JPS61212359A - Coating apparatus - Google Patents
Coating apparatusInfo
- Publication number
- JPS61212359A JPS61212359A JP60052329A JP5232985A JPS61212359A JP S61212359 A JPS61212359 A JP S61212359A JP 60052329 A JP60052329 A JP 60052329A JP 5232985 A JP5232985 A JP 5232985A JP S61212359 A JPS61212359 A JP S61212359A
- Authority
- JP
- Japan
- Prior art keywords
- coating
- paint
- tank
- agitator
- coated
- 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.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F33/00—Other mixers; Mixing plants; Combinations of mixers
- B01F33/80—Mixing plants; Combinations of mixers
Landscapes
- Coating Apparatus (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は塗布直前に塗料を混合し、連続的に塗布し均一
な塗膜をうろことができる浸漬塗布装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Field of Application] The present invention relates to a dip coating device that is capable of mixing a coating material immediately before coating and coating the coating material continuously to form a uniform coating film.
被塗布物の表面に塗料を塗布するには、浸漬塗布方法が
一般的であシ、比較的容易に良好な塗膜が得られる。A dip coating method is generally used to apply a paint to the surface of an object to be coated, and a good paint film can be obtained relatively easily.
反面、多量の塗料を必要とし、特に、2液温合タイプの
工4N−+7.ウレタン、アクリル等の加熱硬化製樹脂
を使用した場合、硬化剤と配合して塗料を調製した後、
常温においても反応による粘度上昇が経時とともに進行
し、同一条件で均一な塗膜を連続して得ることが困難と
なる。との様に連続塗布が不可能な上に塗料槽内に残留
する塗料は粘度上昇、ダル化した時点で廃棄されるため
不経済である。On the other hand, it requires a large amount of paint, especially the two-component heating type 4N-+7. When using heat-curable resins such as urethane and acrylic, after preparing the paint by mixing it with a curing agent,
Even at room temperature, the viscosity increases over time due to the reaction, making it difficult to continuously obtain uniform coatings under the same conditions. As such, continuous coating is not possible, and the paint remaining in the paint tank is uneconomical because it is discarded once its viscosity increases and it becomes dull.
本発明は塗布槽中の塗料を有効に利用でき、とくに2液
温合タイプの加熱硬化製樹脂主剤と硬化剤とを塗布直前
で混合し供給することによシ反応による粘度上昇を最小
限にし連続的塗布な夾施しうる塗布装置を提供すること
にある。The present invention makes it possible to effectively utilize the paint in the coating tank, and in particular minimizes the increase in viscosity due to reaction by mixing and supplying the two-component heating type thermosetting resin base and curing agent immediately before coating. It is an object of the present invention to provide a coating device capable of continuous coating.
本発明に従って、被塗布物の外径とほぼ同じ貫通孔を有
する塗布槽と塗料循環系統とからなり、該塗布槽に被塗
布物の外径よシ僅かに小さい漏液防止シートを設け、該
漏液防止シートと塗布槽とより構成される間隙部分に塗
料を溜めて被塗布物を垂直移動させて塗膜を形成せしめ
る装置において、上記塗布槽に攪拌機を付設した塗料吐
出器が連結されており、28以上の液を混合、攪拌し乍
ら混合塗料が該攪拌機のオリフィスより塗布槽に吐出さ
れることを特徴とする塗布装置が提供される。According to the present invention, the coating tank is comprised of a coating tank having a through hole that is approximately the same as the outer diameter of the object to be coated, and a paint circulation system, and the coating tank is provided with a leakage prevention sheet that is slightly smaller than the outer diameter of the object to be coated. In a device that collects paint in a gap formed by a leakage prevention sheet and a coating tank and moves the object to be coated vertically to form a coating film, a paint discharger equipped with an agitator is connected to the coating tank. There is provided a coating device characterized in that 28 or more liquids are mixed and stirred and the mixed paint is discharged from an orifice of the stirrer into a coating tank.
本発明を添付図面で説明する。第1図は本発明の塗布装
置を説明する概略図である。塗布槽10は被塗布物11
の外径とほぼ同じ貫通孔が穿設されておフ、被塗布物1
1の外径よシ僅かに小さい内径を持つリング状漏液防止
シー)15を備えておシ、被塗布物11と塗布槽10と
漏液防止シー)15とから構成される間隙部分16に塗
料を溜める。被塗布物11を駆動系13によりスクリー
ーネジ14を介し垂直移動させて塗膜を形成させる。第
1図には2液を混合して反応硬化させる塗料を用いる場
合の缶液(一方は主剤、他方は硬化剤)の循環系統及び
洗浄用溶剤タンクが示されている。主剤及υ硬化剤の缶
液をタンク6に投入し定量4ンデにて塗料の硬化条件を
考慮して最適量を決定し定量搬送する。熱交換器7にて
粘度、反応性の均一化を図るための一定温度とする。流
量計8は循環流量を計測する手段である。塗布槽10に
充分な塗料がある場合は三方弁2にて液はタンク6に戻
る。塗布槽10に塗料が必要とされる場合、三方弁2に
よシ液方向が吐出器5側に仕向けられる。吐出器内で合
流された液は攪拌機1を通過する間混合、攪拌され乍ら
塗布槽10に吐出される。塗料がタンク6に戻る場合と
攪拌、吐出される場合に液圧力差が生じ混合流量比が変
化することが考えられるが、調圧弁3を調整することに
よシ適正な混合流量比が確保される。The invention is illustrated in the accompanying drawings. FIG. 1 is a schematic diagram illustrating a coating apparatus of the present invention. The coating tank 10 is used to store objects 11 to be coated.
A through hole is drilled that is approximately the same as the outer diameter of the object to be coated 1.
A ring-shaped liquid leakage prevention sheath) 15 having an inner diameter slightly smaller than the outer diameter of 1 is provided, and a gap portion 16 consisting of the object to be coated 11, the coating tank 10, and the liquid leakage prevention sheath) 15 is provided. Collect paint. The object 11 to be coated is vertically moved by a drive system 13 via a screen screw 14 to form a coating film. FIG. 1 shows a circulation system for can liquid (one is a main agent and the other is a curing agent) and a cleaning solvent tank when using a paint that is cured by reaction by mixing two liquids. The main agent and curing agent cans are put into the tank 6, and the optimal amount is determined in consideration of the curing conditions of the paint, and the amount is transported in a fixed amount. The heat exchanger 7 maintains a constant temperature in order to equalize the viscosity and reactivity. The flow meter 8 is a means for measuring the circulating flow rate. When there is sufficient paint in the coating tank 10, the liquid is returned to the tank 6 by the three-way valve 2. When paint is required in the coating tank 10, the three-way valve 2 directs the liquid toward the discharger 5 side. The combined liquids in the discharge device are mixed and stirred while passing through the stirrer 1, and then discharged into the coating tank 10. It is conceivable that a liquid pressure difference occurs when the paint returns to the tank 6 and when it is stirred and discharged, causing a change in the mixing flow ratio, but by adjusting the pressure regulating valve 3, an appropriate mixing flow ratio can be ensured. Ru.
上記の攪拌機1を付設した塗料吐出量5において、2液
が混合、攪拌されると同時に攪拌機内を通過して混合塗
料が攪拌機1のオリフィスから塗布im””1” o内
に吐出されることが重要である。かかる攪拌押出機はラ
セン型スクリーーを内蔵することが好ましい。とくに好
ましい攪拌押出機は第2図に示すとおシである。攪拌機
1にラセン方向のことなる°ラセン帯翼が内蔵されてお
り、その拡大―が第3図に示されている。At the paint discharge rate 5 with the above-mentioned stirrer 1 attached, the two liquids are mixed and stirred, and at the same time, the mixed paint passes through the stirrer and is discharged from the orifice of the stirrer 1 into the coating im""1" o. It is important that such an agitating extruder has a built-in helical type screen.A particularly preferable agitating extruder is shown in FIG. Its enlargement is shown in Figure 3.
上記の循環系統の操作によシ缶液が吐出器のオリフィス
23よシ吐出されるが、液は攪拌機1内の2セン帯g2
1を通過する間混合され攪拌されて吐出オリフィス22
より塗布槽10に吐出される。オリフィス22と23の
径を適宜選択することによシ塗料粘度の大きさに応じて
循環及び吐出圧力が適正にされる。ラセン帯翼21の径
、ラセンの深さ、数を適宜に選択して攪拌効率の最適値
が得られる。By operating the above-mentioned circulation system, the canned liquid is discharged through the orifice 23 of the discharger, but the liquid is in the 2-sen zone g2 in the stirrer 1.
1 and is mixed and stirred while passing through the discharge orifice 22.
The liquid is then discharged into the coating tank 10. By appropriately selecting the diameters of the orifices 22 and 23, the circulation and discharge pressure can be adjusted appropriately depending on the viscosity of the paint. The optimum value of stirring efficiency can be obtained by appropriately selecting the diameter of the helical band blade 21, the depth and the number of helices.
尚吐出器本体5は攪拌機l及びオリフィス23を支持す
るもので、内部には科液通路24及び25並びに撹拌機
洗浄用溶剤通路26が設けられている、。The discharger main body 5 supports the stirrer 1 and the orifice 23, and is provided with liquid passages 24 and 25 and a solvent passage 26 for cleaning the stirrer inside.
以上のべるとおり、2種以上の液を混合するタイプの硬
化製樹脂塗料を塗布直前に必要量だけ混合攪拌下で塗布
槽に吐出させ補給することによシ、従来反応による増粘
のため連続塗布が不可能で、かつ不経済であった塗布工
程を連続的可能とし、塗料使用歩留シな向上せしめると
とができる。As mentioned above, by discharging the required amount of cured resin paint of the type that mixes two or more liquids into the coating tank while mixing and stirring immediately before coating, continuous coating due to thickening by reaction is possible. The coating process, which was previously impossible and uneconomical, can now be performed continuously, and the yield of paint can be improved.
実施例1 塗料樹脂として熱硬化型アクリレート(商品名。Example 1 Thermosetting acrylate (product name) as a paint resin.
アロニクスM8060.東亜合成化学(株))を準備し
た。との樹脂100重量部に対し50重量部の酸化チタ
ン(商品名5RIT:堺化学(株))をサンドミルにて
2時間分散し塗料とした。この塗料は樹脂100重量部
に対し、1重量部の過酸化ベンシイ ゛ルを混合する
ことによj0130℃で硬化するものであるが、常温で
も5時間後には塗料に小片のダル状のものが発生し、2
4時間後にはほとんど流動性が無くなる経時安定性の悪
い塗料である。Aronix M8060. Toagosei Kagaku Co., Ltd. was prepared. To 100 parts by weight of the resin, 50 parts by weight of titanium oxide (trade name: 5RIT, manufactured by Sakai Chemical Co., Ltd.) was dispersed in a sand mill for 2 hours to prepare a paint. This paint is made by mixing 1 part by weight of benzyl peroxide with 100 parts by weight of resin, and cures at 130°C, but even at room temperature, after 5 hours, small pieces of dull particles appear on the paint. Occurred, 2
The paint has poor stability over time, with almost no fluidity after 4 hours.
第1図の塗布装置にて上記塗料樹脂と過酸化ベンゾイル
を個別にタンクに準備した。尚過酸化ベンゾイルは、攪
拌後の粘度を考瀘に入れ、メチルエチルケトン(MEK
)にて50倍希釈し九ものとした。The coating resin and benzoyl peroxide were separately prepared in tanks using the coating apparatus shown in FIG. Note that benzoyl peroxide was prepared by taking into consideration the viscosity after stirring and using methyl ethyl ketone (MEK).
) and diluted 50 times to make 9 diluted diluted products.
定量ポンプはスイス・マーグ社の小屋歯車定量−ンプを
使用し、塗料樹脂を100.9/分、過酸化ベンゾイル
/ MEK溶液を50 g/分の流量で循環させ、循環
、及び吐出時の液圧力がそれぞれ2sHt7cxi’及
び5に9f/m となる様に圧力調整弁を設定した。A metering pump made by Swiss company Maag was used to circulate the paint resin at a flow rate of 100.9 g/min and the benzoyl peroxide/MEK solution at a flow rate of 50 g/min. The pressure regulating valves were set so that the pressures were 2sHt7cxi' and 5 and 9f/m2, respectively.
これを必要量だけ塗布槽に攪拌下に”吐出し、次次に円
筒状被塗布物を一定の速度で上方に移動させる事によっ
て塗膜形成を行なったところ下表の様に連続の塗布作業
でも均一な膜厚が得られた。The necessary amount of this was discharged into the coating tank while stirring, and then the cylindrical object to be coated was moved upward at a constant speed to form a coating film, resulting in a continuous coating process as shown in the table below. However, a uniform film thickness was obtained.
尚、塗膜は塗布後130℃の乾燥炉で30分加熱硬化さ
せた後膜厚測定なした。The coating film was cured by heating in a drying oven at 130°C for 30 minutes after coating, and then the film thickness was measured.
スター) 20μ 20μ3時
間後 20μ 20μat膜にプ
5時間後 21μ 25μ()ツが
入る
8時間後 21μ 塗布不可能(rル
化による)実施例2
塗料として二液型ウレタンを準備した。主剤としてポリ
エステルIリオール(商品名:エフ42フ8002日本
?リウレタン(株))100重量部、エチルグリコール
アセテート60重量部、酢酸エチル60重量部、トルエ
ン60重量部よりなる均−系、硬化剤としてポリイソシ
アネート(商品名:コロネートL1日本?リウレタン(
株))100重量部、トルエン20重量部よ)なる均−
系をそれぞれ前記塗布装置のタンク6に個別に投入した
。Star) 20μ 20μ After 3 hours 20μ After 5 hours when the 20μ at film is coated 21μ 25μ After 8 hours when () is applied 21μ Unable to apply (due to ruolization) Example 2 A two-component urethane was prepared as a paint. A homogeneous system consisting of 100 parts by weight of polyester Iliol (trade name: F42F 8002 Nippon Riurethane Co., Ltd.) as a main ingredient, 60 parts by weight of ethyl glycol acetate, 60 parts by weight of ethyl acetate, and 60 parts by weight of toluene, as a curing agent. Polyisocyanate (Product name: Coronate L1 Japan? Riurethane (
Co., Ltd.) 100 parts by weight, toluene 20 parts by weight)
Each system was individually charged into the tank 6 of the coating device.
定量47グによる循環量を主剤7097分、硬化剤30
97分とし、実施例1で示した方法と同様に、塗布を実
施したところ、塗布開始時から8時間の連続塗布におh
で、膜厚の変動は与られなかりた。比較例として主剤と
硬化剤の比を70重量部対30重量部として混合し、通
常の浸漬塗布方法で塗布した塗膜は、塗布開始から5時
間後にその膜厚は2倍となシ、8時間後には増粘によシ
塗布不能となった。The circulation amount based on a fixed amount of 47 grams is 7097 minutes for the main agent and 30 minutes for the hardening agent.
When coating was carried out in the same manner as in Example 1 for 97 minutes, continuous coating for 8 hours from the start of coating was h
Therefore, variations in film thickness were not considered. As a comparative example, a coating film was prepared by mixing the base resin and curing agent at a ratio of 70 parts by weight to 30 parts by weight and applied by a normal dip coating method, and the film thickness was doubled 5 hours after the start of coating. After some time, the viscosity increased and it became impossible to apply.
第1図・・・本発明の塗布装置全体の説明図である01
・・・らせん状攪拌器、2・・・3方切換弁、3・・・
圧力調整弁、4・・・定量ポンプ、5・・・吐出器、6
・・・塗料タンク、7・・・熱交換器、8・・・流量計
、9・・・洗浄用溶剤タンク、lO・・・塗布槽、11
・・・被塗布物、12・・・被塗布物昇降台、13・・
・駆動系、14・・・スクリューネジ、15・・・漏液
防止シート、16・・・塗料を溜める間隙部。
第2図・・・攪拌機を付設した吐出器の説明図であるO
第3図・・・ラセン帯翼の拡大図である。
21・・・ラセン帯翼、22・・・吐出オリフィス、2
3・・・オリフィス、24.25・・・塗料通路、26
・・・洗浄用溶剤通路。
第1rXIFig. 1: 01 is an explanatory diagram of the entire coating device of the present invention.
...Spiral stirrer, 2...3-way switching valve, 3...
Pressure regulating valve, 4...metering pump, 5...discharge device, 6
... Paint tank, 7 ... Heat exchanger, 8 ... Flow meter, 9 ... Cleaning solvent tank, lO ... Application tank, 11
...To be coated, 12...To be coated object lifting platform, 13...
- Drive system, 14...Screw screw, 15...Leakage prevention sheet, 16...Gap portion for collecting paint. Fig. 2: An explanatory view of a discharger equipped with an agitator Fig. 3: An enlarged view of a helical band blade. 21... Spiral band blade, 22... Discharge orifice, 2
3... Orifice, 24.25... Paint passage, 26
...Cleaning solvent passage. 1st rXI
Claims (3)
と塗料循環系統とからなり、該塗布槽に被塗布物の外径
より僅かに小さい漏液防止シートを設け該漏液防止シー
トと塗布槽とより構成される間隙部分に塗料を溜めて被
塗布物を垂直移動させて塗膜を形成せしめる装置におい
て、上記塗布槽に攪拌機を付設した塗料吐出器が連結さ
れており、2種以上の液を混合、攪拌し乍ら混合塗料が
該攪拌機のオリフィスから塗布槽に吐出されることを特
徴とする塗布装置。(1) Consists of a coating tank with a through hole that is approximately the same as the outer diameter of the object to be coated and a paint circulation system, and a leak prevention sheet that is slightly smaller than the outer diameter of the object to be coated is provided in the coating tank to prevent liquid leakage. In an apparatus for forming a coating film by storing paint in a gap formed by a sheet and a coating tank and vertically moving an object to be coated, the coating tank is connected to a paint discharger equipped with an agitator, and 2 A coating device characterized in that, while mixing and stirring two or more liquids, the mixed paint is discharged from an orifice of the stirrer into a coating tank.
合わせを内蔵する特許請求の範囲第1項の塗布装置。(2) The coating device according to claim 1, wherein the agitator incorporates a combination of helical band blades having different helical directions.
プ、圧力調整弁を有する循環系統から塗料吐出器に供給
される特許請求の範囲第1項の塗布装置。(3) The coating device according to claim 1, wherein each of the two or more types of liquids is supplied to the paint discharger from a circulation system having at least a paint tank, a pump, and a pressure regulating valve.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60052329A JPS61212359A (en) | 1985-03-18 | 1985-03-18 | Coating apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60052329A JPS61212359A (en) | 1985-03-18 | 1985-03-18 | Coating apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61212359A true JPS61212359A (en) | 1986-09-20 |
Family
ID=12911753
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60052329A Pending JPS61212359A (en) | 1985-03-18 | 1985-03-18 | Coating apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61212359A (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5669238A (en) * | 1979-10-31 | 1981-06-10 | Fujitsu Ltd | Apparatus for coating optical fiber |
-
1985
- 1985-03-18 JP JP60052329A patent/JPS61212359A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5669238A (en) * | 1979-10-31 | 1981-06-10 | Fujitsu Ltd | Apparatus for coating optical fiber |
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