JPS6221511A - Mixing method for reactive raw material and its device - Google Patents
Mixing method for reactive raw material and its deviceInfo
- Publication number
- JPS6221511A JPS6221511A JP60162419A JP16241985A JPS6221511A JP S6221511 A JPS6221511 A JP S6221511A JP 60162419 A JP60162419 A JP 60162419A JP 16241985 A JP16241985 A JP 16241985A JP S6221511 A JPS6221511 A JP S6221511A
- Authority
- JP
- Japan
- Prior art keywords
- raw materials
- mixing
- rotating shaft
- raw material
- rotary shaft
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
- B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
- B29B7/00—Mixing; Kneading
- B29B7/30—Mixing; Kneading continuous, with mechanical mixing or kneading devices
- B29B7/34—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices
- B29B7/38—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary
- B29B7/40—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft
- B29B7/42—Mixing; Kneading continuous, with mechanical mixing or kneading devices with movable mixing or kneading devices rotary with single shaft with screw or helix
-
- 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
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/02—Small extruding apparatus, e.g. handheld, toy or laboratory extruders
-
- 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
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/395—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die using screws surrounded by a cooperating barrel, e.g. single screw extruders
- B29C48/45—Axially movable screws
-
- 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
- B29C48/00—Extrusion moulding, i.e. expressing the moulding material through a die or nozzle which imparts the desired form; Apparatus therefor
- B29C48/25—Component parts, details or accessories; Auxiliary operations
- B29C48/36—Means for plasticising or homogenising the moulding material or forcing it through the nozzle or die
- B29C48/50—Details of extruders
- B29C48/505—Screws
- B29C48/56—Screws having grooves or cavities other than the thread or the channel
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Health & Medical Sciences (AREA)
- Clinical Laboratory Science (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
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、反応原料の混合方法及びそれを用いた混合装
置に関し、2は液混合用のディスペンサー、真空注型装
置9反応性射出成形装置などに利用される。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a method for mixing reaction raw materials and a mixing device using the same. used.
従来の技術
従来エポキシ等の2液液着剤は、スタティックミキサー
を用いた静的な分割混合に代表される、2液温合方法で
使用されるか、又は実用新案公開公報60−113 、
60−114特開昭51−97672などに見られる、
衝突混合ノズルを用いて混合使用されている。BACKGROUND OF THE INVENTION Conventional two-component adhesives such as epoxy are used in a two-component heating method, typified by static divisional mixing using a static mixer, or as disclosed in Utility Model Publication No. 60-113,
60-114, as seen in JP-A-51-97672, etc.
It is used for mixing using impingement mixing nozzles.
発明が解決しようとする問題点
しかし、従来のスタティックミキサーは、混合するのに
ある程度の液量が必要であり、従量で精密混合吐出する
のには不向きであるし、衝突混合ノズルは大量の混合吐
出にしか向かない。Problems to be Solved by the Invention However, conventional static mixers require a certain amount of liquid to mix, making them unsuitable for precise mixing and dispensing in controlled quantities, and impingement mixing nozzles are not suitable for mixing large amounts of liquid. It is only suitable for ejection.
したがって何れも比較的少量の反応原料を、充分に混合
するものとしては満足できない。Therefore, neither method is satisfactory for sufficiently mixing a relatively small amount of reaction materials.
本発明は、そのような問題点を解決しようとするもので
あり、充填剤などを含む、高粘度の反応原料を充分に混
合しようとするものである。The present invention is an attempt to solve such problems, and is an attempt to sufficiently mix highly viscous reaction raw materials containing fillers and the like.
問題点を解決するだめの手段
本発明は、以」二の問題点を解決するために、複数液反
応原料の混合方法において、1条以上の溝を有する回転
軸と回転軸の周囲に形成された複数の原料吐出口とを相
対回転させることにより、吐出口から交互に原料を溝内
へかき取り複数液の反応原料を混合する、反応原料の混
合方法を主たる特徴とするものであり、さらに混合を確
実なものとするために、溝内にかき取った複数液の原料
を同一部に解放すると共に撹拌することにより、複数液
の反応原料を混合することも特徴としている。Means for Solving the Problems In order to solve the following two problems, the present invention provides a method for mixing multiple liquid reaction raw materials, in which a rotating shaft having one or more grooves is formed around the rotating shaft. The main feature is a method of mixing reaction raw materials in which multiple liquids of reaction raw materials are mixed by alternately scraping the raw materials from the discharge ports into the grooves by rotating the plurality of raw material discharge ports relative to each other. In order to ensure mixing, the reaction raw materials of multiple liquids are mixed by releasing the raw materials of multiple liquids scraped into the groove into the same part and stirring them.
寸だ、この混合方法と具現化する装置として1条以上の
溝を有する回転軸が縦通した混合ノズルと複数の原料タ
ンクから混合ノズル内の回転軸の外周面局部に反応原料
を圧送する圧送手段と、回転軸を回転させる駆動手段と
、反応原料の圧送および混合の経路所要部を温度調節す
る温度制御手段とを有する構成としたものである。This mixing method and the device that embodies it include a mixing nozzle in which a rotating shaft with one or more grooves runs vertically through it, and a pressure feeding system that pumps the reaction raw materials from multiple raw material tanks to a localized area on the outer circumferential surface of the rotating shaft in the mixing nozzle. A drive means for rotating a rotating shaft, and a temperature control means for controlling the temperature of a required part of a path for pumping and mixing reaction raw materials.
作 用
以上の様な手段を用いることにより、回転軸が回転する
に伴い、原料吐出口と溝とが一致している間、溝に原料
は吐出され、次の吐出口では次の原料と次々に吐出され
、軸の回転数が500〜66−ン
3200rpm程度の高速で回転される場合、細かい層
状に溝へ充填され混合される。これにより精密混合が可
能となる。さらに溝内の複数液原料を同一部に解放して
撹拌することでよシ一層充分に混合されるものである。Effect By using the above-mentioned means, as the rotating shaft rotates, the raw material is discharged into the groove while the raw material discharge port and the groove are aligned, and the next raw material is sequentially discharged at the next discharge port. When the shaft is rotated at a high speed of about 500 to 66-3200 rpm, it is filled into the grooves in a fine layer and mixed. This allows precise mixing. Furthermore, by releasing the plural liquid raw materials in the groove into the same part and stirring them, they can be mixed even more thoroughly.
尚、回転数が速く、2液量度の場合は、これら原料解放
状態での撹拌なしでも充分混合され反応が進む。Note that when the rotational speed is high and the liquid volume is two degrees, the raw materials are sufficiently mixed and the reaction proceeds even without stirring in a released state.
又、連続で吐出する場合に、気泡を含むこともなく、混
合液を安定して供給することができる。Moreover, when continuously discharging, the mixed liquid can be stably supplied without containing bubbles.
殊に装置の場合、複数液の原料が適時的に圧送されるこ
とで、混合作業を混合物使用・不使用状況等に合せて進
め得るし、供給され、混合される原料に対し温度制御す
ることによシ、所要程度の反応を所要速度で得られる。In particular, in the case of equipment, by timely pressure-feeding of multiple liquid raw materials, the mixing operation can proceed according to whether the mixture is used or not, and the temperature of the raw materials to be supplied and mixed can be controlled. As a result, the required degree of reaction can be obtained at the required rate.
実施例
第1図は、本発明の一実施例を示す、混合方法を具現化
する混合ノズル部の断面図である。詳しくは溝7を有す
る回転軸1(実際は加工用ドリルを使用)と、それが縦
通して接するノズル本体2゜反応原料A、Bをノズル本
体2内の回転軸1外周e S S’
に供給する供給経路3.6と、その回転軸1の外周面局
部と接する吐出口4,6から構成されている。より好ま
しい形として、回転軸の先端を軸より細くすることによ
って、完全混合用小径先端8と、それによって出来る混
合空間9とを有している。必要に応じて小径先端部8の
まわシに撹拌羽根8aが仮想線のように設けられる。Embodiment FIG. 1 is a sectional view of a mixing nozzle section embodying a mixing method, showing one embodiment of the present invention. Specifically, a rotary shaft 1 having a groove 7 (actually, a processing drill is used) and a nozzle body 2 where it runs vertically and contacts the reaction raw materials A and B are supplied to the outer periphery of the rotary shaft 1 inside the nozzle body 2. The supply path 3.6 includes a supply path 3.6, and discharge ports 4, 6 that are in contact with a local part of the outer peripheral surface of the rotating shaft 1. As a more preferable form, the tip of the rotating shaft is made thinner than the shaft to have a small-diameter tip 8 for complete mixing and a mixing space 9 created thereby. If necessary, a stirring blade 8a is provided around the small-diameter tip portion 8 as shown in an imaginary line.
具体的な反応原料の混合方法は、第2図に示した様に原
料吐出口4.6には、圧送された原料A。A specific method of mixing the reaction raw materials is as shown in FIG. 2, where the raw material A is pumped into the raw material discharge port 4.6.
Bが待機されており、回転軸が回転することにより、溝
7と吐出口4が一致する時間だけ原料Aが溝に供給され
、同様に次の吐出口6では原料Bが溝に供給されるとい
う具合に、ブラッグ状1層状に原料Aのかきとり分10
.原料Bのかきとり分11、がかき込まれ充填される。B is on standby, and by rotating the rotating shaft, raw material A is supplied to the groove for the time period when groove 7 and discharge port 4 coincide, and raw material B is similarly supplied to the groove at the next discharge port 6. In this way, 10 pieces of raw material A are scraped off in one Bragg-like layer.
.. A scraped portion 11 of raw material B is scraped and filled.
これをくり返すうちに、原料は回転軸1の先端部まで到
達し、混合空間9へ解放されて、さらに撹拌されること
によって精密に混合される。回転軸の太さと単位時間当
りの回転数、溝の深さ、原料粘度、原料に加える圧力な
どによりかきとり分10,11の単位7 パ−・
量を極く微量にしてより微量精密混合を可能とし、捷だ
解放撹拌なしにも充分な混合を達成させ得る。As this process is repeated, the raw materials reach the tip of the rotating shaft 1, are released into the mixing space 9, and are further stirred and mixed precisely. Depending on the thickness of the rotating shaft, the number of rotations per unit time, the depth of the groove, the viscosity of the raw material, the pressure applied to the raw material, etc., the scraped amount can be made into an extremely small amount (unit 7%) of 10 or 11, allowing for more precise mixing. As a result, sufficient mixing can be achieved even without continuous stirring.
゛ さらに圧送のタイミング調整も加えノズル本体2か
らの混合物総吐出量を制御することができる。Furthermore, the total amount of mixture discharged from the nozzle body 2 can be controlled by adjusting the timing of pressure feeding.
第3図は、本発明を、エポキシ2液接着剤に適用した場
合の一実施例であり、・・ンディタイプの2液温合ディ
スベンザーが示されている。回転軸1が縦通ずるノズル
本体2と、その後方上部に原料A、Bを内填させた医用
のプラスチック製注射器シリンダ12 、12’が接続
され、それらのピストン13 、13’を押すためのバ
ネ式圧力治具14がシリンダ13と13′との間に介在
させられている、各シリンダ12 、12’からのノズ
ル本体2に対する反応液の供給経路15 、15’にノ
ズル部洗浄時に反応原料供給を止める弁16が設けられ
ている。17 、17’は、各供給経路15 、15’
の回転軸1の外周面局部と接する反応原料吐出口である
。回転軸1は、その後方に設置されたDCモータ18と
連結部19を弁連結され、モータ回転をスタート、スト
ップさせるスイッチ21が、それを指でピストル式に操
作する引き金20と共に、手でにぎるディスペンサ本体
22部に設けられている。さらにノズル本体2部には、
冷却させることによって、反応を遅らせることを利用す
る2液反応原料の混合方法を実現させる一例としての半
導体冷却ユニット23が設けられている。FIG. 3 shows an embodiment in which the present invention is applied to a two-component epoxy adhesive, and shows a two-component thermal disbenzer of the Indian type. A nozzle body 2 through which a rotating shaft 1 passes vertically is connected to a medical plastic syringe cylinder 12, 12' filled with raw materials A and B to the rear upper part of the nozzle body 2, and a spring for pushing the pistons 13, 13'. A type pressure jig 14 is interposed between the cylinders 13 and 13', and the reaction liquid is supplied from each cylinder 12, 12' to the nozzle body 2 through the reaction liquid supply path 15, 15' during nozzle cleaning. A valve 16 is provided to stop the. 17 and 17' are each supply route 15 and 15'
This is a reaction raw material discharge port that is in contact with a local part of the outer circumferential surface of the rotating shaft 1. The rotating shaft 1 is connected by a valve to a DC motor 18 installed at the rear thereof and a connecting part 19, and a switch 21 for starting and stopping the rotation of the motor is operated by hand together with a trigger 20 operated by a finger like a pistol. It is provided in the 22 part of the dispenser main body. Furthermore, in the second part of the nozzle body,
A semiconductor cooling unit 23 is provided as an example for realizing a method of mixing two-liquid reaction materials that utilizes cooling to delay the reaction.
この様な構造にすることによって、従来使用しにくかっ
た、室温硬化型の2液タイプのエポキシ系接着剤を、前
記実施例のような複数液混合上の特徴を踏襲しながら、
8時間以上も断続的な作業下で連続して使用することが
できるようになった。With this structure, it is possible to use a two-component type epoxy adhesive that cures at room temperature, which was previously difficult to use, while following the characteristics of mixing multiple components as in the above embodiment.
It has become possible to use it continuously for more than 8 hours with intermittent work.
第4図は、本発明の混合方法を反応性射出成形に適用す
るための一実施例であり、反応原料A。FIG. 4 shows an example of applying the mixing method of the present invention to reactive injection molding, in which reaction raw material A is used.
Bを溶融保存する夕/り24,25に各原料A。At 24 and 25 minutes after melting and preserving B, each raw material A was added.
Bを循環させる配管28,30.32と29.31 。Pipes 28, 30.32 and 29.31 that circulate B.
33とがそれぞれ接続されている。それぞれの配管は、
圧送ポンプ26.27と循環と吐出を制御する3方弁3
4,35とをそれぞれ途中に有し、弁34.35部で前
記各実施例と同様の混合ノズル36に供給経路39.4
0をもって接続され、9 パ−ン
回転軸(図示せず)を回転又は、及び前後動させるモー
タ兼シリンダー弁37と、ナイロン反応成形材料の場合
は80 ’C〜100°C,ポリエステルアミドの場合
は120″C〜150°Cの温度に温度調節する油槽、
熱風槽、2重配管、38とが設けられている。33 are connected to each other. Each pipe is
Pressure pump 26, 27 and 3-way valve 3 that controls circulation and discharge
4 and 35 in the middle, and a supply path 39.4 is connected to a mixing nozzle 36 similar to that in each of the above embodiments at a valve 34.35.
0 and a motor/cylinder valve 37 that rotates or moves the 9 pirn rotating shaft (not shown) back and forth; is an oil bath whose temperature is adjusted to a temperature of 120″C to 150°C,
A hot air tank, double piping, and 38 are provided.
これにより、前記実施例のような複数液混合が、反応性
射出成形工程においてなされる。Thereby, the mixing of multiple liquids as in the above embodiment is performed in the reactive injection molding process.
発明の効果
本発明は、比較的少量の複数液の反応原料を回転軸の溝
による交互かき取りによる混合で、微量でも精密に混合
できる効果を得ると共に、溝の深さや回転軸の径を工夫
することによって、微量から、ある程度の量までを回転
数と圧送力によって制御できるもので接着用ディスペン
サーから反応性射出成形機まで適用可能であり工業的価
値は犬なるものがある。また、前記混合は溝による交互
かき取り複数液を同一部に解放して撹拌することでさら
に促進し得るし、原料圧送ないし混合の所定経路におけ
る温度制御手段を備えた装置によっ10 べ−7′
ては、混合物の各種使用不使用状況に応じた混合作業や
反応度、反応速度が得られ実用上非常に便利である。Effects of the Invention The present invention achieves the effect of precisely mixing even minute amounts by mixing relatively small amounts of multiple liquid reaction materials by alternately scraping them through the grooves of the rotating shaft, and also improves the depth of the grooves and the diameter of the rotating shaft. By doing so, it is possible to control from a minute amount to a certain amount by changing the rotation speed and pumping force, and it is applicable to everything from adhesive dispensers to reactive injection molding machines, and has great industrial value. Further, the mixing can be further promoted by discharging multiple liquids alternately scraped by the grooves and stirring them in the same part, or by using a device equipped with a temperature control means in a predetermined route for pressure feeding or mixing the raw materials. ' This method is very convenient in practice, as it allows mixing operations, reactivity, and reaction rates to be adjusted according to various situations of use or non-use of the mixture.
第1図は本発明の混合方法を具現化した混合ノズル部の
断面図、第2図は本発明の混合方法を示す回転軸の部分
図、第3図は本発明の混合方法を室温硬化エポキシ2液
接着剤用ディスペンサーに実用化した時のディスペンサ
一部分断面図、第4図は本発明をウレタン、ナイロン、
ポリエステルアミドなどの反応性射出成形機に適用した
時の構成図である。
1・・・・・・回転軸、2・・・・・・ノズル本体、3
,5,15゜16’、39.40・・・・・・反応原料
供給経路、4,6゜17 、17’・・・・・・反応原
料吐出口、7・・・・・・溝、12゜12′・・・・・
シリンダー、14・・・・・バネ式圧力治具、23・・
・・・冷却ユニット、26.27・・・・・圧送ポンプ
、A・・・・・反応原料、B・・・・・・反応原料。
代理人の氏名 弁理士 中 尾 敏 男 ほか1名1−
一一回先軸
2−−−ノズール苓)ド
アー 清
ga−−−)嘆ζN’イ司S
第2図Fig. 1 is a cross-sectional view of a mixing nozzle that embodies the mixing method of the present invention, Fig. 2 is a partial view of the rotating shaft showing the mixing method of the present invention, and Fig. 3 is a cross-sectional view of the mixing nozzle section embodying the mixing method of the present invention. Figure 4 is a partial cross-sectional view of the dispenser when it is put into practical use as a two-component adhesive dispenser.
FIG. 2 is a configuration diagram when applied to a reactive injection molding machine for polyesteramide, etc. 1... Rotating shaft, 2... Nozzle body, 3
, 5, 15゜16', 39.40...Reaction raw material supply route, 4,6゜17, 17'...Reaction raw material discharge port, 7...Groove, 12゜12′・・・・・・
Cylinder, 14...Spring pressure jig, 23...
...Cooling unit, 26.27...Pressure pump, A...Reaction raw material, B...Reaction raw material. Name of agent: Patent attorney Toshio Nakao and 1 other person1-
11th axis 2 --- Nozzle 蓓) Door Clearance ---) Lament ζN'Ishi S Figure 2
Claims (6)
溝を有する回転軸と回転軸の周囲に形成された複数の原
料吐出口とを相対回転させることにより、吐出口から交
互に反応原料を溝内へかき取り、複数液の反応原料を混
合することを特徴とする反応原料の混合方法。(1) In a method of mixing multiple liquid reaction materials, by relatively rotating a rotating shaft having one or more grooves and a plurality of raw material discharge ports formed around the rotating shaft, the reaction materials are alternately distributed from the discharge ports. A method for mixing reaction raw materials, characterized in that a plurality of liquid reaction raw materials are mixed by scraping the liquid into a groove.
溝を有する回転軸と回転軸の周囲に形成された複数の原
料吐出口とを相対回転させることにより、吐出口から交
互に反応原料を溝内へかき取り、それを同一部に解放す
ると共に撹拌することにより、複数液の反応原料を混合
することを特徴とする反応原料の混合方法。(2) In a method of mixing multiple liquid reaction materials, by relatively rotating a rotating shaft having one or more grooves and a plurality of raw material discharge ports formed around the rotating shaft, the reaction materials are alternately distributed from the discharge ports. A method for mixing reaction raw materials, characterized in that multiple liquid reaction raw materials are mixed by scraping the liquid into a groove, releasing it into the same part, and stirring.
ルと、複数の原料タンクから混合ノズル内の回転軸の外
周面局部に反応原料を圧送する圧送手段と、回転軸を回
転させる駆動手段と、反応原料の圧送および混合の経路
所要部を温度調節する温度制御手段とを有する反応原料
の混合装置。(3) A mixing nozzle in which a rotating shaft having one or more grooves runs vertically through the mixing nozzle, a pressure feeding means for pumping reaction raw materials from a plurality of raw material tanks to a local part of the outer peripheral surface of the rotating shaft in the mixing nozzle, and rotating the rotating shaft. A mixing device for reaction raw materials, which has a driving means and a temperature control means for controlling the temperature of a required part of a route for pressure feeding and mixing of reaction raw materials.
転数を制御可能とされている特許請求の範囲第3項記載
の反応原料の混合装置。(4) The reaction raw material mixing device according to claim 3, wherein the rotating shaft driving means is capable of controlling the number of revolutions of the rotating shaft per unit time.
マー機能を持つものとされている特許請求の範囲第3項
または第4項記載の反応原料の混合装置。(5) The reaction raw material mixing apparatus according to claim 3 or 4, wherein the pressure feeding means has a timer function for adjusting the timing of pressure feeding of the raw materials.
を温度制御するようにされている特許請求の範囲第3項
または第4項または第5項記載の反応原料の混合装置。(6) The reaction raw material mixing apparatus according to claim 3, 4, or 5, wherein the temperature control means is configured to control the temperature of a mixing nozzle portion through which the rotating shaft runs vertically.
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60162419A JPS6221511A (en) | 1985-07-23 | 1985-07-23 | Mixing method for reactive raw material and its device |
EP86110040A EP0209888B1 (en) | 1985-07-23 | 1986-07-22 | Mixing method of reaction raw-material and its apparatus |
US06/887,922 US4778659A (en) | 1985-07-23 | 1986-07-22 | Mixing method of reaction raw-material |
DE8686110040T DE3669266D1 (en) | 1985-07-23 | 1986-07-22 | MIXING METHOD FOR REACTION INITIAL MATERIAL AND APPARATUS DAFUER. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60162419A JPS6221511A (en) | 1985-07-23 | 1985-07-23 | Mixing method for reactive raw material and its device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6221511A true JPS6221511A (en) | 1987-01-29 |
JPH0378047B2 JPH0378047B2 (en) | 1991-12-12 |
Family
ID=15754238
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60162419A Granted JPS6221511A (en) | 1985-07-23 | 1985-07-23 | Mixing method for reactive raw material and its device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6221511A (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS477451U (en) * | 1971-02-18 | 1972-09-27 |
-
1985
- 1985-07-23 JP JP60162419A patent/JPS6221511A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS477451U (en) * | 1971-02-18 | 1972-09-27 |
Also Published As
Publication number | Publication date |
---|---|
JPH0378047B2 (en) | 1991-12-12 |
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