JPS58168674A - Adhesive composition for spraying - Google Patents

Adhesive composition for spraying

Info

Publication number
JPS58168674A
JPS58168674A JP5289082A JP5289082A JPS58168674A JP S58168674 A JPS58168674 A JP S58168674A JP 5289082 A JP5289082 A JP 5289082A JP 5289082 A JP5289082 A JP 5289082A JP S58168674 A JPS58168674 A JP S58168674A
Authority
JP
Japan
Prior art keywords
cyanoacrylate
adhesive
acid gas
carbonic acid
filled
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
JP5289082A
Other languages
Japanese (ja)
Other versions
JPH0235792B2 (en
Inventor
Masayuki Taniguchi
正幸 谷口
Tomohiko Sada
佐田 友彦
Tetsuya Kimijima
哲也 君島
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.)
Japan Oxygen Co Ltd
Nippon Sanso Corp
Original Assignee
Japan Oxygen Co Ltd
Nippon Sanso Corp
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 Japan Oxygen Co Ltd, Nippon Sanso Corp filed Critical Japan Oxygen Co Ltd
Priority to JP5289082A priority Critical patent/JPH0235792B2/en
Publication of JPS58168674A publication Critical patent/JPS58168674A/en
Publication of JPH0235792B2 publication Critical patent/JPH0235792B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Nozzles (AREA)

Abstract

PURPOSE:To provide the titled adhesive compsn. which can be applied evenly and quickly over the surface of adherend, prepared by dissolving alpha-cyanoacrylate type adhesive in liquefied carbonic acid gas and storing the solution under pressure. CONSTITUTION:alpha-Cyanoacrylate is filled in a pressure container in an amount to obtain a desired blend ratio. Then liquefied carbonic acid gas is filled in it in an amount required for obtaining a predetermined blend ratio until a pressure corresponding to the blend ratio necessary for maintenance of a liquid state, is reached. Thus the container is filled with alpha-cyanoacrylate and liquefied carbonic acid gas which remains in a liquid state even at normal temperature. As the filled container is shaken, alpha-cyanoacrylate is diffused in liquefied carbonic acid gas and is dissolved homogeneously to form an adhesive compsn. for spraying with a desired blend ratio. The carbonic acid gas is incombustible, does no environmental harm, has no danger of fire and explosion and is safe as solvent for spray type adhesive.

Description

【発明の詳細な説明】 本発明は被着体表wK均一、かつ迅速Km増することを
可能とし九噴−用α−シアノアタリレート系接着剤組成
物に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an α-cyanoarylate adhesive composition for nine injections, which enables a uniform increase in wK and rapid increase in Km on the surface of an adherend.

α−シアノアタリレート系接着剤は、加熱、加圧、触媒
などを必要とせず、大気中に含まれゐ微量の水分あるい
は被着材周辺の微量O水分によって、速やかにア二オ/
−合し、数秒ないし数分の短時間で急速に#!化する丸
め、すぐれ九−間接層性を有し、瞬間接着剤として産業
界に広く使用されている。たとえばゴム、プラスチック
ス、金属。
α-Cyanoarylate adhesives do not require heating, pressure, catalysts, etc., and can be quickly anionized/adhesive by a trace amount of moisture contained in the atmosphere or a trace amount of O moisture around the adherend.
- rapidly #! in a short period of seconds or minutes! It has excellent rounding and indirect layering properties, and is widely used in industry as an instant adhesive. For example, rubber, plastics, and metals.

セランツクス、繊維、皮革などほとんどの材料を接着さ
せることができるので、電気器具0機械の製造から外科
手術における皮膚の接着に至るまで利用されている。と
ころがα−シアノアクリレート系接着剤は上記した通り
、硬化速度が極めて適い丸め、広い面を接着する場合薄
く且つ均一に塗布する事が困−である。このことから広
い藺を接着する場合は、通常その面上の適轟な個WtK
シア □ノアクリレート系接着剤の適当量を滴下して液
滴とし九後に貼り合せる方法によるが、塗布むらKよる
不完全接着が生じ鳥〈これをさける丸め必要以上の量を
使用することとtb、接着面を汚すばかりでなく無駄な
使用となって不経済となる不都合があつ九。
Since it can bond most materials such as ceramics, textiles, and leather, it is used in everything from the manufacture of electrical appliances and machines to the bonding of skin in surgical operations. However, as mentioned above, the α-cyanoacrylate adhesive has an extremely suitable curing speed, but it is difficult to apply it thinly and uniformly when bonding a wide surface. For this reason, when gluing a wide area, it is usually necessary to
Shear □It is a method of dropping an appropriate amount of noacrylate adhesive to make droplets and then bonding them together, but incomplete adhesion may occur due to uneven application. This has the disadvantage of not only staining the adhesive surface but also wasteful use and being uneconomical.

このようなことがらα−シアノアタリレートを有機溶剤
に溶解せしめ、これを圧縮空気の如自圧力源ヲ用いてス
プレーガンによって接着面に噴−し九り、又α−シアノ
アクリレートをフロン(8−11,R−1り等のプロペ
ラントに滉合しエアゾル化して噴−使用する方法が提案
されてお勤、広い面でもα−シアノアクリレート系接着
剤をむらなく均一に塗布することを試みている。
To solve this problem, α-cyanoacrylate is dissolved in an organic solvent, and this is sprayed onto the adhesive surface using a spray gun using a pressure source such as compressed air. A method has been proposed in which the adhesive is mixed with a propellant such as -11 and R-1 to form an aerosol and sprayed, and an attempt was made to apply α-cyanoacrylate adhesive evenly and evenly to a large surface. ing.

しかしながら上述の如き噴霧する方法のうち有機溶剤に
α−シアノアクリレートを溶解する方法では、使用する
有機溶剤が(支)相溶性の喪いこと、(P)安定性があ
ること、f→接着効果を妨げる白化現象を生じないこと
、に)揮発性を有すること、(ホ)毒性の少ないもの、
(へ)安価であること等の条件をもとにして選ばれてい
て、その好壇しい溶剤としてメチルイソブチルケント、
酢酸n−ブチル、トリクロルエチレン、四tJI化エタ
ン、ペンタクロルエタン等が提案されている。セしてこ
れら0m鋼は、前記(イ)〜(へ)の条件にもとづいて
選ばれてはいるが、以下のような欠点を有する。即ち (1)毒性が少ないが無毒ではないので、噴射に!!&
って人体に有害でToシ周囲の積項を汚染するお七れが
あること、 (i+)  上記溶剤は揮発性が要求されるえめ引火性
を伴うので火災、爆発等の危険があること、     
、01D  上記有機溶剤はゴム、プラスチックを溶融
して侵蝕するので、該種材料の接着には使用し得ないこ
と、 (ψ 噴霧するために圧縮ガスを必要とするので、附属
装置が必要である−こと。
However, among the above-mentioned spraying methods, in the method of dissolving α-cyanoacrylate in an organic solvent, the organic solvent used must (support) lack of compatibility, (P) be stable, and f→adhesive effect. (2) have volatility; (e) have low toxicity;
(f) Methyl isobutyl kent was selected based on conditions such as being inexpensive, and a suitable solvent is methyl isobutyl kent.
n-Butyl acetate, trichloroethylene, tetratJI ethane, pentachloroethane, etc. have been proposed. Although these 0m steels were selected based on the conditions (a) to (f) above, they have the following drawbacks. In other words, (1) It is less toxic but not non-toxic, so use it as an injection! ! &
(i+) The above solvent is required to be volatile and is flammable, so there is a risk of fire, explosion, etc.
, 01D The above organic solvent melts and corrodes rubber and plastic, so it cannot be used to bond such materials. (ψ Compressed gas is required for spraying, so an attached device is required. -Things.

M 圧縮ガスによる噴霧では、溶剤OS子が粗く必要以
上のα−シアノアクリレートが吐出され、特に薄い塗布
に用いることは1離であること、等の多くの不都合があ
る。
M Spraying with compressed gas has many disadvantages, such as the fact that the solvent particles are coarse and more α-cyanoacrylate than necessary is discharged, and that it is particularly difficult to use for thin coatings.

又一方フロン(R−11、R−12)等のプロペラント
と混合してエアゾール状態で噴11使用する方法では以
下のような不都合がある。即ちフロン(R−11,R−
12)は高価であるばかやでなく、常温で液体状態にあ
る圧力が数11/jli度である丸め、噴−される霧滴
粒子が粗く、この結果塗布に当って不均一に′&つ九抄
又過剰な塗布をも友らすこととなる。そして更に7Wン
の過111!使用は、人体の皮膚へ悪い影響を4九らす
等の不都合がある。
On the other hand, the method of using the spray 11 in an aerosol state by mixing it with a propellant such as Freon (R-11, R-12) has the following disadvantages. That is, Freon (R-11, R-
12) is not expensive, it is rounded and the pressure in the liquid state at room temperature is several 11/jli degrees. It also prevents excessive application. And 111 more 7W! Its use has disadvantages such as having a negative effect on human skin.

本発明は上述の如11現状鴨鑑み、上記不都合を解消す
べく種々考究し九処液化炭酸ガスがα−シアノアクリレ
ートを極めて嵐好に溶解することを見出し、この新しい
知見にもとづきなされえもので、常温下で液体状態を保
持し得るように加圧状態の液化炭酸ガスに所望の濃度で
α−シアノアクリレートを溶解せしめて耐圧容器に貯蔵
したことを特徴とする噴霧用接着剤組成物である。液化
炭酸ガスは一般に常温九とえば6C−25Cでは4Q 
Kl/ajab 〜66 KII/sl ILbの圧力
下で液状態を保持されている無色、無臭の液体でTo砂
、これを大気圧に膨張して噴射すると極めて微粒の粉雪
状となる。そして更に粉雪状の炭酸ガスは常温下で液化
することなく直ちに気化する昇華現象によ〉炭酸ガスと
して逸散し、しかも炭酸ガス杜毒性がなく、不燃性であ
ることが良く知られていて、環境衛生上においても無害
であると共に火災および爆発等の危険性もなく安全であ
る。
The present invention has been made based on the above-mentioned current situation, conducted various studies to solve the above-mentioned disadvantages, and found that liquefied carbon dioxide dissolves α-cyanoacrylate extremely well, and based on this new knowledge. , an adhesive composition for spraying, characterized in that α-cyanoacrylate is dissolved in pressurized liquefied carbon dioxide at a desired concentration so as to maintain a liquid state at room temperature and stored in a pressure-resistant container. . Liquefied carbon dioxide is generally 4Q at room temperature 9, for example 6C-25C.
To sand is a colorless, odorless liquid that is maintained in a liquid state under pressures of Kl/ajab to 66 KII/sl ILb.When this is expanded to atmospheric pressure and injected, it becomes extremely fine powdery snow. Furthermore, it is well known that powdery carbon dioxide gas is not liquefied at room temperature but is immediately vaporized by the sublimation phenomenon, dissipating as carbon dioxide gas, and is non-toxic and non-flammable. In terms of environmental hygiene, it is harmless and safe, with no risk of fire or explosion.

このようなことから本発明者等は上記し丸液化炭酸ガス
に接着剤であるα−シアノアクリレートを溶解せしめ死
処、これらの間では極めて、相溶性が大であることを見
出しえ、即ち図はZSCの温度下で液化炭酸ガスにα−
シアノアクリレートを種々の温合割合(重量−)で連層
ぜしめ九処のその温合液の圧力(−/−ゲージ)を示し
九4のである0図で明らかなように液化炭酸ガス72重
量嘩重量−シアノアクリレート116重量−でO温合比
率で、これ等が液状態を保つには62−/−ゲージ、又
液化庚酸ガス60重量慢、α−シアノアクリレート40
重量−では60−/−ゲージとなり、以下α−シアノア
クリレートの温合比率が増してくるとその圧力は漸次減
少してゆくことがわかる。
Based on this, the present inventors dissolved α-cyanoacrylate, an adhesive, in the liquefied carbon dioxide gas mentioned above, and found that the compatibility between them was extremely high. is α- to liquefied carbon dioxide under the ZSC temperature.
Cyanoacrylate is layered at various heating ratios (weight -) and the pressure (-/- gauge) of the heated solution is shown in Figure 94. The weight of the cyanoacrylate is 116% by weight, and the O temperature ratio is 62-/- gauge to keep these in a liquid state, and the liquefied acid gas is 60% heavy, and the α-cyanoacrylate is 40%.
The weight was 60-/- gauge, and it can be seen that as the heating ratio of α-cyanoacrylate increases, the pressure gradually decreases.

上述の如き液化炭酸ガスにα−シアノアクリレートを所
望の混合比率で溶解せしめ九接着剤は次のようにして製
造し得る。まづ耐圧性容器(ボ/べ)に所望する温合比
率にするに必要な重量のα−シアノアクリレートを注入
して充填し先後、ついで液化炭酸ガスを前記所望の混合
比率に応じ九重量を容器に前記吻a輯【示し九液状を保
持する丸め温合比率に相通する圧力になる迄充填する。
The adhesive can be produced as follows by dissolving α-cyanoacrylate in the above-mentioned liquefied carbon dioxide gas at a desired mixing ratio. First, the weight of α-cyanoacrylate required to achieve the desired heating ratio is injected into a pressure-resistant container (BO/B), and then 9 weight of liquefied carbon dioxide is added according to the desired mixing ratio. Fill the container until the pressure reaches the temperature corresponding to the rounding heating ratio that maintains the liquid state.

    。    .

この結果容器にはα−シアノアクリレートに1常温でも
液状を保持し九液化炭酸ガスが充填され九こととなるが
、ついでこれらが充I11され九容器を振盪すると、α
−シアノアタリレートは液化炭酸ガス中に拡散し、均一
に#IN4シて所望Os合比率の噴霧用接着剤が得られ
る。
As a result, the container is filled with α-cyanoacrylate and liquefied carbon dioxide gas, which remains liquid even at room temperature.Next, when these are filled with α-cyanoacrylate and the container is shaken, α
- The cyanoarylate is diffused into the liquefied carbon dioxide gas, uniformly sprayed with #IN4, and a spray adhesive having a desired Os ratio can be obtained.

上記しえように所望の温合比率に濠化嶽酸ガスにα−シ
アノアクリレ−Fを溶解せしめて所定の圧力で耐圧容器
に充填し九本発明の接着鋼は耐圧溶器の充填口にスプレ
ーガ/を連結して噴射し、接着すぺ1被接着物に噴−す
る、この時スプレーガンを介して、極微粒子O肴雷状の
ドライアイスに同伴してα−シアノアクリレートの接着
剤が粒径1〜数声の粒子として噴出されるが、着雪状O
ドライアイスは直ちに昇華して、同伴され九α−シアノ
アクリレートのみ被接着面に残置される。
As described above, alpha-cyanoacrylate-F is dissolved in moated sulfuric acid gas at the desired heating ratio and filled into a pressure vessel at a predetermined pressure. / is connected and sprayed onto the adhered object. At this time, the α-cyanoacrylate adhesive is granulated through the spray gun, accompanied by ultrafine particles and lightning-shaped dry ice. Although it is ejected as particles with a diameter of 1 to several times, it is snow-like.
The dry ice immediately sublimes and is entrained, leaving only the nine-α-cyanoacrylate on the surface to be adhered.

しか4h聯雷状のドライアイスの噴−で、鋏ドライアイ
スの粉雪粒子I!1面に凝結される大気中の水分カ前記
α−シアノアクリレートと共に残置されるので、α−シ
アノアクリレートの接着効果を助長する作用をする。
However, 4 hours of thunder-shaped dry ice jets caused powdery snow particles of scissors dry ice! Since the atmospheric moisture condensed on one surface remains together with the α-cyanoacrylate, it acts to promote the adhesive effect of α-cyanoacrylate.

次に液化炭酸ガスK11ll解し九α−シアノアクリレ
ートの貯蔵について経時と共にその接着効果への影響を
試験し死処、九とえば液化炭酸ガスs5重量%、α−シ
アノアクリレート45重量慢の組成比率をもち、圧力5
0jCt/cdで充填し九本発明の接着剤は6ケ月後の
経時でもゲル化はなくその接着効果への影響は全く認め
られなかつ九。更にα−シアノアクリレートの長期保存
においては長期間の間に重合が如まり、ゲル化して粘度
が上昇し、ついKは硬化する性質があるため、従来アニ
オン重合防止剤として80.、HF、NOなどの酸性ガ
スや、P−トルエンスルホン酸、メタンスルホン酸が使
用されているが、本発明のlI着剤組成物で社、上記ア
ニオン藁合防止鋼を添加することなく、6ケ月間を経九
後もα−シアノアクリレートは重合して、ゲル化するこ
とがなく長期間にゎ九って安定化していえ。
Next, we tested the effect on the adhesion effect over time by dissolving liquefied carbon dioxide gas K11ll and storing nine α-cyanoacrylates. with a pressure of 5
The adhesive of the present invention, filled with 0jCt/cd, did not gel even after 6 months, and no influence on the adhesive effect was observed at all. Furthermore, during long-term storage of α-cyanoacrylate, polymerization occurs over a long period of time, resulting in gelation and an increase in viscosity, and K has the property of hardening. , HF, NO, and other acid gases, P-toluenesulfonic acid, methanesulfonic acid, etc., but the lI adhesive composition of the present invention can be used without adding the above-mentioned anionic anti-coagulation steel. Even after several months, α-cyanoacrylate polymerizes and remains stable for a long period of time without gelling.

次に本発明の接着剤組成物の実施例を示す。Next, examples of the adhesive composition of the present invention will be shown.

小容量の耐圧容器(内容積s ow*t) 6cα−シ
アノアクリレート系接着剤20gを充填し友後、液化炭
酸ガスsogを25 Ct)111度下で約60に4/
−の圧力で充填しえ、ついで、この充填し九耐圧容器を
振盪して液化炭酸ガスへのα−シアノアクリレ−)0均
一な溶解を促進せしめ友。この耐圧容器の充填口にスプ
レーガンを連結して22o×207−角07 k i 
[K S OamOI!−を隔てて噴−し、5μの膜厚
で塗布して同様のアル電板を接着した。
A small-capacity pressure-resistant container (inner volume so*t) was filled with 20 g of 6cα-cyanoacrylate adhesive and heated to 25 Ct of liquefied carbon dioxide gas at 111 degrees Celsius to approximately 60 to 4/4
The filled pressure vessel was then shaken to promote uniform dissolution of α-cyanoacrylate into the liquefied carbon dioxide gas. Connect a spray gun to the filling port of this pressure-resistant container and make a 22o x 207-square 07k i
[KS OamOI! A similar aluminum plate was bonded by spraying the solution at a distance of - and applying it to a film thickness of 5 μm.

この時塗布し良膜厚は極めて均一になされており、又白
化現象は全く寵められなかっ九、そして装着後の引張抄
せん断秦着強さをJI8−に41・61にもとづき試験
し九結果160麺f/−であった。又セットタイムは1
5秒であり、従来のα−シアノアクリレート系接着剤の
性能と比較して遜色がなかつ丸、そして更に6ケ月経過
後、再びスプレーガンにより耐圧容器より本発明の接着
剤組成物を噴霧して試験した処、前回と全く同様の試験
結果が得られ、しかも保有中に重合によるゲル化は全く
認められなかった。
At this time, the coating thickness was extremely uniform, and there was no whitening phenomenon at all.After installation, the tensile paper shear adhesion strength was tested based on JI8-41/61, and the results were as follows. It was 160 noodles f/-. Also, the set time is 1
The adhesive composition of the present invention was sprayed again from a pressure container with a spray gun after 6 months had passed, and the performance was comparable to that of conventional α-cyanoacrylate adhesives. When tested, the test results were exactly the same as the previous test, and no gelation due to polymerization was observed during storage.

□□ヮよ。よ50.、□ア□。、  “化嶽酸ガスを溶
剤KL、かりこれをイ、ロベラントとして使用している
ので、次のような多くの利点が生づる。翰壕づ液化炭酸
ガスは大気圧への膨張噴出によ砂極めて微粒′&肴雷が
生じるので、これに同伴して極めて薄い膜厚でも均一に
塗布することが可能とな勤接着剤としてのみでなくコー
ティング剤としての使用も可能となる。(ロ)そして本
発明では従乗O如くプロペラントとして圧縮ガスを使用
しているのとは異なり液化炭酸ガスにα−シアノアクリ
レートを溶解し、液状態の組成物を加圧保持し、この圧
力によ勤噴射せしめるので使用によって充填物の圧力や
組成麦勅はなく、常に一8圧力を保持して噴射され、か
つ同一組成のα−シアノアクリレートが噴−されるので
塗布ムラが生じない、す)又液化炭酸ガスへの溶解によ
シα−シアノアクリレートは長期間の保存に充分耐え、
かつ重合防止の友めの安定剤の使用もすることがないの
で、従来の如自安定剤の使用による着色。
□□ヮyo. Yo50. , □A□. ``Since sulfuric acid gas is used as the solvent KL, it has many advantages such as: Since extremely fine particles and grains are generated, it can be used not only as an adhesive, but also as a coating agent, which can be uniformly applied even with an extremely thin film thickness. (b) And In the present invention, unlike the quadratic O which uses compressed gas as a propellant, α-cyanoacrylate is dissolved in liquefied carbon dioxide gas, the liquid composition is kept under pressure, and this pressure is used to effectively inject Therefore, the pressure and composition of the filler do not change depending on the use, and the spray is always maintained at a pressure of 18%, and α-cyanoacrylate of the same composition is sprayed, so uneven coating does not occur. By dissolving in carbon dioxide, α-cyanoacrylate can withstand long-term storage.
In addition, since there is no need to use stabilizers to prevent polymerization, coloring is achieved by using conventional stabilizers.

接着強度の低下等の不都合も生じない。@)更に無毒、
不燃性である液化炭酸ガスの使用によって保安、環境、
衛生上においても、従来の有機接剤やフロンを使用し九
鍍種接着剤より極めて安全であり、(θ)その上ゴム、
プラスチック等の接着においても、これらを侵蝕するこ
とがないので効果的に使用し得る等産業上極めて効果的
な接着剤を提供し得るものである。
Inconveniences such as a decrease in adhesive strength do not occur. @) Even more non-toxic,
The use of nonflammable liquefied carbon dioxide improves safety, the environment, and
Hygiene-wise, it is much safer than conventional organic adhesives or fluorocarbon-based adhesives, and (θ) rubber,
The present invention can provide an industrially extremely effective adhesive that can be effectively used for adhering plastics and the like because it does not corrode them.

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

図はα−シアノアクリレートを炭酸ガスKfi合し死時
の組成と圧力を示す図である。
The figure shows the composition and pressure at the time of death when α-cyanoacrylate is combined with carbon dioxide gas Kfi.

Claims (1)

【特許請求の範囲】[Claims] 16  α−シアノアクリレート系接着剤を液化炭酸ガ
スに漕解し液状を保持するよう加圧状態で保存貯蔵して
なることを臀黴とする噴−用接着剤組成物。
16. An adhesive composition for spraying, which is prepared by dissolving an α-cyanoacrylate adhesive into liquefied carbon dioxide gas and storing it under pressure to maintain its liquid state.
JP5289082A 1982-03-31 1982-03-31 FUNMUYOSETSUCHAKUZAISOSEIBUTSU Expired - Lifetime JPH0235792B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5289082A JPH0235792B2 (en) 1982-03-31 1982-03-31 FUNMUYOSETSUCHAKUZAISOSEIBUTSU

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5289082A JPH0235792B2 (en) 1982-03-31 1982-03-31 FUNMUYOSETSUCHAKUZAISOSEIBUTSU

Publications (2)

Publication Number Publication Date
JPS58168674A true JPS58168674A (en) 1983-10-05
JPH0235792B2 JPH0235792B2 (en) 1990-08-13

Family

ID=12927454

Family Applications (1)

Application Number Title Priority Date Filing Date
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Country Status (1)

Country Link
JP (1) JPH0235792B2 (en)

Cited By (18)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4923720A (en) * 1987-12-21 1990-05-08 Union Carbide Chemicals And Plastics Company Inc. Supercritical fluids as diluents in liquid spray application of coatings
US5009367A (en) * 1989-03-22 1991-04-23 Union Carbide Chemicals And Plastics Technology Corporation Methods and apparatus for obtaining wider sprays when spraying liquids by airless techniques
US5057342A (en) * 1987-12-21 1991-10-15 Union Carbide Chemicals And Plastics Technology Corporation Methods and apparatus for obtaining a feathered spray when spraying liquids by airless techniques
US5066522A (en) * 1988-07-14 1991-11-19 Union Carbide Chemicals And Plastics Technology Corporation Supercritical fluids as diluents in liquid spray applications of adhesives
US5106650A (en) * 1988-07-14 1992-04-21 Union Carbide Chemicals & Plastics Technology Corporation Electrostatic liquid spray application of coating with supercritical fluids as diluents and spraying from an orifice
US5105843A (en) * 1991-03-28 1992-04-21 Union Carbide Chemicals & Plastics Technology Corporation Isocentric low turbulence injector
US5108799A (en) * 1988-07-14 1992-04-28 Union Carbide Chemicals & Plastics Technology Corporation Liquid spray application of coatings with supercritical fluids as diluents and spraying from an orifice
US5141156A (en) * 1987-12-21 1992-08-25 Union Carbide Chemicals & Plastics Technology Corporation Methods and apparatus for obtaining a feathered spray when spraying liquids by airless techniques
US5171613A (en) * 1990-09-21 1992-12-15 Union Carbide Chemicals & Plastics Technology Corporation Apparatus and methods for application of coatings with supercritical fluids as diluents by spraying from an orifice
US5170727A (en) * 1991-03-29 1992-12-15 Union Carbide Chemicals & Plastics Technology Corporation Supercritical fluids as diluents in combustion of liquid fuels and waste materials
US5178325A (en) * 1991-06-25 1993-01-12 Union Carbide Chemicals & Plastics Technology Corporation Apparatus and methods for application of coatings with compressible fluids as diluent by spraying from an orifice
US5203843A (en) * 1988-07-14 1993-04-20 Union Carbide Chemicals & Plastics Technology Corporation Liquid spray application of coatings with supercritical fluids as diluents and spraying from an orifice
US5212229A (en) * 1991-03-28 1993-05-18 Union Carbide Chemicals & Plastics Technology Corporation Monodispersed acrylic polymers in supercritical, near supercritical and subcritical fluids
US5306350A (en) * 1990-12-21 1994-04-26 Union Carbide Chemicals & Plastics Technology Corporation Methods for cleaning apparatus using compressed fluids
US5374305A (en) * 1989-03-22 1994-12-20 Union Carbide Chemicals & Plastics Technology Corporation Precursor coating compositions containing water and an organic coupling solvent suitable for spraying with supercritical fluids as diluents
US5387619A (en) * 1991-03-27 1995-02-07 Union Carbide Chemicals & Plastics Technology Corporation Chemical reaction suppression system
US5509959A (en) * 1989-03-22 1996-04-23 Union Carbide Chemicals & Plastics Technology Corporation Precursor coating compositions suitable for spraying with supercritical fluids as diluents
US6221435B1 (en) 1998-11-18 2001-04-24 Union Carbide Chemicals & Plastics Technology Corporation Method for the spray application of polymeric-containing liquid coating compositions using subcritical compressed fluids under choked flow spraying conditions

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4923720A (en) * 1987-12-21 1990-05-08 Union Carbide Chemicals And Plastics Company Inc. Supercritical fluids as diluents in liquid spray application of coatings
US5027742A (en) * 1987-12-21 1991-07-02 Union Carbide Chemicals And Plastics Technology Corporation Supercritical fluids as diluents in liquid spray application of coatings
US5057342A (en) * 1987-12-21 1991-10-15 Union Carbide Chemicals And Plastics Technology Corporation Methods and apparatus for obtaining a feathered spray when spraying liquids by airless techniques
US5141156A (en) * 1987-12-21 1992-08-25 Union Carbide Chemicals & Plastics Technology Corporation Methods and apparatus for obtaining a feathered spray when spraying liquids by airless techniques
US5203843A (en) * 1988-07-14 1993-04-20 Union Carbide Chemicals & Plastics Technology Corporation Liquid spray application of coatings with supercritical fluids as diluents and spraying from an orifice
US5066522A (en) * 1988-07-14 1991-11-19 Union Carbide Chemicals And Plastics Technology Corporation Supercritical fluids as diluents in liquid spray applications of adhesives
US5106650A (en) * 1988-07-14 1992-04-21 Union Carbide Chemicals & Plastics Technology Corporation Electrostatic liquid spray application of coating with supercritical fluids as diluents and spraying from an orifice
US5211342A (en) * 1988-07-14 1993-05-18 Union Carbide Chemicals & Plastics Technology Corporation Electrostatic liquid spray application of coatings with supercritical fluids as diluents and spraying from an orifice
US5108799A (en) * 1988-07-14 1992-04-28 Union Carbide Chemicals & Plastics Technology Corporation Liquid spray application of coatings with supercritical fluids as diluents and spraying from an orifice
US5509959A (en) * 1989-03-22 1996-04-23 Union Carbide Chemicals & Plastics Technology Corporation Precursor coating compositions suitable for spraying with supercritical fluids as diluents
US5374305A (en) * 1989-03-22 1994-12-20 Union Carbide Chemicals & Plastics Technology Corporation Precursor coating compositions containing water and an organic coupling solvent suitable for spraying with supercritical fluids as diluents
US5009367A (en) * 1989-03-22 1991-04-23 Union Carbide Chemicals And Plastics Technology Corporation Methods and apparatus for obtaining wider sprays when spraying liquids by airless techniques
US5171613A (en) * 1990-09-21 1992-12-15 Union Carbide Chemicals & Plastics Technology Corporation Apparatus and methods for application of coatings with supercritical fluids as diluents by spraying from an orifice
US5306350A (en) * 1990-12-21 1994-04-26 Union Carbide Chemicals & Plastics Technology Corporation Methods for cleaning apparatus using compressed fluids
US5387619A (en) * 1991-03-27 1995-02-07 Union Carbide Chemicals & Plastics Technology Corporation Chemical reaction suppression system
US5212229A (en) * 1991-03-28 1993-05-18 Union Carbide Chemicals & Plastics Technology Corporation Monodispersed acrylic polymers in supercritical, near supercritical and subcritical fluids
US5105843A (en) * 1991-03-28 1992-04-21 Union Carbide Chemicals & Plastics Technology Corporation Isocentric low turbulence injector
US5170727A (en) * 1991-03-29 1992-12-15 Union Carbide Chemicals & Plastics Technology Corporation Supercritical fluids as diluents in combustion of liquid fuels and waste materials
US5178325A (en) * 1991-06-25 1993-01-12 Union Carbide Chemicals & Plastics Technology Corporation Apparatus and methods for application of coatings with compressible fluids as diluent by spraying from an orifice
US6221435B1 (en) 1998-11-18 2001-04-24 Union Carbide Chemicals & Plastics Technology Corporation Method for the spray application of polymeric-containing liquid coating compositions using subcritical compressed fluids under choked flow spraying conditions

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