JPS5816832A - Mixing apparatus of two-pack type aerosol system urethane foam manufacture - Google Patents

Mixing apparatus of two-pack type aerosol system urethane foam manufacture

Info

Publication number
JPS5816832A
JPS5816832A JP56113622A JP11362281A JPS5816832A JP S5816832 A JPS5816832 A JP S5816832A JP 56113622 A JP56113622 A JP 56113622A JP 11362281 A JP11362281 A JP 11362281A JP S5816832 A JPS5816832 A JP S5816832A
Authority
JP
Japan
Prior art keywords
conduits
mixing tube
urethane foam
mixing
conduit
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
JP56113622A
Other languages
Japanese (ja)
Other versions
JPH0150573B2 (en
Inventor
Kazuo Wada
和田 一雄
Yukio Hirose
幸男 廣瀬
Kenichi Shigemura
茂村 健一
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.)
TOKYO AEROSOL KAGAKU KK
Original Assignee
TOKYO AEROSOL KAGAKU KK
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 TOKYO AEROSOL KAGAKU KK filed Critical TOKYO AEROSOL KAGAKU KK
Priority to JP56113622A priority Critical patent/JPS5816832A/en
Publication of JPS5816832A publication Critical patent/JPS5816832A/en
Publication of JPH0150573B2 publication Critical patent/JPH0150573B2/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
    • B29B7/30Mixing; Kneading continuous, with mechanical mixing or kneading devices
    • B29B7/32Mixing; Kneading continuous, with mechanical mixing or kneading devices with non-movable mixing or kneading devices
    • 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
    • B29B7/74Mixing; Kneading using other mixers or combinations of mixers, e.g. of dissimilar mixers ; Plant
    • B29B7/7404Mixing devices specially adapted for foamable substances

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Casting Or Compression Moulding Of Plastics Or The Like (AREA)

Abstract

PURPOSE:To perform excellent foaming of urethane at a desired spot by a simple operation, by joining the conduits of the same diameter and an equal length connected to the pessure vessels into one mixing tube and specifying the ratio of the cross-sectional area of the conduit and that of the mixing tube. CONSTITUTION:The first liquid composed of an isocyanate and Flon and the second liquid composed of a polyol anf Flon are brought under an atmospheric pressure via the conduits 1, 2 from the pressure vessels 5, 5 in which these liquids are respectively contained. A button nozzle 4, 4 is attached at one end of each conduit 1, 2, the conduits 1, 2 of the same diameter and an equal length connected to each pressure vessel 5, 5 are joined into one mixing tube 3 and the ratio of the cross-sectional areas of the conduits 1, 2 and the mixing tube is made 5-100. By the above, it enables to perform urethane foaming at a desired spot by a simple operation and a low cost mixing apparatus.

Description

【発明の詳細な説明】 本発明は2液型工アゾール式つVり/フオーム製造用の
混合装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a mixing apparatus for two-component azole casting/foam production.

エアゾール方式によるウレタンフオームの製造ない。There is no production of urethane foam using the aerosol method.

エアゾール方式による発泡ウレタンの製法には1液法と
2液法があり、1液法においてはイソシアネート樹脂、
界面活性剤、触媒尋を含有するエール容器のノ々ルブを
開放したときに内容物がフロンガスの気化膨張によりウ
レタン発泡を形成し、次いfこの泡が大気中の湿分と反
応して硬化しウレタンフオームが得られる。−万、イソ
7アネートを元成分とするエアゾール原液と噴射剤とし
てのフロン、11をエアゾール容器に入れた第1液と。
There are two methods for manufacturing urethane foam using the aerosol method: a one-part method and a two-part method.In the one-part method, isocyanate resin,
When the nonorubu of the ale container containing surfactant and catalyst fat is opened, the contents form urethane foam due to vaporization expansion of the fluorocarbon gas, and then this foam reacts with moisture in the atmosphere and hardens. A urethane foam is obtained. - 10,000, a first liquid containing an aerosol stock solution containing iso7anate as a main component and CFC 11 as a propellant in an aerosol container.

プロピレングリコール、ホリエテレングリコール。Propylene glycol, polyethylene glycol.

グリセライド等の水産基含有ポリエーテルポリオール、
有機錫化合物、アミン等の触媒、界面活性剤を含有する
エアゾール原液(第2液)とを所望の場所で混合してウ
レタンフオーム・を得る2液法がある。この何れの方法
においてもエアゾール容器の・々ルブを開放した履きに
内容物が噴出して発泡]7ウレタンフオームが形成され
る。2液反応型の場合には、第1液と第2液の噴射物を
/SSジブにより混合装#に導き、該混合装置内で混合
発泡を行わせてウレタンフオームが得られる。
Polyether polyols containing aquatic groups such as glycerides,
There is a two-component method in which a urethane foam is obtained by mixing an aerosol stock solution (second solution) containing an organic tin compound, a catalyst such as an amine, and a surfactant at a desired location. In either of these methods, the contents of the aerosol container are squirted out onto the shoe after the lubricant is opened, forming a foamed urethane foam. In the case of a two-liquid reaction type, the injected materials of the first liquid and the second liquid are introduced into a mixing device by a /SS jib, and mixed and foamed in the mixing device to obtain a urethane foam.

゛ 一般に1液型の漏気硬化反応はエアゾールによって
形成されたイソ7プネート樹脂の泡が空気中の水分によ
り硬化することによつ1行われるものであるが、硬化時
間は空気中の水分や温度によって左右され、硬化に要す
る時間は高温多湿の夏季では平均約12時間であるが、
氷点下の低温がかつ乾燥した冬期には48時間以上かか
ることもある。従って戸外10作業性が劣り実用的に不
満足なものである。これに対して2液型のもの1は殆ん
ど外気の温度や湿度の影響な受けず、硬イヒ時間は3〜
10分程度1充分子あり、発泡倍率も30〜50倍で作
業性も極めて良好〒あるが、イソシアネート樹脂を含有
する第1液とポリエーテルポリオールな含有する第2液
の噴射物が一定割合↑均一に混合されないと所期の硬化
時間が得られないばかりフなく満足なウレタンフオーム
も得られない。大規模な工業的現場発泡において、2液
型;弁≠=詣発発泡よるときには混合により均一な発泡
の得られるような混合装置が設計されている。
゛ In general, the one-component type air leakage curing reaction is carried out by the iso-7 penate resin bubbles formed by an aerosol being cured by moisture in the air, but the curing time depends on the moisture in the air and The curing time depends on the temperature, with an average of about 12 hours in the hot and humid summer months.
In winter, when temperatures are below freezing and dry, it can take more than 48 hours. Therefore, the workability outdoors is poor and is unsatisfactory from a practical standpoint. On the other hand, the two-component type 1 is almost unaffected by outside temperature and humidity, and has a hardening time of 3~
There are 100% foam in about 10 minutes, the expansion ratio is 30 to 50 times, and the workability is very good. However, the injection of the first liquid containing isocyanate resin and the second liquid containing polyether polyol is a certain ratio ↑ If they are not mixed uniformly, the desired curing time will not be obtained, and a satisfactory urethane foam will not be obtained. In large-scale industrial on-site foaming, a two-component mixing device is designed so that uniform foaming can be obtained by mixing when foaming is performed.

現在では混合室の中に螺旋状板な収容したヘリックスミ
キサーが効率、効果に優れていて一般に使用されている
At present, a helix mixer, which has a spiral plate housed in a mixing chamber, is generally used because it is highly efficient and effective.

上記のへリックスミキサ−は優れた性能を有してはいる
、が、エアゾール方式で使用するときは混合装置が使い
捨てとなるの!高価につき、またノンナー等で再使用な
計っても内部の充分な洗浄を行うことができない。
The helix mixer mentioned above has excellent performance, but when used in the aerosol method, the mixing device becomes disposable! It is expensive, and even if it is reused with nonner, etc., the inside cannot be thoroughly cleaned.

本発明は従来のミキサーの上記のような欠点を排除する
ためになされたもの↑あり、操作が簡単fかつ使い捨て
可能f充分に安価な2液型工アゾール式ウレタンフオー
ム混合装置を提供するもの1ある。
The present invention has been made to eliminate the above-mentioned drawbacks of conventional mixers, and provides a two-component azole urethane foam mixing device that is easy to operate, disposable, and sufficiently inexpensive. be.

本発明者等はイソシアネートと噴射剤としてのフロン′
ガスよりなる第1液およびポリオールとフロンガスより
なる第1液となそれぞれ別個の圧力容器に収容し、それ
ぞれの容器から導管を経由して同時に内容物を一つの混
合管の中に噴射して両液を混合するに当り、導管と混合
管の間に特定の関係のあるとき[2液が極めて良好に混
合されて反応し優れたウレタンフオームの得られること
を見出して本発明を完成した。
The present inventors have discovered that isocyanates and fluorocarbons as propellants
A first liquid consisting of gas and a first liquid consisting of polyol and chlorofluorocarbon gas are housed in separate pressure vessels, and the contents are simultaneously injected from each vessel into one mixing tube via a conduit. The present invention was completed by discovering that when there is a specific relationship between the conduit and the mixing tube when mixing the liquids, the two liquids can be mixed and reacted very well and an excellent urethane foam can be obtained.

すなわち、本発明の目的は2液型工アゾール式ウレタン
フオームの製造に当り、各液の収容された圧力容器の出
口弁にそれぞれ一端がゼタン噴口な介して接続するよう
罠なっている同径等長の2本の導管と、この導管の他端
が合流して接続されている混合管とからなり、導管と混
合管の断面積比な5〜100としたことを特徴とする2
液型工アゾール式ウレタンフオーム製造用混合装置によ
つ℃達成される。
That is, the object of the present invention is to manufacture a two-component azole urethane foam, in which two pipes of the same diameter are connected at one end to the outlet valve of a pressure vessel containing each liquid through a zethane spout. It consists of two long conduits and a mixing tube whose other ends meet and are connected, and the cross-sectional area ratio of the conduit to the mixing tube is 5 to 100.
℃ achieved by liquid molding azole type urethane foam manufacturing mixing equipment.

本発明において使用するイソノアネートとフロンよりな
る第1液およびポリオールとフロンよりなる第2液は、
倒れも温度により圧力、噴射速度、液粘度が異なり例え
ば第1表のような値を示す。
The first liquid consisting of isonoanate and fluorocarbons and the second liquid consisting of polyol and fluorocarbons used in the present invention are as follows:
The pressure, injection speed, and liquid viscosity also vary depending on the temperature, and exhibit values as shown in Table 1, for example.

20    70   3.7    95 3.83
0   40   4.6    55 4.7上の第
1表によれば同一の温度1は第1液と第2液は略同程度
の粘度および圧力であり、同時に各圧力容器から取出し
て混合することができることがわかる。
20 70 3.7 95 3.83
0 40 4.6 55 4.7 According to Table 1 above, at the same temperature 1, the first and second liquids have approximately the same viscosity and pressure, and they must be taken out from each pressure vessel and mixed at the same time. It turns out that you can.

本発明によれば第1液および第2液を収容した圧力容器
からそれぞれ導管を弁して内容物を大気圧下にもたらす
とフロンかが・気化して両液は導管中で著しい発泡状態
となり、両導管と混合管の合流点に達し、混合管の中マ
激しい乱流状態で互いに混和され反応してウレタンフオ
ームが連続的に生成する。“ ところで圧力容器内の液は温度が高い程フロンの気化膨
張率は高く、液の粘度は低く、従って内容物の噴射速度
も大となり、混合管における乱流が激しくなって一層充
分な混合・反応が行われるととKなるが、混合管の長さ
の反応に及ぼす影響は第2表の通り〒ある。
According to the present invention, when the conduits from the pressure vessels containing the first liquid and the second liquid are brought to atmospheric pressure by valves, the contents are ignited and vaporized, causing both liquids to form a remarkable foaming state in the conduits. The two conduits reach the confluence of the mixing tube, where they are mixed and reacted with each other in a highly turbulent state in the mixing tube, and urethane foam is continuously produced. “By the way, the higher the temperature of the liquid in the pressure vessel, the higher the vaporization expansion rate of the fluorocarbons and the lower the viscosity of the liquid, so the injection speed of the contents also increases, and the turbulent flow in the mixing tube becomes more intense, resulting in more thorough mixing. When the reaction takes place, it becomes K. The influence of the length of the mixing tube on the reaction is as shown in Table 2.

第   2   表 5      1000      均一5     
 700    不均一 10      500    稍不均−20300均
一 30      200      均−第2表の結沫
から比較的低温(5℃)で作業する場合でも混合管の長
でか1000mmあれげ良好なウレタンフオームの得ら
れることがわかり、常温〒は300mmの長はで充分な
ことがわかる。
2nd Table 5 1000 Uniform 5
700 Uneven 10 500 Slightly Uneven - 20300 Uniform 30 200 Uniform - Good urethane foam can be obtained from the condensation shown in Table 2 even when working at relatively low temperatures (5°C) as long as the mixing tube is 1000 mm long. This shows that a length of 300 mm is sufficient at room temperature.

本発明者等は更に圧力容器から缶液の供給される割合が
両液の反応に及ばず影響を一本の導管径と混合管径との
比を変えることにより検討した。
The inventors of the present invention further investigated the influence of the ratio of the canned liquid supplied from the pressure vessel on the reaction of both liquids by changing the ratio of the diameter of one conduit to the diameter of the mixing tube.

すなわち缶液の温度25℃、圧力4.1 #/cr1.
噴射速度4.59 / secとし、導管はそれぞれ内
径06龍、長さ100關のものを用い、長さ1000m
mの混合管の内径を変えて得られるウレタンフオームの
状態を調べた。その結果を第3表に示す。
That is, the temperature of the can liquid is 25°C, the pressure is 4.1 #/cr1.
The injection speed was 4.59/sec, and each conduit had an inner diameter of 06 mm and a length of 100 mm, and the length was 1000 m.
The state of the urethane foam obtained by changing the inner diameter of the mixing tube was investigated. The results are shown in Table 3.

第   3   表 フオームの形成 0・6     名      が遅い1.4    
  llA        良好2.0      ’
Z        良好3.1      ”A   
     良好3、636名      良好 6.0    1箸       良好7.0    
1当      混合状態不良第3表の結果から、混合
管と一本の導管との断面積比が5〜100″′r!良好
なウレタンフオームの得られることがわかる。
Table 3 Form formation 0.6 people slow 1.4
llA Good 2.0'
Z Good 3.1”A
Good 3, 636 people Good 6.0 1 Chopsticks Good 7.0
From the results in Table 3, it can be seen that a good urethane foam can be obtained with a cross-sectional area ratio of the mixing tube to one conduit of 5 to 100''r!

従って本発明の2液型工アゾール式ウレタンフオーム混
合装置は各圧力容器に接続された同径等長の導管を一本
の混合管に合流接続し、導管の断面積と混合管の断面積
の比を5〜100としたものtあり、この混合装置によ
って現場で極めて簡単な操作により優れたウレタンフオ
ームを所望の箇所に施工するととが1きる。
Therefore, in the two-component azole urethane foam mixing device of the present invention, conduits of the same diameter and length connected to each pressure vessel are connected to a single mixing tube, and the cross-sectional area of the conduit is equal to the cross-sectional area of the mixing tube. There are products with a ratio of 5 to 100, and with this mixing device, it is possible to apply excellent urethane foam to a desired location on-site with extremely simple operations.

本発明1使用する導管および混合管は塩化ビニル樹脂等
1作られた可撓性ナユーブが好ましく、第1図に示した
ように、各導管(1,2)の一端vc13?タン噴口(
4)が取付けてあり、圧力容器(5)への接続が容易に
行えるようになっていて、導管(1,2)と混合管(3
)の接続はヒートノール、接着剤その他の公知の方法に
より行われる。接合部分1は内導管の開口が同一平面内
にあるようにすることにより2液の混合・反応をより完
全にすることが1きるが、二つの導管の開口を少し螺旋
状に配置すると更に混合が充分に行われる。なお。
The conduits and mixing tubes used in the present invention 1 are preferably flexible tubes made of vinyl chloride resin, etc. As shown in FIG. 1, one end of each conduit (1, 2) is VC13? Tongue spout (
4) is attached so that it can be easily connected to the pressure vessel (5), and the conduit pipes (1, 2) and the mixing pipe (3)
) can be connected by heat glue, adhesive or other known methods. In the joint part 1, the openings of the inner conduit can be placed in the same plane to make the mixing and reaction of the two liquids more complete, but if the openings of the two conduits are arranged in a slightly spiral shape, the mixing can be further improved. is carried out sufficiently. In addition.

この混合装置は極めて安価フあシ容易に処分子きるの1
使用後は使い捨て圧することができるの1作業性にも優
れている。
This mixing device is extremely inexpensive and can be easily disposed of.
It also has excellent workability as it can be disposed of after use.

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

第1図は本発明による混合装置を説明するための図1あ
る。 図中符号:1.2・・・導管  3・・・混合管4・・
・ゼタ/噴口 5・・・圧力容器第  1  図 手続補正書 昭和56年 9月々 日 昭和 56年特許願第 113622 号2、発明の名
称 2液型工アゾール式ウレタンフオーム製造用混合装置3
、補正をする者 事件との関係:特許出願人 名称 東京エアゾル化学株式会社 1)明細書第2頁第4行目、「ジエチエーテル」を「ジ
メチルエーテル」と補正する。 2)同 第2頁第9行目、1元成分」を1主成分」と補
正する。 3)同 第2頁第10行目、「フロン11」を[フロン
12.11等の噴射剤−1と補正する。 4)同 第2頁第12行目、「水産基」を「水酸基」と
補正する。 5)同 第2頁第13〜第14行目、「界面活性剤−1
と「を含有する」の間に1、フロン12.11等の噴射
剤」を加入する。 6)同 第3頁第7行目、[低温が−1を「低温t」と
補正する。 7)同 第4頁下から第5行目、「第1液」を「第2液
」と補正する。 8)同 第6頁第6行目、「弁して」を「介して」と補
正する。
FIG. 1 is a diagram for explaining a mixing device according to the present invention. Code in the figure: 1.2...Conduit 3...Mixing pipe 4...
・Zeta/nozzle 5...Pressure vessel No. 1 Drawing procedure amendment September 1982 Patent application No. 113622 2, title of invention 2-component azole mixing device for manufacturing urethane foam 3
, Person making the amendment Relationship to the case: Name of patent applicant: Tokyo Aerosol Chemical Co., Ltd. 1) On page 2, line 4 of the specification, "diethiether" is amended to "dimethyl ether." 2) On page 2, line 9, "one element component" is corrected to "one principal component". 3) On page 2, line 10, "Freon 11" is corrected to [propellant-1 such as Freon 12.11]. 4) On page 2, line 12, "aquatic group" is corrected to "hydroxyl group." 5) Page 2, lines 13-14, “Surfactant-1
and ``contains'', add 1, ``propellant such as fluorocarbon 12.11''. 6) Same page 3, line 7, [low temperature corrects -1 to "low temperature t". 7) On the 5th line from the bottom of page 4, "1st liquid" is corrected to "2nd liquid." 8) On page 6, line 6 of the same, amend "benshite" to "via".

Claims (1)

【特許請求の範囲】[Claims] 各圧力容器の出口弁[&タン噴口を介してそれぞれ一端
を接続可能にした内径および長さの等しい2本の導管と
、これらの導管の他端が合流しで接続され℃いる混合管
とからなり、1本の導管と混合管の断面積比を5〜10
0にしたことを特徴とする2液型工アゾール式ウレタン
フオーム製造用混合装置。
Two conduits of equal inner diameter and length, each with one end connectable via the outlet valve [& tongue nozzle of each pressure vessel], and a mixing tube with the other ends of these conduits connected at a confluence. Therefore, the cross-sectional area ratio of one conduit and mixing tube is 5 to 10.
2. A two-component azole mixing device for producing urethane foam, characterized in that the mixing device has a temperature of 0.
JP56113622A 1981-07-22 1981-07-22 Mixing apparatus of two-pack type aerosol system urethane foam manufacture Granted JPS5816832A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56113622A JPS5816832A (en) 1981-07-22 1981-07-22 Mixing apparatus of two-pack type aerosol system urethane foam manufacture

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56113622A JPS5816832A (en) 1981-07-22 1981-07-22 Mixing apparatus of two-pack type aerosol system urethane foam manufacture

Publications (2)

Publication Number Publication Date
JPS5816832A true JPS5816832A (en) 1983-01-31
JPH0150573B2 JPH0150573B2 (en) 1989-10-30

Family

ID=14616875

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56113622A Granted JPS5816832A (en) 1981-07-22 1981-07-22 Mixing apparatus of two-pack type aerosol system urethane foam manufacture

Country Status (1)

Country Link
JP (1) JPS5816832A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4668097A (en) * 1985-11-01 1987-05-26 Magnetic Peripherals Inc. Epoxy mixing system
US4777906A (en) * 1985-11-01 1988-10-18 Magnetic Peripherals Inc. Epoxy mixing and dispensing system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4668097A (en) * 1985-11-01 1987-05-26 Magnetic Peripherals Inc. Epoxy mixing system
US4777906A (en) * 1985-11-01 1988-10-18 Magnetic Peripherals Inc. Epoxy mixing and dispensing system

Also Published As

Publication number Publication date
JPH0150573B2 (en) 1989-10-30

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