JPS6231989B2 - - Google Patents
Info
- Publication number
- JPS6231989B2 JPS6231989B2 JP19993183A JP19993183A JPS6231989B2 JP S6231989 B2 JPS6231989 B2 JP S6231989B2 JP 19993183 A JP19993183 A JP 19993183A JP 19993183 A JP19993183 A JP 19993183A JP S6231989 B2 JPS6231989 B2 JP S6231989B2
- Authority
- JP
- Japan
- Prior art keywords
- curing
- amine
- curing chamber
- coating film
- coating
- 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.)
- Expired
Links
- 238000000576 coating method Methods 0.000 claims description 51
- 239000011248 coating agent Substances 0.000 claims description 47
- 150000001412 amines Chemical class 0.000 claims description 44
- 230000007246 mechanism Effects 0.000 claims description 16
- IQPQWNKOIGAROB-UHFFFAOYSA-N isocyanate group Chemical group [N-]=C=O IQPQWNKOIGAROB-UHFFFAOYSA-N 0.000 claims description 10
- 238000001723 curing Methods 0.000 description 72
- 239000003973 paint Substances 0.000 description 19
- 239000007789 gas Substances 0.000 description 14
- 238000011417 postcuring Methods 0.000 description 13
- 239000000758 substrate Substances 0.000 description 12
- 238000000034 method Methods 0.000 description 10
- 238000010422 painting Methods 0.000 description 8
- 239000007921 spray Substances 0.000 description 8
- 238000005192 partition Methods 0.000 description 5
- 238000007789 sealing Methods 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- 239000003795 chemical substances by application Substances 0.000 description 4
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 3
- 229920001228 polyisocyanate Polymers 0.000 description 3
- 239000005056 polyisocyanate Substances 0.000 description 3
- 229920000642 polymer Polymers 0.000 description 3
- 229920005989 resin Polymers 0.000 description 3
- 239000011347 resin Substances 0.000 description 3
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- QUSNBJAOOMFDIB-UHFFFAOYSA-N Ethylamine Chemical compound CCN QUSNBJAOOMFDIB-UHFFFAOYSA-N 0.000 description 2
- BAVYZALUXZFZLV-UHFFFAOYSA-N Methylamine Chemical compound NC BAVYZALUXZFZLV-UHFFFAOYSA-N 0.000 description 2
- YNAVUWVOSKDBBP-UHFFFAOYSA-N Morpholine Chemical compound C1COCCN1 YNAVUWVOSKDBBP-UHFFFAOYSA-N 0.000 description 2
- GLUUGHFHXGJENI-UHFFFAOYSA-N Piperazine Chemical compound C1CNCCN1 GLUUGHFHXGJENI-UHFFFAOYSA-N 0.000 description 2
- NQRYJNQNLNOLGT-UHFFFAOYSA-N Piperidine Chemical compound C1CCNCC1 NQRYJNQNLNOLGT-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 239000012298 atmosphere Substances 0.000 description 2
- PAFZNILMFXTMIY-UHFFFAOYSA-N cyclohexylamine Chemical compound NC1CCCCC1 PAFZNILMFXTMIY-UHFFFAOYSA-N 0.000 description 2
- 238000001514 detection method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- 239000012948 isocyanate Substances 0.000 description 2
- 150000002513 isocyanates Chemical group 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000012071 phase Substances 0.000 description 2
- WGYKZJWCGVVSQN-UHFFFAOYSA-N propylamine Chemical compound CCCN WGYKZJWCGVVSQN-UHFFFAOYSA-N 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 238000005507 spraying Methods 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 230000007723 transport mechanism Effects 0.000 description 2
- UPMLOUAZCHDJJD-UHFFFAOYSA-N 4,4'-Diphenylmethane Diisocyanate Chemical compound C1=CC(N=C=O)=CC=C1CC1=CC=C(N=C=O)C=C1 UPMLOUAZCHDJJD-UHFFFAOYSA-N 0.000 description 1
- 239000004925 Acrylic resin Substances 0.000 description 1
- 229920000178 Acrylic resin Polymers 0.000 description 1
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 1
- 239000005057 Hexamethylene diisocyanate Substances 0.000 description 1
- KWYHDKDOAIKMQN-UHFFFAOYSA-N N,N,N',N'-tetramethylethylenediamine Chemical compound CN(C)CCN(C)C KWYHDKDOAIKMQN-UHFFFAOYSA-N 0.000 description 1
- OMRDSWJXRLDPBB-UHFFFAOYSA-N N=C=O.N=C=O.C1CCCCC1 Chemical compound N=C=O.N=C=O.C1CCCCC1 OMRDSWJXRLDPBB-UHFFFAOYSA-N 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000004721 Polyphenylene oxide Substances 0.000 description 1
- GSEJCLTVZPLZKY-UHFFFAOYSA-N Triethanolamine Chemical compound OCCN(CCO)CCO GSEJCLTVZPLZKY-UHFFFAOYSA-N 0.000 description 1
- 238000007605 air drying Methods 0.000 description 1
- 229920000180 alkyd Polymers 0.000 description 1
- 238000000889 atomisation Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000004202 carbamide Substances 0.000 description 1
- 239000012159 carrier gas Substances 0.000 description 1
- 238000005266 casting Methods 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- ZBCBWPMODOFKDW-UHFFFAOYSA-N diethanolamine Chemical compound OCCNCCO ZBCBWPMODOFKDW-UHFFFAOYSA-N 0.000 description 1
- HPNMFZURTQLUMO-UHFFFAOYSA-N diethylamine Chemical compound CCNCC HPNMFZURTQLUMO-UHFFFAOYSA-N 0.000 description 1
- 238000003618 dip coating Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 210000004905 finger nail Anatomy 0.000 description 1
- 239000007792 gaseous phase Substances 0.000 description 1
- 238000013007 heat curing Methods 0.000 description 1
- RRAMGCGOFNQTLD-UHFFFAOYSA-N hexamethylene diisocyanate Chemical compound O=C=NCCCCCCN=C=O RRAMGCGOFNQTLD-UHFFFAOYSA-N 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000004014 plasticizer Substances 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 229920005906 polyester polyol Polymers 0.000 description 1
- 229920000570 polyether Polymers 0.000 description 1
- 229920005862 polyol Polymers 0.000 description 1
- 150000003077 polyols Chemical class 0.000 description 1
- 230000003449 preventive effect Effects 0.000 description 1
- 230000002250 progressing effect Effects 0.000 description 1
- 238000007761 roller coating Methods 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
- DVKJHBMWWAPEIU-UHFFFAOYSA-N toluene 2,4-diisocyanate Chemical compound CC1=CC=C(N=C=O)C=C1N=C=O DVKJHBMWWAPEIU-UHFFFAOYSA-N 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 239000012808 vapor phase Substances 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
Landscapes
- Coating Apparatus (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
Description
【発明の詳細な説明】
本発明は、塗膜用硬化装置に関し、より詳細に
は、遊離イソシアネート基含有プレポリマーを含
む塗膜を、アミン雰囲気中で硬化させるための塗
膜用硬化装置に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a coating curing device, and more particularly to a coating curing device for curing a coating containing a prepolymer containing free isocyanate groups in an amine atmosphere.
従来、塗膜の形成には、熱エネルギー、公害及
び生産性の点で種々の問題が内在している。工業
的に最も普通に採用されている塗膜形成方法で
は、基体物品に塗装を行つた後、この塗装物品を
焼付炉に搬入し、高温で塗膜の焼付を行う。この
焼付に多大の熱エネルギーが必要であり、また塗
膜の焼付時に発生する溶媒、塗料ヤニ等の有害成
分を排気から除去するために、高価な排気処理シ
ステムが必要となる。また、塗膜の焼付を高温で
行えない木工品塗装等の場合には、この塗膜を自
然乾燥で硬化させねばならず、塗膜の硬化に著し
く長時間を必要とし、またその間湿つた塗膜にゴ
ミ等が付着しないような厳密な管理が必要とな
る。 Traditionally, the formation of coatings presents various problems in terms of thermal energy, pollution, and productivity. In the coating film forming method most commonly employed in industry, after a substrate article is coated, the coated article is transported into a baking oven and the coating film is baked at high temperature. This baking requires a large amount of thermal energy, and an expensive exhaust treatment system is required to remove harmful components such as solvents and paint tar generated during baking of the paint film from the exhaust gas. In addition, in the case of painting woodwork, etc., where the paint film cannot be baked at high temperatures, the paint film must be cured by air drying, which requires an extremely long time to harden, and during which time the wet paint cannot be used. Strict management is required to prevent dust from adhering to the membrane.
近年に至つて、熱による硬化の不要な塗膜の乾
燥方法が提案されており、特公昭53−13038号公
報には、遊離イソシアネート基を含有するプレポ
リマーを含むビヒクルを基材上に塗布し、次いで
このビヒクルを蒸気相の状態にあるアンモニアま
たはアミンからなる薬剤で処理することからなる
乾燥塗膜の形成方法が記載されている。 In recent years, a method for drying a coating film that does not require heat curing has been proposed, and Japanese Patent Publication No. 13038/1983 describes a method in which a vehicle containing a prepolymer containing free isocyanate groups is applied onto a substrate. A method for forming a dry coating is described, which consists in subsequently treating this vehicle with an agent consisting of ammonia or an amine in the vapor phase.
然しながら、このアンモニアまたはアミンは非
常に臭気の強いものであつて、極く微量の存在で
人に不快感を与える。従つてかかる方法を採用し
た場合に装置の密閉性が重要な問題となる。 However, this ammonia or amine has a very strong odor, and its presence in very small amounts causes discomfort to humans. Therefore, when such a method is adopted, the airtightness of the device becomes an important issue.
本発明は、上記方法を実施するための装置に関
するものであり、特にアミンを使用した上記方法
による塗膜の焼付乃至は硬化を、連続的に、しか
も実質上密閉系で効率良く行うための装置に関す
る。 The present invention relates to an apparatus for carrying out the above method, and in particular, an apparatus for efficiently baking or curing a coating film by the above method using an amine continuously and in a substantially closed system. Regarding.
即ち本発明の目的は、遊離イソシアネート基を
含む塗膜のアミンによる硬化を、密閉系において
しかも連続的に行うための装置を提供するにあ
る。 That is, an object of the present invention is to provide an apparatus for continuously curing coating films containing free isocyanate groups with amines in a closed system.
本発明の他の目的は、高温での焼付操作が不要
で、しかも著しく短時間で塗膜の硬化が可能であ
り、その結果として設備が小型でしかも生産性が
高く、また装置のメンテナンスも容易な塗膜硬化
装置を提供するにある。 Another object of the present invention is to eliminate the need for high-temperature baking operations and allow the coating film to be cured in an extremely short period of time.As a result, the equipment is compact and has high productivity, and the equipment is easy to maintain. The purpose of the present invention is to provide a coating film curing device.
本発明の更に他の目的は、木工品、油圧機器、
熱容量の著しく大きい物品等の、従来熱による塗
膜焼付が困難であつた物品に対しても、著しく短
時間で塗膜の硬化が可能となる装置を提供するに
ある。 Still other objects of the present invention include woodwork, hydraulic equipment,
It is an object of the present invention to provide an apparatus capable of curing a coating film in an extremely short time even on articles for which it has been difficult to bake the coating film by heat, such as articles having an extremely large heat capacity.
本発明によれば、遊離イソシアネート基を有す
るプリポリマーを含有する塗膜を気相のアミンと
接触させて該塗膜を硬化させるための装置であつ
て、
硬化室と、該硬化室内に塗装物品を搬入するた
めの搬入口を有する搬入用通路及び搬出するため
の搬出口を有する搬出用通路と、アミンの蒸気を
含む気流を発生させるための蒸気発生装置と、該
蒸気発生装置からの気流を硬化室に供給し且つ塗
装物品と接触後の気体を蒸気発生装置に循環する
循環系と、該硬化室への搬入口及び搬出口をアミ
ン蒸気の漏洩が生じないようにシールする機構と
から成り、前記硬化室は前記搬入口及び搬出口に
比して下方部位に位置することを特徴とする塗膜
用硬化装置が提供される。 According to the invention, there is provided an apparatus for curing a coating film containing a prepolymer having free isocyanate groups by contacting it with an amine in the gas phase, comprising: a curing chamber; and a coated article in the curing chamber. an inlet passageway having an inlet for carrying in the amine; an outlet passageway having an outlet for carrying out the amine; a steam generator for generating an airflow containing amine vapor; and an airflow from the steam generator. It consists of a circulation system that supplies the gas to the curing chamber and circulates the gas after contact with the coated article to the steam generator, and a mechanism that seals the inlet and outlet to the curing chamber to prevent leakage of amine vapor. There is provided a coating film curing apparatus, wherein the curing chamber is located at a lower portion than the inlet and the outlet.
本発明を以下添付図面を参照して詳細に説明す
る。 The present invention will be described in detail below with reference to the accompanying drawings.
第1図は本発明の塗膜用硬化装置の概要を示す
側面断面図、及び第2図は第1図の硬化装置のA
−A断面図を示す。 FIG. 1 is a side sectional view showing an outline of the coating film curing device of the present invention, and FIG. 2 is an A of the curing device of FIG. 1.
-A cross-sectional view is shown.
この第1図及び第2図において、本発明の塗膜
用硬化装置は、大まかに言つて、硬化室1と、搬
入口5を有する搬入用通路2a及び搬出口6を有
する搬出用通路2bと、蒸気発生装置3と、硬化
用気流の循環系4と、搬入口5及び搬出口6に設
けられたシール機構7とから成つている。 In FIG. 1 and FIG. 2, the coating film curing apparatus of the present invention generally includes a curing chamber 1, a carry-in passage 2a having a carry-in port 5, and a carry-out passage 2b having a carry-in port 6. , a steam generator 3, a curing airflow circulation system 4, and a sealing mechanism 7 provided at an inlet 5 and an outlet 6.
更に第3図は、この塗膜用硬化装置を付属の塗
装室及び後硬化室と組み合わせた平面配置の一例
を示す図である。 Further, FIG. 3 is a diagram showing an example of a planar arrangement in which this coating film curing device is combined with an attached painting room and a post-curing room.
第3図に示す具体例において、硬化室1の上流
側には塗装室8が、また硬化室1の下流側には後
硬化室9が夫々配置され、これを通るように搬送
系100が設けられている。 In the specific example shown in FIG. 3, a coating chamber 8 is disposed upstream of the curing chamber 1, and a post-curing chamber 9 is disposed downstream of the curing chamber 1, and a conveyance system 100 is provided to pass through these. It is being
塗装室8は、塗装処理されるべき物品(基体)
10に、特定の塗料、即ち遊離イソシアネート基
含有プレポリマーを含む塗料を塗布するためのも
のであり、通常の簡易型塗装ブースと同様に、基
体10が搬入される入口11及び塗装基体が搬出
される出口12を備えており、しかも基体10の
移動路の一方の側には、前記塗料を基体に塗布す
るためのスプレーガンのような塗布機構13が、
また他方の側には、必要に応じ、フイルター等の
塗料ミスト捕集機構14を介して、排気吸引ダク
ト15が設けられている。 The painting room 8 contains articles (substrates) to be painted.
10 is for applying a specific paint, that is, a paint containing a prepolymer containing free isocyanate groups, and, like a normal simple painting booth, there is an entrance 11 into which the substrate 10 is brought in, and an entrance 11 through which the coated substrate is taken out. An application mechanism 13 such as a spray gun for applying the paint onto the substrate is provided on one side of the movement path of the substrate 10.
Further, on the other side, an exhaust suction duct 15 is provided via a paint mist collection mechanism 14 such as a filter, if necessary.
本発明装置に用いる塗料は、遊離イソシアネー
ト基含有プレポリマーを含む塗料であり、後に詳
述する気相のアミンとの接触で硬化が行われるも
のである。このような塗料の適当な例は、イソシ
アネート基末端プレポリマーと呼ばれるものであ
り、例えばポリエステルポリオール、ポリエーテ
ルポリオール、水酸基含有アクリル樹脂、水酸基
含有ビニル樹脂、アルキド樹脂、ポリアミド、等
のイソシアネート基に対して反応性を有するオリ
ゴマー乃至ポリマーをポリイソシアネート、例え
ばトリレンジイソシアネート、ヘキサメチレンジ
イソシアネート、シクロヘキサンジイソシアネー
ト、ジフエニルメタンジイソシアネートと反応さ
せ、該イソシアネートをウレタン結合、尿素結合
等を介して、該オリゴマー乃至ポリマーの骨格に
結合させたものが使用される。勿論、上述したイ
ソシアネート基に対して反応性のオリゴマー乃至
ポリマーと、ポリイソシアネートとは、予め反応
させたものでも、或いは混合物の形で部分的に反
応させたものでもよく、また、この塗料は複数種
の樹脂の混合物であつてよい。要するに、本発明
の目的には、気相のアミンで硬化するに足る量の
遊離イソシアネート基が含有されている限り任意
の塗料が使用し得ることが了解されるべきであ
る。 The paint used in the apparatus of the present invention is a paint containing a prepolymer containing free isocyanate groups, and is cured by contact with a gaseous amine, which will be described in detail later. Suitable examples of such coatings are those called isocyanate group-terminated prepolymers, such as polyester polyols, polyether polyols, hydroxyl group-containing acrylic resins, hydroxyl group-containing vinyl resins, alkyd resins, polyamides, etc. A reactive oligomer or polymer is reacted with a polyisocyanate such as tolylene diisocyanate, hexamethylene diisocyanate, cyclohexane diisocyanate, or diphenylmethane diisocyanate, and the isocyanate is reacted with the oligomer or polymer through urethane bonds, urea bonds, etc. It is used attached to a skeleton. Of course, the above-mentioned oligomer or polymer reactive with isocyanate groups and the polyisocyanate may be reacted in advance or partially reacted in the form of a mixture, and this coating material may be used in combination with multiple polyisocyanates. It may be a mixture of different resins. In summary, it should be understood that any coating material may be used for purposes of the present invention as long as it contains a sufficient amount of free isocyanate groups to be cured with a gas phase amine.
遊離イソシアネート基の濃度は、一般に樹脂分
100g当り10乃至500ミリモル、特に30乃至300ミ
リモルの範囲にあるのが望ましい。 The concentration of free isocyanate groups is generally determined by the resin content.
A range of 10 to 500 mmol, particularly 30 to 300 mmol per 100 g is preferred.
この塗料は、塗装に適した粘度の液体である場
合には、無溶媒塗料としても使用でき、また前記
プレポリマーを幾分溶剤で稀釈した溶液型塗料と
しても使用できる。勿論、この塗料には、それ自
体公知の塗料配合成分、例えば、顔料、可塑剤、
界面活性剤、垂れ防止剤、防錆剤、等にそれ自体
公知の配合比で配合される。好適な塗料は、不揮
発分濃度が20乃至100重量%で且つ動粘度(フオ
ードカツプ#4)が15乃至150秒の範囲のもので
ある。 This paint can be used as a solvent-free paint if it is a liquid with a viscosity suitable for painting, or it can be used as a solution-type paint in which the prepolymer is diluted with a solvent. Of course, this paint contains components known per se, such as pigments, plasticizers,
It is blended with surfactants, anti-sag agents, rust preventive agents, etc. in known proportions. Suitable coatings have a non-volatile concentration of 20 to 100% by weight and a kinematic viscosity (foed cup #4) of 15 to 150 seconds.
塗装すべき基体10としては、通常の鋼板乃至
表面処理鋼板から形成された基体の他に、熱によ
る塗膜焼付の困難な本工製品、繊維製品、プラス
チツク製品、油圧機器製品、熱容量の大きい鋳造
製品等を挙げることができ、特に後者の基体の場
合には、熱による焼付が不要であり、しかも塗膜
の硬化が迅速に行われることによる本発明の顕著
な利点が達成される。 Substrates 10 to be coated include, in addition to substrates formed from ordinary steel plates or surface-treated steel plates, manufactured products whose paint film is difficult to bake due to heat, textile products, plastic products, hydraulic equipment products, and castings with a large heat capacity. Particularly in the case of the latter substrates, the significant advantages of the present invention are achieved in that no thermal baking is necessary and the coating film hardens quickly.
塗布機構13としては、スプレーによる塗布機
構、例えばエアスプレーガン、エアレススプレー
ガン、回転霧化式塗装装置等が、非静電式、静電
式のものを含めて好適に使用される。勿論、基体
の種類によつては、浸漬塗布、ローラコート、フ
ローコート等の他の塗布方式も採用し得る。 As the coating mechanism 13, a spray coating mechanism such as an air spray gun, an airless spray gun, a rotary atomization coating device, etc., including non-electrostatic type and electrostatic type, is suitably used. Of course, other coating methods such as dip coating, roller coating, flow coating, etc. may also be employed depending on the type of substrate.
再び第1図及び第2図に戻つて硬化室1は、塗
布室8からの塗装物品10′を気相のアミンと接
触させて、形成された塗膜の硬化反応を行うため
のものであり、連続処理を可能にするために、塗
装物品10′を室内に搬入するための搬入口5を
有する搬入用通路2a及びアミンと接触後の物品
を搬出するための搬出口6を有する搬出用通路2
bを備えている。 Returning again to FIGS. 1 and 2, the curing chamber 1 is for bringing the coated article 10' from the coating chamber 8 into contact with a gaseous amine to effect a curing reaction of the formed coating film. , a carry-in passage 2a having a carry-in port 5 for carrying the coated article 10' into the room and a carry-out passage having a carry-out port 6 for carrying out the article after contact with the amine, in order to enable continuous processing. 2
It is equipped with b.
本発明の塗膜用硬化装置には、塗膜の硬化処理
を連続的に、しかも短時間の内に有効に行うため
に、硬化室1と、硬化用のアミンの蒸気発生装置
3と、硬化用気流の循環系4とが、以下に詳述す
る関連のもとに設けられている。 The coating film curing apparatus of the present invention includes a curing chamber 1, an amine steam generator 3 for curing, and a curing chamber 1, an amine vapor generator 3 for curing, and a curing chamber 1, a curing amine vapor generator 3, A circulation system 4 for the air flow is provided in connection with which it will be explained in more detail below.
先ず、硬化室1は、アミンを含む硬化用ガス
(気流)を均一且つ一様に供給し塗装物品10′に
吹付けるために、底壁部に吹付口16aを有する
給気ダクト16を設けるとともに、両側壁部には
多数のフイン17aを備えた給気ダクト17を設
け、自転しながら移動する塗装物品10′に対し
て硬化用ガスを吹き付ける。 First, the curing chamber 1 is provided with an air supply duct 16 having a spray port 16a on the bottom wall in order to uniformly and uniformly supply a curing gas (airflow) containing amine and spray it onto the coated article 10'. An air supply duct 17 having a large number of fins 17a is provided on both side walls, and a curing gas is sprayed onto the coating article 10' which is rotating and moving.
これらダクト16,17は、供給ダクト18を
介して硬化用蒸気発生装置3に接続されている。
この硬化用蒸気発生装置は、アミン類を気相で硬
化室1に送るためのものであり、図面に示す具体
例では、フアン19で送られる空気、窒素等のキ
ヤリヤガス中にスプレー装置20によりアミンを
スプレーすることにより硬化用蒸気を発生させ
る。 These ducts 16 and 17 are connected to the curing steam generator 3 via a supply duct 18.
This curing steam generator is for sending amines in a gaseous phase to the curing chamber 1. In the specific example shown in the drawings, amines are supplied by a spray device 20 into a carrier gas such as air or nitrogen sent by a fan 19. The curing steam is generated by spraying.
硬化室1には、排風口21aを備えた排気ダク
ト21が設けられ、排風ダクト22を介し且つ必
要によりフイルター等の過清浄化機構23を介
して、フアン19の吸引側に接続されている。 The curing chamber 1 is provided with an exhaust duct 21 having an exhaust port 21a, and is connected to the suction side of the fan 19 via an exhaust duct 22 and, if necessary, a supercleaning mechanism 23 such as a filter. .
かくして、本発明の塗膜用硬化装置における硬
化用蒸気の循環系4は、排風口21aを備えた排
気ダクト21、排風ダクト22、フアン19、供
給ダクト18、及び給気ダクト16,17で構成
されていることが了解されよう。この循環系4に
は、必要により硬化用ガスの加熱機構(図示せ
ず)を設けることができ、温度の低下する冬期中
には、硬化用ガスの温度を室温と同程度、即ち常
温乃至は30℃程度の温度に維持し得るようになつ
ている。 Thus, the curing steam circulation system 4 in the coating film curing apparatus of the present invention includes the exhaust duct 21 equipped with the exhaust port 21a, the exhaust duct 22, the fan 19, the supply duct 18, and the supply air ducts 16, 17. It will be understood that it is configured. This circulation system 4 can be provided with a curing gas heating mechanism (not shown) if necessary, and during the winter when the temperature drops, the temperature of the curing gas is kept at the same level as room temperature, that is, room temperature or The temperature can be maintained at around 30℃.
また本発明の重要な特徴は、硬化室1が搬入口
5及び搬出口6に比して下方部位に位置している
ことにある。即ち、本発明において硬化用薬剤と
してアミンを使用するが、このアミンの蒸気は空
気より重く、従つて上記の如く硬化室1を下方部
位に位置せしめることにより、アミン蒸気が搬入
口5及び搬出口6から外気中へ漏出することがよ
り有効に防止されるのである。 Further, an important feature of the present invention is that the curing chamber 1 is located at a lower portion than the entrance 5 and the exit 6. That is, although amine is used as a curing agent in the present invention, the vapor of this amine is heavier than air, so by locating the curing chamber 1 in the lower part as described above, the amine vapor flows into the inlet 5 and the outlet. 6 into the outside air can be more effectively prevented.
また、硬化用蒸気の供給口或いは硬化室内に、
アミン類の濃度検出機構25aを設け、この検出
信号によつて、濃度制御回路25を介してスプレ
ー装置20のバルブ26を制御し、硬化室内のア
ミン濃度を、常に所定の値に設定し得る。 In addition, in the curing steam supply port or in the curing chamber,
An amine concentration detection mechanism 25a is provided, and this detection signal controls the valve 26 of the spray device 20 via the concentration control circuit 25, so that the amine concentration in the curing chamber can always be set to a predetermined value.
尚、本発明に用いるアミン類は一級、二級或い
は三級のモノアミン類の他に、多価アミン類であ
つても良く、例えばメチルアミン、エチルアミ
ン、プロピルアミン、ジエチルアミン、トリエチ
ルアミン、ピペリジン、モルホリン、ピペラジ
ン、エタノールアミン、ジエタノールアミン、ト
リエタノールアミン、シクロヘキシルアミン、エ
チレンジアミン、テトラメチルエチレンジアミ
ン、エチレントリアミン、等の1種又は2種以上
の組合せを挙げることができる。 In addition to primary, secondary, or tertiary monoamines, the amines used in the present invention may be polyvalent amines, such as methylamine, ethylamine, propylamine, diethylamine, triethylamine, piperidine, morpholine, Examples include one or a combination of two or more of piperazine, ethanolamine, diethanolamine, triethanolamine, cyclohexylamine, ethylenediamine, tetramethylethylenediamine, ethylenetriamine, and the like.
硬化用気流中に、アミンは無稀釈の蒸気の状態
で存在させることもできるが、操作の容易性や経
済性の見地からは、50乃至50000ppm特に100乃
至10000ppmとなる濃度で気流中に含有させるこ
とが望ましい。 The amine can be present in the form of undiluted vapor in the curing air stream, but from the standpoint of ease of operation and economic efficiency, it is preferred to include it in the air stream at a concentration of 50 to 50,000 ppm, particularly 100 to 10,000 ppm. This is desirable.
本発明においては更に、アミン蒸気の漏出を完
全に防止するために、搬入用通路2aの搬入口5
及び搬出用通路2bの搬出口6に全体として7で
示すシール機構7を設ける。 In the present invention, furthermore, in order to completely prevent leakage of amine vapor, the inlet 5 of the inlet passage 2a is
A sealing mechanism 7 generally indicated by 7 is provided at the exit 6 of the exit passage 2b.
このシール機構7の構成を説明するための、第
1図の装置のB−B断面図及びその一部平面図を
示す第4図を参照して、シール機構7は搬入口5
及び搬出口6に設けられた、物品の通過を可能に
する仕切板乃至はフラツプ27及び吸気ダクト2
8に連なる周状の吸気口29とから成つている。 In order to explain the configuration of the sealing mechanism 7, with reference to FIG. 4 showing a BB sectional view and a partial plan view of the device in FIG.
and a partition plate or flap 27 provided at the exit 6 to allow passage of articles, and an intake duct 2
8 and a continuous circumferential intake port 29.
即ち、仕切板乃至はフラツプ27はスライド可
能乃至は回動自在となつており、通過する物品1
0′の形状に応じて種々の形の通過口が形成し得
る様になつており、この通過口面積の調整により
アミンの蒸気の漏出が有効に防止される。 That is, the partition plate or flap 27 is slidable or rotatable, and the article 1 passing therethrough is
Various shapes of passage ports can be formed depending on the shape of 0', and leakage of amine vapor can be effectively prevented by adjusting the area of the passage holes.
更に吸気口29から搬入口及び搬出口近傍の空
気を吸引してエアーシールが形成され、アミン蒸
気が外気中に漏出するのが完全に防止される。 Furthermore, an air seal is formed by suctioning the air near the inlet and outlet through the intake port 29, completely preventing amine vapor from leaking into the outside air.
尚、吸気ダクト28から排出されるガス及び前
述した循環系に連なる排気ダクト30から取出し
た硬化用ガスの一部を、スクラバー、吸着装置、
接触分解装置、等の排気処理装置31を経て、実
質上の無臭の無害ガスとして大気中に放出でき
る。尚、吸着装置で捕集されるアミンは、これを
脱着させて回収し、硬化の目的で再利用できるこ
とは当然である。 Note that a part of the gas discharged from the intake duct 28 and the curing gas taken out from the exhaust duct 30 connected to the above-mentioned circulation system is passed through a scrubber, an adsorption device,
It can be released into the atmosphere as a substantially odorless and harmless gas through an exhaust treatment device 31 such as a catalytic cracker. It goes without saying that the amine collected by the adsorption device can be recovered by desorption and reused for the purpose of curing.
塗装物品がアミンと接触する時間は、塗料の種
類や厚み、硬化用ガス中の濃度や温度によつても
相違するが、一般的に言つて、10乃至600秒、特
に20乃至300秒のような極めて短時間でよい。 The time that the coated article is in contact with the amine varies depending on the type and thickness of the paint, the concentration in the curing gas, and the temperature, but generally speaking it is 10 to 600 seconds, especially 20 to 300 seconds. It only takes a very short time.
本発明によれば、上述した構成により、有害な
アミンの蒸気が外部に漏洩することなしに、密閉
系でアミンによる塗膜の硬化処理を連続的に行う
ことが可能となる。しかも、実質上密閉された硬
化室内にアミン蒸気を気流として供給し、しかも
この気流を蒸気発生装置を介して循環させること
により、塗膜と蒸気との接触が均一且つ一様にし
かも密に行われることにより、塗膜の硬化反応が
有効にしかも短時間の内に行われる。また、密閉
系で蒸気を循環させることにより、アミンの損失
を防止しながら経済的な硬化処理が可能となる。 According to the present invention, the above-described configuration makes it possible to continuously perform curing treatment of a coating film using an amine in a closed system without leaking harmful amine vapor to the outside. Moreover, by supplying the amine vapor as an air stream into the virtually sealed curing chamber and circulating this air stream through a steam generator, the coating film and the vapor come into contact evenly, uniformly, and closely. As a result, the curing reaction of the coating film is carried out effectively and within a short period of time. Moreover, by circulating the steam in a closed system, an economical curing process is possible while preventing loss of amine.
第3図に示す具体例では、硬化室1において、
アミンを含有する硬化用ガスと接触した塗装物品
10″を、後硬化室9において空気流と接触させ
る。 In the specific example shown in FIG. 3, in the curing chamber 1,
The coated article 10'', which has been in contact with the amine-containing curing gas, is contacted with a stream of air in the post-curing chamber 9.
即ち、アミン類との接触が終了したばかりの塗
膜は、硬化が進行しているとしても、その塗膜を
爪でこすると塗膜に引掻傷が容易に入るようなも
のであり、その塗膜を鉛筆硬度で測定し得るよう
に硬化を続行させるためには、空気との接触を必
要とする。 In other words, a paint film that has just come into contact with amines will easily be scratched if you rub it with your fingernail, even if the hardening process is progressing. Contact with air is required for continued curing of the coating as measured by pencil hardness.
後硬化室9は、塗装物品10″の搬入口32と
搬出口33とがあるトンネル状の形状を有してお
り、その内部には、塗装物品の移動路に沿つて、
多孔質の仕切壁34が設けられている。この仕切
壁34を介して空気通路35があり、通路35に
導入される空気は、仕切壁34を介して塗装物品
10″に吹付けられ、これにより塗膜の後硬化が
進行する。空気通路35は供給ダクト36を介し
て送風フアン37に接続され、一方後硬化室にお
いて塗膜と接触した後の空気流は排気ダクト38
から、過清浄化機構39加熱機構40を経てフ
アン37の吸引側に循環される。 The post-curing chamber 9 has a tunnel-like shape with an inlet 32 and an outlet 33 for the coated article 10'', and inside the post-curing chamber 9, along the movement path of the coated article,
A porous partition wall 34 is provided. There is an air passage 35 through this partition wall 34, and the air introduced into the passage 35 is blown onto the coated article 10'' through the partition wall 34, thereby proceeding with the post-curing of the coating film.Air passage 35 is connected to a blower fan 37 via a supply duct 36, while the airflow after contacting the coating in the post-curing chamber is directed to an exhaust duct 38.
From there, it is circulated to the suction side of the fan 37 via the supercleaning mechanism 39 and the heating mechanism 40.
後硬化用空気は、室温で十分であるが、後硬化
を促進させるには、50℃程度迄の温度に加温され
ていることが有利である。 Room temperature is sufficient for post-curing air, but in order to accelerate post-curing, it is advantageous to heat the air to a temperature of about 50°C.
本実施例において、搬送機構100は、一連の
ホイール乃至スプロケツト41を介して、塗装室
8、硬化室1及び後硬化室9を順次通過するよう
に配置され、駆動機構42により、連続的に或い
は間欠的に駆動される。この具体例において搬送
機構100は、エンドレスのオーバーヘツドコン
ベアであり、塗装すべき物品10は、積込位置4
3でコンベアに載せられ、塗装製品10aは降し
位置44でコンベアから取外される。 In this embodiment, the transport mechanism 100 is arranged to pass sequentially through the painting chamber 8, the curing chamber 1, and the post-curing chamber 9 via a series of wheels or sprockets 41, and is continuously or Driven intermittently. In this embodiment, the transport mechanism 100 is an endless overhead conveyor, and the articles 10 to be painted are placed at a loading position 4.
3, the coated product 10a is removed from the conveyor at an unloading position 44.
本発明において、塗膜の後硬化に或る程度の時
間をかけてもよい場合には、後硬化室9を省略
し、半硬化の塗装物品を空気中に放置する方式を
も採用し得る。また、塗装室8と切離して塗膜用
硬化装置にのみ搬送系を設けることも可能であ
る。 In the present invention, if it is acceptable to take a certain amount of time to post-cure the coating film, a method may be adopted in which the post-curing chamber 9 is omitted and the semi-cured coated article is left in the air. Further, it is also possible to separate from the coating room 8 and provide a conveyance system only in the coating film curing device.
以上説明した本発明の装置によれば、次の顕著
な利点が付加的に達成される。即ち、塗装設備の
中で塗膜を乾燥焼付するための炉が消費する熱エ
ネルギーは膨大なものであるが、本発明によれ
ば、高温での焼付が必要でないので、大巾な省エ
ネルギーとなる。また、塗膜の高温焼付が困難な
物品に対しても、短時間での塗膜硬化が可能とな
り、更に硬化時間が短かいことから、設備が小型
ですみ、しかも生産能力を著しく向上させ得る。
更に、室温乃至は室温附近での操業であることか
ら火災の危険性がなく、また従来の焼付炉のよう
なヤニ清掃が不要で、メンテナンスも容易であ
る。 According to the device of the invention as described above, the following significant advantages are additionally achieved. That is, although the furnace for drying and baking the paint film in the painting equipment consumes a huge amount of thermal energy, according to the present invention, baking at high temperatures is not necessary, resulting in significant energy savings. . In addition, it is possible to cure the coating film in a short time even on items for which it is difficult to bake the coating film at high temperatures.Furthermore, because the curing time is short, the equipment can be small-sized and production capacity can be significantly improved. .
Furthermore, since it is operated at or near room temperature, there is no danger of fire, and there is no need to clean tar as in conventional baking furnaces, making maintenance easy.
尚、以上の具体例においては本発明の硬化装置
を連続式の硬化装置として適用した例を示した
が、この硬化装置を所謂バツチ式の硬化装置とし
て適用することも可能である。この場合には、硬
化すべき塗膜を有する物品の搬入及び搬出兼用の
通路を硬化室上方に設け、好ましくは、搬入兼搬
出口に密閉用の扉を設ければよい。そうすれば扉
の開放中でも重いアミン蒸気が上方の通路を介し
て漏出することがより有効に防止されることが理
解されよう。 In the above specific example, an example was shown in which the curing device of the present invention was applied as a continuous type curing device, but it is also possible to apply this curing device as a so-called batch type curing device. In this case, a passageway for carrying in and out the article having a coating film to be cured may be provided above the curing chamber, and preferably a sealing door may be provided at the carrying-in/outlet. It will be appreciated that this will more effectively prevent heavy amine vapors from escaping through the upper passage even when the door is open.
第1図は本発明の硬化装置の概要を示す側面断
面図、第2図は、第1図の装置のA−A断面図、
第3図は、第1図の硬化装置を付属の塗装置及び
後硬化室とともに示す平面配置図である。第4図
は、第1図の装置のB−B断面図及びその一部平
面図を示す。
1は硬化室、2aは搬入用通路、2bは搬出用
通路、3は蒸気発生装置、4は硬化用気流の循環
系、5は搬入口、6は搬出口、7はシール機構、
8は塗装室、9は後硬化室、10,10′,1
0″は塗装物品(基体)、10aは塗装製品、13
は塗布機構、16及び17は給気ダクト、18は
供給ダクト、19はフアン、20はスプレー装
置、21は排気ダクト、22は排風ダクト、28
は吸気ダクト、29は周状の吸気口、31は排気
処理装置、100は搬送系を夫々示す。
FIG. 1 is a side sectional view showing an outline of the curing device of the present invention, FIG. 2 is an AA sectional view of the device in FIG. 1,
FIG. 3 is a plan layout diagram showing the curing apparatus of FIG. 1 together with an attached coating station and a post-curing chamber. FIG. 4 shows a BB sectional view and a partial plan view of the device shown in FIG. 1. 1 is a curing chamber, 2a is a carry-in passage, 2b is a carry-out passage, 3 is a steam generator, 4 is a curing airflow circulation system, 5 is a carry-in port, 6 is a carry-out port, 7 is a sealing mechanism,
8 is a painting room, 9 is a post-curing room, 10, 10', 1
0'' is a painted article (substrate), 10a is a painted product, 13
1 is a coating mechanism, 16 and 17 are air supply ducts, 18 is a supply duct, 19 is a fan, 20 is a spray device, 21 is an exhaust duct, 22 is an exhaust duct, 28
29 is an intake duct, 29 is a circumferential intake port, 31 is an exhaust treatment device, and 100 is a conveyance system.
Claims (1)
を含有する塗膜を気相のアミンと接触させて該塗
膜を硬化させるための装置であつて、 硬化室と、該硬化室内に塗装物品を搬入するた
めの搬入口を有する搬入用通路及び搬出するため
の搬出口を有する搬送用通路と、アミンの蒸気を
含む気流を発生させるための蒸気発生装置と、該
蒸気発生装置からの気流を硬化室に供給し且つ塗
装物品と接触後の気体を蒸気発生装置に循環する
循環系と、該硬化室への搬入口及び搬出口をアミ
ン蒸気の漏洩が生じないようにシールする機構と
から成り、前記硬化室は搬入口及び搬出口に比し
て下方部位に位置することを特徴とする塗膜用硬
化装置。[Scope of Claims] 1. An apparatus for curing a coating film containing a prepolymer having free isocyanate groups by bringing it into contact with a gaseous amine, comprising: a curing chamber; and a coating inside the curing chamber. A carry-in passageway having an inlet for carrying in articles, a conveyance passageway having an outlet for carrying out goods, a steam generation device for generating an airflow containing amine vapor, and an airflow from the steam generation device. A circulation system that supplies amine vapor to the curing chamber and circulates the gas after contact with the coated article to a steam generator, and a mechanism that seals the inlet and outlet to the curing chamber to prevent leakage of amine vapor. A coating film curing apparatus characterized in that the curing chamber is located at a lower portion than an inlet and an outlet.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19993183A JPS6094169A (en) | 1983-10-27 | 1983-10-27 | Curing device for coating film |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP19993183A JPS6094169A (en) | 1983-10-27 | 1983-10-27 | Curing device for coating film |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6094169A JPS6094169A (en) | 1985-05-27 |
| JPS6231989B2 true JPS6231989B2 (en) | 1987-07-11 |
Family
ID=16415972
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP19993183A Granted JPS6094169A (en) | 1983-10-27 | 1983-10-27 | Curing device for coating film |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6094169A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02108703U (en) * | 1989-02-16 | 1990-08-29 |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4993666B2 (en) * | 2006-05-23 | 2012-08-08 | トリニティ工業株式会社 | UV paint curing equipment, paint curing method |
-
1983
- 1983-10-27 JP JP19993183A patent/JPS6094169A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH02108703U (en) * | 1989-02-16 | 1990-08-29 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6094169A (en) | 1985-05-27 |
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