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JPS6341629B2 - - Google Patents
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JPS6341629B2 - - Google Patents

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Publication number
JPS6341629B2
JPS6341629B2 JP54035689A JP3568979A JPS6341629B2 JP S6341629 B2 JPS6341629 B2 JP S6341629B2 JP 54035689 A JP54035689 A JP 54035689A JP 3568979 A JP3568979 A JP 3568979A JP S6341629 B2 JPS6341629 B2 JP S6341629B2
Authority
JP
Japan
Prior art keywords
coating
coating agent
coated
paint
glass containers
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
Application number
JP54035689A
Other languages
Japanese (ja)
Other versions
JPS55129175A (en
Inventor
Motoaki Suzuki
Naoto Yabe
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.)
Artience Co Ltd
Original Assignee
Toyo Ink Mfg Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Toyo Ink Mfg Co Ltd filed Critical Toyo Ink Mfg Co Ltd
Priority to JP3568979A priority Critical patent/JPS55129175A/en
Publication of JPS55129175A publication Critical patent/JPS55129175A/en
Publication of JPS6341629B2 publication Critical patent/JPS6341629B2/ja
Granted legal-status Critical Current

Links

Landscapes

  • Application Of Or Painting With Fluid Materials (AREA)
  • Surface Treatment Of Glass (AREA)

Description

【発明の詳細な説明】 本発明は高速度で連続的に塗装でき塗料の損失
がなく、かつ装置的にもシンプルで故障等の問題
の少ない塗装方法に関するものである。従来、炭
酸飲料用等のガラス容器の破損防止ならびに破損
時のガラス片飛散防止の目的でガラス容器に合成
樹脂もしくは合成ゴム等を被覆する方法が数多く
知られている。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a coating method that allows continuous coating at high speed without loss of paint, is simple in terms of equipment, and has fewer problems such as breakdowns. Conventionally, many methods have been known for coating glass containers, such as those for carbonated beverages, with synthetic resin, synthetic rubber, etc. for the purpose of preventing breakage of glass containers and preventing glass pieces from scattering when broken.

その一例を示すとガラス容器にポリエチレン、
ポリプロピレン、サーリン等を収縮させて緊密に
係合させる方法(特開昭47−12148号)、水酸基、
カルボキシル基、アセトキシ基の少なくとも一種
を有するオレフイン共重合体を粉体塗装等により
被覆した容器(特公昭47−23882号)、未処理また
はプライマー処理されたガラス容器にゴムもしく
は合成樹脂の第1層を形成し、更にその外側に合
成樹脂の第2層を形成した容器(特開昭48−
55210号、特開昭48−65214号等)等多数がある。
使用されている高分子物質は多岐にわたり、ポリ
エチレン、ポリプロピレン、ポリスチレン、ポリ
塩化ビニル、ポリアミド等の熱可塑性樹脂、メラ
ミン樹脂、エポキシ樹脂、ポリウレタン樹脂等の
熱硬化性樹脂があり、これらの被覆樹脂に要求さ
れる物性として、摩擦等による傷の発生を防止
し、破損を防ぐと共に炭酸飲料の如き内圧のある
ガラス容器が衝撃等により破損した場合でも、ガ
ラスの破片を飛散させない被覆でなければならな
い。更にガラス容器の繰り返し使用に伴う温水お
よび冷水、アルカリ水溶液等に対して皮膜が耐久
性を有していなければならない。この様な要求に
適合する皮膜とするため、被覆樹脂として熱可塑
性樹脂よりも熱硬化性樹脂が要望されている。し
かもガラス容器に施された皮膜は膜厚が一定であ
り、外観の良好な皮膜が要求される。従つて塗装
方法としては定量性の良好な塗装方法が望まし
い。また、省力化の目的から塗装回数を少なくし
て所定の膜厚に塗膜を形成させることが望まれる
ために、液状の塗装剤では塗装剤の固形分が増加
し、必然的に粘度が高くなる傾向にある。更に、
無公害型塗装剤が要望され、無溶剤の塗装剤が好
ましく、液状の塗装剤では一般的に高粘度塗装剤
となる。
One example is polyethylene in glass containers.
A method of contracting polypropylene, Surlyn, etc. to tightly engage them (Japanese Patent Application Laid-Open No. 12148/1983), hydroxyl group,
A container coated with an olefin copolymer having at least one of a carboxyl group and an acetoxy group by powder coating (Japanese Patent Publication No. 47-23882), a first layer of rubber or synthetic resin on an untreated or primer-treated glass container and a second layer of synthetic resin on the outside (Japanese Patent Application Laid-open No. 1973-
55210, JP-A-48-65214, etc.).
A wide variety of polymer materials are used, including thermoplastic resins such as polyethylene, polypropylene, polystyrene, polyvinyl chloride, and polyamide, and thermosetting resins such as melamine resin, epoxy resin, and polyurethane resin. The required physical properties include a coating that prevents scratches due to friction, etc., prevents breakage, and does not scatter glass fragments even if a glass container with internal pressure, such as a carbonated drink, is damaged by impact or the like. Furthermore, the film must be durable against hot and cold water, alkaline aqueous solutions, etc. that accompany repeated use of glass containers. In order to provide a film that meets these requirements, thermosetting resins are desired rather than thermoplastic resins as coating resins. Moreover, the coating applied to the glass container must have a constant thickness and have a good appearance. Therefore, as a coating method, a coating method with good quantitative properties is desirable. In addition, for the purpose of saving labor, it is desirable to reduce the number of times of coating and form a coating film to a predetermined thickness, so with liquid coating agents, the solid content of the coating agent increases, which inevitably results in a high viscosity. There is a tendency to Furthermore,
A non-polluting coating agent is desired, a solvent-free coating agent is preferred, and a liquid coating agent generally has a high viscosity.

ガラス容器等の被塗装物に塗装を行なう場合、
複数の被塗装物を間隔に置いて保持し、1本ない
し数本ずつ塗装される。
When painting objects such as glass containers,
Multiple objects to be painted are held at intervals and painted one or several at a time.

この塗装作業を連続的に行なうこと、しかも高
速に処理出来ることが望まれる。しかしながら、
連続して塗装しようとした場合、被塗装物が断続
的に存在するため、塗装剤を連続して被塗装物に
供給すると、塗装剤の損失を覚悟しなければなら
ない。更に、塗装剤が液状の反応硬化型塗装剤で
は損失となる塗装剤の回収再使用は不可能であ
り、塗装装置の汚染を来たす。浸漬塗装の場合で
も同様のことが言える。また、塗装剤を被塗装物
に同調させて断続的に供給する場合では、自動化
装置が大がかりとなる。
It is desired that this coating work be performed continuously and that it can be processed at high speed. however,
When attempting to paint continuously, the object to be painted exists intermittently, so if the paint is continuously supplied to the object, one must be prepared for loss of the paint. Furthermore, in the case of a reaction-curing type coating agent in which the coating agent is a liquid, it is impossible to recover and reuse the lost coating agent, resulting in contamination of the coating equipment. The same can be said for dip coating. Further, in the case where the coating agent is intermittently supplied in synchronization with the object to be coated, the automation device becomes large-scale.

ガラス容器等の被塗装物に塗装剤を塗装する方
法としてハケ塗り、浸漬塗装の方法では塗装剤の
粘度が低い場合には効果のある塗装方法である
が、高粘度塗装剤では均一な皮膜の塗装を高速度
に行なうことは困難である。スプレー塗装の方法
では、低粘度の塗装剤に適した塗装方法であり、
一般に飛散による塗料の損失が大きく、また塗装
装置を汚し、高粘度の塗装剤では室温塗装が困難
なため、塗装剤を加温もしくは溶剤等により低粘
度化しなければならない。流下式塗装法では高粘
度の塗装剤であつても塗装が可能であるが、被塗
装物が連続した物品の場合、問題ではないが、被
塗装物が間欠的に存在する場合、連続的に塗装す
るには塗装剤の流下を同調させて断続的に行なわ
なければならず、自動化装置が大がかりとなり、
費用も高く、複雑で故障等の問題も大きく、また
塗装スピードが劣る欠点がある。反応が早く、硬
化し易い塗装剤を用いて、断続的に塗装する場
合、塗装剤の一部がノズルの出口等に付着した
り、ノズルを詰まらせる原因となり易い。
Brushing and dipping are effective methods for applying paint to objects such as glass containers, but they are effective when the viscosity of the paint is low; however, with high viscosity paints, it is difficult to form a uniform film. It is difficult to perform painting at high speed. The spray painting method is suitable for low viscosity paints,
In general, there is a large loss of paint due to scattering, and it also contaminates the coating equipment, making it difficult to apply at room temperature with a highly viscous paint, so the viscosity of the paint must be reduced by heating or using a solvent. With the flow-down coating method, it is possible to coat even high-viscosity paints, but if the object to be coated is continuous, this is not a problem, but if the object to be coated is intermittently present, it is possible to coat even with a highly viscous coating agent. To paint, the flow of paint must be synchronized and carried out intermittently, requiring extensive automated equipment.
It is expensive, complex, has many problems such as failure, and has the disadvantage of being inferior in painting speed. When coating intermittently using a coating agent that reacts quickly and hardens easily, a portion of the coating agent tends to adhere to the nozzle outlet or the like, causing the nozzle to become clogged.

以上、いずれの塗装方法においても、一定間隔
をもつて配置された連続移動する複数の被塗装物
を塗装する場合、塗装剤の有効利用(損失がな
い)、高速塗装、均一塗膜の形成、塗装装置の簡
略化等のいずれの条件も満足する方法は少なく、
特に高粘度液状塗装剤を用いた塗装において、上
記の条件を満足させる塗装方法が要望されてい
た。
As mentioned above, in any of the painting methods, when painting multiple objects to be painted that are continuously moving and arranged at regular intervals, effective use of the paint agent (no loss), high-speed painting, formation of a uniform coating film, There are few methods that satisfy all conditions such as simplifying the coating equipment.
There has been a demand for a coating method that satisfies the above conditions, especially in coating using a high viscosity liquid coating agent.

本発明は連続的に、かつ高速度で塗装できる方
法であり、しかも塗装剤の無駄がなく、装置的に
も非常に簡素化され、故障の少ない塗装方法であ
る。
The present invention is a method that enables continuous coating at high speed, eliminates waste of coating agent, is extremely simple in terms of equipment, and has fewer failures.

すなわち、本発明は、塗装剤を連続的にほぼ垂
直に流下させ、一定間隔をもつて配置された複数
のガラス容器をその回転対象軸を水平に保持しつ
つ該回転対象軸を中心として回転させながら、流
下被覆域を通過させ、かつ流下被覆域に実質上絶
えず1ないし複数のガラス容器が存在するように
移動させてなることを特徴とするガラス容器の連
続塗装方法である。連続的に塗装剤を流下し、
個々の被塗装物に合せて塗装剤の流下を停止する
必要が全くないため、装置的にも簡素化され安価
な装置となるだけでなく、塗装処理能力をあげて
スピード化され、また従来塗装剤の流下を各々止
めたことによるノズルの先端の塗装剤だまりによ
る膜厚の不均一性もなくなり平滑な皮膜を得るこ
とができる。
That is, the present invention allows a coating agent to flow down continuously almost vertically, and rotates a plurality of glass containers arranged at regular intervals around the rotational axis while holding the rotational axis horizontally. This is a continuous coating method for glass containers, characterized in that the glass containers are moved through a falling coating area and one or more glass containers are substantially constantly present in the falling coating area. The paint is continuously poured down,
Since there is no need to stop the flow of paint according to each object to be painted, the equipment is not only simpler and cheaper, but also has faster painting processing capacity and is faster than conventional painting methods. Non-uniformity in film thickness caused by pooling of paint at the tip of the nozzle due to stopping the flow of each agent is eliminated, and a smooth film can be obtained.

塗装剤の流下方法として、被塗装物の水平面に
合せた垂直状の複数個の管状ノズル、実質上水平
位にある管状ノズルから垂直に複数個の小管を分
岐したノズルあるいは容器底に小穴のあいたノズ
ル等から実質上垂直にシヤワー状に流下するもの
でよく、エアースプレー並びエアーレススプレー
方式による霧化された塗装剤が飛流されてもよ
く、またスリツト状ノズルからのカーテンフロー
コーターならび水平面からのオーバーフロー方式
によるフローコーターでも使用できる。また筒状
ブラシ、棒状ブラシあるいはメツシユ状の容器等
からの粉末状塗装剤の落下方法も使用できる。な
お、本発明に係わる流下において完全に垂直であ
る場合だけでなく、極くわずかに垂直から傾いた
場合、一定の広がりをもつて流下する場合も含ま
れる。
The paint can be flowed down using multiple tubular nozzles vertically aligned with the horizontal surface of the object to be coated, a nozzle with multiple small tubes branching vertically from a substantially horizontal tubular nozzle, or a small hole in the bottom of the container. It may flow down from a nozzle substantially vertically in a shower-like manner, or atomized paint may be flown by air spray or airless spray methods, or curtain flow coater from a slit-shaped nozzle or from a horizontal surface. It can also be used with a flow coater using the overflow method. It is also possible to use a method of dropping the powder coating agent from a cylindrical brush, a rod-shaped brush, a mesh-shaped container, or the like. Note that the flow according to the present invention includes not only cases where the flow is completely vertical, but also cases where the flow is slightly inclined from the vertical, and cases where the flow flows down with a certain extent.

本発明に係わる塗装剤としては溶剤型(有機溶
剤、水)、無溶剤型(液状及び粉体)いずれも適
用出来る。熱可塑性樹脂としてはポリエチレン、
ポリプロピレン、ポリスチレン、アクリル樹脂、
塩化ビニル樹脂、塩化ビニリデン樹脂、酢酸ビニ
ル樹脂、ポリアミド、ポリエステル、ポリカーボ
ネート、シリコーン樹脂、ポリエーテル樹脂、繊
維素誘導体等である。熱硬化性樹脂としてはメラ
ミン樹脂、ユリア樹脂、エポキシ樹脂、ケイ素樹
脂、ポリウレタン樹脂、キシレン樹脂等である。
又、ゴム類としては天然ゴム、合成ゴムが適用し
得る。これらの中で、前記したように熱硬化性樹
脂がより好ましく、更に熱硬化性樹脂の中でもポ
リウレタン樹脂が被塗装物であるガラス容器の強
化に適している。塗装量は被塗装物および塗装目
的により異なるが、通常は10〜500μ(ミクロン)
程度(乾燥塗膜)である。
As the coating agent according to the present invention, both solvent type (organic solvent, water) and non-solvent type (liquid and powder) can be applied. Thermoplastic resins include polyethylene,
polypropylene, polystyrene, acrylic resin,
These include vinyl chloride resin, vinylidene chloride resin, vinyl acetate resin, polyamide, polyester, polycarbonate, silicone resin, polyether resin, and cellulose derivatives. Examples of thermosetting resins include melamine resin, urea resin, epoxy resin, silicone resin, polyurethane resin, and xylene resin.
Further, as the rubber, natural rubber and synthetic rubber can be used. Among these, as described above, thermosetting resins are more preferred, and among thermosetting resins, polyurethane resins are suitable for strengthening glass containers to be coated. The amount of coating varies depending on the object to be coated and the purpose of coating, but is usually 10 to 500μ (microns).
(dry coating film).

使用される塗装剤によつて流下方法が異なり、
例えば反応硬化型のウレタン樹脂もしくはエポキ
シ樹脂等の無溶剤型、溶剤型あるいはエマルジヨ
ン型塗装剤は垂直状の単数あるいは複数個の管状
ノズルあるいは水平状の管状ノズルから垂直に複
数個の小管に分岐した管状あるいは小穴状のノズ
ルからの塗装が好ましく、また反応硬化型樹脂を
用いた塗装剤で可使時間が長い低粘度の塗装であ
ればエアースプレー並びエアレススプレー方式や
カーテンフローコーターや、オーバーフローコー
ター方式によつても塗装できる。またエポキシ樹
脂粉体塗料やウレタン樹脂粉体塗料の如く熱硬化
性樹脂粉体塗料あるいはポリエチレン、ポリプロ
ピレン、ポリスチレン等の熱可塑性粉体樹脂塗料
は筒状ブラシ又は棒状ブラシから、あるいはメツ
シユ状の容器からこれらの回転あるいは振動によ
り粉体塗料を実質上均一に流下させて塗装するこ
とができる。熱可塑性樹脂の液状塗装剤では特に
制約なく、各種流下方法が適用できる。
The flow down method varies depending on the paint used,
For example, solvent-free, solvent-based, or emulsion-type coating agents such as reaction-curing urethane resins or epoxy resins have one or more vertical tubular nozzles or a horizontal tubular nozzle that branches vertically into a plurality of small tubes. Painting from a tubular or small-hole nozzle is preferable, and for low-viscosity coatings that use reaction-curing resins and have a long pot life, air spray, airless spray, curtain flow coaters, and overflow coaters can be used. It can also be painted by In addition, thermosetting resin powder coatings such as epoxy resin powder coatings and urethane resin powder coatings, and thermoplastic resin powder coatings such as polyethylene, polypropylene, and polystyrene are obtained from cylindrical or rod-shaped brushes, or from mesh-shaped containers. Due to these rotations or vibrations, the powder coating material can be applied by flowing down substantially uniformly. There are no particular restrictions on liquid coating agents made of thermoplastic resins, and various pouring methods can be applied.

被塗装物はその中心軸が線対象に回転しうるも
の例えば、棒状、筒状、瓶状あるいは缶状のもの
の表面等で、これらの塗装物が各々触れ合わない
程度に一定間隔をもつて連続して各々が回転しつ
つ塗装剤の流下被覆域に直続供給され塗装され
る。
The object to be painted is something whose central axis can rotate symmetrically, such as the surface of a rod, cylinder, bottle, or can, and the objects to be painted are continuous at regular intervals to the extent that they do not touch each other. While rotating, each of them is directly supplied to the falling coating area of the coating agent and is coated.

この様な複数の被塗装物を一定間隔をもつて配
置する方法の一例として、ガラスビンにおいて
は、立体的に移動する無端コンベヤーチエンに一
定間隔をもつて取り付けた回転自在のビン保持具
にガラスビンの口元を該ビン保持具にビン長軸が
水平になる様に保持せしめる。該ガラスビンの塗
装はガラスビンに塗装剤を被覆するに、必要に応
じてビン保持具ごと回転し、該ビン長軸を中心に
ビン各々が回転しつゝ、コンベヤーが塗装剤の流
下被覆域を通過して塗装される。この時、コンベ
ヤー速度ならびビンの回転数は必要に応じて可変
できるものである。ガラスビンを水平に保持し、
回転することにより、均一な塗膜とすることが出
来、レベリングを起こさせる。
As an example of such a method of arranging a plurality of objects to be coated at regular intervals, glass bottles are placed on rotatable bottle holders attached at regular intervals to an endless conveyor chain that moves three-dimensionally. Hold the mouth of the bottle in the bottle holder so that the long axis of the bottle is horizontal. To coat the glass bottles with the paint, the bottle holder is rotated as necessary, and each bottle is rotated around the long axis of the bottle, while a conveyor passes through the falling coating area of the paint. and then painted. At this time, the conveyor speed and the number of rotations of the bin can be varied as necessary. Hold the glass bottle horizontally
By rotating, it is possible to form a uniform coating film and cause leveling.

本発明における流下被覆域とは塗装剤が流下す
る方向において被塗装物の一部分あるいは全面に
塗装剤が塗着されうる範囲をいうものである。
In the present invention, the falling coverage area refers to an area where the coating agent can be applied to a part or the entire surface of the object in the direction in which the coating agent flows down.

次に本発明の連続塗装方法を図面により説明す
る。第1図、第4図〜第7図は本発明の実施態様
の概要を示す側面図である。第2図は第1図A−
A線断面図である。第3図は第1図の部分拡大図
である。第1図はコンベヤー1に一定間隔をもつ
て回転自在に水平保持された複数の被塗装物2を
塗装剤の流下手段3からほぼ垂直に流下している
塗装剤4に対し斜めに移動させる。流下被覆域に
おけるコンベヤーの傾きはコンベヤーの移動速
度、被塗装物の間隔に応じて異なり、塗装剤が被
塗装物以外の部分に流下しないように設計する。
つまり、流下被覆域に実質上絶えず被塗装物が存
在するように移動させる。なお、被塗装物が流下
被覆域において極くわずかの間だけ存在しない場
合でも、塗装剤の種類によつては直前に流下被覆
域に存在した被塗装物によつて塗装剤の流下が一
部曲げられたりするため、塗装剤の損失を防ぐこ
とが出来る。
Next, the continuous coating method of the present invention will be explained with reference to the drawings. 1 and 4 to 7 are side views showing an outline of an embodiment of the present invention. Figure 2 is Figure 1A-
It is an A-line sectional view. FIG. 3 is a partially enlarged view of FIG. 1. In FIG. 1, a plurality of objects 2 to be coated, which are rotatably held horizontally at regular intervals on a conveyor 1, are moved obliquely to a coating material 4 that is flowing down almost vertically from a coating material flowing down means 3. The inclination of the conveyor in the falling coverage area varies depending on the moving speed of the conveyor and the spacing of the objects to be coated, and is designed so that the coating agent does not flow down to areas other than the objects to be coated.
That is, the object to be coated is moved so that it is substantially constantly present in the falling coverage area. Note that even if the object to be painted does not exist in the falling coverage area for a very short time, depending on the type of coating agent, some of the flowing down of the coating agent may be caused by the object that was present in the falling coverage area immediately before. Since it can be bent, it is possible to prevent loss of paint.

第2図はノズルを用いた流下手段3を示してい
る。第2図では1本のノズルとしているが、被塗
装物の形状に応じて、複数本のノズルとしてもよ
い。また、ノズルの代わりにカーテンフローコー
ター等の流下手段であつてもよい。
FIG. 2 shows the flow means 3 using a nozzle. Although one nozzle is shown in FIG. 2, a plurality of nozzles may be used depending on the shape of the object to be coated. Moreover, a flow means such as a curtain flow coater may be used instead of a nozzle.

第3図は流下被覆域を説明するための第1図の
一部分拡大側面であり、点線で示された被塗装物
2が5の位置から6の位置に移動する状態を示し
た図である。5から6の位置に移動する間被塗装
物2は少なくとも1回転させる。塗装剤4が5の
位置にある被塗装物2に初めて接する部分7(被
塗装物2が垂直方向において流下手段3から一番
遠ざかつた位置)から被塗装物2が垂直方向にお
いて流下手段3に一番近づいた6の位置にある被
塗装物2の塗装部分8の間の塗装剤がほぼ垂直に
流下する点線で示した域が第1図の場合の流下被
覆域である。
FIG. 3 is a partially enlarged side view of FIG. 1 for explaining the falling coverage area, and shows a state in which the object 2 to be coated, indicated by a dotted line, moves from position 5 to position 6. While moving from position 5 to position 6, the object 2 to be coated is rotated at least once. The object to be coated 2 is moved vertically from the part 7 where the coating agent 4 comes into contact with the object 2 to be coated for the first time (the position where the object 2 is farthest from the flowing means 3 in the vertical direction) to the flowing means 3 in the vertical direction. The area indicated by the dotted line in which the coating agent flows down almost vertically between the painted parts 8 of the object 2 at the closest position 6 is the falling coverage area in the case of FIG.

第4図は塗装剤4の流下手段3に対し、下から
上へ垂直に被塗装物2を移動させ、塗装の終つた
被塗装物2を水平に移動させて、流下被覆域を出
るようにした方法である。なお、流下被覆域から
出る方法として水平に移動させる場合だけには限
らず、斜めに移動させてもよい。
FIG. 4 shows the object 2 to be coated being moved vertically from bottom to top with respect to the flowing down means 3 for the coating material 4, and the object 2 to be coated which has been coated being moved horizontally so as to exit the falling coating area. This is the method. Note that the method of leaving the downstream coverage area is not limited to horizontal movement, but may also be diagonal movement.

第5図は塗装剤4の流下手段3を1本から3本
にした実施態を示す。それぞれの流下手段3から
の塗装剤をすべて同一としてもよく、またそれぞ
れの流下手段3からの塗装剤4を異なるものとし
てもよい。
FIG. 5 shows an embodiment in which the number of flow means 3 for the coating material 4 is increased from one to three. All the coating agents from the respective flow down means 3 may be the same, or the coating agents 4 from the respective flow down means 3 may be different.

第6図はコンベヤーによつて被塗装物が斜め上
方に連続移動中にスプレーガンを用いた流下手段
3により塗装剤4を霧化状にして真下に向け連続
吐出して塗装する方法を示す。一般のスプレー塗
装では塗装剤の飛散が大きいが、本発明の方法で
はスプレーガンをなるべく被塗装物に接近させ、
塗装剤の広がりを小さくすることおよび塗装剤の
広がりにわたつて被塗装物を存在させることのた
め、損失は小さくなる。
FIG. 6 shows a coating method in which the coating material 4 is atomized by the falling means 3 using a spray gun and continuously discharged directly downward while the object to be coated is continuously moved obliquely upward by a conveyor. In general spray painting, the paint scatters a lot, but in the method of the present invention, the spray gun is moved as close to the object to be painted as possible.
Due to the smaller spread of the coating material and the presence of the object to be coated over the spread of the coating material, losses are reduced.

第7図は棒状ブラシ9の回転で金網状の吐出口
10から粉体樹脂塗料4を流下し、その塗装剤の
流下被覆域中をコンベヤーによりビンを連続移動
して塗装することを示す。粉体塗装の場合、被塗
装物を加熱させておくか、静電塗装によつて、粉
体塗装剤を被塗装物に塗着させる。
FIG. 7 shows that the powder resin paint 4 is caused to flow down from the wire-mesh-like outlet 10 by the rotation of the rod-shaped brush 9, and the bottle is continuously moved by a conveyor through the area covered by the paint. In the case of powder coating, the object to be coated is heated or a powder coating agent is applied to the object by electrostatic coating.

以上の図面において示した方法に限られたもの
ではなく、例えば第7図のような被塗装物の移動
方法に第1図の流下手段組合せ塗装できるもので
あり、またコンベヤーの移動方向がこれら図示し
た方向の逆方向であつてもかまわない。また流下
手段は1本とは限らない、第5図のように複数本
のノズルにより塗装してもよい。この場合、1つ
の被塗装物に対し、塗装域を分割し、複数個の流
下手段で順次塗装するようにしてもよい。
The method is not limited to the method shown in the above drawings; for example, the moving method of the object to be coated as shown in FIG. 7 can be combined with the flow means shown in FIG. It doesn't matter if it is in the opposite direction. Further, the number of flow means is not limited to one, and coating may be performed using a plurality of nozzles as shown in FIG. In this case, the coating area for one object to be coated may be divided and sequentially coated using a plurality of flowing means.

各ノズルの吐出量を考慮し、3ケ所の流下被覆
域を通過したのち被覆すべき部分に全て塗装する
ように各ノズルの位置、構造等を工夫する。また
塗布量、被塗装物の大きさ、移動速度、ガラスビ
ン等の被塗装物の回転数、移動斜度等によりそれ
ぞれの条件に合つた塗装方法を考慮する。
Considering the discharge amount of each nozzle, the position and structure of each nozzle are designed so that the coating passes through three downstream coating areas and then coats all the areas to be coated. Also, consider the coating method that suits each condition, depending on the amount of coating, the size of the object to be painted, the speed of movement, the number of revolutions of the object to be painted such as a glass bottle, the slope of movement, etc.

第8図は被塗装物としてのガラス容器に対し、
強化皮膜を施す場合に、本発明に係わる連続塗装
方法を適用したシステム全体の概略を1例として
示す側面図である。無端コンベヤーチエーンに一
定間隔を置いて複数のガラス容器2が保持具によ
り水平に保持され、かつガラス容器2が回転しつ
つ、連続的に移動できるようにされている。ガラ
ス容器の保持方法は水平に、かつ回転し得る方法
であればいずれでもよい。11の位置からガラス
容器を保持具に装着し、洗條槽等の洗條手段12
でガラス容器を洗條する。洗條においてはガラス
容器を垂直に保持する方法であつてもよい。洗條
後、乾燥手段14により十分乾燥し、プライマー
塗装手段13によりシランカツプリング剤、合成
樹脂等のプライマーを塗装し、乾燥手段14で乾
燥もしくは硬化させる。本発明に係わる塗装方法
で塗装してもよい。なお、プライマー塗装は必ず
しも塗装する必要はない。またガラス容器を予熱
する手段を設けてもよい。次に本発明に係わる塗
装を行なう。流下手段3には塗装剤供給手段15
があり、例えば熱硬化性樹脂の液状塗装剤ではそ
れぞれの貯蔵槽からの2液を混合して流下手段3
に供給する。なお、塗装剤を加温する手段を設け
てもよい。塗装を終えた被塗装物2を乾燥硬化手
段16により、塗装剤を乾燥もしくは硬化させ
る。必要に応じ、冷却手段を設けてもよい。17
の位置で塗装を完了した被塗装物2を脱着する。
なお、ガラス容器の回転は本発明に係わる塗装時
には必ず行なうが、その他の部分では必ずしも行
なうとは限らず、また回転数を変えてもよい。
Figure 8 shows a glass container as an object to be painted.
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a side view schematically showing, as an example, an entire system to which a continuous coating method according to the present invention is applied when applying a reinforced film. A plurality of glass containers 2 are held horizontally by a holder at regular intervals on an endless conveyor chain, and the glass containers 2 are allowed to move continuously while rotating. The glass container may be held in any manner as long as it can be held horizontally and rotated. The glass container is attached to the holder from position 11, and washing means 12 such as a washing tank is installed.
Wash the glass container with During washing, the glass container may be held vertically. After washing, it is sufficiently dried by the drying means 14, and a primer such as a silane coupling agent, synthetic resin, etc. is applied by the primer coating means 13, and then dried or hardened by the drying means 14. Coating may be performed using the coating method according to the present invention. Note that it is not necessary to apply primer coating. Further, a means for preheating the glass container may be provided. Next, coating according to the present invention is performed. The flowing means 3 includes a coating agent supplying means 15.
For example, in the case of a liquid coating agent made of a thermosetting resin, the two liquids from each storage tank are mixed and the flowing means 3
supply to. Note that a means for heating the coating agent may be provided. The coating agent on the coated object 2 that has been coated is dried or cured by a drying and curing means 16. A cooling means may be provided if necessary. 17
The object to be painted 2, which has been painted, is attached and detached at the position shown in FIG.
Although the glass container is always rotated during the coating according to the present invention, it is not necessarily rotated in other parts, and the rotation speed may be changed.

実施例 1 塗装剤 PCP−0300(米国、ユニオンカーバイド社製ポ
リエステルポリオール) 46.5重量部 PCP−0210(米国、ユニオンカーバイド社製ポ
リエステルポリオール) 11.6重量部 イソホロンジイソシアネート 41.9重量部 オクチル酸第一スズ 0.02重量部 第1図の塗装方法において、フアンタの1ガ
ラスビン(米国、コカコーラ社製)をビン間隔
154mmでコンベヤーチエーンに装着し、ビン回転
数60rpm、コンベヤー速度3.8m/分、傾斜角度
77度にてガラスビンを連続移動させ、上記塗装剤
を移動するガラスビンに接触しないような高さに
設定した第2図に示す流下手段により吐出量−
500g/分でほぼ垂直に流下させ、1本のガラス
ビンに20gの塗装剤を施こし、約220μの塗膜を
形成した。なお、塗装剤の焼付はプロパンガス炉
により180℃、12分間で行なつた。
Example 1 Coating agent PCP-0300 (polyester polyol manufactured by Union Carbide, USA) 46.5 parts by weight PCP-0210 (polyester polyol manufactured by Union Carbide, USA) 11.6 parts by weight Isophorone diisocyanate 41.9 parts by weight Stannous octylate 0.02 parts by weight In the painting method shown in Figure 1, one glass bottle of Juanta (manufactured by the Coca-Cola Company, USA) was
Attached to the conveyor chain with 154mm, bin rotation speed 60rpm, conveyor speed 3.8m/min, tilt angle
The glass bottle is continuously moved at an angle of 77 degrees, and the amount of discharge is -
The paint was allowed to flow down almost vertically at a rate of 500 g/min, and 20 g of the paint was applied to one glass bottle, forming a coating film of approximately 220 μm. The coating agent was baked in a propane gas oven at 180°C for 12 minutes.

塗装剤を連続的に流下させて、塗装が行なえる
ため、装置が簡略化出来、しかも塗装剤の損失も
ない。得られた塗装ビンには均一な塗膜の形成が
出来た。
Since the coating can be performed by continuously flowing down the coating agent, the equipment can be simplified and there is no loss of the coating agent. A uniform coating film could be formed on the obtained coating bottle.

実施例 2 実施例1の塗装方法(第1図)の代わりに第4
図に示す塗装方法で行なつた。コンベヤーチエー
ンを半径200mmで垂直移動から水平移動にした。
他の条件は実施例1と同様にして塗装したとこ
ろ、塗装剤の損失もなく、均一な塗膜が形成出来
た。
Example 2 Instead of the coating method of Example 1 (Fig. 1), the 4th coating method was used.
This was done using the painting method shown in the figure. The conveyor chain was changed from vertical movement to horizontal movement with a radius of 200mm.
When coating was carried out under the same conditions as in Example 1, a uniform coating film was formed without any loss of coating agent.

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

第1図、第4〜第7図は本発明の実施態様を示
す側面図、第2図は第1図におけるA−A線断面
図、第3図は第1図の一部分拡大図、第8図はガ
ラス容器に強化皮膜を施す場合に、本発明の塗装
方法を適用したシステム全体の1例を示す側面図
をそれぞれ表わす。 図中の符号、1……コンベヤー、2……被塗装
物、3……流下手段、4……塗装剤、5,6……
流下被覆域を説明するための被塗装物の位置、7
……流下被覆域を説明するための位置、9……棒
状ブラシ、10……吐出口、11……ガラス容器
の装着部分、12……洗條手段、13……プライ
マー塗装手段、14……乾燥手段、15……塗装
剤供給手段、16……乾燥硬化手段、17……ガ
ラス容器の脱着部分。
1 and 4 to 7 are side views showing embodiments of the present invention, FIG. 2 is a sectional view taken along line A-A in FIG. 1, FIG. 3 is a partially enlarged view of FIG. 1, and FIG. The figures each represent a side view showing an example of the entire system to which the coating method of the present invention is applied when applying a reinforced coating to a glass container. Symbols in the diagram: 1...Conveyor, 2...Object to be painted, 3...Flowing means, 4...Painting agent, 5, 6...
Position of the object to be painted to explain the falling coverage area, 7
. . . Position for explaining the falling coverage area, 9 . . . Rod-shaped brush, 10 . . . Discharge port, 11 . Drying means, 15... Painting agent supplying means, 16... Drying hardening means, 17... Desorption portion of the glass container.

Claims (1)

【特許請求の範囲】 1 塗装剤を連続的にほぼ垂直に流下させ、一定
間隔をもつて配置された複数のガラス容器をその
回転対象軸を水平に保持しつつ該回転対象軸を中
心として回転させながら流下被覆域を通過させ、
かつ流下被覆域に実質上絶えず1ないし複数のガ
ラス容器が存在するように移動させてなることを
特徴とするガラス容器の連続塗装方法。 2 塗装剤が高粘度液状塗装剤である特許請求の
範囲第1項記載の連続塗装方法。 3 塗装剤が反応硬化型塗装剤である特許請求の
範囲第1項または第2項記載の連続塗装方法。 4 複数のガラス容器を水平方向に対し傾斜を持
たせて移動させてなる特許請求の範囲第1項〜第
3項いずれか記載の連続塗装方法。
[Scope of Claims] 1. A method of rotating a plurality of glass containers arranged at regular intervals around an axis of rotation while holding the axis of rotation horizontally while causing a coating agent to flow down continuously almost vertically. passing through the downstream coverage area while
A continuous coating method for glass containers, characterized in that the glass containers are moved so that one or more glass containers are substantially constantly present in the falling coverage area. 2. The continuous coating method according to claim 1, wherein the coating agent is a high viscosity liquid coating agent. 3. The continuous coating method according to claim 1 or 2, wherein the coating agent is a reaction curing type coating agent. 4. The continuous coating method according to any one of claims 1 to 3, wherein a plurality of glass containers are moved at an angle with respect to the horizontal direction.
JP3568979A 1979-03-28 1979-03-28 Continuous coating method Granted JPS55129175A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3568979A JPS55129175A (en) 1979-03-28 1979-03-28 Continuous coating method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3568979A JPS55129175A (en) 1979-03-28 1979-03-28 Continuous coating method

Publications (2)

Publication Number Publication Date
JPS55129175A JPS55129175A (en) 1980-10-06
JPS6341629B2 true JPS6341629B2 (en) 1988-08-18

Family

ID=12448859

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3568979A Granted JPS55129175A (en) 1979-03-28 1979-03-28 Continuous coating method

Country Status (1)

Country Link
JP (1) JPS55129175A (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58214374A (en) * 1982-06-04 1983-12-13 Kyowa Denki Kagaku Kk Method and apparatus for coating vessel by letting coating agent continuously flow downwards
EP0142583B1 (en) * 1983-11-14 1987-05-20 Kyowa Denki Kagaku K.K. Process and apparatus for coating the surfaces of containers with coating material
KR100644201B1 (en) 2005-09-30 2006-11-10 (주)대영리버스 Automatic coating system inside the kitchen container

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS53134841A (en) * 1977-04-27 1978-11-24 Andatsukusu Pty Ltd Liquid coating method and apparatus for flat article

Also Published As

Publication number Publication date
JPS55129175A (en) 1980-10-06

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