JPS6169406A - Reactive injection molding method and device thereof - Google Patents

Reactive injection molding method and device thereof

Info

Publication number
JPS6169406A
JPS6169406A JP19281384A JP19281384A JPS6169406A JP S6169406 A JPS6169406 A JP S6169406A JP 19281384 A JP19281384 A JP 19281384A JP 19281384 A JP19281384 A JP 19281384A JP S6169406 A JPS6169406 A JP S6169406A
Authority
JP
Japan
Prior art keywords
tank
valve
mold
liquid
vacuum
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
JP19281384A
Other languages
Japanese (ja)
Other versions
JPH0461761B2 (en
Inventor
Takao Inoue
孝夫 井上
Kenichiro Suetsugu
憲一郎 末次
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 JP19281384A priority Critical patent/JPS6169406A/en
Publication of JPS6169406A publication Critical patent/JPS6169406A/en
Publication of JPH0461761B2 publication Critical patent/JPH0461761B2/ja
Granted legal-status Critical Current

Links

Classifications

    • 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
    • B29B7/86Component parts, details or accessories; Auxiliary operations for working at sub- or superatmospheric pressure
    • 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
    • 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
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2077/00Use of PA, i.e. polyamides, e.g. polyesteramides or derivatives thereof, as moulding material

Landscapes

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

Abstract

PURPOSE:To speedily mold resin exterior trim part, resin structural part or the like at low cost by a method wherein rubber mold, simple mold, ceramic mold or the like is employed. CONSTITUTION:In order to perform the vacuum casting, firstly, a vacuum chamber and a mold, which is placed in the vacuum chamber and heated up to the reaction temperature for vacuum casting, are provided at the lower part of an injection section. Secondly, the chamber is evacuated to 5X10<-1>Torr or less before injection. Thirdly, after the predetermined amount of material is injected, the chamber is gradually brought back to the atmospheric pressure. Concretely, agitating blades and gear pumps P1 and P2 are respectively provided to a main material liquid tank A and an assistant liquid tank B for agitation and circulation. Though the deterioration of the material may slightly develop by the circulation of the mate rial, the residual bubbles in the piping are eliminated by said circulation. Because the tanks are evacuated, while the material stands in the tanks, bubbles in the material escape from the material. In addition, valves V1 and V2 are closed during the circulation of the material. When the injection of the material is intended, the valves V1 and V2 are open to pour the liquids in the tanks A and B in a mixing part M and, after that, a valve V5 is open so as to discard the small amount of the liquid in the mixing part M in order to remove epsilon- caprolactam. Finally, the valve V5 is closed and a valve V4 is open for injecting the predeter mined amount I1 of the material into the mold in the vacuum chamber.

Description

【発明の詳細な説明】 産業上の利用分野 本発明は、反応性射出成形を用いた真空注型方法及びそ
の装置であり、ゴム型や簡易型、セラミック型などを用
いることにより、樹脂外装部品。
DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a vacuum casting method and apparatus using reactive injection molding, and by using a rubber mold, simple mold, ceramic mold, etc. .

樹脂機構部品等を素速く、安価に成形するものであり、
従来の真空注型に代替すると共に多種少量2.    
  生産工法として用いられるものである。
It is used to quickly and inexpensively mold resin mechanical parts, etc.
As an alternative to conventional vacuum casting, a wide variety of small quantities can be produced.2.
This is used as a production method.

従来例の構成とその問題点 従来の方法は、材料面、工法面、設備面の3点で、本発
明の構成は無く問題があった。従来の真空注型に用いら
れる材料は、そのほとんどがウレタン系の材料であり、
H&にや、日本がオン等の真空注型材料があるが、耐熱
性(熱変形温度が1s、5KLi/Cn下で)が100
’C以上でかつ耐衝撃性(アイゾノトノノテ付き)10
に9・α/an以上というABS樹脂材料に変わる材料
はなかった。
The structure of the conventional example and its problems The conventional method had three problems in terms of materials, construction method, and equipment, and the structure of the present invention did not have the structure. Most of the materials used in conventional vacuum casting are urethane-based materials.
There are vacuum casting materials such as H&Niya and Japan On, but the heat resistance (heat distortion temperature is 1s, under 5KLi/Cn) is 100%.
'C or higher and impact resistance (with eyenote) 10
There was no material that could replace the ABS resin material, which has a value of 9.alpha./an or higher.

これが無いということは、従来の真空注型品は試作品の
みに用いられ、製品用には用いられないという欠点を有
していたのである。又、従来のウレタン材料は、60’
Cと硬化反応温度は低いものの、60’C以上の温度で
30分から2時間半ものアフターキュアーが必要であっ
た。これは、型の使用回数が制御されると共に、金属型
は使えず、多種少量生産に適さないものとなり、100
個以上の生産は難があった。
Without this, conventional vacuum cast products had the disadvantage that they could only be used for prototypes and not for commercial products. Also, conventional urethane materials are 60'
Although the curing reaction temperature was low, an after-cure of 30 minutes to 2.5 hours was required at a temperature of 60'C or higher. This means that the number of times the mold is used is controlled, and metal molds cannot be used, making them unsuitable for high-mix, low-volume production.
It was difficult to produce more than one piece.

又、設備面では、従来のウレタン反応性射出成形機は加
温不可能であり、材料特性の優れたナイロン材料を射出
することは不可能であった。又、文献等で見られるナイ
ロン反応性射出成形機は、衝突混合のものが多く、空気
を巻き込む難があり、精密な成形品を得るためには、独
自の精密注型機が必要であった。又本発明者らは、自作
した注型機を使用している間に、ミキシング部のメンテ
ナンスの仕易さが、注型機の生命であシ、かつ、主剤液
、助剤液、洗浄液の温度差が、注型時の物性にも影響を
与える問題点も発見した。
Furthermore, in terms of equipment, conventional urethane reactive injection molding machines cannot be heated, making it impossible to inject nylon materials with excellent material properties. In addition, many of the nylon reactive injection molding machines found in literature use collision mixing, which has the difficulty of entraining air, and in order to obtain precision molded products, a unique precision casting machine was required. . In addition, while using the self-made casting machine, the inventors found that the ease of maintenance of the mixing section was critical to the life of the casting machine, and that the maintenance of the main liquid, auxiliary liquid, and cleaning liquid was difficult. They also discovered a problem in which temperature differences affect physical properties during casting.

発明の目的 本発明の目的は、ABS樹脂材料に替わる材料物性を有
する反応性材料のナイロン系主剤液と助剤液を用い、気
泡が少い精密な樹脂成形品を得る反応性射出成形方法と
その装置を提供することである。
Purpose of the Invention The purpose of the present invention is to provide a reactive injection molding method for producing precise resin molded products with few air bubbles using a nylon-based main liquid and an auxiliary liquid, which are reactive materials having physical properties that can replace ABS resin materials. The purpose is to provide such equipment.

発明の構成 少くとも2液以上を混合し反応させ所定の形状を得る反
応性射出成形において、各液の貯蔵タンクと洗浄液用タ
ンクとポンプとミキシング部と配管とが全て所定の温度
に加温可能な油槽中に配置され、少くとも各タンクは、
円筒直径より長い高さを有し、垂直に設置され、少くと
もミキシング部はタンク中心の半分の高さ以上の高さに
位置しミキシング部の修善時に油槽のオイルを半分程度
抜くだけで、貯蔵タンク内の材料の温度を下げることな
く修理可能にした反応性射出成形装置であり射出圧力が
小さくて済むため、ミキシング部力(真空チャンバー上
にあり、かつタンク中央より高い位置で突出した構造が
良く、油量を少くするため、出来るだけ幅方向に狭い構
造程良い。尚ポンプは、ギヤポンプ、シリンダーポンプ
(ランスシリンダーポンプ)から選ばれるいずれかであ
れば良い。
Structure of the Invention In reactive injection molding where at least two or more liquids are mixed and reacted to form a predetermined shape, the storage tank for each liquid, the cleaning liquid tank, the pump, the mixing part, and the piping can all be heated to a predetermined temperature. each tank is located in an oil tank with at least
The height is longer than the diameter of the cylinder, and it is installed vertically, and the mixing section is located at least half the height of the center of the tank.When repairing the mixing section, you only need to drain about half of the oil from the oil tank, and it can be stored. This is a reactive injection molding machine that can be repaired without lowering the temperature of the material in the tank, and requires low injection pressure. In order to reduce the amount of oil, it is better to have a structure as narrow as possible in the width direction.The pump may be one selected from gear pumps and cylinder pumps (lance cylinder pumps).

反応に用いる主剤液と助剤液とはポンプによ−り射出時
以外はタンクから出て配管を通りポンプを過て配管を通
り弁を過てタンクにもどるように循環され、射出時には
、今まで通過していた弁を閉じポンプと弁間に設けられ
たミキシング部の弁を開くことにより主剤液と助剤液を
ミキサー部に注液し所定の量を射出した後弁を閉じ、主
剤液と助剤液は循環させた後ミキシング部の射出部先端
の弁を閉じ、洗浄液用の弁を開き洗浄液をミキシング部
に注液し洗浄するというサイクルで射出サイイクルを行
い、射出部下部には、真空チャンバーとその中に真空注
型用の反応温度まで加熱された型を設置し射出前にチャ
ンバーを5×10−’Torr以下の真空に吸引し、そ
の後、前記の反応液を所定量射出後、チャンバーを徐々
に大気圧にもどすことにより真空注型する反応性射出成
形方法である。尚、弁及びミキシングは、衝突混合法を
用いたミキシングヘッドにすることも可能である。但し
その場合は真空チャンバーを型クランプ機と入替えるこ
とにより可能である。
The main agent liquid and the auxiliary agent liquid used in the reaction are circulated by a pump, except during injection, from the tank, through the piping, through the pump, through the piping, through the valve, and back into the tank. The main and auxiliary liquids are injected into the mixer section by closing the valve that has passed through the pump and opening the valve of the mixing section installed between the pump and the valve.After the predetermined amount has been injected, the valve is closed and the main agent liquid is injected into the mixer section. After circulating the auxiliary agent liquid, the valve at the tip of the injection part of the mixing part is closed, and the cleaning liquid valve is opened to inject the cleaning liquid into the mixing part to perform the injection cycle. A vacuum chamber and a mold heated to the reaction temperature for vacuum casting are installed in the vacuum chamber, and the chamber is vacuumed to a vacuum of 5 x 10-' Torr or less before injection, and then a predetermined amount of the reaction liquid is injected. , is a reactive injection molding method in which vacuum casting is performed by gradually returning the chamber to atmospheric pressure. Note that the valve and mixing can also be a mixing head using an impingement mixing method. However, in that case, it is possible to replace the vacuum chamber with a mold clamp machine.

前記反応液がナイロン系のイオン重合材料でちり、洗浄
液がε−カプロラクタム又はその組成物である反応性射
出成形方法である。ε−カプロラクタムは、90’C付
近で数十センチボイズであり、洗浄力を上げるため飽和
炭化水素高分子を溶融した組成物が良い。
In this reactive injection molding method, the reaction liquid is a nylon-based ionic polymer material dust, and the cleaning liquid is ε-caprolactam or a composition thereof. ε-caprolactam has a void of several tens of centimeters at around 90'C, and in order to increase its detergency, a composition prepared by melting a saturated hydrocarbon polymer is preferable.

−・“      前言、真空注型#J、)型は、付ヵ
。重合、イブ。7リコーンゴムが少くとも反応液と接す
る面に配置させた簡易型又はセラミックス型である反応
性射出成形方法である。シリコーンゴムはアンダーカッ
トのある成形物に適しており、セラミックスは耐久性に
優れている。
-・“ Previously, vacuum casting #J) The mold is attached.Polymerization, Eve.7 It is a reactive injection molding method in which silicone rubber is a simple mold or ceramic mold placed at least on the surface that comes into contact with the reaction liquid. .Silicone rubber is suitable for molded products with undercuts, and ceramics are highly durable.

特許請求の範囲第4項記載の反応性射出成形方法及びそ
の装置が、少くともオイル抜きタンクと洗浄液の廃液タ
ンクと真空ポンプとそのトラップと、弁、温度、圧力な
どのコントロール部を有する台部と真空チャ/バーと、
2個以上のタンクと1個以上のポンプとミキシングヘッ
ド部と配管の駆動用モータ、ギヤ、駆動弁(電礎弁、油
圧弁等)を除く全てが収納された恒温油槽部の3つの部
分で構成されたことを特徴とする反応性射出成形装置で
ある。
The reactive injection molding method and the apparatus thereof according to claim 4 provide a platform having at least an oil removal tank, a cleaning liquid waste tank, a vacuum pump, a trap thereof, and control units for valves, temperature, pressure, etc. and vacuum chamber/bar,
It consists of three parts: two or more tanks, one or more pumps, a mixing head part, a piping drive motor, gears, and a constant temperature oil tank part that houses everything except the drive valves (electric foundation valves, hydraulic valves, etc.). This is a reactive injection molding apparatus characterized by the following configuration.

実施例の説明 本発明の実施例は、第1図に示した様に、主剤液タンク
人と助剤液タンクBには、攪拌羽根が設けられており、
ギヤポンプP1とP2によりそれぞれ循環されている。
DESCRIPTION OF THE EMBODIMENTS In the embodiment of the present invention, as shown in FIG. 1, the main liquid tank B and the auxiliary liquid tank B are provided with stirring blades.
It is circulated by gear pumps P1 and P2, respectively.

循環することにより材料の劣化が多少進むが配管、中へ
の気泡残留は無くタンクを真空に引くことにより溜って
いる間に気泡は抜けてしまう。又、循環中は弁V、とv
2は閉じている。v6  には逆止弁を用いた。ゲージ
s Kq/ ciまで液は流れないようにしたものであ
る。(20に9/ Caまで可変である。)タンク及び
配管は全て5US316を用い、ギヤポンプは高千穂機
械製を用いた。射出時には、弁V、とv2を開きミキシ
ング部Mに注゛液し、v5  を開き微少量を廃液して
、ε−カプロラクタムを除去する。その後弁v5  を
閉じv4  を開いて所定量射出後、を行う。v4  
とv5  は兼ねる構造にすることもできる。ミキシン
グ部Mは、スタティックミキサーでも良いが、実1M例
では、パワーミキサーとした。射出部、の後、v4 r
 vI y v2  を閉じ、v3  を開イテ、所定
ノN2圧力で押された、溶融ε−カプロラクタムを弁V
Although the material deteriorates to some extent due to circulation, there are no air bubbles remaining in the piping or inside, and by evacuating the tank, the air bubbles will escape while they remain. Also, during circulation, valves V and V
2 is closed. A check valve was used for v6. The liquid is not allowed to flow up to the gauge s Kq/ci. (It is variable from 20 to 9/Ca.) The tank and piping were all made of 5US316, and the gear pump was made by Takachiho Kikai. At the time of injection, valves V and V2 are opened to inject the liquid into the mixing section M, and valve V5 is opened to drain a small amount of liquid to remove ε-caprolactam. Thereafter, valve v5 is closed and valve v4 is opened to inject a predetermined amount. v4
and v5 can also be structured to serve as both. The mixing section M may be a static mixer, but in the actual 1M example, a power mixer was used. After the injection part, v4 r
Close vI y v2, open v3, and pour the molten ε-caprolactam into the valve V, pressed under a predetermined N2 pressure.
.

を開いてミキシング部に注液し、弁v5  を開いて廃
液工2 にする。但し工2  も80’Cに加温してお
く必要があり、100’Cの恒温油槽中を配管しである
。本発明に用いたナイロン系材料は、(宇部興産製)U
B−Xである。
Open to inject liquid into the mixing section, and open valve v5 to drain liquid. However, process 2 also needs to be heated to 80'C, and the piping is installed in a constant temperature oil bath at 100'C. The nylon material used in the present invention is U (manufactured by Ube Industries).
It is B-X.

又、実施例は、第2図に示した様に、第1図に示した、
反応性射出成形機能を全て設置した恒温油槽部1と真空
チャンバ一部2と、作業者17の高さに設置する役割と
、恒温油槽のオイル抜き用の弁7とタンク8及び、廃液
タンク11と真空チャンバーを5×10−’ Torr
以下まで吸引する真空ポンプ16とトラップ16及び、
制御用ブロックを有する台部21とから構成されており
、注型型は、出入れを19に示した位置で可能であり、
真空チャンバーは、弁14を閉じ弁13を開き真空ポン
プを動かすことによって5×1Φ−’ Torr以下ま
で吸引される。射出部は上下に動く機構ぢが好ましいが
今実施例では、手動でノズルを密着させた。射出後は、
弁9(図1のVs  )を開いて廃・液管10を通じて
廃液する。この射出サイクルは、永久的に使用できるも
のではなく、ミキシング部及び、弁部を周期的に取換え
る必要があるが、これを効率良くするために、恒温油槽
の油面を、ミキシング部に油が残らない油面20まで油
を抜き、ポンプ部22、弁部23、ミキシング部24を
修養又は取換えることを可能にしている。主剤液、助剤
液、洗浄液(ε−カプロラクタム)は、80’C以下で
凝固するが、この様な構成であれば、溶融させたまま、
取換えることが可能である。又、夜間の放置時には、油
槽が冷えに<<ミキシング部に残存した混合液が放置時
間中にゲル化を起こすことがあるが、これも、この様に
オイル面を下げることによってミキシング部の急冷も可
能である。すなわち、メンテ回数を少くすることができ
たのである。又、パワーミキサー部は、つねに、ε−カ
プロラクタムが、主剤液と助剤液との混合液で満たされ
ておシ気泡が巻込まれることもなく、さらに真空中に射
出するため、型中の気泡の残留も少く、気泡が少く、精
密な注型が可能である。
In addition, as shown in FIG. 2, the embodiment shown in FIG.
A constant temperature oil tank section 1 in which all reactive injection molding functions are installed, a vacuum chamber section 2, a role to be installed at the height of the operator 17, a valve 7 and tank 8 for draining oil from the constant temperature oil tank, and a waste liquid tank 11. and the vacuum chamber at 5 × 10-' Torr.
A vacuum pump 16 and a trap 16 that suck up to
It consists of a stand 21 having a control block, and the casting mold can be put in and taken out at the position shown at 19,
The vacuum chamber is suctioned to below 5×1Φ-' Torr by closing the valve 14 and opening the valve 13 and operating the vacuum pump. It is preferable that the injection part has a mechanism that moves up and down, but in this example, the nozzle was brought into close contact manually. After injection,
The valve 9 (Vs in FIG. 1) is opened to drain the liquid through the waste/liquid pipe 10. This injection cycle cannot be used permanently, and it is necessary to periodically replace the mixing section and valve section, but in order to make this process more efficient, the oil level in the constant temperature oil tank is adjusted to the mixing section. The oil is drained to an oil level 20 where no oil remains, and the pump section 22, valve section 23, and mixing section 24 can be repaired or replaced. The main agent liquid, auxiliary agent liquid, and cleaning liquid (ε-caprolactam) solidify at temperatures below 80'C, but with such a configuration, they can remain molten.
It is possible to replace it. Also, when left at night, the oil tank may cool down and the mixed liquid remaining in the mixing section may gel during the standing time, but this is also caused by lowering the oil level in this way, which cools down the mixing section rapidly. is also possible. In other words, the number of maintenance operations could be reduced. In addition, the power mixer section is always filled with the mixed liquid of the main agent liquid and the auxiliary agent liquid, and since the ε-caprolactam is injected into a vacuum without entraining air bubbles, the air bubbles in the mold are injected. There is little residue, there are few bubbles, and precise casting is possible.

表−1には温度制御方法の違いによる物性(成形物)の
安定性とメンテナンス回数を示した。油槽制御はその双
方に効果がある。又、本実施例では付加重合タイプのゴ
ム型を用いたが、150°Cに−加熱しておくことによ
p、3分で脱型することができた。尚、縮合重合タイプ
の型では、表面が白化する現象が起こり、成形に使用で
きないことが解った。セラミック型は真空注型方式では
、表面の光沢に難はあるものの成形することが可能であ
った。空気中での注型では、表面にやはり白化が残った
6セラミソク型でのナイロン成形は、真空中又はN2 
 中で行なうのが最適である。表−2には、型による硬
化性の違いを示した。
Table 1 shows the stability of physical properties (molded product) and the number of maintenance times depending on the temperature control method. Oil tank control has an effect on both. Further, in this example, an addition polymerization type rubber mold was used, but by heating it to 150°C, the mold could be removed in 3 minutes. It has been found that condensation polymerization type molds cannot be used for molding due to the phenomenon of whitening of the surface. It was possible to mold the ceramic mold using the vacuum casting method, although there was a problem with the surface gloss. When casting in air, whitening still remains on the surface of nylon molding in a 6-ceramic mold, but casting in a vacuum or with N2
It is best to do it inside. Table 2 shows the differences in curability depending on the mold.

第3図には、さらに詳しい実施例の構成図を示した。主
剤液用タンク26と助剤液用タンク27、洗浄液用タン
ク28、配管29、ギヤポンプ30、とそのモータ33
、弁ブロック31、パワーミキサー32とそのモータ3
4はモータを除いて全て、ヒータ38と温度センサー4
0で温度制御された恒温油槽25に設けられている。又
タンクには、原料投入口39に攪拌羽根用モータ35と
熱電対36が設けられ、最下位置検出液面計37が、主
剤液と助剤液タンクに設けられている。恒温油槽は上か
ら見ると丁字形状をしておシ、射出部下部に真空チャン
バー42があシ、型43への注液状況を見れる様に、の
ぞき窓41が設けられている。
FIG. 3 shows a more detailed configuration diagram of the embodiment. Main liquid tank 26, auxiliary liquid tank 27, cleaning liquid tank 28, piping 29, gear pump 30, and its motor 33
, valve block 31, power mixer 32 and its motor 3
4 is everything except the motor, heater 38 and temperature sensor 4
It is provided in a constant temperature oil tank 25 whose temperature is controlled at zero. Further, the tank is provided with a stirring blade motor 35 and a thermocouple 36 at the raw material input port 39, and a lowest position detection liquid level gauge 37 is provided in the main liquid and auxiliary liquid tanks. The constant-temperature oil tank has a T-shape when viewed from above, has a vacuum chamber 42 at the bottom of the injection section, and is provided with a viewing window 41 so that the situation of liquid injection into the mold 43 can be observed.

原料投入口が大きく後側を向いているのは、後部から全
ての原料の投入が仕易いようにとの配慮であシ傾斜も設
けられている。この投入口には、ホッパーも設置できる
ようになっている。タンクの攪拌羽根は、タンク上、下
部で固定されており、モータはフタと一緒にはずれる構
成になっている。
The reason why the raw material input port is large and faces toward the rear is to make it easier to input all raw materials from the rear, and it is also slanted. A hopper can also be installed at this input port. The stirring blades of the tank are fixed at the top and bottom of the tank, and the motor is designed to be removed together with the lid.

尚ギヤポンプ用のモータはT字型のポンプ部の側面に設
置することにより、フタの取はずしがさらに良くなると
考えられる。
It is believed that the removal of the lid will be made easier by installing the gear pump motor on the side of the T-shaped pump section.

(以下余白) 発明の効果 本発明では、以上のように、タンク、配管、ミキシング
部など全て恒温油槽に入れることにより、混合液の反応
均一性を増し安定した重合が可能となった。又、循環、
真空注型法により、気泡の少い、特性の良い真空注型樹
脂部品を得ることができた。又ゴム型、セラミック型で
簡単に成珍品を得ることができるようになった。さらに
、ムBS代替材料としてのナイロン系材料UB−Xが安
定した成形が可能な設備として提供できたなどの点で工
業的価値は犬なるものがある。
(Hereinafter in the margin) Effects of the Invention In the present invention, as described above, by placing the tank, piping, mixing part, etc. in a constant temperature oil bath, the reaction uniformity of the mixed liquid is increased and stable polymerization is possible. Also, circulation,
Using the vacuum casting method, we were able to obtain vacuum-cast resin parts with few bubbles and good properties. In addition, it became possible to easily obtain exquisite items using rubber molds and ceramic molds. Furthermore, the nylon-based material UB-X as an alternative material for BS can be provided as equipment capable of stable molding, so it has great industrial value.

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

第1図はタンク、配管、弁、ミキシング部などの構成を
示すブロック図、第2図は本発明の一実流側の構成及び
特徴を示す模式図、第3図は本発明の一実施例の恒温油
槽部と真空チャンバ一部の正面部分断面図、第3図すは
同平面図である。 1・・・・・・恒温油槽部、2・・・・・・真空チャン
バー、3夕、11・・・・・・廃液タンク、16・・・
・・・真空ポンプ、21・・・・・・台部。 代理人の氏名 弁理士 中 尾 敏 男 ほか1名区 域 区 l N  ゝ   へJ 寸 う  Cつ     寸
Fig. 1 is a block diagram showing the configuration of tanks, piping, valves, mixing parts, etc., Fig. 2 is a schematic diagram showing the structure and characteristics of the actual flow side of the present invention, and Fig. 3 is an embodiment of the present invention. FIG. 3 is a front partial cross-sectional view of a constant temperature oil bath section and part of a vacuum chamber, and FIG. 3 is a plan view thereof. 1... Constant temperature oil tank section, 2... Vacuum chamber, 3 evenings, 11... Waste liquid tank, 16...
...Vacuum pump, 21...Base part. Name of agent Patent attorney Toshio Nakao and 1 other person Area Area

Claims (5)

【特許請求の範囲】[Claims] (1)反応に用いる主剤液と助剤液とはポンプにより射
出時以外はタンクから出て配管を通りポンプを過て配管
を通り弁を過てタンクにもどるように循環され、射出時
には、今まで通過していた弁を閉じポンプと弁間に設け
られたミキシング部の弁を開くことにより主剤液と助剤
液をミキサー部に注液し所定の量を射出した後弁を閉じ
、主剤液と助剤液は循環させた後ミキシング部の射出部
先端の弁を閉じ、洗浄液用の弁を開き洗浄液をミキシン
グ部に注液し洗浄するというサイクルで射出サイクルを
行い、射出部下部には、真空チャンバーとその中に真空
注型用の反応温度まで加熱された型を設置し射出前にチ
ャンバーを5×10^−^1Torr以下の真空に吸引
し、その後、前記の所定量射出後、チャンバーを徐々に
大気圧にもどすことにより真空注型する反応性射出成形
方法。
(1) The main agent liquid and the auxiliary agent liquid used for the reaction are circulated by a pump, except during injection, from the tank, through the piping, through the pump, through the piping, through the valve, and back into the tank. The main and auxiliary liquids are injected into the mixer section by closing the valve that has passed through the pump and opening the valve of the mixing section installed between the pump and the valve.After the predetermined amount has been injected, the valve is closed and the main agent liquid is injected into the mixer section. After circulating the auxiliary agent liquid, the valve at the tip of the injection part of the mixing part is closed, and the cleaning liquid valve is opened to inject the cleaning liquid into the mixing part to perform the injection cycle. A vacuum chamber and a mold heated to the reaction temperature for vacuum casting are installed in it, and the chamber is vacuumed to a vacuum of 5 x 10^-^1 Torr or less before injection, and then, after the predetermined amount is injected, the chamber is heated to a reaction temperature for vacuum casting. A reactive injection molding method that involves vacuum casting by gradually returning the material to atmospheric pressure.
(2)反応液がナイロン系のイオン重合材料であり、洗
浄液がε−カプロラクタム又はその組成物である特許請
求の範囲第1項記載の反応性射出成形方法。
(2) The reactive injection molding method according to claim 1, wherein the reaction liquid is a nylon-based ionic polymer material, and the cleaning liquid is ε-caprolactam or a composition thereof.
(3)真空注型用の型は、付加重合タイプのシリコーン
ゴムが少くとも反応液と接する面に配置させた簡易型又
はセラミックス型である特許請求の範囲第1項記載の反
応性射出成形方法。
(3) The reactive injection molding method according to claim 1, wherein the mold for vacuum casting is a simple mold or a ceramic mold in which addition polymerization type silicone rubber is placed at least on the surface in contact with the reaction liquid. .
(4)少くとも2液以上を混合し反応させ所定の形状を
得る反応性射出成形用の各液の貯蔵タンクと洗浄液用タ
ンクとポンプとミキシング部と配管とが全て所定の温度
に加温可能な油槽中に配置され、少くとも各タンクは、
円筒直径より長い高さを有し、垂直に設置され、少くと
もミキシング部はタンク中心の半分の高さ以上の高さに
位置し、ミキシング部の修善時に油槽のオイルを半分程
度抜くだけで、貯蔵タンク内の材料の温度を下げること
なく修理可能にした反応性射出成形装置。
(4) The storage tank for each liquid, the cleaning liquid tank, the pump, the mixing part, and the piping for reactive injection molding, in which at least two or more liquids are mixed and reacted to form a predetermined shape, can all be heated to a predetermined temperature. each tank is located in an oil tank with at least
It has a height longer than the diameter of the cylinder, is installed vertically, and the mixing section is located at least half the height of the center of the tank, so when repairing the mixing section, you only need to drain about half of the oil from the oil tank. Reactive injection molding equipment that allows repair without lowering the temperature of the material in the storage tank.
(5)特許請求の範囲第4項記載の反応性射出成形装置
にあって、少くともオイル抜きタンクと洗浄液の廃液タ
ンクと真空ポンプとそのトラップと、弁、温度、圧力な
どのコントロール部を有する台部と真空チャンバーと、
2個以上のタンクと1個以上のポンプとミキシングヘッ
ド部と配管の全てが収納された恒温油槽部の3つの部分
で構成されたことを特徴とする反応性射出成形装置。
(5) The reactive injection molding apparatus according to claim 4, which includes at least an oil removal tank, a cleaning liquid waste tank, a vacuum pump and its trap, and a control section for controlling valves, temperature, pressure, etc. A base and a vacuum chamber,
A reactive injection molding device comprising three parts: two or more tanks, one or more pumps, a mixing head part, and a constant temperature oil bath part in which all piping is housed.
JP19281384A 1984-09-14 1984-09-14 Reactive injection molding method and device thereof Granted JPS6169406A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19281384A JPS6169406A (en) 1984-09-14 1984-09-14 Reactive injection molding method and device thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19281384A JPS6169406A (en) 1984-09-14 1984-09-14 Reactive injection molding method and device thereof

Publications (2)

Publication Number Publication Date
JPS6169406A true JPS6169406A (en) 1986-04-10
JPH0461761B2 JPH0461761B2 (en) 1992-10-02

Family

ID=16297411

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19281384A Granted JPS6169406A (en) 1984-09-14 1984-09-14 Reactive injection molding method and device thereof

Country Status (1)

Country Link
JP (1) JPS6169406A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2789621A1 (en) * 1999-02-15 2000-08-18 Secmer VACUUM MIXING DEVICE FOR THE CASTING OF POLYMERIZABLE PLASTIC MATERIALS
EP2743061A1 (en) * 2012-12-13 2014-06-18 Fundacion Tecnalia Research & Innovation Device for polymerizing lactams in molds

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
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
EP2743061A1 (en) * 2012-12-13 2014-06-18 Fundacion Tecnalia Research & Innovation Device for polymerizing lactams in molds
CN104086766A (en) * 2012-12-13 2014-10-08 泰克纳利尔研究与创新基金会 Device for polymerizing lactams in molds

Also Published As

Publication number Publication date
JPH0461761B2 (en) 1992-10-02

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