
緩衝アダプターのリークバルブ、7・・・・・・減圧緩
衝アダプター、8・・・・・バ10べ− ルプ、9・・・真空ホース、10 ・・真空チャンバー
、11・・・・・ゲート口、12・・・・・・型、13
・・・・・・真空バルブ、14・・・セラミックス、1
6・・・・・あわせ面を示す線、16・・・シリコンゴ
ム、1了金属。 代理人の氏名 弁理士 中 尾 敏 男 ほか1名第1
図 第2図
Fig. 1 is an explanatory diagram showing an apparatus for mixing with a static mixer showing one embodiment of the present invention, having one vacuum buffer adapter, and injecting liquid into a rubber mold in a vacuum chamber, and Fig. 2 is a hybrid type. FIG. 3 is an explanatory view showing an apparatus for mixing two liquids with a power mixer, connecting two vacuum adapters in series, and injecting the liquid into a rubber mold in a vacuum chamber. 1...tank for component A, 2...tank for component B, 3...valve, 4...static mixer, 5...valve, 6... ... Leak valve of the vacuum buffer adapter, 7... Vacuum buffer adapter, 8... Vacuum hose, 9... Vacuum hose, 10... Vacuum chamber, 11... ...Gate entrance, 12...Type, 13
...Vacuum valve, 14...Ceramics, 1
6... Line indicating the mating surface, 16... Silicone rubber, 1. Metal. Name of agent: Patent attorney Toshio Nakao and 1 other person No. 1
Figure 2

Claims (3)

【特許請求の範囲】[Claims] (1)ナイロン反応性射出成形用材料において、原材料
のA成分、B成分を加熱して得られたA液、B液を、ス
タティックミキサーによる混合かパワーミキサーによる
混合か、これらのいずれかの方法を用いて得られた混合
液を、減圧緩衝アダプターを経て真空チャンバー内に導
びき、予備加熱したゴム型、セラミックス型、金属型か
またはバイブリッド型内に流しこみ、これらをさらに加
熱して作製する成形物の製造方法。
(1) For nylon reactive injection molding materials, the A and B components obtained by heating the raw materials A and B are mixed using a static mixer or a power mixer, or one of these methods. The mixed solution obtained using the vacuum chamber is introduced into a vacuum chamber through a vacuum buffer adapter, and poured into a preheated rubber mold, ceramic mold, metal mold, or hybrid mold, and these are further heated to create a mold. A method for manufacturing molded products.
(2)減圧緩衝アダプターは、混合液を吐出するノズル
から真空チャンバーにいたるまで、1つまたはいくつか
の液だまりがあり、これらの液だまりは減圧されており
、混合液が液だまりを通過するごとに減圧度が高くなる
よう構成された特許請求の範囲第1項記載の成形物の製
造方法。
(2) A vacuum buffer adapter has one or several liquid pools from the nozzle that discharges the mixed liquid to the vacuum chamber, and these liquid pools are under reduced pressure, and the mixed liquid passes through the liquid pools. 2. The method for manufacturing a molded article according to claim 1, wherein the degree of pressure reduction increases with each step.
(3)ハイブリット型は、型の材質が、ゴム、セラミッ
クス、金属などの複数の材質で構成された型である特許
請求の範囲第1項記載の成形物の製造方法。
(3) The method for manufacturing a molded article according to claim 1, wherein the hybrid mold is a mold made of a plurality of materials such as rubber, ceramics, and metal.
JP24518084A 1984-11-20 1984-11-20 Manufacture of molded product Granted JPS61121903A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24518084A JPS61121903A (en) 1984-11-20 1984-11-20 Manufacture of molded product

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24518084A JPS61121903A (en) 1984-11-20 1984-11-20 Manufacture of molded product

Publications (2)

Publication Number Publication Date
JPS61121903A true JPS61121903A (en) 1986-06-09
JPH0527529B2 JPH0527529B2 (en) 1993-04-21

Family

ID=17129801

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24518084A Granted JPS61121903A (en) 1984-11-20 1984-11-20 Manufacture of molded product

Country Status (1)

Country Link
JP (1) JPS61121903A (en)

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0226377A2 (en) * 1985-12-06 1987-06-24 Marbltone Group Australia Pty. Ltd. Method and apparatus for the production of moulded plastics articles
JPS62204905A (en) * 1986-03-06 1987-09-09 Ube Ind Ltd Reactive injection molding method
EP0639443A2 (en) * 1993-08-05 1995-02-22 Nibco Inc. Reaction injection molded valve and method for producing same
FR2789621A1 (en) * 1999-02-15 2000-08-18 Secmer VACUUM MIXING DEVICE FOR THE CASTING OF POLYMERIZABLE PLASTIC MATERIALS
WO2001072861A3 (en) * 1999-11-12 2002-02-28 Ten Cate Enbi Internat Apparatus for mixing and injection molding thermosetting polyurethane
EP1186391A1 (en) * 2000-09-05 2002-03-13 Hennecke GmbH Method for producing plastic formpieces from a flowable reaction mixture
EP1293323A1 (en) * 2001-09-14 2003-03-19 Demag Ergotech Wiehe GmbH Method and device for injection moulding of liquid silicon rubber (LSR)
GB2386859A (en) * 2002-01-08 2003-10-01 Mcp Tooling Technologies Ltd Moulding thermoplastic articles
FR2871734A1 (en) * 2004-06-22 2005-12-23 Birouste Nicolas Decorative object e.g. jewel, fabricating device, has container receiving mix from mixer to which compartments containing pasty resins are opened, and having cover which blocks opening that permits to access mix receiving impression
ES2260969A1 (en) * 2003-01-22 2006-11-01 Angel Salas Masdeu System of filling molds with resin. (Machine-translation by Google Translate, not legally binding)
WO2007033696A1 (en) * 2005-09-21 2007-03-29 Akemi Chemisch Technische Spezialfabrik Gmbh Metering and mixing installation for two-component liquid systems
EP1777060A1 (en) * 2005-10-18 2007-04-25 Adolf Würth GmbH & Co. KG Method and apparatus for casting thermoplastic materials
US7988903B2 (en) 2008-07-02 2011-08-02 Zeon Chemicals L.P. Fast curing vulcanizable multi-part elastomer composition, and process for blending, injection molding and curing of elastomer composition

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0226377A2 (en) * 1985-12-06 1987-06-24 Marbltone Group Australia Pty. Ltd. Method and apparatus for the production of moulded plastics articles
JPS62204905A (en) * 1986-03-06 1987-09-09 Ube Ind Ltd Reactive injection molding method
EP0639443A2 (en) * 1993-08-05 1995-02-22 Nibco Inc. Reaction injection molded valve and method for producing same
EP0639443A3 (en) * 1993-08-05 1996-01-31 Nibco Reaction injection molded valve and method for producing same.
FR2789621A1 (en) * 1999-02-15 2000-08-18 Secmer VACUUM MIXING DEVICE FOR THE CASTING OF POLYMERIZABLE PLASTIC MATERIALS
EP1029652A1 (en) * 1999-02-15 2000-08-23 Secmer Vacuum mixing device for reactive casting of plastics
WO2001072861A3 (en) * 1999-11-12 2002-02-28 Ten Cate Enbi Internat Apparatus for mixing and injection molding thermosetting polyurethane
US6635200B2 (en) 2000-09-05 2003-10-21 Hennecke Gmbh Process and device for producing plastic moldings from a flowable reaction mixture
EP1186391A1 (en) * 2000-09-05 2002-03-13 Hennecke GmbH Method for producing plastic formpieces from a flowable reaction mixture
EP1293323A1 (en) * 2001-09-14 2003-03-19 Demag Ergotech Wiehe GmbH Method and device for injection moulding of liquid silicon rubber (LSR)
GB2386859A (en) * 2002-01-08 2003-10-01 Mcp Tooling Technologies Ltd Moulding thermoplastic articles
ES2260969A1 (en) * 2003-01-22 2006-11-01 Angel Salas Masdeu System of filling molds with resin. (Machine-translation by Google Translate, not legally binding)
FR2871734A1 (en) * 2004-06-22 2005-12-23 Birouste Nicolas Decorative object e.g. jewel, fabricating device, has container receiving mix from mixer to which compartments containing pasty resins are opened, and having cover which blocks opening that permits to access mix receiving impression
WO2007033696A1 (en) * 2005-09-21 2007-03-29 Akemi Chemisch Technische Spezialfabrik Gmbh Metering and mixing installation for two-component liquid systems
EP1777060A1 (en) * 2005-10-18 2007-04-25 Adolf Würth GmbH & Co. KG Method and apparatus for casting thermoplastic materials
US7988903B2 (en) 2008-07-02 2011-08-02 Zeon Chemicals L.P. Fast curing vulcanizable multi-part elastomer composition, and process for blending, injection molding and curing of elastomer composition

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